-------
50% FREEBOARD RATIO
RFC OFF
OPEN
CLOSED
LID POSITION
Figure 20. Effect of lid in reducing solvent loss from idle
degreaser holding nonboiling methylene chloride.
64
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50
40
^30
O
LjJ
OS
00
O
20
o
to
50% FREEBOARD RATIO
RFC OFF
OPEN
LID POSITION
CLOSED
Figure 21. Effect of lid in reducing solvent loss from idle
degreaser holding boiling methylene chloride.
65
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(40)
75 TOO
FREEBOARD RATIO, %
125
Figure 22. Effect of freeboard ratio in reducing solvent loss
from idle degreaser holding nonboiling methylene chloride.
66
-------
40
30
20
o
o
O
LU
ee
00 10
«/0
o
o
1/1
(10)
(20)
LID OPEN
RFC OFF
50
75 100
FREEBOARD RATIO, %
125
Figure 23. Effect of freeboard ratio in reducing solvent loss
from idle degreaser holding boiling methylene chloride.
67
-------
10
0 -
(10)
(20)
(30)
(40)
r (50)
i/o
oo
o
(60)
(70)
(80)
(90)
(100)
(110)
(120)
(130)
(140) '
LID OPEN
O RFC OFF
O RFC I TEMP., !• TO 2*C
D RFC II TEMP., -29° to -40°C
_L
50
75 100
FREEBOARD RATIO, %
i25
Figure 24. Effect of refrigerated freeboard chiller in reducing solvent
loss from idle degreaser holding nonboiling methylene chloride.
68
-------
LID OPEN
O RFC OFF
O RFC I TEMP.,
1° TO 2°C (ONLY ONE
VALUE OBTAINED).
DRFC II TEMP., -29
TO -40°C
75 100 125
FREEBOARD RATIO, *
Figure 25. Effect of refrigerated freeboard chiller in reducing
solvent loss from idle degreaser holding boiling methylene chloride.
69
-------
70
60
50
40
(10)
LID OPEN
RFC OFF
O BOILING SOLVENT
D HONBOILING SOLVENT
50 75 100
FREEBOARD RATIO, X
125
Figure 26. Effect of freeboard ratio in reducing solvent
loss from idle degreaser holding methylene chloride.
70
-------
20
10
*« 0
o
i—»
t—
u
1
UJ
"(10)
(20)
(30)
(40)
(50)
O 50% LOAD AREA
D 701 LOAD AREA
RFC OFF
HOIST SPEED 0.04 m/s
(8 ft/m1n)
50 75 100
FREEBOARD RATIO, X
125
Figure 27. Effect of freeboard ratio in reducing solvent
loss from operating degreaser using methylene chloride.
71
-------
70
60
50
40
«
g"
20
(10)
(20)
ORFC OFF
O*fC I TEMP., >0»C
ORFC II TEMP., -29* TO -40°C
HOIST SPEED 0.04 m/s
(8 ft/mln)
I
SO 75 100
FREEBOARD RATIO. I
125
Figure 28.. Effect.of refrigerated freeboard chiller in reducing
solvent loss from operating degreaser using methylene chloride
and 50 percent load area.
72
-------
AVERAGE CROSSCURRENT AIR VELOCITY, ft/min
20 40 60
100 —
(100)-
o
*—i
h-
<_>
(200) —
(300) —
o
to
(400) —
(500) —
(600)-
(700)
ill i i i i I i i i I i i I I i i i iii
O50% FREEBOARD RATIO
£75% FREEBOARD RATIO
0.1 0.2 0.3
AVERAGE CROSSCURRENT AIR VELOCITY, m/s
Figure 29. Effect of crosscurrent air velocity
on solvent loss from idle degreaser holding
boiling methylene chloride.
73
-------
100
a-?
o
UJ
(100)
(200)
(300)
OO
l/>
O
(400)
(500)
(600)
(700;
(800)
AVERAGE CROSSCURRENT AIR VELOCITY, ft/min
20 40 60 80 100
50% FREEBOARD RATIO
O IDLE DEGREASER HOLDING
BOILING SOLVENT
A IDLE DEGREASER HOLDING
NONBOILING SOLVENT
D OPERATING DEGREASER AT
0.04 m/s (8 ft/min)
I I I
I
0.1 0.2 0.3 0.4
AVERAGE CROSSCURRENT AIR VELOCITY, m/s
0.5
Figure 30. Effect of crosscurrent air velocity on
solvent loss from degreaser using methylene chloride.
74
-------
LIP EXHAUST RATE, ft3/min per ft2 of top opening
50 100
(100)
»*
*
o
a:
i/i
(200)
(300)
(400)
50% LOAD AREA
-OIDLE DEGREASER WITH 50% FREEBOARD
- RATIO HOLDING BOILING SOLVENT^
A IDLE DEGREASER WITH 75% FREEBOARD
_ RATIO HOLDING BOILING SOLVENT
D OPERATING DEGREASER AT 0.04 m/s (8 ft/min)
HOIST SPEED, 50% LOAD AREA
I
I
I
0.1
0.2
0.4
0.5
0.3
LIP EXHAUST RATE, m3/s per m2 of top opening
Figure 31. Effect of lip exhaust rate in reducing solvent
loss from degreaser using methylene chloride.
75
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degreasers holding nonboiling MC, from 22 to 61 percent. For
idle degreasers holding boiling TE and MC, the corresponding
ranges of solvent loss reduction are 7 to 61 percent and 34 to
35 percent.
Freeboard Ratio—
The results of tests on operating degreasers using both TE
and MC show a clear trend toward a decrease in solvent loss as
the freeboard ratio is increased. With degreasers using TE and
a normal load area of 50 percent, solvent loss was reduced by a
range of 7 to 25 percent as FR increased from 50 to 75 percent;
and was reduced by a range of 47 to 53 percent as FR increased
from 50 to 100 percent (Figure 12). With degreasers using MC
and a load area of 50 percent, solvent loss was reduced by a
range of 17 to 22 percent as FR was increased to 75 percent;
solvent loss was reduced 25 percent as FR was increased to 125
percent (Figure 27). When the load area was increased to 70
percent, similar results were obtained. Using TE, solvent loss
was reduced by a range of 8 to 16 percent when FR was increased
to 125 percent; using MC, solvent loss was reduced about 40
percent under the same conditions.
Similar tests were run with a change of hoist speed from
0.04 to 0.08 m/s (8 to 16 ft/min). In these tests (Figure 13),
solvent loss was reduced by 28 percent as FR was increased from
50 to 75 percent (using TE and a normal load of 50 percent).
When FR was increased beyond 75 percent, however, no further
significant reduction in solvent loss was obtained. Solvent
loss was also reduced 30 percent as FR was increased from 50 to
125 percent using TE and a load area of 70 percent.
The test results indicated that increased freeboard ratio
has a negligible effect on solvent loss from idle degreasers
(Figures 22 and 23). Figure 22 shows that solvent loss in-
creases with increasing freeboard height. When FR was increased
to 75, 100, and 125 percent on degreasers holding nonboiling MC,
the minimum increases in solvent loss were 0, 2, and 14 percent,
respectively. The maximum increases in solvent loss were about
22, 16, and 34 percent. Although these values seem to show a
significant increase in solvent loss, they are derived from the
absolute solvent loss rates for degreasers holding nonboiling
MC. These rates are magnified when translated into percentages
of solvent loss. The increase in solvent loss that accompanies
the increase in freeboard ratio can be presumed to be caused by
experimental error.
When FR was increased to 75 percent on degreasers holding
boiling MC, solvent loss was reduced by a range of 12 to 26
percent. When FR was increased to 100 percent, solvent loss was
76
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reduced by a range of 15 to 20 percent. When FR was increased
to 125 percent, solvent loss was reduced by as much as 18 per-
cent (see Figure 23).
Refrigerated Freeboard Chiller—
Data on refrigerated freeboard chillers were gathered
simultaneously from Degreaser A, which was equipped with RFC I,
and Degreaser B, equipped with RFC II. Figures 16, 17, 18, 24,
25, and 28 show the capability of the chillers to reduce solvent
loss.
RFC I operated at refrigeration temperatures of 1° to 2°C
(34° to 36°F). RFC II operated at two temperatures (before and
after the corrections noted in Section 2): -23° to -32°C (-10°
to -25°F), and -29° to -40°C (-20° to -40°F). Test data are
available on RFC I and on RFC II (at both temperatures) for
degreasers using TE and cleaning a load of 50 percent of the top
opening area; on RFC I and RFC II (at -23° to -32°C) degreasers
using TE and cleaning a load of 70 percent; and on RFC I and RFC
II (at -29° to -40°C) for degreasers using MC.
On degreasers using TE, both chillers [with RFC II at -23°
to -32°C (-10° to -25°F)] to -32°C (-10° to -25°F)] were some-
what effective in reducing solvent loss at 50 percent FR; they
had no effect at 75 percent FR, and they increased solvent loss
at 100 percent FR and above, when compared with corresponding
degreasers without RFC (Figure 16).
RFC II at -29° to -40°C (-20° to -40°F) was effective up to
75 percent FR and ineffective at 100 percent FR when compared
with the corresponding system without RFC. (See Figure 17.)
On degreasers using MC, RFC I increased solvent loss and
RFC II at -29° to -40°C (-20° to -40°F) decreased solvent loss
to levels lower than those with no RFC (Figure 28). RFC I
increased solvent loss by 15 percent at 50 percent FR, by 15 to
23 percent at 75 percent FR, and by zero percent at 125 percent
FR; RFC II at -29° to -40°C (-20° to -40°F) decreased solvent
loss by 16 percent at 50 percent FR, by 30 to 35 percent at 75
percent FR, and by 50 percent at 125 percent FR.
On degreasers using TE and a load area of 70 percent, both
chillers [with RFC II at -23° to -32°C (-10° to -25°F)] proved
effective (Figure 18). The RFC I reduced solvent loss by 34 to
37 percent at 125 percent FR; RFC II reduced solvent loss by 18
percent at 50 percent FR and by 30 to 33 percent at 125 percent
FR.
77
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On idle degreasers holding nonboiling MC, both chillers
proved ineffective. RFC I increased solvent loss by 5 percent
at 50 percent FR and by 4 to 27 percent at 75 percent FR; it
decreased solvent loss by negligible amounts to 15 percent at
100 percent FR. RFC II [at -29° to -40°C (-20° to -40°F)]
increased solvent loss by 135 percent at 50 percent FR, 60 to
100 percent at 75 percent FR, and 50 to 70 percent at 100 per-
cent FR (Figure 24).
On an idle degreaser holding boiling MC, RFC I was inef-
fective and RFC II was effective. RFC I increased solvent loss
by 43 percent at 50 percent FR and decreased solvent loss by 28
percent at 100 FR when compared with an idle degreaser at 50
percent FR and no chiller. RFC II decreased solvent loss by 37
percent at 50 percent FR and by 54 percent at 100 percent FR
when compared with an idle degreaser at 50 percent FR and no
chiller (Figure 25).
Load Cross-Sectional Area—
Results of tests varying the load cross-sectional area are
displayed in Figures 12, 13, and 27. When the load area was
increased from 50 to 70 percent ratio in degreasers using TE and
operating at a hoist speed of 0.04 m/s (8 ft/min), solvent loss
increased by 6 to 25 percent at 50 percent FR, by 10 to 70
percent at 75 percent FR, and by 80 to 100 percent at 100 per-
cent FR (Figure 12). The latter two results were obtained by
interpolation.
When the load area was increased from 50 to 70 percent in
degreasers using TE and operating at 0.08 m/s (16 ft/min),
solvent loss increased by 35 percent at 50 percent FR, 81 per-
cent at 75 percent FR (by interpolation), 46 percent at 100
percent FR (by interpolation), and 33 percent at 125 percent FR
(Figure 13). The corresponding increases in solvent loss when
MC was used in an operating degreaser at 0.04 m/s (8 ft/min)
were 55 percent at 50 FR, 54 to 75 percent (by interpolation) at
75 percent FR, 39 to 47 percent (by interpolation) at 100 FR,
and 21 to 25 percent at 125 FR (Figure 27).
Hoist Speed—
Tests were run at hoist speeds of both 0.04 and 0.08 m/s (8
and 16 ft/min) on degreasers using TE (Figures 14 and 15). The
higher hoist speed increased solvent loss at all freeboard
ratios except 75 percent FR, where no difference was observed.
The overall test data, however, indicated that increased free-
board ratio reduced solvent loss under all conditions. The data
point at 75 FR may thus have been influenced by some unknown
error. The increase in hoist speed increased solvent loss by 11
percent when the degreaser had 50 percent FR and by 64 to 94
percent when the degreaser had 100 percent FR (Figure 14).
78
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The results were different when the degreasers tested had a
load area of 70 percent. The increase in hoist speed increased
solvent loss by 22 percent when the degreaser had 50 percent FR;
however, no difference could be observed between the rates of
solvent loss at the two speeds when the degreaser had 125 per-
cent FR (Figure 15).
Crosscurrent Air Velocity—
Figures 29 and 30 present the data on the effects of in-
creased crosscurrent air velocities on idle and operating
degreasers. The data were collected from tests on Degreaser B
using MC. The air velocity across the degreaser width was
increased by a fan suspended from the ceiling that blew air
across the top of the degreaser.
Although the operating degreaser had more solvent loss in
calm air than the idle degreaser holding boiling MC, it had less
than the corresponding idle degreaser at increased air velo-
cities. At velocities of calm air (0.1 m/s or 20 ft/min) and of
0.26 m/s (52 ft/min), the operating degreaser had about 100
percent more and 50 percent less emissions, respectively, than
the corresponding idle degreaser holding boiling MC (Figure 30).
At an air velocity of 0.26 m/s (52 ft/min), the idle de-
greaser holding boiling MC at 75 percent FR had a solvent loss
reduction of about 45 percent compared to the loss at 50 percent
FR all other conditions being the same. Comparisons were also
made between calm air of 0.1 m/s (20 ft/min) and air moving at
0.26 m/s (52 ft/min). When the velocity was increased, the idle
degreaser had an increase in solvent loss of about 600 percent
at 50 percent FR and of more than 300 percent at 75 percent FR
(Figure 29).
When the air velocity was increased from calm air to 0.43
m/s (84 ft/min), solvent loss from the idle degreaser holding
nonboiling MC increased more than ten times (Figure 30).
Lip Exhaust—
The lip exhaust modification was tested by installing a
system on Degreaser A. Because the data on solvent loss repre-
sent the total that is lost through the exhaust system and from
the degreaser top opening, definite conclusions cannot be drawn
about loss through the exhaust system alone. Comparisons can be
made, however, between the effects of lip exhaust on operating
and on idle degreasers.
Figure 31 presents the test results. The three data points
at the lip exhaust rate of zero correspond to the degreaser with
no exhaust system in use; all other data points correspond to
the degreaser with the exhaust system on. When compared with a
79
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degreaser without the modification, an operating degreaser with
lip exhaust had a rate of solvent loss about 110 percent higher
at 0.25 m3/s per m2 (50 ft3/min per ft2), and 150 percent higher
at 0.50 m3/s per m2 (100 ft3/min per ft2).
At an exhaust rate of 0.25 m3/s per m2 (50 ft3/min per
ft2), the operating degreaser had about 20 percent higher sol-
vent loss (by interpolation) than the idle degreaser; at 0.50
m3/s per m2 (100 ft3/min per ft2), it had about 16 percent less
solvent loss than the idle degreaser at the corresponding ex-
haust rate.
Solvent loss from the idle degreaser with the exhaust
system was less at 75 percent FR than at 50 percent FR. At a
lip exhaust rate of 0.25 m3/s per m2 (50 ft3/min per ft2), the
idle degreaser at 75 percent FR had about 55 percent less sol-
vent loss than at 50 percent FR; it also had about 55 percent
less solvent loss than the degreaser operating at 50 percent FR.
At both 50 and 75 percent FR, solvent loss from the idle
degreasers increased by 25 percent when the lip exhaust rate was
increased from 0.25 to 0.50 m3/s per m2 (50 to 100 ft3/min per
ft2).
Degreaser Size—
Solvent loss rates from a small and a large degreaser were
compared. Both the larger degreaser (Degreaser A) and the
smaller one (Degreaser C) used TE solvent in the test.
The data show that solvent loss from the large degreaser,
which had a 1.39 m2 (15 ft2) top opening area, was about 300 to
400 percent greater than from the small degreaser, which had a
0.35 m2 (3.78 ft2) top opening area. Solvent loss per unit area
from the large degreaser, however, was 28 to 35 percent greater
than that loss from the small degreaser (Figure 19).
Measurement of Vapor Level Drop
It is difficult to measure the vapor level drop in the
degreaser during load cleaning, but crude measurements were made
from time to time. Table 28 presents relative data for esti-
mated average vapor level drop as the basket descended into the
degreaser.
80
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TABLE 28. OBSERVED VAPOR LEVEL DATA
Item
Degreaser A or
Degreaser B
Degreaser C
Basket height, cm (in.)
Load height in the basket, cm (in.)
Vapor zone height, cm (in.)
Position of the top of the basket
during degreasing
Total vapor drop level during
degreasing, using 1,1,1-tri-
chloroethane, cm (in.)
Vapor recovery time, min
31 (12)
15 to 20 (6 to 8)
76 (30)
Top goes 9 cm (3-1/2
in.) below the ini-
tial vapor level
25 (10)
1-1/2
14 (5-1/2)
10 (4)
51 (20)
Top goes 22 cm
(8-1/2 in.) be-
low the initial
vapor level
25 (10)
1-1/3
Table 29 presents calculated (theoretical) vapor level drop
data for the degreasers. When a cold load was lowered into a
vapor zone, the level of that zone dropped along with the load.
The observed vapor level drop for the degreasers using TE was
less than the calculated rate.
The discrepancy between the theoretical and the observed
vapor level drop can be explained by assuming that, in the
theoretical case, the load is descended into a degreaser with
solvent vapor up to the vapor level and no further solvent vapor
is generated. In the actual case, however, solvent vaporization
and condensation were continuous. As a result, the theoretical
vapor level drop calculations, which are based on load heat
requirements and definite vapor heat content in the degreaser,
may differ from the observed vapor level drop.
Table 30 presents solvent restoration (boilup) rate calcu-
lations .
Water Accumulation
Water that enters the degreaser system is collected by a
water separator. Water can enter the degreaser system in
several ways: condensation on the degreaser interior, including
icing on refrigerated freeboard chiller coils and the trough
beneath the coils when the chiller is on; and water brought in
with the solvent (minute amounts of water may enter solvent
81
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TABLE 29. VAPOR LEVEL DROP CALCULATIONS
Item
Hoist speed, m/s (ft/min)
Heat input at 100% capacity,
kW
kcal/min (Btu/min)
Load input per cycle (exclud-
ing basket weight), kg (Ib)
Solvent boiling point, °C (°F)
Vapor density, kg/m3 (lb/ft3)
Volume of solvent vapor,
m3 (ft3)
Weight of solvent vapor,
kg (Ib)
Latent heat content of solvent
vapor, cal/g (Btu/lb)
Total heat in vapor zone,
cal/cm (Btu/in. )
Heat of condensate,c kcal
(Btu) per cycle
Calculated vapor drop height,
cm (in. ) per cycle
Degreasers A
and B using
1,1,1-tri-
chloroethane
0.04 (8)
24
344 (1365)
45.4 (100)
74 (165)
0.45 (0.28)
1.08 (38)a
4.81 (10.6)
57 (102)
3572 (36.0)
244 (968)
68.6 (27.0)
Degreasers A
and B using
methyl ene
chloride
0.04 (8)
12
172 (683)
45.4 (100)
39 (103)
0.30 (0.187)
1.08 (38)a
3.23 (7.11)
78 (141)
3313 (33.4)
72 (286)
22.9 (8.6)
Degreaser C
using 1,1,1-
trichloroethane
0.04 (8)
8.5
122 (484)
10.4 (23)
74 (165)
0.45 (0.28)
0.08 (2.77)b
0.352 (0.776)
57 (102)
655 (6.60)
56 (223)
93.0 (33.7)
Based on degreaser vapor level dimensions of 86.4 cm by 162.6 cm by 76.2
cm (34 in. by 64 in. by 30 in.).
Based on degreaser vapor level dimensions of 63.5 cm by 40.6 cm by 30.5
cm (25 in. by 10 in. by 12 in.).
c Based on ambient temperature of 25°C (77°F) and heat capacity of 0.11
cal/g per °C (0.11 Btu/lb per °F) for the load.
82
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TABLE 30. SOLVENT RESTORATION (BOILUP) RATE CALCULATIONS
Data
Molecular weight
Liquid density, kg/1 (Ib/gal)
Specific heat, cal/g per °C
(Btu/lb per °F)
Latent heat, cal/g (Btu/lb)
Solvent vapor, kg/h (Ib/h) per kW
input
Total solvent vapor generation
rate, kg/h (Ib/h)
Volume of solvent vapor,
generated, m /min (ft /min)
Height of solvent vapor
generated, cm/mi n (in. /min)
1,1,1-Trichloroethane
133.42
1.3 (10.84)a
0.266
58 (104)
15.18 (33.46)C
364 (803)d
1.19 (42)
84 (33)
Methyl ene chloride
85
82.81b
0.276
78 (141)
10.98 (24.21)
132 (291)e
0.65 (23)
46 (18)
a At 25°C (77°F) ambient temperature.
b At 20°C (68°F).
c Assuming radiation losses equal to solvent specific heat.
d At 24 kW input.
e At 12 kW input.
For a cross-sectional area of 86 cm by 163 cm (34 in. by 64 in.).
83
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storage from the atmosphere and other sources). Water also
condenses on the outside of the degreaser walls when the chiller
is on, but this water does not enter the water separator.
Several precautions were taken during the tests to monitor
water accumulation and to eliminate its effect on solvent loss
readings. When the degreaser had not been used for a long time,
after solvent changeover, or when an unknown quantity of water
had entered the system, the degreaser was run at idle with the
solvent boiling for 16 hours or overnight for the purpose of
moving the water into the water separator. Water separators
were also emptied before and after each test. Samples of reser-
voir solvent were checked thoroughly before many tests to ensure
that water was not being retained in the degreaser.
During the test program, water was occasionally found and
removed from the water separators immediately after solvent
changeover and degreaser startup. With one exception, no water
accumulated in either degreaser during tests with and without
the use of refrigerated freeboard chiller, although frosting of
chiller coils was observed on Degreaser B during tests of
refrigerated freeboard chiller. No evidence of water content
was found in the frost. Representatives of the manufacturers of
the test degreasers observed test operation and indicated that
the lack of water in the separators was not unusual.
The exception occurred during two tests with RFC II operat-
ing at -29° to -40° C (-20° to -40°F). Ice accumulated on the
trough below the chiller coils for Degreaser B when using TE.
Before these tests, similar tests were conducted with MC and no
ice buildup was observed anywhere in the degreaser. All the ice
that accumulated during the two TE tests was condensed at the
end of the tests by turning off the water supply to the primary
condenser and allowing hot vapors to rise up in the degreaser.
(The ice did not melt during the defrost cycle because of the
cold temperature of the coils.) The water that collected in the
water separator after this procedure was negligible in compari-
son with hourly solvent loss.
84
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SECTION 4
ECONOMIC EVALUATIONS
The economic impact of selected degreaser modifications is
discussed in this section. Because the solvent loss capability
of a modification is not proportional to its cost, no direct
relationship exists between evaluation of solvent loss reduction
capability and economic benefit. (It is possible that a modifi-
cation that is less efficient in reducing solvent loss may prove
to be more cost-effective.)
METHODOLOGY
The typical degreaser, which is the base case for the
evaluation, has a 50 percent freeboard ratio, uses a 50 percent
load area and has no refrigerated freeboard chiller. The mod-
ifications evaluated are freeboard ratio, refrigerated freeboard
chiller, load area, hoist speed, lip exhaust, crosscurrent air
velocity, and lid. Several of these—hoist speed, load size,
crosscurrent air velocity—are operational practices rather than
actual modifications. They have a considerable effect on sol-
vent loss and thus on degreaser economics.
The modifications are evaluated economically on the basis
of the additional costs they bring to degreaser operation. The
capital costs and those of operation and maintenance are con-
sidered.
These costs are different for new and for retrofit instal-
lations. A new installation is one in which the modification is
built into the degreaser at the factory. A retrofit is added at
a later time on the site. This report presents cost evaluations
for both new and retrofit installations of degreaser modifica-
tions. All the costs are given in 1979 dollars.
COST ELEMENTS
Capital Cost
The capital cost of a modification includes purchase price,
installation, engineering, and startup. Freight is considered
as part of the purchase price.
85
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Annual Operating Costs
Annual operating costs are the total of fixed charges
(capital charges, insurance, and maintenance) and direct oper-
ating costs. Direct operating costs include the costs of main-
tenance, labor, replacement parts, utilities that are incurred
because of the modification, and credits from the savings in the
solvent loss over the base case.
Annual capital charges are calculated using a 10 percent
interest rate and a 12 year equipment life. Estimate of equip-
ment life is based on conversations with manufacturers. The
capital charges are equivalent to 14.676 percent of the total
capital cost. Insurance and taxes are estimated at 4 percent of
the capital cost; maintenance and labor, at 2 percent. Costs of
replacement parts are based on information supplied by the
manufacturers. Utility costs are based on $0.04 per kWh.
Capital and Operating Costs of Various Modifications
A brief description of the cost of each modification (i.e.,
the cost as it exceeds that for a base case degreaser) is given
in Appendix D.
Refrigerator Freeboard Chiller—
Cost estimates for refrigerated freeboard chillers are
based on information from the manufacturers of the test
degreaser units. RFC I has a refrigeration system that includes
a 1.12 kW (IH-hp) compressor. According to the manufacturer,
the size of the chiller is based on the solvent used. Fifty
percent more refrigeration is needed for new or retrofit instal-
lations of RFC II on degreasers using MC than on degreasers
using TE. In the latter case, a 0.75 kW (1-hp) compressor is
sufficient.
The capital cost of a refrigerated freeboard chiller in a
new installation is limited to the price of the factory-
installed chiller. The capital cost of a retrofit chiller also
covers installation, including refrigeration, electrical
plumbing (if water cooled), and mechanical connection.
The primary operating cost of a chiller is that of the
additional utilities. These costs are based on energy-use data
accumulated during testing, and assume a rate of $0.04/kWh and
8000 h/yr operation (regardless of the number of shifts of
degreaser operation).
RFC I (operating at temperatures above freezing) installed
at the factory on a new degreaser costs $3300 above the cost of
86
-------
the degreaser. A similar retrofit unit costs $4000. Annual
utility costs are $223 for both new and retrofit units. An RFC
II (operating at temperatures below freezing) costs $3717 when
installed at the factory. A similar retrofit unit costs $7340.
Annual utility costs are estimated at $341 for both new and
retrofit units.
The cost of RFC II is based on a 1.12 kW (IVhp) compres-
sor. Replacement parts are assumed to be the same as that of
the degreaser.
Additional operating and maintenance costs depend upon the
condenser type, whether air cooled or water cooled; they are
also negligible. Air-cooled condensers usually cost less than
water-cooled units. Water-cooled units need virtually no main-
tenance; at the most, dirt may accumulate on the condenser tubes
and need to be chemically removed once a year. Air-cooled
condensers require air blowing for cleaning purposes about every
two months. Total maintenance of a secondary freeboard chiller
may amount to 8 man-hours per year.
Load Area (Oversized Basket) —
The typical cross-sectional area is a 50 percent ratio of
load to degreaser top opening. A 70 percent ratio, which allows
a heavier load, is not common. Loads are usually placed in a
basket for easy movement into and out of the degreaser. The
load cross-sectional area can be defined as the size of the
basket in which the load is placed. In the test program, two
baskets, sized at 50 and 70 percent ratios of load to degreaser
top, were used, and the same load was placed in both. The equal
weights used in the tests should be considered when evaluating
the economic and solvent loss data in the report.
The capital cost of the modification is limited to the
purchase of a new basket. A basket that is 70 percent of the
size of the degreaser top open area costs about $242. A hot dip
galvanized basket that is 50 percent of this area costs about
$164. Installation costs are negligible. A retrofit installa-
tion of a basket sized at 70 percent requires the purchase of a
new basket and retirement of the basket sized at 50 percent,
with no salvage value. No installation, engineering, startup,
replacement parts, or utilities are required. The additional
cost of a new basket sized at 70 percent is thus equal to the
difference in the price of the baskets, or $78. The calculation
is based on the assumption that a choice is made between the two
options when a new degreaser is ordered, and only the cost
differential can be charged to the modification.
Hoist Speed —
The capital cost of modifying the hoist speed on a new
degreaser installation is an estimated premium of $50 for a
87
-------
hoist with a chain speed of 0.08 m/s (16 ft/min) versus one with
a chain speed of 0.04 m/s (8 ft/min). In a retrofit modifica-
tion, the cost includes the purchase and installation of a new
hoist and scrapping of the old hoist. The cost is $609 for the
hoist and $120 for the installation; engineering and startup
costs are estimated to be zero.
Annual utility costs are estimated to be the same for a
hoist speed of 0.08 m/s (16 ft/min) and one of 0.04 m/s (8
ft/min); therefore, no additional utility charges are added to
the modification costs. Replacement parts are also estimated to
be zero.
During the tests, the number of cycles was held the same
for both the 0.04- and 0.08-m/s (8- and 16-ft/min) hoist speeds.
As a result, the number of loads did not change when the hoist
speed did. It can be estimated, however, that 2 minutes can be
saved per 6.5-minute cycle by using an 0.08-m/s (16-ft/min)
hoist speed. The potential increase in work capacity is 31
percent, but the solvent loss also increases with the number of
cycles per hour.
Lip Exhaust—
The capital cost of a lip exhaust system includes the lip
exhaust manifold, exhaust fan, connecting ductwork, and exterior
outlet. Installation, engineering, and startup costs are addi-
tional for a retrofit modification. Annual operating costs
include electricity to operate the fan. According to season,
the makeup air exhausted from the fan must be heated or cooled
to maintain comfortable working conditions, however, an air-
conditioned shop is unlikely.
The cost of the lip exhaust system is $1330, and the esti-
mated installation cost is $90. Engineering and startup costs
are estimated at zero. Annual electricity expenses are about
$60, and the cost of heating the load (based on use of natural
gas) is about $343. Both of these costs assume an operating
schedule of one shift per day. Costs for replacement parts are
considered negligible.
The main function of the lip exhaust is to segregate the
solvent loss emissions from the degreaser by routing them to
connecting equipment or to the atmosphere. In this study, no
efforts were made to measure the rate of solvent loss through
the exhaust system. No economic evaluation of lip exhaust was
made from the data.
Crosscurrent Air Velocity—
Increased crosscurrent air velocities involve no additional
capital costs. The only additional annual cost is from the
solvent that is lost per year.
88
-------
Lid—
Because the lid is an integral part of a standard
degreaser, it involves no additional capital costs.
ECONOMIC SUMMARY
The economic evaluations of the modifications tested are
summarized in tabular form in Appendix D. These evaluations
include data on capital and annual operating costs, net profit
(or loss), ratio of savings to cost, payback period, and capac-
ity lost because of the modification. Idle degreasers cannot be
compared with the base case and as a result they are excluded
from the evaluations. Three schedules for using the degreasers
are considered: one, two, or three shifts per day (2000, 4000,
or 6000 h/yr).
Degreaser utilization has a significant impact on the
evaluations. All the manufacturers agree that degreaser life is
unaffected by using it for more than one shift a day. Conse-
quently, the credit (or expenditure) resulting from solvent
savings (or loss) is increased twofold and threefold when the
degreaser is operated 4000 and 6000 hours per year instead of
2000 hours; however, the annual operating costs (capital
charges, insurance and taxes, maintenance and labor) remain the
same. In other words, the effectiveness (savings or expendi-
ture) of a given modification is multiplied as the degreaser is
used more. A degreaser with a given modification that operates
2000 hours per year and has a minimum solvent savings rate is
least profitable (or expensive); while the degreaser with the
same modification that operates 6000 hours per year and has a
maximum solvent savings rate is most profitable (or expensive).
For some of the modifications, special attention should be
paid to aspects of their operation that affect the savings or
expenditures. In an actual degreaser operation, the large load
basket (at 70 percent ratio) is used to degrease a heavier load
per unit of time. Similarly, a faster hoist speed means shorter
cycle time (i.e., more cleaning cycles per unit of time). In
the test program, however, the load weight and the total cycle
time were held constant. For other modifications, such as
freeboard ratio and refrigerated freeboard chiller, economic
evaluations are useful.
Another key factor in the economic evaluations is whether
the installation is new or retrofitted. The credits (or expend-
itures) that are gained from solvent loss reduction (or in-
crease) are the same in both cases, whereas the annual operating
costs are always higher in retrofit installations. Consequent-
ly, a new installation of a degreaser modification is economic-
ally more effective than the corresponding retrofit installa-
tion.
89
-------
The ratio of savings to cost that is calculated in each
table has no significance except to indicate the monetary value
of the modification. Because only secondary chillers involve
any significant capital annual operating costs, the calculation
of payback period is of little importance in most cases. Where
the modifications result in a net loss, no payback period is
calculated.
The lost capacity is the difference between the load that
can be cleaned after modification and the load that can be
cleaned under base conditions. Only the modifications of free-
board ratio involve lost capacity. The increased ratio results
in a longer hoist traveling time, which in turn slows the move-
ment of the load from floor to platform to basket. The oper-
ating cycle is longer than in the base case, and less load is
thus cleaned per unit of time. The extent of this lost capacity
increases as the freeboard ratio increases, and depends also
upon the hoist speed and cycle time. The percentage of lost
capacity is expressed in the following equation:
where t = present cycle time, min
v = hoist speed, m/min (ft/min)
x = increase in freeboard, m (ft).
During the test program, the total time of the degreasing
cycle was held constant when the hoist speed changed. There-
fore, tests run at a hoist speed of 0.08 m/s (16 ft/min) show no
difference in lost capacity from those run at 0.04 m/s (8
ft/min) .
Of all the modifications evaluated, only changes in free-
board ratio show a definite economic benefit. Capital costs are
low and annual operating costs are negligible (refer to the
tables for specific values). The savings in solvent loss are
substantially greater than the expenses incurred by the modifi-
cation. Lost capacity has not been figured into the profit-
ability calculations, but this negative effect is not expected
to have a significant impact.
The other modifications have less of a capacity either to
reduce solvent loss or to do so on an economic basis.
90
-------
SECTION 5
CONCLUSIONS AND RECOMMENDATIONS
The solvent loss capabilities of the various modifications
are summarized in Tables 31 and 32. A graphic summary is shown
in Figures 32 and 33. An analysis was also made of the relative
economic benefits of the modifications. This analysis is sum-
marized in Tables 33 and 34.
The following conclusions can be derived from the data.
Under all conditions, increased freeboard ratio decreased sol-
vent loss. On idle degreasers, refrigerated freeboard chillers
either had no effect or increased solvent loss. On operating
degreasers, chillers decreased solvent loss better when operated
at lower temperatures. Load area of 70 percent increased sol-
vent loss. The rate of solvent loss was directly proportional
to the size of the degreaser top opening.
With one exception, degreaser operation under any of the
modifications (including freeboard chiller) and using TE re-
sulted in less solvent loss than the base case. (Base case or
typical degreaser operation is 50 percent FR, 50 percent load
area at 0.04 m/s or 8 ft/min hoist speed.) The exception—the
modification that resulted in more solvent loss—was operation
without RFC at either hoist speed and cleaning a 70 percent load
area; and operation without RFC at 0.08 m/s (16 ft/min) hoist
speed, 50 percent load area, and FR at or below 75 percent.
At 50 percent FR, the only degreaser operation using MC
that resulted in less solvent loss than the base case was use of
RFC at -29° to -40°C (-20° to -40°F); all other modifications
had more solvent loss. At increased FR, all modifications had
less solvent loss except operation with no RFC, a 70 percent
load area, and FR below 125 percent; and operation with RFC I,
cleaning a 70 percent load area, and FR at or below 100 percent.
For degreasers using 1,1,1-trichloroethane, the best sol-
vent loss control was achieved by any of the following modifica-
tions:
Incorporation of RFC II at -29° to -40°C (-20° to -40°F)
on degreasers with at least 75 percent FR.
91
-------
TABLE 31. EFFECT ON SOLVENT LOSS REDUCTION OF VARIOUS MODIFICATIONS TO AN
OPERATING DEGREASER USING 1,1,1-TRICHLOROETHANE
(percentage of reduction or increase over the base case )
vD
to
- . .
ratio, b
X
SO
75
100
125
Hoist speed, 0.04 m/sc
1 J e C.IW
RFC-f
Off
oa
7-25
47-53
RFC I
1° to 2°C9
5
8
34
RFC II
-23° to -32°Ch
8
18
47
-29° to -40°C1
2
46
51
•in*
RFC.
Off
(5-23)J
(3)-4
RFC I
1° to 2°C
27
RFC II
-23° to -32°C
14
34
Hoist speed, 0.08 m/s
RFC Off
Load
area-
50%
(11)
16
9
20
Load
area-
70X
(50)
(5)
Base case- FR = 50, RFC: Off, hoist speed = 0.04 m/s, load cross-sectional area = 507.
Ratio of freeboard height to degreaser width.
8 ft/min.
16 ft/min.
Ratio of load cross-sectional area to degreaser top opening
Refrigerated freeboard chiller
34° to 36°F.
-10° to -25°F.
-20° to -40°F.
Percentages in parentheses represent increases in solvent loss over the base case
-------
CO
TABLE 32. EFFECT ON SOLVENT LOSS REDUCTION OF VARIOUS MODIFICATIONS
TO AN OPERATING DEGREASER USING METHYLENE CHLORIDE AT A HOIST SPEED OF 0.04 m/sc
(percentage of decrease or Increase over the base case )
Freeboard
ratio,0
%
50
75
125
Load area:d 50%
RFC:6
Off
0
17-22
25
RFC I
L° to 2°Cf
(4)9
5
25
RFC II
-29° to -40°C9
16
46
61
Load area: 70%
RFC:
Off
(53)
9
RFC I
1° to 2°C
(39)
22
RFC II
-29° to -40°C
(5)
44
d 8 ft/min.
Base case: FR = 50, RFC: Off, hoist speed = 0.04 m/s, load cross-sectional area = 50%.
Ratio of freeboard height to degreaser width.
Ratio of load cross-sectional area to degreaser top opening.
e Refrigerated freeboard chiller.
f 34° to 36°F.
9 -20° to -40°F.
Percentages in parentheses represent increases in solvent loss over the base case.
-------
TABLE 33. ANNUAL SAVINGS RESULTING FROM MODIFICATIONS TO A DEGREASER
USING 1,1,1-TRICHLOROETHANE AND OPERATING ONLY ONE SHIFT PER DAYa«b
(1979 dollars)
Freeboard
ratio,
X
50
75
100
125
Hoist speed. 0.04 m/sc
Load area: 50Xe
f
RFC:
Off
0
51-291
629-686
RFC I
1° to 2°C9
(834)J
(778)
(590)
RFC II
-23° to -32°Ch
(997)
(1031)
(521)
-29° to -40°C1
(1082)
(523)
(260)
Load area: 70%
RFC:
Off
(87-355)
(34-133)
RFC I
1° to 2°C
(586)
RFC II
-23° to -32°C
(929)
(735)
Hoist speed. 0.08 m/sd
per. nff
Load
area:
SOX
(166)
168
56
197
Load
area:
70X
(760)
(171)
Profit due to solvent savings less the cost and operation of modification.
Lost capacity resulting from Increase In freeboard ratio not Included In analysis.
c 8 ft/mln.
d 16 ft/m1n.
e Ratio of load cross-sectional area to degreaser top opening.
Refrigerated freeboard chiller.
9 34° to 36°F.
h
1
-10° to -25°F.
-20° to -40eF.
Values 1n parentheses represent losses.
-------
TABLE 34. ANNUAL SAVINGS RESULTING FROM MODIFICATIONS TO A DEGREASER
USING METHYLENE CHLORIDE AND OPERATING ONLY ONE SHIFT PER DAY
AT A HOIST SPEED OF 0.04 m/s (8 ft/min)a
(1979 dollars)
Freeboard
ratio, b
%
50
75
125
Load area: 50%°
RFC:d
Off
0
173-186
172-289
RFC I
1° to 2°Ce
(1179)9
(887)
(733)
RFC II
-29° to -40°Cf
(902)
(522)
(354)
Load area: 70%
RFC:
Off
(535-743)
0-13
RFC I
1° to 2°C
(1310)
(759)
RFC II
-29° to -40°C
(1191)
(591)
Profit due to solvent savings less the cost and operation of modification.
Lost capacity resulting from increasing freeboard ratio not included in analyses.
Ratio of load cross-sectional area to degreaser top opening.
Refrigerated freeboard chiller.
e 34° to 36°F.
f -20° to -40°F.
9 Values in parentheses represent losses.
-------
60
50
40
** 30
to
•f
K 20
CO
to
s
10
£(20)
o
I (30)
o
V)
(40)
(50)
(60)
I
I
I
I
50% IPAQ AREA. Q.Q4-m/s HOIST SPEED
A RFC OFF
D RFC I AT 1° TO 2°C
O RFC II AT -23° TO -32°C
O RFC II AT -29° TO -40°C
70% LOAD AREA, 0.04-m/s HOIST SPEED
° RFC OFF
a RFC II AT -23° TO -32°C
OTHER
D RFC OFF, 50% LOAD AREA,
0.08-m/s HOIST SPEED
o RFC OFF, 70X LOAD AREA,
0.08-m/s HOIST SPEED
<
• INTERPOLATED DATA
DATA POINT AT 75% FR IGNORED
I
50 75 100 125
FREEBOARD RATIO, %
150
Figure 32. Summary of solvent loss reduction capabilities of
various modifications to degreaser using 1,1,1-trichloroethane.
96
-------
70
60
50
40
co
_
uj 30
co
-------
Degreaser equipped with 100 percent FR.
Incorporation of RFC II at -23° to -32°C (-10° to -25°F)
on degreasers with at least 100 percent FR.
Although all of these modifications are profitable, the use
of a degreaser equipped with 100 percent FR is economically and
technically the best control.
For degreasers using methylene chloride, the best solvent
loss control is achieved by the following modification:
Incorporation of RFC II at -29° to -40°C (-20° to -40°F)
on degreasers with 125 percent FR.
Although this modification is technically effective, it is
not economically profitable.
Caution should be used in evaluating the results of the
refrigerated freeboard chiller at -29° to -40°C because the
possible impact of high humidity has not been studied. Testing
to date has been under conditions where little or no water was
condensed on the chiller coils.
The degreaser evaluations in this study are based on tests
conducted under ideal conditions of calm air velocities within
the testroom. Further, only a limited number of variables were
tested. Future studies of degreaser systems should be directed
toward evaluations that will apply to actual degreaser opera-
tions and that will include a greater number of variables.
Recommendations follow:
Simulate all the present test conditions at higher air
velocities. The combined data will provide degreaser
evaluations for various air velocities.
Evaluate the effect of load weight on solvent loss from
operating degreasers by using different load weights.
Evaluate the effect of increased or decreased cycle time
and determine its relation to hoist speed.
Conduct tests to determine whether refrigerated freeboard
chiller temperature and blanket temperature are inter-
related.
Make accurate and continuous measurements of vapor level
drop during load cleaning in degreasers operating with
various modifications. Compare the vapor level drop obser-
vation with theoretical estimates.
98
-------
Evaluate power-operated lid.
Evaluate effect of humidity on low temperature chiller.
99
-------
APPENDIX A
REDUCTION OF TEST DATA
The raw data are given in the series of tables (A-l through
A-161) following these pages. Almost every test is represented
by two tables, one for each degreaser used. The top portion of
the table identifies the test number, date, ambient conditions,
and the degreaser and its operating parameters.* The body of
the table consists of successive readings of degreaser weights
at different test times and reduced data showing the rate of
solvent loss under given conditions.
The successive data points (or test readings) are identi-
fied by a number, starting at 1. Data points having no numbers
(which are located at the beginning and end of some of the
tables) are from readings taken during the solvent heating
period at the beginning of the test and the solvent cooling
period at the end; these readings were not considered in solvent
loss rate evaluations. Reading No. 1 represents the data point
taken after the equilibrium condition was reached. This condi-
tion was assumed to be attained when the solvent in the de-
greaser was completely boiling and a definite and stable vapor
line had been established at the top of the degreaser. Reading
No. 1 was usually taken a half hour after equilibrium was
reached. In tests of operating degreasers, hoist operation
(load cleaning) was started when Reading No. 1 was taken.
* In the tables, freeboard ratio (FR) is represented by FB;
refrigerated freeboard chiller (RFC) is represented by SC.
100
-------
The items presented in the table are explained below:
T: Time (in minutes) when the degreaser was weighed.
W: Total weight (in pounds) of the degreaser, as measured
by the two separate scales for each degreaser. All
the weighings were made when the load was out of the
degreaser.
AT: Difference between the successive T readings, con-
verted to hours.
AW: Difference between the successive W readings, in
pounds .
I AT: Cumulative time difference (i.e., difference between
the corresponding T reading and the first T reading),
converted to hours.
ZAW: Cumulative weight loss (i.e., difference between the
corresponding W reading and the first W reading).
These values are all given as negative numbers, which
represent the cumulative decrease in the weight.
AW
Solvent loss between successive readings, expressed
as pounds per hour.
ZAW
Cumulative solvent loss, expressed as pounds per hour.
Average of successive cumulative weight loss rates
ZAW
( )' expressed as pounds per hour.
For each test, the solvent loss rate from each degreaser is
estimated by relating the cumulative solvent loss (ZAW), which
is a dependent variable, with the cumulative time (ZAT), which
is an independent variable. The relationship is given by a
simple regression equation:
(ZAW) = a + b (ZAT) (Eg. A-l)
Coefficients a and b are evaluated by using the least
squares method, which minimize the square of the difference
between the predicted value and the experimental value of the
dependent variable. Once the coefficients have been determined,
they can be used in Equation A-l to calculate the total solvent
loss in a given amount of time. Because Reading No. 1 is always
101
-------
the starting point (i.e., ZAW and IAT are zero at that reading),
a plot of ZAWs vs. ZATs theoretically should pass through the
origin (i.e., intercept a should be zero). The value of coef-
ficient a is negligible, and it has been omitted from the cal-
culations. Coefficient b of the regression equation was thus
used as the solvent loss rate under the given conditions. This
coefficient is the crucial element that has been used for the
degreaser evaluation.
Confidence intervals were calculated at 95 percent to
obtain an indication of the accuracy of b. These interval
estimates are a range of values that can be expected to include
the correct value up to 95 percent of the time, which is a
measure of the error involved in the estimate.
The confidence interval for the solvent loss rate at b, and
the other terms for obtaining it, are presented on the last
sheet of each table. An explanation of the items follows:
n: The number of data points used in the analysis.
Slope: The coefficient b of the regression equation. (The
slope is a positive value. It is shown here as a
negative number because the test readings were given
as decreases in total degreaser weight.)
Inter- The coefficient a of the regression equation. (When
cept: this value appears in a table as a negative number,
the actual value is positive, and vice versa. The
reason for this reversal was noted in the preceding
item. )
S : The standard deviation of the dependent variable ZAW
yx for a fixed ZAT.
Svv = [(Z(ZAW)2-aZ(ZAW)-bZ(ZAW)(ZAT))/n-2]*s (Eq. A-2)
JrA
S : The standard deviation of ZAT.
4t
Sx = UnZUAxJMKlAT))2]/,^} (Eq. A.3)
yx
S : S = - (Eq. A-4)
Sx
102
-------
S.: The S. term that is calculated here is of no use for
estimating the confidence interval. (The term is
designed to estimate the confidence interval for b.)
b • E
s • + -* (Eq' A'
AW
SG: The standard deviation of .
t /2 : Value of Student 't1 for n-2 degrees of freedom at
95 percent confidence levels.
r: The correlation coefficient. The r value is also a
positive number.
. Z(ZAW)(ZAT)
r ~ [Z(ZAW)*][
CI: The confidence interval (CI) is given in the
following equation:
CI = slope b + tQ/2 Sfl (Eg. A-7)
The correlation coefficient (r) is a measure of the degree
of closeness of the linear relationship between the two varia-
bles. The r is a pure number, it has no dimensions, and it
always falls between -1 and +1. Positive values of r indicate a
tendency of the dependent variable ZAW and independent variable
ZAT to increase together. Negative values of r indicate the
association of large values of ZAW with small values of ZAT. A
perfect correlation is indicated by r = 1.
103
-------
TABLE AJ SUMMARY OF DATA FROM TEST NO. 1-A.
Page ; of _4_
Degreaser A, operating
Solvent: 1,1,1-THchloroethane
Inlet air
Other
PC * SC
Exhaust air x
A 50 »
8 TTTmin
Date 10/10/78
Ambient afr
Temperature 61 *F
Pressure25.67^"* Hg
Humidity aa*
Reading
No.
T, mln
IT. 1b
AT, h
AW, 1b
CAT, h
CAW, 1b
(S). ™
(far). lb'h
X, Ib/h
85. 000
3601.900
100.000
3613. 100
1.
166.000
3615.300
2.
222. 000
3613.700
0. 933
-1.600
0. 933
-1.600
-1.714
-1.714
-1.714
3.
272. 000
3612. 100
0. 833
-1.600
1.767
-3. 200
-1.920
-1.811
-1.76C:
4.
340. 000
3609. 500
1. 133
-2. 600
2. 900
-5. 800
-2. 294
-2. 000
-1. S4i:
-------
TABLE A-1. (continued)
Page 2 of 4
Reading
No.
T. «in
U, 1b
AT. h
AM. 1b
IAT. h
CAM. 1b
00. """
(fir). 1b/h
X. 1b/h
5.
391.000
3608. 200
0. 850
-1.300
3. 750
-7. 100
-1.52?
-1.893
-1.855
6.
456. 000
3605. 500
,.03,
-2. 700
4. 833
-9. 800
-2. 492:
-2. 02?:
-1.8S?
7.
515.000
3602. 900
0. 983
-2. 600
5.817
-12.400
-2. 644
-2. 132:
-1.930
8.
573. 000
3600. 600
0. 967
-2. 300
6. 783
-14.700
-2. 379
-2. 167
-1.961
9.
664. 000
3597. 200
1.517
-3. 400
8. 300
-18. 100
-2. 242:
-2. 18J
-1.99J
10.
695. 000
3595. 900
0.517
-1.300
8.817
-19.400
-2. 516
-2. 200
-2.014
M
O
in
(continued)
-------
TABLE A-1. (continued)
Page 3 of V
Reading
No.
T. Bin
U. lb
AT. h
AW. lb
CAT. h
CAM. lb
($). "">
A*A lb/h
\IA y.
X. lb/h
11.
755. 000
3592. 700
1.000
-3. 200
9.817
-22. 600
-3. 200
-2. 302:
-2. 043
•
12.
814.000
3590. 500
0. 933
-2. 200
10.800
-24. 800
-2. 237
-2. 296
-2. 066
13.
835. 000
3588. 000
1. 183
-2. 500
11.983
-27. 300
-2. 113
-2. 276:
-2. 03<
14.
931.000
3585. 500
0. 767
-2. 500
12.750
-29. 800
-3.261
-2. 337
-2. 103
15.
1004.000
3582. 300
1.217
-3. 200
13.967
-33. 000
-2. 630
-2. 363
-2. 122:
16.
1068.000
3579. 500
1.067
-2. 800
15.033
-35. 800
-2. 625
-2.381
-2. 139
M
O
(continued)
-------
TABLE A-1_. (continued)
Page JL of _L
Reading
No.
T. «1n
H. Ib
AT. h
AH. Ib
CAT. h
ZAU. Ib
(*\ Ib/h
1 77 1 iD/n
\AT/.
(or). 1b/h
X. 1b/h
17.
1112.000
3577. 200
0. 733
-2. 300
15.767
-38. 100
-3. 136
-2.416
-2. 156
18.
1171.000
3574. 900
0. 983
-2. 300
16.750
-40. 400
-2. 339
-2. 4K:
-2. 17J
19.
1230.000
3572. 500
0. 983
-2. 400
17.733
-42. 800
-2.441
-2. 4K
-2. 18S
20.
1260.000
3570. 600
0. 500
-1.900
18.233
-44. 700
-3. 800
-2. 45?
-2. 19?
1263.000
3551.900
n 19
Slope -2.509
Intercept 1.955
0.591
5.565
0.02B
0.226
2.110
r -0.999
Confidence Interval
2.509 + 0.053
Sc 0.552
-------
TABLE A-2. SUMMARY OF DATA FROM TEST NO. 1-A
Page j_ of 4
Degreaser B. operating
Solvent: 1,1,1-THchloroethane
Date 10/10/78
FB 50 I
Inlet air
Other
PC x SC
Exhaust air x
A 50 i
V 8 ft/min
Ambient air
Temperature 61 *F
Pressure 29.67 ^n. Hq
Humidity ~~~
Reading
No.
T, win
N, Ib
AT. h
AN. Ib
CAT, h
CAN. Ib
(S), '*
(8ft »"
X, Ib/h
90.
2758. C:
100.
2774. 1
1.
165.000
2767. 100
•
2.
226. 000
2764. 100
1.017
-3. 000
1.017
-3. 000
-2.951
-2.951
-2.951
3.
294. 000
2760. 500
1. 133
-3. 600
2. 150
-6. 600
-3. 176
-3. 070
-3.010
4.
346. 000
2759. 300
0. 867
-1.200
3.017
-7. 800
-1.385
-2. 58t
1 -2. 869
o
09.
-------
TABLE A-2. (continued)
Page J_ of _4_
Reading
No.
T. ofn
M. 1b
AT. h
AM. 1b
CAT. h
CAM. Ib
(^ IK/h
IT?) ID/I)
VAT/.
(Mr). lb/h
X, lb/h
5.
413.000
2756. 000
1. 117
-3. 300
4. 133
-11. 100
-2. 955
-2. 685
-2. 823
6.
466. 000
2753. 800
0. 883
-2. 200
5.017
-13.300
-2.491
-2.651
-2. 789
r .
525. 000
2751.700
0. 983
-2. 100
6. 000
-15.400
-2. 136
-2. 567
-2. 752:
8.
584. 000
2750. 500
0. 983
-1.200
6. 933
-16.600
-1.220
-2. 377
-2. 69?:
9.
650. 000
2743. 700
1. 100
-1.800
8. 083
-18.400
-1.636
-2. 276
-2. 645
10.
701.000
2746. 700
0. 850
-2. 000
8. 933
-20. 400
-2. 353
-2. 284
-2. 605
o
VD
(continued)
-------
TABLE A-a (continued)
Page JL of 1_
Reading
No.
T. «in
U. Ib
AT. h
AV. Ib
EAT. h
EAM. Ib
(SO. ""•
(8ft ""•
I. Ib/h
11.
765. 000
2743. 700
1.067
-3.000
10.000
-23.400
-2. SK-
-2. 340
-2. 57?'
12.
825. 000
2744. 000
1.000
0. 300
1 1 . 000
-2.3. 100
0. 300
-2. 100
-2*. 5 35
13.
883.000
2740.500
0. 967
-3.500
1 1 . 967
-26. 600
-3.621
-2. 22:-:
-2. 509
14.
946. 000
2738. 400
1.050
2. 100
13.017
28. 700
2. 000
2.205
2.496
15.
1006.000
2738.000
2. 000
-0. 400
14.017
-29. 100
-0. 200
-2. 076
-2. 470
16.
1078.000
2733. 500
1.200
-4. 500
15.217
-33. 600
-3. 750
-2. 20?:
-2. 452
(continued)
-------
TABLE A^. (continued)
Page 4 of 4
Reading
No.
T. Bin
U. 1b
AT. h
AU. 1b
CAT. h
CAM. Ib
(*"} Ih/h
iTrJ to/a
\AT/,
GAT). 1b/h
X. 1b/h
17.
1123.000
2731.600
0. 750
-1.900
15.967
-35. 500
-2. 533
-2. 22C:
-2. 43?:
18.
1195.000
2728. 000
1.200
-3. 600
17. 167
-39. 100
-3. 000
-2. 27?:
-2. 42?:
19.
1254.000
2725. 600
0. 98':
-2. 400
18. 150
-41.500
-2.441
-2. 287
-2.421
20.
1304.000
2725. 500
0. 833
-0. 100
18. 983
-41.600
-0. 120
-2. 191
-2. 40?:
21.
1364.000
2723. 200
1.000
-2. 300
19.983
-43. 900
-2. 300
-2. 197
-2. 39?:
22.
1422. 000
2721.000
0. 967
-2. 200
20. 950
-46. 100
-2. 276
-2. 200
-2. 38?:
n 21
Slope -2.113
Intercept -1.671
s
s
0.921
6.200
0.033
U.206
2-093
r +1.000
Confidence interval
2.113 + 0.069
-------
TABLE A-3 SUMMARY OF DATA FROM TEST NO. 2
Page i of
Degreaser A, Idle
Solvent: 1,1,1-THchloroethane
(Boiling ; nonboiling _x )
FB 5n •1 PC SC
Inlet"1 air Exhaust air
Other
Lid closed
A
V 0
ft/mil
min
Date 10/12/78
Amb 1 enTair'
Temperature 71 *F
Pressure 29.7.1'
Humidity 70 7.
Reading
No.
T, m1n
", 1b
flT, h
AW. 1b
IftT, h
ZAV, lb
W Ih/S
i TT 1 lo/n
\Ai/»
(w). 1b/h
X. Ib/h
1.
0. 000
3590. 000
2.
940. 000
3533. 500
15.667'
-1.500
15.667
-1.500
-0. 09*.
-0. 09*.
-0. 09*.
•
-------
TABLE A-4 SUMMARY OF DATA FROM TEST NO. 2
Page i of
Degreaser B* Idle
Solvent: 1,1,1-THchloroethane
(Boiling ; nonboilinq x )
FB 50 I PC SC
Inlet atr Exhaust air
Other
Lid closed
A _0_I
V 0 ft/mln
Date 10/12/78
Ambient afr
Temperature 71 °F
Pressure 29.73 in. Hg
Humidity 7Q' _i
Reading
No.
T, win
M. 1b
•
•
•
AT. h
AW. 1b
tAT, h
EAH. 1b
(S), ™
(M?). iw
X, ib/h
i.
0. 000
2486. 700
2.
?40. 000
2485. 200
15.667
-1.500
15.667
-1.500
-0. 096
-0. 0?*.
-0. 09t.
-------
TABLE A-5 SUMMARY OF DATA FROM TEST NO. 3
Page j of
Degreaser A, Idle
Solvent: 1,1,1-THchloroethane
(Boiling
FB 50 l
Inlet air
Other
__; nonboiling x_)
PC _^_ SC
Exhaust air
0 %
mln
Date 10/16/78
AmbientaTr.
Temperature _ 60 °F
Pressure ?g.jTfiJn. Hg
Humidity R? "X
Reading
No.
T, m1n
N, Ib
AT, h
AN, Ib
EAT, h
IAN, Ib
(A^f %
OW • • •_ xfv
(i?i ""-
X. Ib/h
1.
0. 000
3580. 500
o.
1310.000
3576. 600
21.83;:
-3. 900
21.83;:
-3. 900
-0. 179
-0. 179
-0. 179
-------
TABLE A-6 SUMMARY OF DATA FROM TEST NO. 3
Page r of i
Degreaser B, Idle.
Solvent: 1,1,1-TMchloroethane
(Boiling ; nonboiling x
FB JO t PC ^_^ "SC~
Inlet air Exhaust air
Other ~
A 0 %
0 fT/min
Date 10/16/78
Ambient air•
Temperature 60 *F
Pressure 23.bbtn. Mq
Humidity ~~
Reading
No.
T( mln
W, 1b
AT. n
AW, Ib
EAT, h
ZAH. Ib
(i?). w
(&). '"»
X, Ib/h
1.
0. 000
3180. 100
2.
1310.000
3178.000
21.83;:
-2. 100
21.83G:
-2. 100
-0. 096
-0. 096
-0. 096
•
-
•
-------
TABLE A-7 SUMMARY OF DATA FROM TEST NO. 4
Page 1 of 1
Degreaser A, Idle*
Solvent: 1,1,1-THchloroethane
(Boiling ; nonboiling ^
n so i PC sc
Inlet air Exhaust air
Other ™
01
m\n
Date 10/19/78
Ambient a*ir
Temperature 69 *F
Pressure 25.6dJ"- Hq
Humidity 68 "
Reading
No.
Tt mln
W. 1b
AT. h
AN, 1b
MT, h
IAN, 1b
(ar). 1b/h
(IST). lb/h
.
X. fb/h
1.
0. 000
3573. 000
2.
6^15. OL'U
3565. l.'iJO
115. 25U
12. 500
1 15. 250
12. 500
0. lOo
0. i MS
0. 1 ill"!
-------
TABLE A-8 SUMMARY OF DATA FROM TEST NO. 4
Page
of
Degreaser B, Idle
Solvent: 1,1,1-THchloroethane
(Boiling ; nonboiling x )
FB 50 t PC SC
InleTTfr Exhaust air
Other
A q %
V 0 ft/mi i
Date 10/19/78
Ambient air
Temperature
Pressure 29.64*".
Humidity 68 jt
Reading
No.
T, mln
M. Ib
AT. h
AW, Ib
EAT, h
CAW, Ib
(AW) ,b/||
(ffl)L """
X, Ib/h
1.
0. 000
T1A1 400
2t
b1:1 1 LJ. l.iflO
"IlS^. h.nn
115. .1-50
7. 800
1 15, 250
7. 800
0. 0*3
0. Oti"-:
0. I.I'. •:
-------
TABLE A-9 SUMMARY OF DATA FROM TEST NO. 5
Page 1 of 1
Degreaser A, idle
Solvent: 1,1,1-Trichloroethane
(Boiling ; nonboiling x )
FB 50 % PC SC _
Inlet air Exhaust air
Other
0 %
0 ft/min
Date 10/27/78
Ambient air
Temperature
54 °F
Pressure 29.64 in. Hg
Humidity 73%
Reading
No.
T, win
tf. 1b
AT, h
AW, 1b
EAT, h
EAW, 1b
(S). ">»
(fsr). 1b'h
X, 1b/h
1.
o. o-i' o
.3063. 200
2.
3*30. 000
35 j1?. T"5Q
t-5. 500
3. 4f.O
65. 500
3. 450
0. 053
0.053
0. ni:,3
-------
TABLE A-1Q SUMMARY OF DATA FROM TEST MO. 5
P«9* } of
Degreaser B, Idle •
Solvent: 1,1,1-TMchloroethane
(Boiling ; nonboiling _x )
FB 50 i PC SC
Inlet afr Exhaust air
Other
0 1
min
Date 10/27/78
Ambient rfir
Temperature
54 °F
Pressure29.64 jn- Hg
Humidity 73 t
Reading
No.
Tf win
M, 1b
ftT, h
AW, 1b
CAT, h
CAW. 1b
(S). ""•
(MO. ™
X. 1b/h
1.
0. Ofin
23^4. ?00
2.
S'r'SO. I'liJU
2351. 700
t-5. T.OO
3. 200
t-5. 500
3. 200
0. 04'?
0. 04?
n. rm'-i
•
-------
TABLE A-ll SUMMARY OF DATA FROM TEST NO. 6
Page 1 of 2
Degreaser A, Idle
Solvent: IJJ-Trichloroethane
(Boiling x '» nonboiling )
FB 50 % PC x SC
Inlet air Exhaust air
Other
A
8
50 %
Ft/mi n
Date 11/3/78
Amb i ent "ai r' *""
Temperature 76 °F
Pressure 29.71in. Hg
Humidi ty 45 7,
Reading
No.
Tt min
W. 1b
AT. h
AW. 1b
TAT. h
CAW. 1b
(AWN lh/h
i XT I iDf n
\tJl/t
(far). lb/h
X, 1b/h
0. 000
3670. 300
1.
73. 000
3683.000
2.
140. 000
3680. 100
1.033
-2. 900
1 . 03 ]:
-2. 900
-2. 806
-2. SOt.
-2. 80t.
3.
197. 000
3678. 900
0. 950
-1.200
1.98::
-4. 100
-1. 26'::
-2. 067
-2.437
4.
262. 000
3675. 000
LOS']:
-3. 900
3. 067
-3. 000
-3. 600
-2. 609
W • *T _ *T
327. 000
3657. 900
N>
O
-------
TABLE A-11 (continued)
Page 2 of 2
IV)
Reading
No.
T, mln
U. Ib
AT. h
AW. Ib
EAT. h
EAU. Ib
(M\ ,b/n
\AT/,
X. 1b/h
•
•
n 3 S 0.965 t .- 12.706
j U/ t
Slope -2.534 Sx 1.017 r -1.000 •
Intercept 0.138 Sa 0.671 Confidence Interval
O
Sb 2.320 2.53A+8.526
1.188
-------
TABLE A-12 SUMMARY OF DATA FROM TEST NO. 6
Page 1 of 2
Degreaser B, Idle
Solvent: 1,1,1-THchloroethane
(Boiling x ; nonboiling )
FB 50 % PC x SC
Inlet air TxKaust air
Other
Date H/3/78
50 %
TTmin
Ambient'air
Temperature 76_ °F
Pressure 29.71 in~ Hg
Humidity 4(T"%
Reading
No.
T, mln
». 1b
AT. h
AW, 1b
IAT, h
raw, ib
/ftW\ 1K.fc
VBTJ. 1b'h
(Sft """
X, Ib/h
0. 000
230S. 400
1.
120.000
2S03. 400
2.
135.000
2306. 100
i.os::
-3. 300
1.03C:
-3. 800
-3. 50?:
-3. 50?:
-3. 50?:
3.
246. 000
2305. 100
1.017'
-1. 000
2. 100
-4. 800
-0. 93*J
-2. 286
-2. 89T'
4.
302. 000
2802. 300
o. 93;;
-2. 800
3. 03::
-7. 600
-•>.. nnn
-2. 505
-2. 76*.
380. 000
27S3. 600
-------
TABLE A-12 (continued)
Page _2 of
Kl
Reading
No.
T, win
H. 1b
AT. h
AU. 1b
CAT. h
EAU. Ib
(S) lb'h
\AI/,
(¥" AU\
••U" • 1 It /kV
X, Ib/h
•
•
n 3 Syx 0.801 tQ/2 12.706
Slope -1.934 Sx 0.975 r -1.000
Intercept -1.392 Sa 0.581 Confidence interval
Sb 2.591 1.934+7.382
S^ 1.335
-------
TABLE A-1 j SUMMARY OF DATA FROM TEST NO. 7
Page i of 5 .
Degreaser A. operating
Solvent: 1,1,1-Trlchloroethane
FB 50 I PC x SC
Inlet afr - Exhaust air x
Other ~~"
' V g ft/ml n
Date 10/12/78
Ambient air
Temperature 65 °F
Pressure 29 . 72 In. Hg
Humidity J2~~*
Reading
No.
T, mln
H. Ib
AT, h
AW. Ib
EAT. h
EAWV Ib
(AT) 1b/h
(IAT) 1b/h
X. Ib/h
1.
0. 000
3616.000
2.
58. 000
3613.500
0. 967
-2. 500
0. 967
-2. 500
-2. 58t.
-2. 5St.
-2. 5St-
3.
1 1 7. 000
3611.900
0. 933
-1.600
1.950
-4. 100
-1.627
-2. 10;:
-2. 34'-
4.
174.000
3609. 600
0. 950
-2. 300
2. 900
-6. 400
-2.421
-2. 207
-2. 299
5.
240. 000
3607. 200
1. 100
-2. 400
4. 000
-8. 800
-2. 182:
-2. 200
-2. 27'-
6.
298. 020
3604. 500
0. 967
-2. 700
4. 967
-11.500
-2. 79::
-2.315
-2. 282:
10
-------
TABLE A-13 (continued)
Page ? Of 5
Reading
No.
T. «1n
U. 1b
AT. h
AH. Ib
EAT. h
EAH. Ib
09. »"•
($). «•/"
X, 1b/h
T
1 •
362. 04Ci
3602. 000
1.067
-2. 500
6. 03<-
-14.000
-2. 34::
-2. 320
-2. 239
8.
414.060
3599. 800
0. 867
-2. 200
6.901
-16.200
-2.537
-2. 347
-2. 297
9.
472. 030
3597. 000
0. 967
-2. SOO
7. 86?:
-19.000
-2. 896
-2.415
-2.312
10.
531. 060
3594. 200
0. 98C:
-2. 800
8.851
-21.800
-2. 848
-2. 463
-2. 32S
11.
596. 040
3592. 100
1.083
-2. 100
9. 93<-
-23. 900
-1.939
-2. 406
-2. 336
12.
655. 020
3589. 600
0. 983
-2. 500
10.917
-26. 400
-2. 543
-2.418
-2. 34<-
N>
(continued)
-------
TABLE A-13 (continued)
3 of 5
Reading
No.
T, Mil)
U, Ib
AT. h
AU. Ib .
CAT, h
CAM. Ib
(ir). lb/h
(Mr). lb/h
X. 1b/h
13.
715.020
3583. 300
1.000
- 1 . 300
11.917
-27. 700
-1.300
-2. 32<
-2. 34C:
14.
777. 000
3586. 200
1.03::
-2. 100
12.950
-29. 800
-2.030
-2.301
-2.339
15.
335. 020
3537. 000
0. 967
0. 800
13.917
-29. 000
0. 827
-2. 08<-
-2.321
16.
898. 020
3580. 700
1.050
-6. 300
14.967
-35. 300
-6. 000
-2. 359
-2. 320
1 7
954. 000
3579. 500
0. 930
-1.200
15.900
-36. 500
-1.286
-2. 296
-2. 322:
18.
1012.020
3576. 800
0. 967
-2. 700
16.867
-39. 200
-2. 792:
-2. 32<-
-2. 32::
IS)
(continued)
-------
TABLE A-13 (continued)
Page 4 of s
Reading
No.
T, win
U. 1b
AT. h
AW, 1b
EAT. h
EAU. 1b
($r). lb/h
/EAW\ ]b/h
VEAT/.
X. 1b/h
19.
1071.000
3574. 500
0.98]:
-2. 300
17.850
-41.500
-2. 340
-2. 325
-2. 322:
20.
1129.980
3572. 200
0. 98':
-2. 300
18.83-::
-43.800
-2. 340
-2. 326
-2. 32J:
21.
1194.000
3570. 500
1.067
-1.700
19.900
-45. 500
-1.593
-2. 28*
-2. 320
22.
1252.020
3569. 000
0. 967
-1.500
20. 867
-47. 000
-1.551
-2. 252:
-2.317
23.
1317.000
3567. 300
1.083
-1.700
21.950
-48. 700
-1.570
-2.219
-2. 3 1C:
24.
1378.980
3565. 600
1.033
-1.700
22. 983
-50. 400
-1.646
-2. 193
-2. 307
(continued)
-------
TABLE A-13 (continued)
Page _5 of 5
Reading
No.
T. min
U. Ib
AT. h
AU. Ib
EAT. h
CAW. Ib
«). ™
(fir). 1b/h
X. lb/h
25.
1440.000
35*3. 700
1.017
-1.900
24. 000
-52. 300
-1.86.
™" 0.033 Confidence Interval
d
Sb 0.176 2.27 + 0.068
S 1.130
00
-------
TABLE A-15 SUMMARY OF DATA FROM TEST NO. 7
Page _]__ of _5__
Degreaser B, operating
Solvent: 1.1,1-THchloroethane
PC
Date 11/12/78
FB _50 t
Inlet air
Other
x SC
xhaust air x
A _50 %
8 ft/min
Ambient 'air
Temperature 65 °F
Pressure 29.TTHTTkg
Humidity "IF"*
Reading
No.
Tv mln
N, 1b
AT, h
AH. Ib
EAT. h
CAW. Ib
(SX "»•
(it?). «""
X. 1b/h
1.
0. 000
27Sq. ^00
2.
53. 930
2737. 700
0. 98.1!
-1.800
0. 983
-l.SOO
-1.331
-1.33J
-1.831
3.
1 1 7. 000
2737. 100
0.967
-0. 600
1.950
-2. 400
-0. 620
-1.231
-1.531
4.
175.020
"J7:::c'i inn
h« i — — • & — -
0. 967
-2. 000
2.917
-4. 400
-2. 06?:
-1.505:
-1.52-::
5.
233.040
2733. 900
0. 967
-1.200
3. 38f
-5. 600
-1.241
-1.441:
-1.50::
6.
292. 020
2782. 100
0. 933
-1.800
4. 867
-7. 400
-1.83J
-1.520
-1.507
ro
\o
-------
TABLE A*]4 (continued)
Page 2 of 5
Reading
No.
T, mln
U, 1b
AT. h
AH, 1b
EAT, h
CAM. 1b
00. ""*
(sft "•"'
X. 1b/h
7.
363. 000
2778. 500
1. 18;:
-3. 600
6. 050
-11.000
-3. 043
-1.816
7 1.556
8.
415.020
2776. 800
0. 867'
-1.700
6.917
-12.700
-1.961
-1.836
-1.596
9.
473.040
2775. 700
0. 967
-1. 100
7.884
-13.800
-1. 136
-1.750
-1.617
10.
533.040
2772. 200
1.000
-3. 500
8. 881
-17.300
-3. 500
-1.947
-1.654
11.
591.060
2769. 500
0. 967
-2. 700
9. 85 J
-20. 000
-2. 79::
-2.030
-1.691
12.
655. 080
2767. 700
1.067
-1.800
10.915:
-21.800
-1.687
-1.997
-1.719
w
o
(continued)
-------
TABLE A-14 (continued)
Page 3 of 5
Reading
No.
T, mln
W, 1b
AT, h
aw, ib
EAT, h
EAW, Ib
00. ""*
(SO. ""-
X, 1b/h
13.
714.060
2765. 300
0. 93C:
-2. 400
11.901
-24. 200
-2. 44;:
-2. 033
^1.745
14.
779. 040
2762. 900
i.os::
-2. 400
12.984
-26. 600
-2.216
-2. 049
-1.769
15.
831. 060
2760. 000
0. 867
-2. 900
13.851
-29. 500
-3. 345
-2. 130
-1.795
16.
895. 080
2756. 500
1.067
-3.500
14.91?:
-33.000
-3. 280
-2.21?
-1.82;-
17.
949. 080
2755. 200
0. 900
-1.300
15. 81?:
-34. 300
-1.444
-2. 16?:
-1.84-1
18.
1012.680
2751.300
1.060
-3. 900
16.87?:
-38. 200
-3. 679
-2. 260
-1.869
(continued)
-------
TABLE A-14 (continued)
Page _* of _5__
Reading
No.
T, mln
M. Ib
AT, h
AH, Ib
CAT, h
CAN, Ib
(£). »«•
(SO. "">
X, lb/h
19.
1070.700
2749. 600
0. 967
-1.700
•17. 845
-39. 900
-1.758
-2. 236
-1.889
20.
1129.680
2748. 000
0.93::
-1.600
18.825:
-41.500
-1.62?:
-2. 20'-
-1.906
21.
1193.700
2745. 000
1.067
-3. 000
19.895
-44. 500
-2.812:
-2. 237
-1.922:
:o
t_ t_ •
1251.720
2744. 800
0. 967
-0. 200
20. 362!
-44. 700
-0. 207
-2. 14C:
-1.93^:
23.
1317.720
2742. 100
1. 100
-2. 700
21.962
-47. 400
-2. 455
-2. 15£:
-1.94C:
24.
1381.740
2738. 000
1.067
-4. 100
23. 029
-51.500
-3. 84;:
-2. 236
-1.956
ro
(continued)
-------
TABLE A-14 (continued)
Page 5 of 5
Reading
No.
T, mln
H, Ib
AT, h
AW, Ib
EAT, h
EAW, Ib
(Ir) lb'h
faM\ lb/h
X, lb/h
25.
1434.720
2739. 000
0. 883
1.000
23. 91i:
-50. 500
1. 133
-2. 112:
-1.96*
•
n 24 Suy 1.122 t „ 2.074
Jr A \tj C
Slope -2.314 Sx 7.062 r -0.998
Intercept 2.707 Sa 0.033 Confidence Interval
a
Sb 0.176 2.31A + 0.068
S^ 1.171
-------
TABLEA-15 SUMMARY OF DATA FROM TEST NO. 8
of
Degreaser A, operating
Solvent: 1,1,1-THchloroethane
Date 11/13/78
FB 50 X
Inlet air x
Other
PC x SC
txhaust air x
A 50 %
V 8 ft/mln
Ambient air
Temperature °F
Pressure - in. Hg
Humidity - %
Reading
No.
T, mln
W. 1b
AT. h
AW, 1b
EAT, h
IAW. 1b
(S). ™
(I?). «"•
X, lb/h
1.
0. 000
3630. 800
2.
52. 980
3628. 500
0. 883
-2. 300
0. 883
-2. 300
-2. 60?:
-2. 605
-2. 60^
3.
111.000
3625. 900
0. 96?
-2. 600
1.850
-4. 900
-2. 689
-2. 649
-2. 62T1
4.
169.930
3623. 400
0. 98C:
-2. 500
2.833
-7. 400
-2. 543
-2.612:
-2. 62J1
5.
234. 980
3621.800
i.os::
-1.600
3.916
-9. 000
-1.477
-2. 29?:
-2.541
6.
292. 980
3620. 000
0. 967
-1.800
4. 883
-10.800
-1.862
-2.212:
-2. 47«:
-------
TABLE A-15 (continued)
1 Page 2 of 3
Reading
No.
T, mln
W, 1b
AT, h
AW, 1b
EAT, h
SAW. 1b
C^\ Ih/h
1 TV I la/n
\AT/f
Ol*A^^V
2i£jN A llh/k
X. Ib/h
7.
351.960
3617. 100
0. 983
-2. 900
5. 866
-13.700
-2. 950
-2. 335
-2. 452
8.
417.960
3615. 100
1. 100
-2. 000
6. 966
-15.700
-1.818
-2. 25^
-2. 424
9.
463. 960
3612.600
0. 850
-2. 500
7.816
-13.200
-2.941
-2. 329
-2. 4K:
10.
533.940
3609. 700
1.083
-2. 900
8. 399
-21. 100
-2. 67?:
-2. 37 J
-2. 40?
11.
592. 920
3606. 700
0. 983
-3. 000
9. S3Z:
-24. 100
-3. 052:
-2. 439
-2.410
12.
650. 940
3605. 600
0. 967
-1. 100
10.849
-25. 200
-1. 13?:
-2. 323
-2. 402:
tn
(continued)
-------
TABLEA-15 (continued)
i Pa9e 3 of _3_
Reading
No.
T, m1n
H, Ib
AT.'h
AH, Ib
EAT, h
CAN, Ib
($). lb/h
faj!j£\ lb/h
X, lb/h
13.
709. 920
3603. 600
0. 983
-2. 000
11.832
-27. 200
-2. 035
-2. 299
-2. 394.
14.
773.940
•^ni.^nn
1.067
-2. 300
12.899
-29. 500
-2. 156
-2. 287
-2. 386
15.
827. 940
3599. 400
0. 900
-1.900
1 3. 799
-31.400
-2. Ill
-2. 276
-2. 37?:
16.
891. 960
3596. 500
1.067
-2. 900
14.866
-34. 300
-2.715:
-2. 307
-2. 370
•
"15 Syx o.499 ^ 2.160
Slope -2.28 Sx 4.463 r -1.000
Intercept -0.419 sa 0.030 Confidence Interval
Sb 0.289 2.23 + 0.065
S,. 0.573
O>
-------
TABLE A-16 SUMMARY OF DATA FROM TEST NO. 8
Page j of 3
Degreaser B. operating
Solvent: 1,1,1-Trlchloroethane
FB 50 *
Inlet air
Other
PC
SC
Exhaust air
Rn
rt/m
mln
Date 11/13/78
Amb 1 en fair
Temperature - °F
Pressure - f rT." Hg
Humidity - 1
Reading
No.
T, win
W, 1b
AT. h
AW. 1b
EAT. h
CAM. 1b
(S). ">'"
(IST). 1b/h
X. Ib/h
1.
0. 000
2802. 500
•
w •
61.980
2801.300
1.03::
-1.200
1.033
-1.200
-1. 16J:
1 1 " "'
-i. it-:-
•3.
118. 980
2799. 100
0. 950
-2. 200
1.980
-3. 400
-2. 31*.
-1.715
-1.438
4.
177.960
2797. 500
0. 98-::
-1.600
2. 966
-5. 000
-1.62?:
-1.686
-1.521
5.
235.980
2796. 100
0. 967
-1.400
3. 93C:
-6. 400
-1.44?:
-1.627
-1.547
6.
301.980
2796. 900
1. 100
0. 800
5. 033
-5. 600
0. 727
-i. 113
-1.460
U)
-------
TABLE /\_]6 (continued)
Page _2_ of 3,
Reading
No.
T, m1n
W. 1b
AT, h
AU. 1b
EAT, h
EAM. 1b
/AU\
i an i it. ji.
iTTi ID/n
W/t
(fir). lb'h
X, Ib/h
7.
354. 000
2792. 200
0. 867
-4. 700
5. 900
-10.300
-5. 42J
-1.746
-1.506
8.
418.980
2790. 400
1.081:
- 1 . 800
6. 983
-12. 100
-1.66::
— 1 . i o> •.:
-1.540
9.
471.960
2787. 300
0.881:
-3. 100
7. 866
-15.200
-3.511
-1.932:
-1.539
10.
541. 980
2734. 400
1. 167
-2. 900
9. 033
-18. 100
-2. 485
-2. 00^
-1.633
11.
594. 000
2783. 400
0. 867
-1.000
9. 900
-19. 100
-1. 153
-1.929
~" * • t'\T ^'
12.
652. 980
2781.000
0. 983
-2. 400
10.883
-21.500
-2. 442:
-1.976
-1.693
tJ
00
(continued)
-------
TABLE A-16 (continued)
Page 3 of 3
Reading
No.
T, mln
U, Ib
AT, h
AW, Ib
EAT. h
EAW. Ib
(M\ lh/h
ITT/ iD/n
W/,
(fir). lb/h
X, lb/h
13.
711.960
2778. 400
0.98::
-2. 600
ll.S6t.
-24. 100
-2. 645
-2.031
-1.721
14.
786. 960
2775. 500
1.250
-2. 900
13. lit.
-27. 000
-2. 320
-2. 059
-1.747
15.
834.960
2773.600
0. 800
-1.900
13. 9 It.
-28. 900
- o T* S
-2. 077
-1.771
16.
892. 980
2772. 400
0. 967
-1.200
14. 88C:
-.30. 100
-1.241
-2. 022
-1.787
•
u-
VD
n 15
Slope -2.130
Intercept 2.136
Syx 1.114
Sx 4.451
S. 0.067
a
Sb 0.29b
S_ 1.339
2.160
r -0.997
Confidence Interval
2.130 + 0.145
-------
TABLE A-17 SUMMARY OF DATA FROM TEST NO. 9
Page 1 of 2
Degreaser A, Idle
Solvent: 1,1,1-Tr1chloroethane
(Boiling x__; nonboiling )
FB 50 * PC x SC
Inlet air . Exhaust air
Other
A
0
o %
FtTmin
Date 11/14/78 •
Ambient air '•
Temperature 70 °F
Pressure 29.?Tjn. Hg
Humidity 28 %
Reading
No.
T, mln
M. lb
AT. h
AM. lb
IAT. h
EAH, lb
(S). ">"
(Mr). 1b/h
X. Ib/h
1.
0. 000
3619.400
,
">
»_ •
57. 000
3615.700
0. 950
-3.700
0. 950
-3.700
-3.895
-3.895
"• •"• f» C "
J* • O • • '
3.
116.000
3613.200
0. 93::
-2. 500
1.933
-6. 200
-2. 54::
-3. 207
-3. HI
4.
178.000
3611.300
1.033
-1.900
2. 967
-8. 100
-1.839
-2.730
- 3. 277
5.
242. 000
3610.800
1.067
-0. 500
4. 033
-8. 600
-0. 469
-2. 132:
-2.991
6.
296. 000
3609. 500
0. 900
-1.300
4. 933
-9. 900
-1.444,
-2. 007
-2. 791
-------
TABLE A-17 (continued)
Page _z_ of 2
Reading
No.
T. m\n
W. Ib
AT. h
AW, Ib
CAT. h
CAU. Ib
(M\ Ih/h
I T5" 1 10 fn
\Al/.
(fir) lb/h
X. lb/h
1 •
362. 000
3606. 600
1. 100
-2. 900
6.03::
-12.800
-2. 636
-2. 12^:
-2. 682
B.
4 IS. 000
3605. 700
0.93::
-0. 900
6. 967
- 1 3. 700
-0. 96^
-1.967
-2. 5SO
9.
476. 000
3603. 600
0. 967
-2. 100
7.93;:
-15. SOO
-2. 1 72'-
-1.99::
-2. 506
•
n 8
Slope -1.804
Intercept -2.543
'yx
0.575
2.^54
0.089
0.599
1.074
2.447
r -0.993
Confidence Interval
1.804 + 0.218
-------
TABLE A-L8 SUMMARY OF DATA FROM TEST NO. 9
Page 1 of 2
Degreaser B, Idle
Solvent: 1,1,1-THchloroethane
(Boiling x ; nonboiling )
FB 50 % PC x SC _ x
Inlet air - Exhaust air x_
Other
A
0
0 I
7m In
Date 11/14/78
Ambient air
Temperature 70 *F
Pressure 29.71 in. Hg
Humidity
Reading
No.
Tt mln
W, 1b
AT, h
AW, 1b
EftT, h
CAM. Ib
(Sf). »"*
(8ft "">
X. 1b/h
1.
0. 000
2sn*. nnn
2.
55. 000
2fini ftnn
0.917
-4. 200
0.917
-4. 200
-4. 58?
-4. 5S?
-4. 5SJ'
3.
1 1*5. 000
2Rnn 7on
1.000
-1. 100
1.917
-5. 300
-1. 100
-2. 765
-5.674
4.
172. 000
?flfi 1 'nfi
0. 950
0. 600
2. S67
-4. 700
0.632!
-1.640
-2. ??t.
5.
239. 000
oonn ^nfi
iOU'J. TU'J
1. 117
-0. 800
•3. 983
-5. 500
-0. 716
-1.381
-2. 59J1
6.
294. 000
i 99. 900
0.917
-0. 600
4. 900
-6. 100
-0. 655
-1.245
-2. 32;-
-------
TABLE A-18 (continued)
t Page 2 of 2
Reading
No.
T, mln
W, 1b
AT, h
AH. 1b
CAT, h
W CAM. 1b
(ir) lb/h
(fir) lb/h
X, lb/h
7.
353.000
2798. 300
0. 983
-1.600
5. 883
-7. 700
-1.627
-1.309
_o i ^A
h. . i j ^
8.
415.000
2797. 200
1.033
-1. 100
6.917
-8. 800
-1.065
-1.272:
-2. 02?:
9.
475. 000
2796. 900
1.000
-0. 300
7.917
-9. 100
-0. 300
-1. 149
-1.91?.:
•
n 8 Syx 0.597 tQ/2 2.447
Slope -0.94 $x 2.449 r -0.972
Intercept -3.199 S Q.092 Confidence Interval
a
Sb 0.589 0.94 +0.225
Sc I.b28
-------
TABLE A-19 SUMMARY OF DATA FROM TEST NO. 10
Page 1 of 2 _
Oegreaser A, Idle
Solvent: 1,1,1-THchloroe thane
(Boiling _x ; nonboiling )
FB 50 % PC x SC
Inlet air -_
Other
Date 11/15/78
Exhaust air x"
A 0%
V 0 ft/min
Ambient air
Temperature 63 °F
Pressure 29.75in. Hq
Humidity 44 %
Reading
No.
T, mln
H. Ib
AT, h
AM. Ib
EAT. h
ZAM. Ib
(S). ">»
(Isf). lb/h
X. Ib/h
1.
0. 000
3605. 000
••
2.
60. 000
3604. 600
1.000
-0. 400
1.000
-0. 400
-0. 400
-0. 400
-0. 400
3.
120.000
3601.400
1.000
-3. 200
2. 000
-3.600
-3.200
-l.SOO
-1. 100
4.
175.000
3600. 500
0.917
-0. 900
2.917
-4. 500
-o. 9s;-
-1.54::
-1.24*
5.
236. 000
3599. 900
1.017
-0. 600
3.93-::
-5. 100
-0. 590
-1.297
- 1 . 260
6.
295. 000
'3598. 900
o. ?s;:
-1.000
4.917
• -6. 100
-1.017
-1.241
-1.25t-
-------
TABLE A-19 (continued)
Page 2 of _2_
Reading
No.
T, m1n
W, Ib
AT, h
AW, Ib
EAT, h
CAW, Ib
(ir). lb/h
flM\ ,h/h
VST;. lb/h
X, lb/h
1 •
35*. 000
3596-. 000
1.01T1
-2. 900
5.93::
-9. 000
-2. 85C:
-1.517
-1.299
8.
42t-. 000
3594. SOO
1. lt-7
-1.200
7. 100
-10.200
-1.029
-1.437
-1.319
n 7 Suv 0.766 t ., 2.571
y« a/ f.
Slope -1.456 Sx 2.174 r -0.994
Intercept 0.339 S. 0.144 Confidence interval
a
Sb 0.699 1.456 + 0.370
Sc 1.115
l/l
-------
TABLE A-2(l SUMMARY OF DATA FROM TEST NO. 11
Page J of 2
Oegreaser B, Idle
Solvent: 1,1,1-Trichloroethane
(Boiling x ; nonboiling )
FB 50 % PC x SC
Inlet air _- Exhaust air x"
Other
A
0
Date 11/15/78
Ambient air
Temperature 63 °F
Pressure 29./bi'n. Hg
Humidity 44 I
Reading
No.
T, mln
U. Ib
AT. h
AW. Ib
CAT, h
CAM. Ib
(S). ">"•
(8ft '»*
X. lb/h
1.
0. 000
2791. 100
••
-.
t-4. 000
278?. 100
1.0*7
-2. 000
1.067'
-2. 000
-1.375
-1.875
-1.875
3.
122.000
2787. 000
0. 9*7
-2. 100
2.03::
-4. 100
-2. 17::
-2.0 It.
-1.94*.
4.
178.000
2781.200
0.93::
-5. 800
2. 9*7
-9. 900
-b. 21f
-'3. 337
-2. 409
5.
240. 000
2779. t-00
1.03;:
-1.600
4. 000
-11.500
-1.548
-2. 875
-2. 526
6.
299. 000
2777. 300
0. 983
-2. 300
4. 983
-13.800
-2. 339
-2. 769
-2. 575
-------
TABLE A-20 (continued)
Page 2 of 2
Reading
No.
T, mln
W. Ib
AT, h
AM. Ib
EAT. h
IAW. Ib
(0. '*
(M). ">/••
X. lb/h
•^
I •
359. 000
2775.200
1.000
-2. 100
5. ?8C:
-15.900
-2. 100
-2. 657
-2. 58*
S.
425. 000
2772. 200
1. 100
-3. 000
7. 08::
-18.900
-2. 727
-2. bb?:
-2. bOO
n7 Syx 1.164 tQ/2 2.571
Slope -2.765 Sx 2.158 r -0.997
Intercept 0.333 Sa 0.220 Confidence Interval
O
Sb 0.720 2.765 + 0.566
S,. 1.538
-------
TABLE A-21 SUMMARY OF DATA FROM TEST NO. 11
Page 1 of 2
Degreaser A. operating
Solvent: 1,1,1-Trlchloroethane
Date 11/15/78
™ 50-,-*
Inlet air -
Other
x
Exhau
_ sc _
aust air x
A sp *
V 3 Tt/min
Ambient air
Temperature 65 *f
Pressure - Tn. Hg
Humidity £5 %
Reading
No.
T, mln
W, lb
AT. h
AW, lb
EAT, h
£AW. lb
(S). """
(nr). lb/h
X. lb/h
0. 000
.3603. 900
1.
22. 000
3614. 100
w •
SO. 000
360?. 900
0. 967
-4. 200
0. 967
-4. 200
-4. 34".
-4. 34S
-4. 34«,
3.
159. 000
3605. 400
1.317
-4. 500
2. 28'::
-8. 700
-3.41?:
-3.810
-4. 07£:
4.
198.000
3604. 000
0. 650
-1.400
2. 93::
-10. 100
™ »!> • 1 - *T
-3.44^:
-3. 36*.
5.
256. 000
3601. 100
0. 967
-2. 900
3. 900
-13.000
-3. 000
-3.33:::
-3. 73C:
00
-------
TABLE A-21 (continued)
Page 2 of 2
Reading
No.
T, mln
U. Ib
AT. h
AH. Ib
CAT. h
I AW, Ib
UA lb/h
WA
X, lb/h
6.
321.000
3598. 400
i.os::
-2. 700
<1 Q£J ''
-15.700
--3. 151
-3.61*
1 •
380. 000
3595. 600
0.98::
-2. 800
5. 967
-18.500
-2. 847
-3. 101
-3. 530
8.
445. 000
3593. 000
1.08::
-2. 600
7. 050
-21. 100
-2. 400
-2. 99':
-?. 454
476. 000
3580. 000
••
n 7 Syx 0.333 tQ/2 2.571
Slope -2.92 Sx 2.138 r -0.998
Intercept -2.024 Sa 0.064 Confidence Interval
a
Sb 0.730 2.92+0.165
S,. 0.744
-------
TABLE A-22 SUMMARY OF DATA FROM TEST NO. 11
Page ,1 of 2 .
Degreaser B. operating
Solvent: 1,1,1-THchloroethane
PC
re so i
Inlet air
Other
x SC _
xhaust air x
A
8
Date 11/15/78
Ambient air*~
nun
Temperature 65 °F
Pressure - In. Hq
Humidity 6b I
Reading
No.
T. m1n
W, Ib
AT. h
AW. Ib
EAT. h
CAW, Ib
\ O • /•
/ FA^f ^
X. Ib/h
0. 000
27:38. 500
1.
17.000
2790. 20*
W. •
82. 000
2795. 600
1.08.':
5. 400
i.os::
5. 400
4. 985
4. 9 SI-
4. 9S1.
3.
160. 000
2789. 700
1. 300
-5. 900
2.3:3!:
-0. 500
-4. 53:!:
-0.210
2. 387
4.
212.000
2796. 400
0. 867
6. 700
3. 250
6. 200
7.731
1.90*
-• -• ? •:•
t_ • •_ t_ •-•
5.
258. 000
2794. 000
0. 767
-2. 400
4.017
3. 800
-3. 130
0. 94 1.
1.907
IT
O
-------
TABLE A-22 (continued)
Page 2 of 2
Reading
No.
T. m1n
W. Ib
AT. h
AW. Ib
CAT. h
CAW. Ib
(^\ 1h/h
iTrJ io/n
\AT/.
(fir). lb/h
X, lb/h
6.
323. 000
2791.500
1 . 03 1:
5. 100
1 . 300
-2. 30?:
0. 25'.
1.57;-1
1 •
381. 000
2785. 700
0. 9*7
b. 0*7
-4. 500
-b. 000
-o. 74::
1. 190
8.
443.000
2783. 300
1 . 0 3 ::
". 100
-6. 900
- "• 3 ' ":
»_ • ^^ .'
-o. 97::
0. 83 1
509. 000
2758. 100
•
n 1
Slope -1.858
Intercept 8.382
'yx
3.366
2.107
0.652
0.787
5.120
V« 2-571
r -0.198
Confidence Interval
1.858 + 1.676
-------
TABLE A-23 SUMMARY OF DATA FROM TEST NO. 12
Page 1 of 2
Degreaser A, Idle
Solvent: 1,1,1-THchloroethane
(Boiling _x ; nonboiling )
FB 50 * PC x SC x
Inlet air - Exhaust air x"
Other L1d closed
Date H/16/78
A Q %
0 ft/min
Ambient'fcir
Temperature 65 °F
Pressure - in. Hg
Humidity 4Z %
Reading
No.
T, win
N. 1b
AT. h
AW, 1b
TAT. h
EAW. 1b
(S). ""*
(KT). 1b/h
X. 1b/h
0. 000
3614.600
1.
9. 000
3623. 000
2.
66. 000
3622. 300
0. 950
-0. 200
0. 950
-0. 200
-0.211
-0.211
-0. 21 !
3.
127.000
3621. 800
1.017
-1.000
1.967
-1.200
-0. 984
-0.610
-0.410
4.
193. 000
3623. 000
1. IS!:
1.200
3. 150
0. 000
l.OH
0. 000
-0. 27^
5.
243. 000
3622. 200
0.831:
-0. 800
3. 983
-0. 800
-0. 960
-0.201
-0. 2t5'.'
N)
-------
TABLE A-2.1 (continued)
Page ? of ?
Reading
No.
Tt win
H, Ib
AT. h
AW, Ib
CAT. h
CAW. Ib
(M\ .h/h
1 TT I iD/n
\AT/,
(BOl '»"
X, Ib/h
6.
Tin. nnn
TA^I snn
1.03::
-0. 700
5.017
-1.500
-0. 677
-0. 299
-0. 26^
-f
17*,. nnn
3f. "°. 4nn
1.083
0. 900
6. 100
-0. 600
0.831
-0. 09?:
-Q.23*.
'_* •
4 38. nnn
1.050
3. 500
7. 150
2. 900
3. 333
0. 406
-0. 14S
4S~:. nnn
•ih-fift. 4nn
U)
n 8
Slope 0.321
Intercept -1.499
yx
1.401
2.218
0.258
0.697
2.447
r 0.088
Confidence Interval
+ 0.631
-------
TABLE A-24 SUMMARY OF DATA FROM TEST NO. 12
Page 1 of 2
Degreaser B, Idle
Solvent: 1,1,1-Trlchloroethane
(Boiling x ; nonboiling )
FB 50 t PC x SC x
Inlet air _;___ txhaust air x_
Other Lid closed
Date 11/16/78
A 0 I
V 0 ft/min
Ambient air
Temperature 65 *f
Pressure - fn.'Hg
Humidity W %
Reading
No.
Tf m1n
W. Ib
_• •
AT, h
AW, Ib
EAT, h
EAW, Ib
(S). ""*
(Mf) ib/h
\EA /.
X, Ib/h
0. 000
2778. 600
1.
67. 000
2775. 900
2.
127.000
2773.400
1.000
-2. 500
1.000
-2. 500
-2. 500
-2. 500
-?. =•,--' n
3.
186.000
2770. 700
0. 98-:
-2. 700
1.98C:
-5. 200
-2. 746
-2. 622:
-2.561
4.
255. 000
2767. 400
1. 150
-3.300
3. 1 30
-8. 500
-2. 870
-2.713
-2. 61J:
5.
305. 000
2765. 900
0. 830
-1.500
3. 967
-10.000
-1.800
-2.521
-2. 58?
-------
TABLE A-24 (continued)
Page 2 of 2
Reading
No.
, mln
W, Ib
AT, h
AH, Ib
EAT, h
EAM, Ib
V AT^f
(CAN A 1 1* / L
-- 1 iD/n
1" A T i **»
X, Ib/h
6.
•;7': nnn
2763.400
1. 133
-2. 500
5. 100
-12.500
-2. 20*.
-2.451
-2.561
1 •
4": 7. nnn
2760. 100
1. 067'
-3. 300
6. 16?
-15.800
-3. 094
-2. 562
-2.561
8.
4q*. nnn
2762. 50n
1.031:
2. 400
7. 200
-13.400
2. 323
-1.861
-2.461
532. nnn
2734. son
l/l
IT
n 7
Slope -2.149
Intercept -1.543
yx
1.592
2.233
0.291
0.699
1.886
a/2
r -0.990
Confidence Interval
2.149 + 0.748
-------
TABLE A-25 SUMMARY OF DATA FROM TEST NO. 13
of
Degreaser A, Idle
Solvent: 1,1,1-Tr1chloroethane
(Boiling x_; nonboiling )
FB 50 X PC x SC
Inlet air
Other , . . , .
Lid closed
Date 11/16/78
Exhaust air x
A 0 %
V 0 ft/min
Ambient air
Temperature 68
Pressure
- In. Hg
Humidity 38 ~X
Reading
No.
T, mln
W, lb
AT. h
AW, lb
EAT, h
CAW, lb
(S). ">'"
(tw\ lb/h
X. 1b/h
0. 000
?5?7. 600
1.
15. 000
3610. SOO
2.
SO. 000
3607. SOO
i.os::
-3. 000
i.os-::
-3.000
w • 1 t* I
-2. 76*
-2. 76'-'
3.
142.000
3606. 500
1.033
-1.300
2. 1 1 7
-4. 300
-1.25?:
-2. 03 J
-2. 400
4.
202. 000
3606. 000
1.000
-0. 500
3. 117
-4. 800
-0. 500
-1.540
-2. 114
5.
262. 000
3606. 100
1 . 000
0. 100
4. 117
-4. 700
0. 100
-1. 142:
-1.871
IP
-------
TABLE £-2_5 (continued)
Page 2 of 2
Reading
No.
T, m1n
W, lb
AT, h
AW, lb
CAT, h
CAW, lb
(AW\ 1|>/h
I Tr I ID/R
\AT/,
X, Ib/h
6.
322. 000
3605. 600
1.000
-0. 500
5. 117
-5. 200
-0. 500
-l.Olfr
-1.700
7.
337. 000
3605. 100
1.080
-0. 500
6. 200
-5. 700
-0. 465:
-0. ?1?
-t.57'!'
*•" •
439. 000
3604. 600
0. 867
-0. 500
7. 067
-6. 200
-0. 577
-0. 877
-1.47J
45". 000
3592. 200
•
n 7 Syx 0.334 to/2 2.571
Slope -0.704 Sx 2.170 r -0.963
Intercept -2.968 Sa 0.063 Confidence Interval
O
Sfa 0.743 0.704 + 0.162
Sc 0.933
-------
TABLE A-26 SUMMARY OF DATA FROM TEST NO. 13
Page ]__ of _f_
Degreaser B, Idle
Solvent: 1,1,1-THchloroethane
(Boiling x_; nonboiling )
FB 50 I PC x SC _
Exhaust air x
Inlet air
Other
A _0 I
0 ft/min
Date
Ambient'air
11/16/78
68
L1d closed
Temperature
Pressure -in.
Humidity 38I
•F
Reading
No.
T( mln
W. 1b
AT. h
AW. 1b
EAT, h
£AW, 1b
(S). "">
(8ft ">"•
X. 1b/h
0. 000
2779. 90fi
1.
17.000
279-:. tOO
2.
82. 000
2794. 300
i.os:-;
-4. 300
i.os::
-4. 300
- 3. 969
-3.969
- ?. 969
3.
143. 000
2794. 300
1.017
0. 000
2. 100
-4. 300
0. 000
-2. 04?:
-3. 00?:
4.
200. 000
2793. 100
0. 950
-1.200
3. 050
-5. 500
-1.26;:
-1.803
-2. 607
5.
266. 000
2793.300
1. 100
0. 200
4. 150
-5. 300
0. 185:
-1.277
-2. 274
00
-------
TABLE A-26 (continued)
Page 2 of 2
Reading
No.
THliii
, nun
H. Ib
AT. h
AW, Ib
EAT, h
CAN. Ib
(IM\ 1h/h
I FIT ) '°/n
VEAT /,
X, lb/h
6.
'^'•'•: nnn
2792. 400
0. 950
-0. 900
5. 100
-f>. 200
-0. 947'
-1.216
-2. 06?
i •
3 fin. nnn
2792. 000
0. 950
-0. 400
6. 050
-6. 600
-0.421
-1.09J
-1.90J
4=;":. noo
2776. 200
.-
\D
n 6
Slope -0.876
Intercept -3.629
'yx
0.325
1.868
0.078
0.905
1.523
t ., 2.776
a/2
r -0.957
Confidence Interval
0.876 + 0.217
-------
TABLE A-27 SUMMARY OF DATA FROM TEST NO. 14
Degreaser A, operating
Solvent: 1,1,1-Trichloroethane
FB 50 t PC x SC x A 50 *
Inlet air - Exhaust air x V Q ft/min
Other
Date 11/17/78
Ambient air
Temperature 72 '
Pressure - in. 1
Humidity 5Q~ I
Page 1 of 2
°F
Reading
No.
T. m1n
H. 1b
AT, h
AW. Ib
EAT. h
CAW. Ib
(ir) 1b/h
(S?). "">
X. Ib/h
6S4. nnn
••^.ns. inn
1.
63 n. nnn
':fc 1*. 5nn
o
h. •
722. nnn
3Ms. 7nn
0. 700
- 3. 800
0. 700
-3. 300
_er A? ft
_' • ~ k_ .
-5. 429
-5. 42?'
3.
7ftn. nnn
3A12. "inn
0. 967
-3.200
1.667
-7. 000
-3.310
-4. 200
-4. 814
4.
R":ft nnn
?*%ns ^inn
0. 967
-4. 200
»1« t'Ov1
-11.200
-4. 345
-4. t-27
5.
QHA nnn
r'JO. L11.".1
ocnc nnri
-3. 300
3. 767
-14.500
-2.912:
-3. 850
-4.431:
-------
TABLE A-27 (continued)
Page 2 of 2
Reading
No.
T, mln
W, lb
AT, h
AH, lb
EAT, h
EAW. lb
oa ""
(fir), lb/h
X. lb/h
6.
965. 000
3602. snn
0. 93::
-2. 500
4. 750
-17.000
-2. 542:
-3. 579
-4. 26J1
1 •
102^. onn
'3600. 300
0. 967
-2. 200
5.717
-19.200
-2. 276
-3.359
-4. 11J
10S3. 000
3532. 900
n 6 Syx 0.719 ta/2 2.776
Slope -3.33 Sx 1.896 r -0.996
Intercept -2.150 Sa 0.170 Confidence Interval
O
Sb 0.736 3.33+0.472
S 1.202
-------
TABLE A-28 SUMMARY OF DATA FROM TEST NO. 14
Page
Of 2
Degreaser 8, operating
Solvent: 1,1,1-Trichloroethane
Date 11/17/78
FB 50 %
Inlet air
Other
PC x SC __x
Exhaust air x
A 50 Tt,
8ft/min
Ambient air
Temperature _72 °F
Pressure -~ in. Hg
Humidity 50 %
Reading
No.
T mln
If III 1 VI
W, lb
AT. h
AW. lb
EAT, h
CAW. lb
(&\ Ih/h
I TT 1 lofn
\AI/,
fw\ ,b/h
_
X. lb/h
654. 000
2730. 600
1.
6Kci. 000
2791. 400
2.
724. 000
2783. 900
0. 93::
-7. 500
0. 93::
-7. 500
-7. 627
-7. 627
-7. 6271
3.
775. 000
2731.. 300
0. 850
-2. 600
I.?'?.::
-10. 100
-.3. 059
-5. 509
-K. 56f:
4.
847. 000
27ftO. 700
1.200
-0. 600
"" l"l ^ "" *
-* • '.' • If m '
-10. 700
-0. 500
-3.527
-=; =:se;
5.
906. 000
2783. 600
0. 93.':
2. 900
4.017
-7. 800
2. 949
-1.94J:
-4 AS]
* • v J i
-------
TABLE A-2R (continued)
Page 2 of 2
Reading
No.
T, mln
W, 1b
AT. h
AW, 1b
EAT, h
EAW, 1b
(LAN i ii>/u
2.AI /,
X, Ib/h
6.
9*4. 000
27? 1.000
0. 9*7
-2. 600
4. 93':
-10.400
-2. 037
-4. 13?
i •
1021.000
2779. 100
0. 950
-1.900
5.9.3::
-12. 300
-2. 000
-2. 07C:
-3.79-
10S3. 000
27*4. 300
-
••
U)
n 6
Slope -i.43
Intercept -7.686
s
s
1.597
1.882
0.380
0.844
3.460
2.776
r -0.930
Confidence Interval
1.43 + 1.055
-------
TABLE A-29 SUMMARY OF DATA FROM TEST NO. 15
Page 1 of 2
Degreaser A, operating
Solvent: 1,1,1-Trlchloroethane
FB 50 * PC x SC
InlcT
Other
_^_ -.-*«— —= A 50 »
Inlet air - Exhaust air x V 8 FfTinin
Top was closed one-half hour between each load cycle
Date 11/20/78
Ambient air
Temperature _65__"F
Pressure - jn. Hg
Humidity 42___*
Reading
No.
T, mln
W. Ib
AT, h
AW, Ib
rat, h
CAN. Ib
(£). '»"•
(8ft ™
X, 1b/h
3937. 000
3650. 400
1.
4003. 000
36*58. 600
-•
«_ •
4067. 000
.3672. 400
1.067
1 ?.. 800
1.067
1 3. 800
12.937
i 5 -q^T1
ik.. . -• i
1 "• O "• "'
1 c. . r :• i
3.
4129.000
3670. 900
1 . 0:3 ;:
-1.500
2. 100
12. 300
-\.45i'
5. 85T1
•3 0-3"
r . .' r i
4.
4196. 000
3669. 100
1. 117
-1.800
3.217
10.500
-1.6K:
3. 261
7. ^"V:
5.
4254. 000
3668. 000 .
0. 967
-1. 100
4. 18C:
9. 400
-1. 13?:
2. 247
6. 07*.
-------
TABLE A-29 (continued)
Page 2 of 2
Reading
No.
T, m1n
H, 1b
AT. h
AW. 1b
CAT. h
CAW. 1b
(ffll ">"•
(CAT). lb/h
X. lb/h
6.
4387. 000
2667. 300
2.217
-0. 700
6. 400
3. 700
-0.316
1.359
5. 1 3-::
i •
4464. 000
3664. 600
1.28:-:
-2. 700
7. 68 ::
6. 000
-2. 10<
0. 7SJ
4. 40:1:
8.
4485. 000
3664. 100
0. 350
-0. 500
8.03::
5. 500
-1.429
0. 685
O O"^ t
•_•• '-' ' v
4506. 000
3654. 300
n 8
Slope -1.092
Intercept 14.554
"yx
0.663
2.748
0.099
U.624
'a/2 2'447
r 0.706
Confidence Interval
+ 0.242
-------
TABLE A-30 SUMMARY OF DATA FROM TEST NO. 15
Page ] of 2
Degreaser B, operating
Solvent: IJJ-THchloroethane
Date 11/20/78
PC .x SC _^ A 50*
Exhaust air x V 8 ft/min
FB 50 *
Inlet air
Other
Top was closed one-half hour between each load cycle
Ambient'air
Temperature 62 "F
Pressure - in. Hg
Humidity 50 T,
Reading
No.
T, mln
W, 1b
AT. h
AW, 1b
EAT. h
EAW, 1b
(S). ""*
(M?). """
X. lb/h
3976. 000
27-P7. SOO
1.
4006. 000
2818. 300
2.
4070. 000
2S 15. 300
1.067
-3. 000
1.067
-3. 000
-2. 8K1
-2. si:-
-.2. Si:1
3.
4 13 1.000
23 U. 200
1.017
-1. 100
2. OS •:
-4. 100
-1.03C1
-1.968
-2. 3?0
4.
4200. 000
2812.400
1. 150
-1.800
•3. 23J:
-T.. 900
-1.56!.
-i *5^e;
1 . O.1 .'
- ' ^n "•
»_ . ». '-* •.
5.
4261.000
2811.500
1.017
-0. 900
4. 250
-6. 800
-0. 88«i
-1.600
-2. 05 J
-------
TABLE A-3n (continued)
Page
of
Reading
No.
T. m1n
W. Ib
AT. h
AW. Ib
CAT. h
CAW. Ib
(Sr) lb'h
\AT/,
(SO. 1Wh
X. Ib/h
43S6. 000
2S19. 500
4471.000
27i:il=i. ':nn
.
•
*
•
n 5 Syx 0.231 tQ/2 3.18
Slope 1.237 S^ 1.382 r Q.991
Intercept 1.663 S 0.089 Confidence Interval
d
Sb 1.484 1.237 +_ 0.283
Sr 0.866
L.
-------
TABLE A-31 SUMMARY OF DATA FROM TEST NO. 16
Page 1 of 2
Degreaser A, Idle
Solvent: 1,1,1-Trlchloroethane
(Boiling x ; nonboiling )
FB 50 % PC x SC x
Inlet air - Exhaust air x"
Other
Date 11/20778
A U %
V o ft/min
Ambient air
Temperature 60 °F
Pressure - in. Hq
Humidity 441
Reading
No.
T, m1n
W, 1b
AT. h
AW, 1b
EAT, h
EAH, 1b
(AT). lb'h
(TAT). lb/h
X. lb/h
45:31. 000
3666. 600
••
1.
4629. 000
3661. 700
2.
4688. 000
3659. 800
0. 98'::
-1.900
0.93::
-1.900
-1.93J1
-1.93:-
-1.93J:
3.
4749. 000
3657. 800
1.01?
-2. 000
j.1. 000
-3. 900
-1.967
- 1 . 950
-1.941
4.
4805. 000
3656. 400
0.933
-1.400
2. 930
-5. 300
-1.500
-1.807
-1.89t.
5.
4863. 000
3655. 000
0. 967
-1.400
3. 900
-6. 700
-1.44&
-1.718
-1.852:
00
-------
TABLE A-31 (continued)
Page 2 of 2
Reading
No.
T. mln
U. 1b
AT. h
AW, lb
EAT. h
EAW, lb
(*"} ih/h
I TTI ID/n
\AT/.
(fir) lb/h
X. lb/h
6.
4924. 000
3654. 400
1.017
-0. 600
4.917
-7. 300
-0.590
-1.485
-1.77?:
t •
4985. 000
3653. 000
1.017
-1.400
5.93C:
-8. 700
-1.377
-1.466
-1.72t-
8.
5046. 000
3651. 100
1.017
-1.900
6. 950
-10. 600
-1.869
-1.525
-1.698
•
vO
n 7
Slope -1.44
Intercept -0.985
yx
0.395
2.141
0.075
0.709
0.480
t ., 2.571
a/2
r -0.997
Confidence Interval
1.44 + 0.193
-------
TABLE A-32 SUMMARY OF DATA FROM TEST NO
Page 1 of 2
Degreaser B, Idle
Solvent: 1,1.1-Trichloroethane
(Boiling _x ; nonbolling )
FB 50 % PC x SC
Inlet air -_ Exhaust air
Other
A 0 %
V 0 ft/min
Date T1/20/78
Ambient air
Temperature 60 °F
Pressure - in. Hg
Humidity 44 %
Reading
No.
Tm4n
» imn
W, 1b
AT. h
AM. Ib
EAT, h
EAW, Ib
(ff). "•"•
(8ft """
X, 1b/h
1.
4*2*. finn
2SH":. -inn
2.
468ft. nrm
2!=inn. ^nn
0. 930
-3. 100
o.??::
-3. 100
-3. 151:
-3. 15-::
-3. 1^::
3.
4749. 000
27*ft. ^nn
1.0171
-1.400
2. 000
-4. 500
-1. 377
-2. 250
-2. 701
4.
4303.000
2797. 7nn
0. 900
-1.200
2. 900
-5. 700
-1. 333
-1.96"?.
-2. 45*.
5.
4 ft *n. nnn
27*7. nnn
0. 950
-0. 700
:3. S50
-6. 400
-0. 737'
-1.66;-
-2. 25£:
6.
4Q?3. nnn
°7e*ft nnn
1.050
-1.000
4. 900
-7. 400
-0. 952:
-1.510
-2. 10?:
•sj
o
-------
TABLE A-32 (continued)
Page 2 of _2_
Reading
No.
T, m1n
W, Ib
AT. h
AH, Ib
EAT, h
I AH, Ib
(£). lb/H
(fir). 1b/h
X. Ib/h
1 •
4984. 000
2795. 000
1.017
-1.000
5.917
-3. 400
-0. 98<-
-1.420
-1,993
8.
5045. 000
2794. 200
1.017
-0. 800
6. 933
-9. 200
-0. 787
-1.327
-1.898
n 7
Slope -1.21
Intercept -2.448
"yx
0.238
2.136
0.045
0.706
0.840
2.571
Confidence Interval
1.21 + 0.116
-------
TABLE A-33 SUMMARY OF DATA FROM TEST NO. 17
Page j_of _L
Degreaser A, Idle
Solvent: 1,1,1-THchloroethane
(Boiling x ; nonbolling )
FB 75 % PC _ x SC x
Inlet air -
Other
Exhaust air x
A 0 %
0ft/min
Date 11/21/78
Ambient air
Temperature 68 *p-
Pressure - In. Hq
Humidity 30 1
Reading
No.
T mln
W. Ib
AT. h
AH. Ib
EAT. h
CAU. Ib
(&} lh/h
V TT I lD/n
\AI/»
(Mr) lb/h
X. Ib/h
54*0. nnn
~:7J2. 5nfi
1.
5514. nnn
•2.
5571. nnn
0. 950
-0. 400
0. 950
-0. 400
-0.421
-0. 421
-0. 421
3.
5h.^:4. 000
^7::4. 100
1 . 050
-1.700
2. 000
-2. 100
-1.619
-1.050
-0. 73i
4.
5 A *-\. nnn
~\7~:?.. 5nn
0. 983
-0. 600
2. 933
-2. 700
-0.610
-0. 905
-0. 7-?-;-
5.
5753. 000
3733. 100
1.000
-0. 400
3. 983
-3. 100
-0. 400
-0. 77f:
-0. 759
-------
TABLE A-33 (continued)
Page 2 of 2
Reading
No.
T. mln
M, Ib
AT. h
AH. Ib
EAT. h
EAW. Ib
(S). ">"
(ft?). "">
X. Ib/h
6.
5814.000
3730. 900
1.017
-2. 200
5. 000
-5. '300
-2. 164
-1.060
-0. 343
i .
5871.000
3730. 100
0. 950
-0. 800
5. 950
-6. 100
-0. 84::
-1.02?;
-0. 873
8.
5932.000
3728. 500
1.017
-1. 600
6. 967
-7. 700
-1.574
-1. 105
-0. 906
3950. 000
3709. 800
-J
OJ
n 7
Slope -1.07
Intercept 0.7U8
Sy> 0.460
S 2.158
S 0.087
a
S. 0.709
D
S 0.693
t ., 2.571
a/2
r -0.994
Confidence interval
1.07 + 0.224
-------
TABLE A-34 SUMMARY OF DATA FROM TEST NO. 17
Page .1 of 2
Oegreaser B, Idle-
Solvent: 1,1,1-THchloroethane
(Boiling x ; nonboiling )
FB 75 % PC x SC x
Inlet air -_
Other
Date H/21/78
Exhaust air x
A 0 %
0 ft/mln
Ambient air
Temperature b8 °F
Pressure - In. Hg
Humidity ,30 t
Reading
No.
T, m1n
W. 1b
AT. h
AW, 1b
EAT, h
EAW. 1b
(S). ™
(M?). ""-
X, 1b/h
5451.000
2965. 000
1.
5512.000
2856. 900
2.
557?. 000
2855. 800
1.017
-1. 100
1.017
-1. 100
-1.082:
-i.os;:
-i. os;-
3.
5633.000
2855. 200
1.000
-0. 600
2. 017
-1.700
-0. 600
-0. 84':
-0. 962:
4.
5691.000
2854. 300
0. 967
-0. 900
2. 983
-2. 600
-0.931
-0. 872
-0.93*:
5.
5755. 000
2853. 800
1.067
-0. 500
4. 050
-3. 100
-0. 469
-0. 765
-0. 890
-------
TABLE A-34 (continued)
Page 2. of 2
Reading
No.
T. mln
H, Ib
AT. h
AU. Ib
EAT. h
EAU. Ib
(0. ""*
(Sft ">"•
X. Ib/h
6.
5813. OOCi
2853. 200
0. 967
-0. 600
5.017
-3. 700
-0. 62 J
-0. 73?:
-0. 860
7.
5870. 000
2852. 600
0. 950
-0. 600
5. 967
-4. 300
-0. 632:
-0.721
-0. 837
8.
5931.000
2852. 300
1.017
-0. 300
6. 983
-4. 600
-0. 295
-0. 659
-0. 811
5954. 000
2842. 500
*
w
n 7
Slope -0.660
Intercept 0.597
Syx 0.162
S 2.148
0.031
0.722
V2 2.571
r -0.996
Confidence Interval
0.660 + 0.080
0.267
-------
TABLE A-35 SUMMARY OF DATA FROM TEST NO. 18
Degreaser A, operating
Solvent: 1,1,1-Trlchloroethane
FB 75 X PC x SC x A 50 %
Inlet air . Exhaust air x V 8 TfTmln
Other
Date 11/21/70
Ambient air
Temperature - '
Pressure - In. 1
Humidity ~^~l
Page 1 of 2
Reading
No.
T( mln
W, 1b
AT, h
AW. 1b
tAT. h
CAN, 1b
(AT). lb/h
(fsr) lb'h
X, lb/h
1.
6109.000
3722. 200
2.
6168.000
3721.300
0. 983
-0. 900
0. 983
-0. 900
-0.915
-0.915
-0. 91!.
3.
6232. 000
3717.400
1.067
-3. 900
2. 050
-4. 800
-3.656
-2. 34 J
-1.62?:
4.
6292. 000
3716.000
1.000
-1.400
3. 050
-6. 200
-1.400
-2. 033
-1.763
5.
6350. 000
3713.800
0. 967
-2. 200
4.017
-8. 400
-2. 276
-2.091
-1.845
6.
6415.000
3711.500
1.083
-2. 300
5. 100
-10.700
-2. 123
-2. 09*
-1.896
-------
TABLE A-3S (continued)
Page 2 of 2
Reading
No.
T, m1n
W, Ib
AT, h
AW, Ib
EAT, h
CAW, Ib
(st9. lb/h
(ZM\ lb/h
\EAT /,
X, lb/h
7.
6467. 000
3710.400
0. 867
-1. 100
5. 967
-11.800
-1.269
-1.97*
-1.909
8.
6526. 000
3707. 300
0. 983
-3. 100
6. 950
-14.900
-3. 15C:
-2. 144
-1.94C:
.. •
n 7 S 0.606 t /. 2.571
J" "f ^
Slope -2.140 $x 2.144 r -0.998
Intercept o.blS S_ o.llb Confidence Interval
d
Sb 0.728 2.140 +_ 0.296
Sc 1.012
-------
TABLE A-36 SUMMARY OF DATA FROM TEST NO. 18
Page 1 of 2
Degreaser B, operating
Solvent: 1,1,1-THchloroethane
FB 75 *
Inlet air
Other
PC v SC
Exnaust air
A cn 1
V 8 ft/min
Date 11/21/78
Ambient air
Temperature °F
Pressure - in. Hq
Humidity - %
Reading
No.
T, mln
H, 1b
AT. h
AW, 1b
EAT, h
CAW, 1b
(S). "•"•
^EAW\ jD^h
X. Ib/h
1.
6109.000
2355. 000
2.
6172.000
2346. 700
1.050
-8. 300
1.050
-3. 300
-7. 905
-7. 905
-7. 905
3.
6231.000
2846. 700
0. 93;:
0. 000
2. 03 •:
-3. 300
0. 000
-4. 082'
-5. 993
4.
6296. 000
2844. 300
1.083
-2. 400
3. 117
-10.700
-2.215
-3. 433
-5. 140
5.
6348. 000
2342. 800
0. 867
-1.500
?. 983
-12.200
-1.731
-3. 063
-•*. 62J
6.
6413.000
2341.300
1.083
-1.000
5. 067
-13.200
-0. 923
-2. 605
-4.21?:
-J
00
-------
TABLE A-3b (continued)
Page _2_ of _2_
Reading
No.
T, fliln
U. Ib
AT. h
AW. Ib
CAT. h
CAW. Ib
(S 1b'h
X. lb/h
7.
6458. 000
2839.900
0. 750
-1.900
5.817
-15. 100
-2. 533
-2. 59«.
-?. 947
8.
6523. 000
2838. 500
1.08:!
-1.400
6. 900
-16.500
-1.292:
-2. 39J
-3. 72S
•
-
•• '
vO
n 7
Slope -1.800
Intercept -6.050
yx
0.538
2.090
0.105
0.752
2.581
t ., 2.571
a/2
r -0.976
Confidence Interval
1.800 + 0.270
-------
TABLE A-37 SUMMARY OF DATA FROM TEST NO. 19
1 of 2
Degreaser A, operating
Solvent: 1,1,1-Trlchloroethane
FB sn *
Inleiair
Other
PC y SC
Exhaust air
_50*
ft/mil
m1n
Date 11/22/78
Ambient air
Temperature 60 *F
Pressure In. Hq
Humidity ~~
Reading
No.
T, mln
N. Ib
AT, h
AN, Ib
EAT, h
CAN, Ib
(ST), 1b/h
(if). "•"•
X, Ib/h
1.
7331.000
3607. 100
2.
7383. 000
3605. 100
0. 867
-2. 000
0. 867
-2. 000
-2. 30*
-2. 30?:
-I1. 30?:
3.
7448. 000
3602. 400
1.083
-2. 700
1.950
-4. 700
-2. 492
-2.410
-2. 359
4.
7506. 000
3601.200
0. 967
-1.200
2.917
-5. 900
-1.24J
-2. 023
-2.247
5.
7566. 000
3598. 600
1.000
-2. 600
3.917
-8. 500
-2. 600
-2. 170
-2. 22?:
6.
7630. 000
3595. 300
1.067
-3. 300
4. 983
-11.800
-3. 094
-2. 368
-2. 256
00
o
-------
TABLE A-37 (continued)
Page 2 of 2
Reading
No.
T. mln
M, Ib
AT. h
AU. Ib
CAT. h
CAU. Ib
(M\ lh/h
I -rs- 1 ID/n
\AV.
(Hr) lb/h
X, lb/h
1 •
7689. 000
3592. 500
0. 983
-2. 800
5. 967
-14.600
-2. 847
-2. 447
-2.288
•
n 6 $„„ 0.606 t .. 2.776
yx o/t
Slope -2.43 Sx 1.903 r -0.998
Intercept 0.469 S. 0.142 Confidence Interval
O
S. 0.818 2.43 + 0.394
D —
S 0.644
09
-------
TABLE A-38 SUMMARY OF DATA FROM TEST NO. 19
Page 1 of 2
Degreaser B, operating
Solvent: 1,1,1-Trlchloroethane
FB 50*
Inlet air
Other
PC
SC
Exhaust air
A 50 *
V 8 ft/mln
Date 11/22/78
Ambient air
Temperature 60 *F
Pressure - In. Hg
Humidity 49 _*
Reading
No.
T, mln
W, 1b
AT, h
AM, Ib
EAT, h
EAN, Ib
(S). ""*
(8ft ">"•
X, 1b/h
1.
7326. 000
2772. 800
2.
7385. OOCi
2770. 300
0. 980
-2. 500
0. 983
-2. 500
-2. 54;:
-2. 542:
-2. 54?
3.
7444. 000
2767. 900
0. 983
-2. 400
1.967
-4. 900
-2. 44J
-2. 492:
-2.517'
4.
7507. 000
2765. 500
1.050
-2. 400
3.017
-7. 300
-2. 286
-2. 420
-2. 485J
5.
7567. 000
2763. 800
1.000
-1.700
4.017
-9. 000
-1.700
-2. 241
-2.424
6.
7625. 000
2761.900
0. 967
-1.900
4. 983
-10.900
-1.966
-2. 187
-2. 376
M
09
N)
-------
TABLE A-38 (continued)
Page 2 of 2
Reading
No.
T. mln
U. 1b
AT. h
AW. 1b
EAT, h
EAU. 1b
(M\ lh/h
1 TF 1 iD/n
W/,
fEAH\ lh/h
VESTA lb/h
X. lb/h
7.
7634. 000
2753. 200
0. 930
-3. 700
5. 967
-14.600
-3. 76C:
-2. 447
-2. 38?:
•
n 6 $„„ 0.567 t ., 2.571
yx a/c
Slope -2.31 - S^ 1.869 r -O.y99
Intercept -0.202 Sfl 0.136 Confidence Interval
Sb 0.86J 2.31 + 0.350
S0 0.715
00
C*>
-------
TABLE A-39 SUMMARY OF DATA FROM TEST NO. 20
Page _i_of 2
Degreaser A. operating
Solvent: 1.1.1-Trlchloroethane
Date 11/26/78
FB 50 I
Inlet air
Other
PC x SC
Exhaust air
ft/mi
In In
Ambient air
Temperature 53 °F
Pressure NA in. Hq
Humidity "88~"*
Reading
No.
T, mln
W, 1b
AT, h
AW, 1b
CAT, h
CAW, 1b
(AW\ lh/h
1 TT I IDf n
\«ji /•
(m). 1b/h
X, Ib/h
1.
8103.000
362?. 400
•
2e
3160. 000
3626. 600
0. 367
2. 800
0. 367
2. 800
3.J3/
3.231
.3. 2 -: t
~\m
3225. OUO
3626. 200
1.083
0. 400
1.950
3. 200
0.369
1 . 64 1
2. 4 :-:6
8233. noo
3621. 200
0. 967
5. 000
2.917
8. 200
5. 1 7J
2.311
2. 563
5.
3341.000
3618.500
0. ?&"
2. 700
3. 833
10.900
2.793
2. 807
2. t-J3
6.
3399. 000
3615. 900
0.967
2. 600
4.350
13.500
2.690
2.784
2. 655
00
-------
TABLE A-39 (continued)
Page 2 of 2
Reading
No.
T. min
U, Ib
AT. h
AU. Ib
CAT. h
I AW. Ib
(ir). lb/h
(fir). lb/h
X. lb/h
-.
84 64. 000
3*13. MJM
1. 083
2. 400
5.?::::
1 S. "HOO
2. 2 1 b
"^ - ,-, -
•I. • t1 'I1 '-'
"i " C" i
il • t1 _'
1
00
n 6
Slope 2.823
Intercept -0.515
Syx 1.074
0.257
0.327
1.553
2.78
r 0.996
Confidence interval
2.823 + 0.714
-------
TABLE A-40 SUMMARY OF DATA FROM TEST NO. 20
Degreaser B, operating
Solvent: 1,1,1-Trlchloroethane
Date 11/26/78
FB sflt
InleTaTF
Other
PC x SC
Exhaust air ,
A 70 *
a ft/mi
min
Ambient air
Temperature b3 °F
Pressure NA In. Hq
Humidity
Reading
No.
T, win
W. 1b
AT. h
AM, 1b
CAT. h
CAM. 1b
(S). «"•
(SOt "'"
X. 1b/h
i.
8163.000
"^Rm ^i ii i
.
•_ •
8221. 000
28 on. ftnn
0. ?&.'
2. 50U
o. ^tr
2. ^I.HJ
"• "^C'l.
C . J O t-
2. ^:>-
2. '"•":•
•:.
8280. 000
•"•"•'po 1 1 |fi
0. '?:? -:
2. TOO
1. 950
5. 200
2. 74*
2. i>
4.
S.::45. 000
2 7 96. hi'ifl
1.0 S3
1.500
3. 07: ::
6. "00
1. JW5
2. 2i r?
2. 4-.T
5.
8404. OOU
27*':. rnn
0.9:53
2. 900
4.017
9. 600
2. 9-* ?
2. 39IJ
2. 4*:. '
6.
34 69. 000
27*1. inn
1.0S3
2. 600
5. 100
12.200
2. 400
2. 392
2. 44*
or
-------
TABLE A-40 (continued)
Page 2 of 2
00
Reading
No.
T, mln
U. Ib
AT. h
AW. Ib
EAT. h
I AW, Ib
(M} Ih/h
I T-=- I iD/n
\AT/t
X. Ib/h
n 5 Syx 0.423 ^a/2 3.18
Slope 2.301
Intercept 0.306
\ 1.634
S, 0.130
d
Sb 1.050
S,. 0.609
r 0.999
Confidence interval
2.301 + 0.413
-------
TABLE A-41 SUMMARY OF DATA FROM TEST NO. 22
Page
of
Degreaser A, operating
Solvent: 1,1,1-THchloroethane
Date 12/21/70
FB 75 *
Inlet air
Other
PC
sc
aust air
A SO *
n ft/min
Amb i ent a'ir
Temperature 54 °f
Pressure - in. Hg
Humidity ~
Reading
No.
T, mln
N. Ib
AT. h
AN. Ib
EAT. h
CAN. Ib
(flM) Ib/h
(Uj*\ Ib/h
X, Ib/h
33531.000
3506. 500
3:?-f.4 l.ooo
3505. 10O
3 3 6 33.QOO
3496. ':'OO
1.
39012. 000
3495. 700
2.
39074. 000
3430. 000
1.03::
-15.700
1.03::
-15.700
-15. 194
-15. 194
-15. 194
3.
•39140.000
•3473. 200
1. 100
-1.300
2. 13::
-17.500
-1.63*.
-3.20::
-11. 69*
00
00
-------
TABLE A-t(\ (continued)
Page 2 of 2_
Reading
No.
T. min
U. Ib
AT. h
AU. Ib
EAT. h
EAU. Ib
(*"} ih/h
Iryl lb/h
\AT/.
(fir). lb/h
X. lb/h
4.
39193.000
3478. 000
0.88::
-0. 200
3.017
-17.700
-0. 22t-
-5. 867
-9. 755
5.
39249. 000
3475. 200
0.93::
-2. 800
3. 950
-20. 500
-3.000
-5. 190
•"' t! 1 "'
•_•• D 1 .'
6.
39310.000
•3473. 600
1.017
-1.600
4. 967
-22. 100
-1.57^
-4. 450
-7.781
1 •
39362. 000
3474. 000
0. 867
0. 400
5.83.::
-21.700
0. 461:
-3. 720
-7. 104
•
" 6 Sw, 0.787 t ., 2.776
y* o/e
Slope -1.399 S^ 1.788 r -0.949
Intercept -14.321 Sa 0.197 Confidence interval
d
Sb 0.928 1.399 + 0.547
Sc b.841
IX)
10
-------
TABLE A-42 SUMMARY OF DATA FROM TEST NO. 22
Page i of 3
Degreaser B, operating
Solvent: 1,1,1-Trlchloroethane
Oatc 12/21/73
FB 75 *
Inlet air
Other
PC x SC
Exhaust air
A sn *
V 8 ft/min
Ambient a*ir '
Temperature 54 °F
Pressure - in. Hg
Humidity 39 T,
Reading
No.
T, min
W, lb
AT. h
AW. lb
EAT, h
£AM. lb
(CT) lb/h
AAW) lb/h
X, lb/h
3857S.OOO
28S1. ::o0
3S611.000
2861. '-00
3S618.OOo
2? 3?. 'i'OO
1.
33651. 000
2:345. 600
2.
3:3715. 000
2846. 700
1.067
1. 100
1.067
1. 100
1.031
1.03J
1.031
3.
-3:3775. 000
2842. 300
1 . 000
-4. 400
2. 067
-3. 300
-4. 400
-1.597
-0. 2 S3
vD
-------
TABLE A-42 (continued)
Page 2 of 3
Reading
No.
T»
, aid
U. 1b
OTf IV
AT. h
AW. 1b
CAT. h
EAH. 1b
(10. ""*
(MO, »"•
•
X. 1b/h
4.
38839. 000
2R^Q cififi
£• "— " •' . • _ '» " '. •
1.067'
-2. 400
? 1 :: ":
-• • i _* .'
-5. 700
-2. 25fi
-1.81?
-0. 7?^.
5.
33898. 000
?:r;:: .5 inn
k— '-'-'.I X '_' '. '
0. 98::
-0. 800
4 1 17'
T • A A 1
-b. 500
-0.8 If
-1.57?
-0. 991
t-.
38?^h. nnn
2837. 200
0. 967
-1. 900
=!. rift':
-8. 400
-l.9t.ir.
-1.65;1
-i. i:::
1 •
"i^nis. nnn
2 ft •:'-:. r^n
0. 981:
-::. 450
6. 067'
-11.850
-3.508
-1.95]:
-i.2t.;-
3.
39074. 000
2333. 500
0.981:
-0. 250
7. 050
-12. 100
-0. 254
-1. 71t-
-1. 327'
9.
39133. 000
2831. 000
1.0671
-2. 500
3. 1 17
-14.600
-2. 344
-1.799
-1. 38t.
(continued)
-------
TABLE JV-42 (continued)
Page 3 of 3
Reading
No.
T, min
U. Ib
AT. h
AU. Ib
CAT. h
CAW. Ib
(fr) 1b/h
/EAW\ IK/h
(m). lb/h
X. lb/h
10.
-39191. 000
2829. bOO
0. 38?
-1.400
9. 000
-It-. 000
-1.535
-1.77?:
-1.429
11.
39249. 000
2823. 350
0. 9*7'
-1.250
9. 9*7
-17. 250
-1.2"?::
-1.731
-1. 459
12.
39317. 000
282*. 300
• 1. 13::
-2. 050
11. 100
-19. 300
-1.809
-1. 739
-1.485
13.
393*0. 000
282*. 200
0.717
-0. 100
11.317
-19. 400
-0. 14fi
-i. *4:-
~" * • ** . C*
vD
K>
n 12
Slope -1.836
Intercept 0.914
yx
1.033
3.554
0.088
0.392
1.484
la/2
1.812
r -0.997
Confidence interval
1.836 * 0.159
-------
TABLE A-43 SUMMARY OF DATA FROM TEST NO. 23
Page 1 of 3
Degreaser A. operating
Solvent: 1,1,1-Trichloroethane
PC
Date 12/22/78
FB 100 %
Inlet air -
Other
x SC
xhaust air x
50 X
7m~in
Ambient 'air
Temperature 50 *F
Pressure - in. Hg
Humidity 45 'I
Reading
No.
T, mln
M, Ib
AT, h
AH. Ib
EAT, h
CAU, Ib
(S). '""
(f»ljH i it 4k.
TTT-I lO/H
X. Ib/h
40002. 000
3548. 800
1.
40064. 000
3527. 400
tZ. •
40124.000
3531.500
1.000
4. 100
1.000
4. 100
4. 100
4. 100
4. 100
3.
40182.000
3529. bOO
0. 967
-1.900
1.9*7
2. 200
-l.9t.t-
1.111"
2. bOI'
4.
40254. 000
3528. 400
1.200
-1.200
3. 167
1.000
-1.000
0.3 It-
1.84S
5.
40298. 000
3527. 500
0. 73C:
-0. 900
3. 900
0. 100
-1.227
0. 02*.
1.390
lO
-------
TABLE A-43 (continued)
Page 2. of 3_
Reading
No.
T. nin
y. ib
AT. h
AM. Ib
I AT, h
IAU. Ib
(ir). 1b/h
f LuU \ • . **
I EAT/ '
X. Ib/h
6.
4036S. 000
3525. 300
1. 167
-1.700
5. 067
-1.600
-1.457
-0.316
1.049
i •
40414. 000
3523.900
0. 767
-1.900
5.33::
-3.500
-2. 473
-0. 600
0. 771
3.
40473. 000
3524. 700
1.067
0. 300
6. 900
-2. 700
0. 750
-0.391
0. 60S:
9.
40552. 000
3523.000
1.23::
-1.700
3. 13::
-4. 400
-1. 373
-0.541
0. 46-?
10.
40593. 000
3522. 000
0. 767
-1.000
8. 900
-5. 400
-1.304.
-0. 607
0. 345
11.
40660. 000
3520. 000
1.033
-2. 000
9. 933
-7. 400
-1.935
-0. 745
0. 23*.
(continued)
-------
TABLE A-43 (continued)
Page 1 of
Reading
No.
T. nin
y. ib
AT. h
AU. Ib
EAT. h
EAU. Ib
/AWN ....
1771 tO/n
\AT/,
1 — . . - 1 ib/ii
• •
X. Ib/h
12.
40717.000
35 IS. 400
0. ?50
-l.t-00
1 fi Q O "•
1 U. OC1-.1
-9. 000
-1.684
-0. 82?
0. 13^
•
•
n . 11 Syx 0.649 tQ/2 2.262
Slope -1.222 Sx 3.282 r -0.858
Intercept 4.881 S^ 0.063 Confidence interval
d
Sb 0.422 1.222 + 0.143
Sr 1 .840
-------
TABLE A-44 SUMMARY OF DATA FROM TEST NO. 23
Page
of
Degreaser B, operating
Solvent: 1,1,1-Trlchloroethane
12/22/78
FB inn *
Inlet air
Other
PC x SC
Exhaust air
A 50 *
8 ft/mln
Ambient air
Temperature - *F
Pressure - in. Mq
Humidity ~T~T;
Reading
No.
T, mln
W, 1b
AT, h
AW, 1b
ZAT, n
CAW. 1b
(&} Ih/h
I TT 1 * v/n
\AT/,
X. Ib/h
40030. 000
2927. 100
1.
40088. 000
2912.200
2.
40135. OOCi
2907. 000
0. 73.::
-5. 200
0.78::
-5. 200
-6. 63*
-6. 638
-6.63P
3.
40245. 000
2906. 500
1.833
-0. 500
2. 617
-5. 70fi
-0.27::
-2. 173
-4. 40?:
4.
4029-:.. 000
2QnK. nnn
0. 850
-0. 500
3. 467
-6. 200
-0. 533
-1.78P
-3. 53«:
5.
40-35t.. 000
,Qn4 snf|
1.000
-1.500
4. 467
-7. 700
-1.500
-1.724
-?. os;:
sO
-------
TABLE A-44 (continued)
Page 2 of 2
vD
>J
Reading
No.
T, min
U. Ib
AT. h
AU. Ib
CAT. h
CAW. Ib
Of). ™
(fir). lb/h
x. lb/h
6.
40414. OOO
2905. 000
0. 967
0. 500
5.43::
-7. 200
0.517
-1.325
-2.731
i •
40473. 000
290':. 20fi
1.067
-1.800
6. 500
-9. 000
-1.687'
-1.385
-2. 50*
8.
4fici4 ':. nnn
••*ni. snn
1.081:
-1.700
7. 58;:
-10.700
-1.569
-1.411
-2. 350
j
405°ft. nnn
2902. 750
0.917
1.250
8. 500
-9. 450
1 . 364
-i. n:-
-2. 195
10.
40654. 000
2897. 900
0.93::
-4. 850
9.43::
-14.300
-5. 196
-1.516
-2. 120
11.
407 IS. 000
2896. 900
1.067
-1.000
10.500
-15.300
-0. 937
-1.457
-2.05::
n 10
Slope -1.031
Intercept -2.962
s
s
1.349
3.140
0.143
0.496
2.468
lo/2 2-306
r -0.983
Confidence Interval
1.031 + 0.330
-------
TABLE A-45 SUMMARY OF DATA FROM TEST NO. 25
Page l of 5
Degreaser A, operating
Solvent: 1,1,1-Trichloroethane
1/15/79
FB _50 t
Inlet air
Other
PC x SC
x "Exhaust air
w
ft/m
mi n
Date _
Ambient'air
Temperature 61 °F
Pressure - in. Hq
Humidity 23 *
Reading
No.
T. mln
H. lb
AT. h
AH, lb
CAT. h
CAW. lb
(S). ">"
(far). lb/h
X, lb/h
1.
76746. 000
3392. 500
2.
76S11. 000
3333.600
1.081:
-3.900
i.os::
-3. 900
-3.600
- 3. 600
-3. 600
•— ' •
76375. 000
3337.900
1.067
-0. 700
2. 150
-4. 600
-0. 65t.
-2. 140
-2. 370
4.
76936.000
3384.000
1.017
-3. 900
3. 167
-8. 500
-3. 33t.
-2. 681
-2. 303
5.
77007. 000
3330. 500
1. 13C:
-3. 500
4. 350
-12.000
-2. 953
-2. 759
-2. 79t-
6.
77075. 000
3380. 500
1. 13C:
0. 000
5. 483
-12.000
0. 000
-2. 183
-2.674
\D
CD
-------
TABLE A-45 (continued)
Page 2 of 5
Reading
No.
T. «tn
U. Ib
AT. h
AH. Ib
I AT. h
IAM. Ib
GO. '*•
(M?). »"•
X. Ib/h
i .
77136. 000
5377.500
1.0171
-3.000
6. 500
-15.000
-2. 95 J
-2. '305:
-2.61:::
8.
77202. 000
3377.000
1. 100
-0. 500
7. 600
-15.500
-0. 455
-2. 0.3':'
-2.531
9.
77259. 000
3375. 000
0. 950
-2. 000
8. 550
-17.500
-2. 105
-2. 047
-2.471
10.
77-325. 000
3-372. 500
1. 100
-2. 500
9. 650
-20. 000
.-, .-, -i .;
>-• •_ 1 .*
-2.07::
-2. 42t.
11.
?7-38'3. 000
3370. 500
0. 967
-2. 000
10.617
-22. 000
-2. 069
-2. 07;:
-2. 391
12.
77442. 000
3368. 250
0. 983
-2. 250
11.600
-24. 250
-2. 28£:
-2. 091
-2. 361
vO
(continued)
-------
TABLE A-45 (continued)
Page j_ of 5 _
Reading
No.
T. ntn
U. Ib
AT. h
AM. Ib
I AT, h
EAU. Ib
(30. "•»
(i£r). lb/h
X. 1b/h
13.
77507. 000
3366. 900
1.083
-1. 350
12.68::
-25. 600
-1.24t.
-2.01?:
-2. 33S
14.
77572. 000
3365. 500
1.083
-1.400
1 _• . i t- 1
-27. 000
-1.29;- •
-1.961
-2. 30t.
15.
77621. 000
3364.000
0.317
-1.500
14.58-::
-28. 500
-1.837
-1.95^
-2.231
16.
776S9. 000
3362. 000
1. 13::
-2. 000
15.717
-30. 500
-1.76!.
-1.941
-2. 25?:
17.
77747. 000
3359.500
0. 967
-2. 500
16.683
-33.000
-2. 58t.
-1.97?:
-2.241
18.
77804. 000
3358. 500
0. 950
-1.000
17.633
-34. 000
-1.053
-1.92?:
-2. 222
O
O
(continued)
-------
TABLE A-45 (continued)
Page -4_ of
Redding
No.
T. «in
y. ib
AT. h
AM, Ib
I AT, h
IAU, )b
(Sft ""»
W/»
(zir). lb/h
X, lb/h
19.
77872. 000
3356. 500
1. 13::
-2. 000
18.767
-36.000
-1.765
-1.918
-2. 20*.
20.
77920. 000
3354.500
0. 800
-2. 000
19.567
-38.000
-2. 500
-1.94:-
-2. 19J1
21.
77982. 000
3353.600
1.030
-0. 900
20. 600
-38.900
-0.871
-1.88:;:
-2. 17t.
22.
78049. 000
3351. 200
1. 117
-2. 400
21.717
-41.300
-2. 149
-1.90J:
-2. 16::
23.
78118.000
3349. 000
1. 150
-2. 200
22. 867
-43. 500
-1.913
-1.902
-2. 152
24.
78177.000
3347. 800
0. 980
-1.200
23. 850
-44. 700
-1.220
-1.374
-2. 139
K>
O
(continued)
-------
TABLE A-45 (continued)
Page 5 of j>
Reading
No.
T, «in
U. Ib
AT. h
AU. Ib
CAT. h
CAU. Ib
AAU\ IK/K
(m). Ib/h
X, Ib/h
25.
78244. 000
3345.400
1.117
-2. 400
24. 967
-47. 100
-2. 149
-1.887
-2. 129
26.
78275. 000
3344. 000
0.517
-1. 400
25. 4 81:
-48. 500
-2.710
-1.90::
-2. 120
:.-
78296. 000
3345. 900
0. 350
1.900
25.83::
-46. 600
5. 429
-1.804
-2. 10:1:
to
o
N>
n 26
Slope -1.775
Intercept -2.683
s
s
0.782
7.755
O.U20
0.170
1.711
2.064
r -0.999
Confidence interval
1.775 + 0.041
-------
TABLE A-46 SUMMARY OF DATA FROM TEST NO. 25
Page
of
Degreaser B, operating
Solvent: 1,1,1-THchloroethane
FB 50 *
Inlet air x
Other
PC x SC
_ Exhaust air _x
*_ A 50. *
V 8 *t /m in
Ambient' air
Temperature 61 '
Pressure - in. 1
Humidity 28 *
Date 1/15/79
*F
q
Reading
No.
Tv min
W, 1b
AT. h
AW. 1b
EAT, h
EAW, 1b
(I?). ""*
(Sft ™
X, Ib/h
7532?. 000
2742. 500
75341. 000
2741.500
1.
75414. 000
2740. 000
-.
hi •
75493. 000
27 •-:*. SOO
1. 317
-0. 500
1.317
-0. 500
-0. 330
-0. 380
-0. 330
"3.
755t-5. 000
2736. 400
1.200
-3. 100
2.517
-'3. 600
-2. 53::
-1. 430
-0. 903
4.
75631.000
2734. 000
1. 100
-2. 400
3.617
-6. 000
-2. is::
-1.65?
-1. 15*.
10
o
CJ
-------
TABLE A-46 (continued)
Page 2 of
Reading
No.
Tnlit
i Bin
U. Ib
AT. h
AU, Ib
I AT, h
E6U. Ib
(8). ""•
(fift »•"•
•
X. 1b/h
5.
75694. 000
2732. 000
1.050
-2. 000
4. 667
-3. 000
-1.905
-1.7H
-1.29t.
6.
75760. 000
2730. 500
1. lOCi
-1.500
5. 767
-9. 500
-1. 36*-
-1.647
-1. 36t.
^
I •
75319. OOn
2727. 500
0. 93 1:
- 3. 000
b. 750
-12.500
-3. 051
-1.35J1
-1.447
8.
7 sap 4. non
2724. 500
i.os::
-3.000
7.8?-::
-15.500
-2. 769
-1.979
- 1 . 52-::
9.
7F.-34*. nnn
2720. 500
i.os::
-4. 000
8.917
-19.500
-3. 69J:
-2. 187
- 1 . 606
10.
76014.000
2719.000
1.08.':
-1.500
10.000
-21.000
-1.335
-2. 100
-1.661
(continued)
-------
TABLE A-46 (continued)
Page 3 of 5_
N)
O
VI
Reading
No.
T, nin
U. Ib
AT, h
AU, Ib
EAT, h
EAU. Ib
(ir). lb/h
(IAT), 1b'h
1. lb/h
11.
76079. 000
2713.250
1.03::
-0. 750
11.081:
-21.750
-0. 692
-1.9621
• -1.691
12.
761-38. 000
2716. 000
0. 98.;:
-2. 250
12.067
-24. 000
-2. 23?:
-1.939
-1.71?:
13.
76189.000
2714.300
0. 350
-1.200
12.917
-25. 200
-i.4i:-
-1.951
-1.73?:
14.
76255. 000
2712.500
1. 100
-2. 300
14.017
-27. 500
-2.091
-1.96::
-1.755
15.
76312. 000
2710.000
0. 950
-2. 500
14.967
-30. 000
-2. 63::
-2. 004
- 1 . i > %••
16.
76373. 000
2709. 500
1. 100
-0. 500
16.067
-30. 500
-0. 455
-1.89?:
-1.731
(continued)
-------
TABLE A-46 (continued)
Page _$_ of
Reading
No.
T. Bin
V. Ib
• •
AT. h
AU. Ib
CAT. h
IAU. Ib
(3). "•»
f £AU\ IL»».
vorJ '
-
I. lb/h
17.
76429. 000
2708. 000
0. 850
-1.500
16.917
-32. 000
-1.765
-1.89;:
7 1.78?:
18.
76472. 000
2706. 500
0.717
-1.500
17.633
-33.500
-2. 093
-1.900
-1. 795
19.
76550. 000
2705. 600
1.300
-0. 900
13.93::
-34.400
-0. 692
-1.817
-1.796
20.
76637.000
2704. 600
1.450
-1.000
20. 383
-35. 400
-0. 690
-1.737
-1.79 3
21.
76714.000
2699. 200
1.28;:
-5. 400
21.667
-40. 800
-4. 20S:
-1.883
-1.797
22.
76780. 000
2695. 900
1. 100
-3. 300
22. 767
-44. 100
-3. 000
-1.937
-1.804
(continued)
-------
TABLE A-46 (continued)
Page 5 of 5
Reading
No.
T, n1n
M. Ib
AT. h
AU. Ib
EAT. h
IAN. Ib
(6M\ 1h/h
I Tr" 1 •O/n
\AT/,
(ffr). lb/h
X. lb/h
23.
76845. 000
2693. 800
1.08C:
-2. 100
23. 850
-46. 200
-1.938
-1.937
-1.810
24.
76906. 000
2692. 000
1.017
-1.800
24. 867
-48. 000
-1.770
-1.930
-1.81?:
25.
76974. 000
2688. 800
1. 13':
-3. 200
26. 000
-51.200
-2. 82<
-1.969
-1.82:-
26.
76987. 000
2690. 500
0.217
1.700
26.217
-49. 500
7. 84t-
-1.888
-1.8*
.
n 25 Syx 1.358 tQ/2 2.069
Slope -1.936 Sx 7.738 r -1.000
Intercept 0.435 Sfl 0.036 Confidence Interval
Sb 0.178 1.936 + .074
S,. 2.202
o
-J
-------
TABLE A^i? SUMMARY OF DATA FROM TEST NO. 26
Page 1 of 5
Oegrcascf B, operating
Solvent: 1,1,1-Trichloroethane
Date 1/18/79
FB 50 I
Inlet air x
Other
PC
x SC
xhaust air
A
8
70 r-*
nnn
Extensive problems with Degreaser A
Ambient' air'
Temperature - °F
Pressure - in. Hg
Humidity - I
Reading
No.
T, m1n
U. lb
AT, h
AW, lb
EAT, h
CAW. lb
(AT). lb/h
flM\ lh/ll
l TTT i io/n
\EAI/,
X. Ib/h
78426. OOO
2859.000
78449.000
2853.000
78459.00C
2854.OOC
1.
7S493.00i:i
2853. 000
kl •
78536.000
2353. 000
0.717
0. 000
0.717
0. 000
0. 000
0. 000
0. 000
3.
73609. 000
2351.250
1.217
-1.750
1.9-3::
-1.750
-1.435:
-0. 905
-0. 45'l:
O
OP
-------
TABLE A-47 (continued)
2 of 5
Reading
No.
T. nin
U. Ib
AT. h
AU. Ib
CAT. h
CAU. Ib
/AU\
f um 1 1 t> 1 1»
iTrJ ID/n
\AT/,
(fir) lb/h
. ib/n
4.
78669. 000
2850. 000
1.000
-1.250
2.93::
-3. 000
-1.250
-1.02::
-0. £4":
5.
78731.000
2847. 000
1.03::
-3.000
.3. 967
-6. 000
-2. 90::
-1.51::
-fl. fthfi
6.
73792. 000
2845. 500
1.01 7
-1.500
4. 93.":
-7. 500
-1.475
-1.505
•• iH i O '— * *• I
-
733-19. 000
2341. 500
0. 950
-4. 000
5. 93::
-11.500
-1.211
-1.93?:
-1. 147
8.
73916. 000
2839.250
1. 117
-2. 250
7. 050
-13.750
-2.015
-1.950
. 26?
9.
78972. 000
2834.900
0. 93,::
-4. 350
7. 98 ::
-18. 100
-4.661
-2. 267
_ 1 '5OO
1 . o o t-
(continued)
-------
TABLE A-47 (continued)
Page _a_ of _5_
Reading
No.
T. mln
U. lb
AT. h
AU. lb
EAT. h
EAU. lb
(AT). lb/h
AAM\ lb/h
^EAT;, lb'h
X. lb/h
10.
79028. 000
2834. 700
0.933
-0. 200
8.917
-18. 300
-0.214
-2. 05::
-1.46:-
11.
79089. 000
2832. 500
1.017
-2. 200
9. 93J:
-20. 500
-2. 16?
-2. 06*
-1.52::
12.
79155. 000
2830.200
1. 100
-2. 300
11.03::
-22. 300
-2.091
— ^ O £ t
-1.57}
13.
79213.000
2327. 500
0. 967
-2. 700
12.000
-25. 500
-2. 79::
-2. 125
-1.617'
14.
79279. 000
2826. 000
1. 100
-1.500
13. 100
-27. 000
-1.361
-2. 061
-1.65:1
15.
79330. 000
2826. 000
0. 850
0. 000
1 3. 950
-27. 000
0. 000
-1.935
-1.67:-
(continued)
-------
TABLE A-47 (continued)
Page 4 of 5
Reading
No.
T. min
W. Ib
AT. h
AU. Ib
EAT. h
EAU. Ib
(Ir) lb/h
(i?). •"
X, lb/h
16.
79391.000
2822. 750
1.017
-3. 250
14.967
-30.250
-3. 197
-2.021
-1.695
17.
79446. 000
2821.400
0.917
- 1 . 350
15.881:
-31.600
-1.47.;:
-1.990
-1. 71-
18.
79508. 000
2820. 200
1.031:
-1.200
16.917
-32.800
1 1 ' 4
-1.9 39
-1.727
19.
79572. 000
2819.200
1.067
- 1 . 000
17.983
-33. 800
-0. 937
-1.880
-1.735
20.
79633. 000
2816.400
1.017
-2. 800
1 9. 000
-36. 600
-2. 75<-
-1.926
-1.745
21.
79699. 000
2815.500
1. 100
-0. 900
20. 100
-37.500
-0. 8 If:
-1.866
-1.751
(continued)
-------
TABLE A-47 (continued)
Page 5 of 5__
Reading
No.
T, min
U. Ib
AT. h
AW, Ib
I AT, h
CAU. Ib
®. ""*
/fAU\
(ZAT) lb/h
.
X. lb/h
22.
79759. 000
2314. t-OO
1. 000
-0. 900
21. 100
-33.400
-0. 900
-1.820
-1.755
23.
79330. 000
281 3. 000
i. is::
- 1 . bOO
22.23::
-40. 000
-1.35;1
-1. 795
-1. 75*.
24.
79390. 000
2310. 500
1 . 000
-2. 590
^1 -• • hi, Z1 . •
-42. 500
-2. 500
-1. 325
-1.759
25.
79947. 000
2309. 500
0. 950
-1. 000
24.23::
-43.500
-1.051:
-1. 795
-1.761
79931. 000
2303. 750
CO
n 24
Slope -1.836
Intercept -0.148
yx
7.161
0.052
0.174
1.204
la/2 2'074
r -1.000
Confidence interval
1.886 + 0.108
-------
TABLE A-48 SUMMARY OF DATA FROM TEST NO. 20.
Pag* J of 5
Degreaser A, operating
Solvent: 1,1,1-THchloroethane
Date 1/20/79
FB 125 <
Inlet air x
Other
PC x SC _x_
Exhaust air x
A
V 8
70 %
7m in
Ambient air
Temperature 70 *F
Pressure - in. Hg
Humidity 4b %
Reading
No.
T, m1n
H. Ib
AT, h
AW. Ib
EAT, h
CAW, Ib
(51). 1b>"
(if) lb'h
X, Ib/h
31345. 000
3696. 850
•
31379. 000
3692. 500,
31 390. 000
3692. 500
1.
31422. 000
3691.000
2.
31492.000
3687. 600
i. ur
-3.400
1. It 7
-3. 400
-2.911
-2.914
-2.914
3.
SI 549. 000
3686. 500
0. 950
-1. 100
2. 117
-4. 500
-1. 15?:
-2. 12*.
-2.520
U)
-------
TABLE A-48 (continued)
Page 9 of ^
Redding
No.
T, min
U. 1b
. » •
AT. h
AU. 1b
CAT. h
CAU. 1b
(sft w
\AT/,
(fir) lb'h
X. lb/h
4.
81607.000
3685. 000
0. 967
-1.500
3. 031:
-6. 000
-1.55::
-1.946
. -2. 329
5.
31673.000
3682. 000
1. 100
-3. 000
4. is::
-9. 000
-2. 727
-2. 151
-2. 234
6.
31733.000
3680. 500
1.081:
-1.500
5. 267
-10. 500
-1. 385
-1.994
-2. 22-..
i .
81797. 000
3678. 500
0.93::
-2. 000
6. 250
- 1 2. 500
-2. 034
-2. 000
-2. 139
8.
81857.000
3677. 500
1.000
-1.000
7. 250
-13.500
-1.000
-1.86J1
-2. 14:-
9.
81920. 000
3675. 750
1.050
-1.750
3. 300
-15.250
-1.667
-1.837
-2. 104
(continued)
-------
TABLE &4B (continued)
Page 3 of _5_
N)
t-«
tn
Reading
No.
T, nin
U. Ib
AT. h
AW, Ib
EAT. h
£AU. Ib
(*»} Ih/h
i —s i iD/n
\AT/.
/fAU\
(nr) 1b/h
.
X. Ib/h
10.
81972.000
3675. 250
0. 867
-0. 500
9. 167
-15.750
-0. 577
-1.718
-2. 061
11.
82038.000
?67:3. 250
1. 100
-2. 000
10.267
-17.750
-1.818
-1.729
-2. 02?:
12.
82091.000
3670. 500
0. '38::
-2. 750
11. 150
-20. 500
-3. 11'.:
-1.8:39
-2.011
13.
82151.000
3670. 000
1.000
-0. 500
12. 150
-21.000
-0. 500
-1.728
-1.987
14.
82220. 000
3667. 000
1. 150
-3.000
1 3. 300
-2-*. 000
-2. 609
-1.305
- 1 . 97-1:
15.
82274. 000
3662. 500
0. 900
-4. 500
14.200
-28. 500
-5. 000
-2. 007
-1.975
(continued)
-------
TABLE A-48 (continued)
Page 4 of _5__
IS)
Reading
No.
T. ntn
y. ib
AT. h
AU. Ib
EAT. h
EAU. Ib
(AT) lb/h
(ir) lb'h
X. lb/h
16.
82346. 000
3651.700
1.200
-10.300
15. 400
-39. 300
-9. 000
-2. 55£
. -2.014
17.
32430.000
3661.200
1.400
9. 500
16.300
-29. 800
6. 786
-1.77*
-1.999
18.
82457. 000
3660. 700
0. 450
-0. 500
17.250
-30. 300
-1. Ill
-1.757
-1.935
19.
32521.000
3653. 700
1.067
-2. 000
18.317
-32. 300
-1.875
-1. 761:
-1.97::
20.
32594. 000
3657. 000
1.217
-1.700
19.533
-34.000
-1. 397
-1.741
-1.960
21.
32633. 000
3656. 200
0.73::
-0. 800
20. 267
-34.300
-1.091
-1.717
-1.94?:
(continued)
-------
TABLE A-48 (continued)
Page 5 of 5
Reading
No.
T, min
W, Ib
AT, h
AM, Ib
EAT. h
EAW. Ib
(XT) ">/"
\AT/,
X, Ib/h
22.
82699. 000
3655. 100
1.017
-1. 100
21.28;:
-35.900
-i.os::
. 68 r
-1.93*.
2.3.
82756. 000
3654. 100
0. 950
-1.000
22. 2?;:
-36.900
-1.05;:
. 6*0
-1.923
24.
32320. 000
'3651. 100
1.067
-3.000
23. '300
-39.900
-2. SK1
1-^ 4 'i
. i K
-1.91'
25.
32374. 000
3649. 600
0. 900
-1.500
24. 200
-41.400
-1.667
i ~* i i
i . f ii
-1.905
82912. 000
3649. 000
82935.000
'3650. 500
rs>
n 24
Slope -1.676
Intercept -1.805
Syx 2.720
Sx 7.129
Sa 0.080
d
Sb 0.181
S 2.537
ta/2 • 2.074
r -1.000
Confidence interval
1.676 + .166
-------
TABLE A-49 SUMMARY OF DATA FROM TEST NO. 28
Page j__ of 5
Degreaser B, operating
Solvent: 1,1,1-THchloroethane
PC
FB 125 I
Inlet air
Other
x SC _
xhaust air x
A 70 I
8 ft/min
Date 1/20/79
Ambient'air
Temperature 70 °F
Pressure - in. Hg
Humidity 4b t,
Reading
No.
T, min
H, 1b
AT, h
AW, 1b
EAT. h
CAW, Ib
($). ">'"
(§?). ">"•
X, 1b/h
Si ">lv nrtri
1 -• J<_. L"JL'
3040. 750
81-377. 000
303?. 000
ftl':fi7. 000
3039. 400
1.
81422.000
303?. 000
o
t_ •
81492.000
3036.000
1. 16T1
-3. 000
1. 167
-3. 000
-2. 57J
-2. 571
-2.571
3.
815^3.000
3033.700
0. 850
-2. 300
2.017
-5. 300
-2. 70*.
-2. 625:
-2. 600
CO
-------
TABLE A-49 (continued)
Page 2 of jj_.
Reading
No.
T. nin
W. 1b
AT. h
AW. 1b
CAT. h
CAW. Ib
(ir) lb/h
(fir) lb/h
X. 1b/h
4.
81602.000
3032. 500
0.98::
-1.200
3. 000
-6. 500
-1.220
-2. 167
-2. 455
,.
81673. 000
3030. 250
1. 18::
-2. 250
4. ISO
-8. 750
-1.90J
-2. 09::
~ fcl • !• O *f
6.
81732.000
3023. 500
0. 98'::
-1.750
5. 167
-10.500
-1.730
-2.031:
-2. 29?:
I •
81797.000
3026. 750
i.os::
-1.750
6. 250
- 1 2. 250
-1.615
-1.960
-2. 24J1
8.
31359.000
3026. 000
1.03:::
-0. 750
7. 28^:
-13.000
-0. 726
-1.785
-2. 176
9.
81915.000
3025. 000
0.930
-1.000
8.217
-14.000
-1.071
-1.70*
-2. 117
vC
(continued)
-------
TABLE £.39 (continued)
Page 3 of 5
N)
N>
O
Reading
No.
T, nin
U, 1b
AT. h
aw, tb
EAT, h
EAH. 1b
(80. 1Wh
(Mr). »"•
•
X. Ib/h
10.
81975.00111
3024. 500
l.OOCi
-0. 500
9. 217'
-14.500
-0. 500
- 1. 57-.!
-1 nc--'
• •! . U j i
11.
82044. 000
•3023. 500
1. 150
-1.000
10. 367
-15.500
-0. 870
-1.495
-2. 00 J
12.
82091. 000
3022. 500
0.78::
-1.000
11. 150
-It-. 500
-1.277
-1.480
-1.95::
13.
32162. 000
3020. 000
1. IS'!:
-2. 500
12. 33::
-19.000
-2. 1 1 ::
-1.541
-1.919
14.
82272. 000
3016.000
1.831:
-4. 000
!•». 167
-23. 000
-2. is::
-1.624
-1.89*.
15.
82343. 000
3015.500
1. 18::
-0. 500
15. 350
-23.500
-0. 42^:
-1.53J
-1.370
(continued)
-------
TABLE A-4q (continued)
Page 4 of 5
M
K)
Reading
No.
T. m\n
U. lb
AT. h
AU, lb
EAT, h
EAU. lb
(ir) lb/h
\EAT/.
X. lb/h
' 16.
82421.000
3012.200
1.300
-3. 300
' 16.650
-26. 800
-2. 53?:
-1.610
. -1.350
17.
82462. 000
3011. 100
0. 683
-1. 100
17.330
-27. 900
-1.610
-1.610
-1.83?:
13.
82525. 000
3009. 700
1.050
-1.400
18.380
-29. 300
-1.330
-1.59
-------
TABLE A-49 (continued)
Page 5 of 5
Reading
No.
T, Riln
W, 1b
AT. h
AW. Ib
EAT. h
EAH, Ib
(fit ""*
(SOL ">"•
«. lb/h
22.
82756. OOCi
3005. 000
0. 950
-0. 800
22. 233
-34. 000
-0. 842:
-1.529
-1.772:
23.
82822. 000
3002. ?00
1. 100
-2. 100
23. 333
-36. 100
-1.90?
-1.547
-1.761
24.
323". OOCi
3001.500
0.917
-1.400
24. 250
-37. 500
-1.527
-1.546
-1.752:
82910. 000
3000. 100
32943. 000
3001.500
i
K)
N>
n 23
Slope -1.455
Intercept -1.982
Syx 0.801
Sx 7.312
Sa 0.023
0.182
2.080
r -1.000
Confidence Interval
1.455 + .048
0.722
-------
TABLE A-50 SUMMARY OF DATA FROM TEST NO. 29
1 Of 6
Degreaser A. operating
Solvent: 1,1,1-THchloroethane
FB T?R I
Inlet air
Other
PC x SC
Exhaust air x
V 8
Ft/ml i
in In
Date 1/21/79 •
Ambient air
Temperature 69 °F
Pressure NA in. Hg
Humidity "
Reading
No.
T, m1n
M, Ib
AT. h
AW. Ib
tAT, h
CAW. Ib
(jjr). Ib/h
(fsr). 1b'h
X. Ib/h
85004. 000
*«. .00
y5D18. OUO
3 6: 3 5. i'OO
85039. 000
>1.50. 400
05055. 000
i.
85U85. 000
-!|:.45. 000
2.
S5143. 000
3642. 300
1.050
2. 200
1.050
2. 200
2.095
2. 095
2. 095
10
2. 095
-------
TABLE A^SO (continued)
Page 2 of 6
Reading
No.
T. m\n
y. ib
• • ^
AT. h
AV, Ib
£AT. h
IAU. Ib
(AT) 1b/h
(MO. "»*
1. Ib/h
i fc
:':'5193. OUO
0.8.^
2. 200
1.883
4. 400
2. t-40
2. -3::*
,.
85259. OOU
3637. nnn
1 . 0 1 7
3. 6 no
2. ?no
8. On,.
3.54J
r* -"."i"*
t,
S5333. nnn
1.2:-:?
6. 3 "JO
4. 133
14.300
5. 5;4
3. 5yl
™i * i *i
•^ • :• i •
i •
LI'."* 51?. nnn
•IN ':n. --:nn
1. 050
2. 200
b. 2^3
14.200
2. 0°5
2. 273
' Sh
!:I.
y 55 18. 000
0.9S3
3. 000
7.217
1 7. 200
:3. 051
2. 3-33
2. 5 :!5
N)
(continued)
-------
TABLE A-50 (continued)
Page 3 of 6
Reading
No.
T. ain
U. Ib
AT. h
AM. Ib
EAT. h
IAU. Ib
(IT) lb/h
(isr). lb>"
•
X. Ib/h
9.
37583. Oi in
3625. 000
1. 167
2. 300
8. 3-3.3
20. 000
2. 400
2. -jt;6
2.eJlT*
i'l.
35642. 000
3622. 770
0. *on
2. 250
?. 233
22. 250
2.5HO
2. 397
-' *~ \ \ •'
1 i.
t:5701. nOO
3620. 500
0.933
2. 250
10. 2^7
24. 500
2. 2 as
T» '• '• i.
::. * :-..
i,-'.
35317. 0"Ll
3616. Oi.'O
!.«•»
4. SuO
12.2MO
29. fl'JO
we ."ll . O
2. 377
.i, - :
13,
••••77bl. CM.IIJ
3617. 2ir.O
-0.933
-1.250
11. 2t."
27. 750
1.339
*^ *• J'.'lJ
7 !•_!
i. • '* 'T1 1
14.
87377. 000
3612. 000
1.933
5. 250
1 3. 200
•33.000
2.716
2. -it .:
2.4:1:'.
(continued)
-------
TABLE A-50 (continued)
Page 4 of 6
Reading
No.
T. aln
UlK
• ID
AT. h
AM, 1b
IAT, h
IAU. 1b
(AT) 1b/h
V^TA
1. tb/h
».
•-S041 nnn
•3610. f 5 0
. 06.
1.2^0
14.267
34. 250
1. 172
2.215
2.401
2. 47S
.«.
O^OQQ f|,m
0. ?b.
3. OUO
15.23?
37. 250
3. 10?
2.274
2.445
2.47?
17,
rth064. 000
i ntf1}
2. ^50
16.317
3?. 700
2. 262
o o-*.i
ii. i_ i "
2. 4 :!3
2.471
:e.
R61 1~. ijfni
"Shn^. nun
n. Rft?
2. -?oo
17.200
42. 000
2. 604
2.293
2.442
2. 46?
n.
C'6175. 000
^nn ^nn
n ^67
2.500
19. 167
44. 500
2. 5S6
2. -?09
2.450
2. 46?
.™.
y6?45. ooo
1 167
2.750
19.333
47.250
2. ?ci7
2. ?12
2.444
2. 4h.7
to
(continued)
-------
TABLE A-50 (continued)
P«ge 5 of c
IV
Redding
No.
T. Bin
U. 1b
AT. h
AW. Ib
EAT. h
IAU. Ib
(S). »»
(SOL ""
I. Ib/h
21.
86298. 000
3596. 050
0. 883
1. 700
20.217
43. 950
1.92*5
2.421
. 2. 46ci
:• .••
k. k. •
86357. 000
.3594. 000
0.9 S3
2. 050
21.200
51.000
2. 0:-:5
2. 406
2. 4b2
23.
St-412. 000
3592. 500
0.917
1 . 500
22. 117
52. 500
1 . t. 3t-
2. 374
2.458
24.
86470. 000
3589. 950
0.967
2. 550
23. OS 3
55. 050
2. 63S
2. 385
2. 4l.-5
/
25.
86531. 000
.3588. 200
1.017
1.750
24. 100
56. 800
1.721
d. 357
2.451
86570. 000
?587. 900
(continued)
-------
TABLE A-50 (continued)
Page 6 of 6
oo
Reading
No.
T. mtn
U. 1b
AT. h
AU. 1b
CAT. h
CAM. lb
(M\ ih/h
I 771 ID/n
\Ai/,
(Sfl """
X. lb/h
•
365^3. O'J'J
3589. V1-'!
•
n 24 Syx 1.147 tQ/2 2.07
Slope 2.369 $x 7.104 r 0.999
Intercept 0.728 SA 0.034 Confidence interval
Sb 0.108 2.369 + 0.071
S^ 1.344
-------
TABLE A-51 SUMMARY OF DATA FROM TEST NO. 29
1 Of 6
Degreaser B, operating
Solvent: 1,1,1-THchloroethane
PB 125 %
Inlet air
Other
PC x SC x
Exhaust air x
A
8
70 %
7m In
Date 1/21/79
Ambient air
Temperature 69 *F
Pressure NA (n. tig
Humidity "
Reading
No.
Tf m1n
H. 1b
AT, h
AN, 1b
CAT, h
CAN, 1b
(AT), 1b/h
(flrr). 1b/h
X, Ib/n
55004. 000
2972. 2*0
•
B5U18.-000
2972. 250
...,...!.,
2973. 350
85051. UOO
2*85. 45H
1.
fc:5Q81. 000
2983. 750
2.
85143.000
2981.850
1. 117
1.900
1. 117
1.900
1.701
1.701
1.701
10
N)
vO
-------
TABLE A-51 (continued)
Page 2 of $.
Reading
No.
Tain
. •in
U, Ib
AT. h
AM. Ib
CAT. h
EAU. Ib
/A«\
1 O>* 1 Ik 4k
ITT) ID/It
\AT/.
1 fTfTT 1 1 D/ fi
V bOI /•
X. 1b/h
-;
35201. Ono
I* SO. nijn
0.833
1.350
2. 000
3. 750
2. 094
1.393
1.H75
4.
:::ci"'h.4. nun
2977. 000
1 . 050
3. 000
•3. 050
6. 77.0
2.213
,.-:0
i.
PS'; -:4. '"""in
1. 1*7
2. ^'OO
4. 2t~
9. 250
2. :-:3
1 • . -
6.
:-:s -:'^h,p rmn
2^71. noo
1.0J3
3. 500
5. 250
12.750
3. 3R"
2. 42?
2. OS..1
I •
,-:ci4c!i:». nnn
2970. 500
1.050
0. 500
6. 3nn
1 3. 250
0. 476
2. 103
2. 086
8.
35.517.000
2968. 500
0. 967
2. 000
7. 267
15.250
2. 069
2. 099
2. 033
N»
Ul
O
(continued)
-------
TABLE A-51 (continued)
Page 3 of 6
Reading
No.
T. «in
y. ib
AT. h
AU. Ib
EAT. h
CAU. Ib
GO. "">
AAW\ ,
V^ATy,
X. Ib/h
^m
::5586. MOM
1. 150
1. 750
•-: -I 1 7
17. 000
2. 0"9
JiX
.• it ~\ "sn
0. 9.::3
3. MOO
•3 :sn
20. nnn
1— 1 1 1 ~l _l
1..
!55 "01. 000
0. 933
1. -50
jo. ::.-•::
21.7-5fj
1. 730
2. 105
2. n&s
1 2,
t, 58 17. 000
1. f :3
5. 250
12. 2*7
27. 000
^ • ' J -'
2. 201
1 :.
:.i;.-b 1.000
2 -i =;:-:. 700
-0. ?:-:3
-1.950
11.3 3 ?
25. 050
2. 0:39
2. 210
2. 10-
14.
85877. 000
2954. 500
1.933
4. 200
1 3. 267
29. 250
2. 172
2. 205
2. 1 1 5
Kl
u*
(continued)
-------
TABLE A-51 (continued)
Page ^ , of 6
Reading
No.
T. «tn
U. 1b
AT. h
AM. 1b
CAT, h
CAM. lb
(fr). ib/h
(ZST). lb/h
X. lb/h
15.
85941. 000
2^"? -i. nnn
1.067
1.500
14. '-:J3
?0. 7'jO
1.400
2. 145
2. H"
16
B-«992. 000
2950. ft".'"'
0. O^O
2. J 50
15. -.::=::
?2. 900
2,V-
2. u.r
2. 120
,7.
8t 064. Oi'O
**4fl --im
• 1.200
2. 650
16. 383
35. 55U
2.20?
2. 1 ,-0
2. 123
18.
ot 1 17. HMO
2'M6. nno
0. o!?3
1. 700
17.267
37. 250
1.-^-.
2. 17."
2. 1 .i'1!1
19.
86 1 75. UOO
2944. 500
0. ^7
2. 000
13.233
":!q. 250
2. Ou?
2. IT.':
2. IE'
10.
Sit 239. 000
2<:"42. 700
1.067
l.SOO
19.300
41.050
l.t>:3
2. 127
2. 127
to
U)
K>
(continued)
-------
TABLE A-51. (continued)
Page £__ of
Reading
No.
T. »1n
U. 1b
AT. h
AM, 1b
EAT. h
EAU. Ib
(Ir) lb/h
(W\ |D/h
I. lb/h
. *1 1 •
86298. 000
2939. 600
0.933
3. 100
20. 233
44. 150
3. 153
2. 177
2. 12?
22.
36357. 000
2933. 600
0. ?33
1.000
21.267
45. 150
1.017
2. 123
2. 12?
23.
86412.000
2936. 300
0.917
1.300
22. 133
46. 950
1.964
2. 116
2. 129
24.
36470. 000
2935. 350
0.967
1.450
23. 150
48. 400
1.500
2.091
2. 127
1
25.
36533. 000
2932. 900
1.050
2.450
24. 200
50. 350
2.333
2. 101
2. 126
86568. 000
i
2931.200
ro
w
to
(continued)
-------
TABLE A-51 (continued)
Page 6 of 6
W
Reading
No.
T. min
H. Ib
AT. h
AU. Ib
EAT. h
CAM. Ib
(M\ lh/h
I Tr" 1 ID/n
\AT/,
• •
X. Ib/h
S6b?4. 000
2933. 200
•
n 24 Syx 0.650 tQ/2 2.07
Slope 2.122 Sx 7.348 r 1.000
Intercept 0.241 Sa 0.018 Confidence Interval
Q
S. 0.175 2.122 + 0.037
Sc 0.687
-------
TABLE A'52 SUMMARY OF DATA FROM TEST NO. 30
Page 1 of _5_
Degreaser A, operating
Solvent: 1,1,1-THchloroethane
Date 1/26/79
FB 125 t
Inlet air _x_
Other
PC x SC
Exhaust air
5Q *
Tt/mii
min
Ambient'alr
Temperature 70 °F
Pressure - In. Hg
Humidity ~38~~*
Reading
No.
T, min
W, Ib
AT. h
AW. Ib
EAT. h
CAW, Ib
(ff). ^
(if), 'w
X, 1b/h
?0796.
3b81.9«:
90808.
3b81. ::
90S 13.
3*77. =.
1.
90319. 000
3678. 200
k. •
90915.000
3676. 300
1.600
-1.400
1.600
-1.400
-0. 37=.
-0. S7S
-0. 37=.
3.
90933. 000
3674. 300
1.217
-2. 000
2.317
-3. 400
-1.644
-1.207
-1.041
N)
U>
LP
-------
TABLE A-52 (continued)
Page 2 of 5
Reading
No.
T. «1n
U. 1b
AT. h
AM. 1b
CAT. h
CAM. Ib
\AT/»
/j^y\
K. Ib/h
4.
91056.000
3673. 600
1. 13'.:
-1.200
3. 950
-4. 600
-1.059
-1. 165
-i.os::
5.
91116.000
3671.800
1.000
-1.800
4. 950
-6. 400
-1.800
-1.291:
-1. 135
6.
91169.000
3670. 600
0.881:
-1.200
5. 33::
-7. 600
-1. 358
-1.303
-1. 168
-e
91223.000
3669. 300
0. 98-::
-1. 300
6.317
-o. 900
-1. 32J1
-1.306
-1.191
8.
91281.000
3667. 200
0. 883
-2. 100
7. 700
-11.000
" •! . O I i
-1.429
-1.225
9.
91354.000
3666. 000
1.217
-1.200
3.917
-12.200
-0. 986
-1.36?:
-1.24;:
10
(continued)
-------
TABLE A-52 (continued)
Page 3 of j_
Reading
No.
T. «1n
M. 16
AT. h
AM. 1b
I AT. h
EAM. 1b
VAT/ ^/^
(fift "»"
X. 16/h
10.
91412.000
3664. 000
0. 967
-2. 000
9. SSI:
-14.200
-2. 069
-1.437
-1.265
11.
9147S.OOO
3662. 000
1. 100
-2. 000
10.9S::
-16.200
-1.818
-1.47=.
-1.286
12.
91542. 000
3660. 500
1.067
-1.500
12.050
-17.700
-1.406
-1.469
-1. 30I1
13.
91593. 000
3659. 750
0. S 50
-0. 750
1 2. 900
-IS. 450
-0. :3S;-
-1.430
-1. 31 ::
14.
91653. 000
3657. 750
1.000
-2. 000
13.900
-20. 450
-2. 000
-1.47J
-1. 325
15.
91717.000
3656. 500
1.067
-1.250
14.967
-21.700
-1. 172:
-1.450
-1.334
(continued)
-------
TABLE A-52 (continued)
Page 4 of j_
Reading
No.
T, «1n
U. 1b
AT. h
AU. 1b
CAT. h
CAU. Ib
©. »"
(Mr). lb/h
X. 1b/h
16.
91770.000
3655. 000
0. 383
-1.500
15.850
-23. 200
-1.695:
-1.464
-1.34::
17.
91843.000
3653. 400
1.217
-1.600
17.067
-24. 800
-1. 315
-1.453
-1.350
18.
91894.000
3652. 300
0. 850
-1. 100
17.917
-25. 900
-1.294
-1.44*.
-1.355
19.
91958. 000
3650. 400
1. 067
-1.900
13.98::
-27. 800
-1.78J
-1.464
-1. 361
20.
92029. 000
3649. 000
1. 183
-1.400
20. 167
-29. 200
-1. 183
-1.448
-1. 36*.
21.
92033. 000
3647. 200
0. 983
-1.300
21. 150
-31.000
-1.83J
-1.46*.
-1.371
to
CJ
09
(continued)
-------
TABLE A^SZ .(continued)
Page 5 of 5
Reading
No.
T, «1n
W. 1b
AT. h
AH. 1b
CAT. h
CAU. 1b
(fi). """
GAT), 1b/h
X. Ib/h
22.
92204. 000
3643. 750
1.931:
-3. 450
23.03.-:
-34. 450
-1.4?::
-1.377
23.
92264. 000
3642. 000
1.000
-1.750
24. 033
-36.200
-1.750
-1.501:
-1.33;:
24.
92324. 000
3641.000
1.000
-1.000
25.03::
-37.200
-1.000
-1.48::
-1.337
. 25.
92335.000
3642. 500
0. 18::
1.500
25. 267
-35. 700
3. is;:
- 1 . 4 1 ::
-1.3SS:
26.
92343.000
364 3. 000
0. 1 33
0. 500
25. 400
-35.200
3. 750
-1.336
-1. 33?:
92434. 000
3644. 000
vo
n 25
Slope -1.495
Intercept 0.809
Sw, 0.634
"
SK 7.593
S, U.017
Q
Sb 0.183
S, 2.199
2.069
r -1.000
Confidence Interval
1.495 + 0.070
-------
TABLE A-53 SUMMARY OF DATA FROM TEST NO. 30
Page j_ of _5_
Degreaser B, operating
Solvent: 1,1,1-Trlchloroethane
Date 1/20/79
FB 12$*
InleTatf
Other
PC y SC
Exhaust air
ft/mi
min
Ambient'air
Temperature 70 *F
Pressure - in. Tig
Humidity JH \
Reading
No.
T, min
W, Ib
AT, h
AH, Ib
EAT. h
CAN, Ib
(S). '^
(Sfi 'k'"
X. Ib/h
?D7?6.
308?.
-------
TABLE A-53 (continued)
Page J_ of _5__
Reading
No.
T. «in
tl. 1b
AT. h
AU. 1b
EAT. h
EAU. 1b
(ir). lb/h
(sir) Ib/h
X. 1b/h
4.
91056.000
3085. 200
1. 13;:
0. 200
3. 43;:
-4. 000
0. 17*.
-1. 165
-1.551
5.
91116. 000
3083. 900
1.000
-1. 300
4. 43-1:
-5. 300
-1.300
-1. 195
-1.46J'
6.
91169.000
3082. 800
0.881:
-1. 100
5.317
-6. 400
-1.245
-1.204
-1.410
1 •
91 SI'S. 000
3031.200
0. 98;:
-1.600
6. 300
-3. 000
-1.627
-1.270
-1. 387
8.
91231.000
3080. 600
0. 83;:
-0. 600
7. 13.;:
-8. 600
-0. 679
-1. 197
-1. 360
9%
91354.000
3079. 500
1.217
-1. 100
8. 400
-9. 700
-0. 904
-1. 155
-1.334
ro
(continued)
-------
TABLE A-53 (continued)
Page _3_ of j>_
Reading
No.
T, Bin
U. Ib
AT. b
AU. Ib
EAT. b
EAV. Ib
(£) ">"•
W/t
(IST). lb/h
X. lb/h
10.
91412.000
3078. 250
0. 967
-1.250
9. 367
-10.950
-1.293
-1. 169
-1.31*
11.
91478.000
3077. 000
1. 100
-1.250
10.467
-12.200
-1. 13*
-1. 16*
-1.301
12.
91542.000
3075. 750
1.067
-1.250
11.53-:
-13.450
-1. 17::
-1. 16*
-1.289
13.
91593.000
3075. 000
0. 850
-0. 750
12. 38.':
-14.200
-o. 88::
-1. 147
-1.277
14.
91653.000
3073.500
1 . 000
-1.500
13.38::
-15.700
-1.500
-1. 17.::
-1.269
15.
91717.000
3071.750
1.067
-1.750
14.450
-17.450
-1.641
-1.20?:
-1.26J
to
.b
N)
(continued)
-------
TABLE A^S.3 (continued)
Page 4 of 5
Reading
No.
T. m\n
y. ib
AT. h
AU. Ib
EAT. h
IAU, Ib
(ir) lb/h
(ZAT) lb/h
X. lb/h
16.
91770.000
3071.250
0. 88;:
-0. 500
15.33::
-17.950
-0. 566
-1. 171
-1.258
17.
91841.000
3069. 900
i. is;:
-1.350
16.517
-19.300
-1. 14J
-1. 16':'
-1.25-::
18.
91894.000
3067. 700
0. 83::
-2. 200
17.400
-21.500
-2.491
-1.236
-1.25:-
19.
91953.000
3065. 900
1.067
-1.800
18.467
-23. 300
-1.637
-1.26J'
-1.25::
20.
92029. 000
3064. 200
i. is::
-1.700
19.650
-25. 000
-1.437
-1.272:
-1.25::
21.
92088. 000
3064. 700
0. 98;:
0. 500
20.63::
-24. 500
0. 508
-1. 187
-1.250
U
(continued)
-------
TABLE A^53 (continued)
Page _5__ of _5
Reading
No.
T. n1n
N. Ib
AT, h
AW. Ib
IAT. h
CAM. Ib
(tM\ |h/h
vsy. lb/h
(fir). 1b/h
X. lb/h
22.
92146.000
3064. 400
0. 967
-0. 300
21.600
-24. 800
-0.310
-1. 14?:
-1.245
,..
92200. 000
3061.000
0. 900
-3.400
22. 500
-28. 200
-3. 77?:
-1.25::
-1.245
24.
92264. 000
3061. 350
1.067
0. 350
23. 567
-27. 850
0. 32?:
-1. 18J1
-1.24::
25.
92324. 000
3060. 250
1.000
-1. 100
24. 567
-28. 950
-1. 100
-1. 17?:
-1.240
26.
92335.000
3060. 750
o. is::
0. 500
24. 750
-28. 450
2.727
-1. 149
-1.23*.
27.
92434.000
3060. 000
1.650
-0. 750
26. 400
-29. 200
-0. 455
-1. 106
-1.231
n. 26 iyx 0.819 *a/2 2.064
Slope -1.160 \ 7.695 r -1.000
Intercept -0.449 $a 0.021 Confidence Interval
Sb 0.169 1.1CO +0.043
S. 1.162
-------
TABLE A-54 SUMMARY OF DATA FROM TEST HO. 31
Piqe 1^ of 5
tegrcaser A. operating
Solvent: 1,1,1-Trlchloroethane
FB 125 « PC x SC
Inlet air
Other Hot load was used throughout the test
Date 1/25/79
. - _.-. PC x SC A en I
Inlet air x Exhaust air x V 8 rt/mln
Ambient* afr '
Temperature 63 *F
Pressure - tn.
Humidity T9""t
Reading
No.
T, win
V. 1b
AT. h
AH. 1b
CAT. h
'CAM. ib
\ A 1 * •
m Vj\^f ^
X. Ib/h
89071.
3722.2
59140.
371-:.. Oe.
•
89154.
1.
**::•.. ..-.:;..:.
3715, 750
,.
•39 J> 33.0™
37| ^H
o. 9tr
-2. 5.!'0
0. ^bT1
--2. 500
-2. 53*.
O ^ '"* *'
4. • •,' *. ' 1 '
-Z. 53».
a.
3?3C-». 000
37 JO. 500
1. 100
-,?- 750
2. 067
-5. 250
-2. 500
2. 540
- 2 •=;<: •'•
&•• •.'..•
-------
TABLE A-54 (continued)
Page 2 of 5^
Reading
No.
T, uln
U. 1b
AT. h
AH. 1b
EAT. h
EAU, 1b
(5ft '»"•
X. Ib/h
39356.010
370S. 3uO
0. 867
-2. 200
2.93:::
-7. 450
-2. 536:
- 2. 540
-2. 555
:3942l. 000
3706. 800
,.or.
-1.500
4.017
-8. 950
•1.385
_» T' O ? 'I*
-2. 474
fr.
e 9 173. ooo
27U4. 2 OH
0, ft 6 7
-2. 600
-11. 550
- 3. 000
- 2. 365
•1. 45J-
I •
39544.000
?70J. 000
i. 13::
-2. 200
1--. 067
- i 3. 750
-1.8^9
-2. 266
-2.421
•3.
8?605. 000
3 •-.•?•:•. 600
1 . 0 1 7
-2. 400
-16. 150
-2.361
-2. 230
•-:-:. 40)
99652. 000
36*6. 200
1.23::
-3.400
8. 367
-2.64-:-
-2. 337'
-2. 39C:
.b
Cf
(continued)
-------
TABLE /U54 (continued)
of
Reading
No.
T. uln
V. Ib
AT. h
AM. Ib
CAT, h
CAW, Ib
ea "»
(EST). 1b/h
X. 1b/h
15.
8973*. 000
?*94. 200
0. 950
-2. 000
9.317
-21. 5*:-0
-2. 103
-2.3i::
11.
i:"?,":^. 000
:•*•--;:. ooo
0.8 33
-2. 200
10. 150
-2?. "50
-2.640
-2. 340
-2. 350
12.
898r."C. 000
Si'.'-'O. 000
i.017
-1. OCU
1 f . 1 1 7
-25. 7TO
\
->.V*
-2. -:r
1 3.
ft**15.:;., u oo
3 1^'7. 250
i . 200
-1, 75fl
1 2. 3t 7
-Z8. 5'1-ri
:• i- •••
». t.
2-i|- L
• -' - '
-Z, 3t--7
14.
—' '-^ *•! '-"' 1 n o r i
~* i" '.' ^ ~* ^i Tl
0. 9?::
-2. 000
' 3. 350
- :'0. 500
-2. o:*-
-2. 283
-2.361
IS.
90'J ;:<5. 000
3t.:;:o. 000
0. 9t7'
-2. 250
M. 317
-32. 750
-i •> - f>
-------
TABLE A-54 (continued)
•a* JL«f J_
Reading
No.
T, «1n
U. 1b
AT. h
AM. 1b
EAT. h
IAU. 1b
(!r). 1b/h
GST). lb/h
X. 1b/h
If.:
q0092. 000
36? 1. 5UO
0. 8S3
-1.500
1 5. 200
-34. 250
-1.695:
-2. 253
:2. 349
IT.
90 it. 3. 000
36~ P. 250
1. is.::
3. 250
It. 3?::
-1:7.500
-?. 746
--2. 269
-2.345
IS.
902)5. 000
3677. uno
o. s^r
-t. J50
17.2^0
-33, 750
-1.44.;-
-;:. 24.
_ ^* ^* "^ •" 1
t - • •* .'
19.
9020. 000
3t-74. 250
1 . Ot I:
-2. 750
1:1. 3":":
—..5-?.-,
2. 5??:
•I-.2H
- :. :'?5
20.
90339. 000
3672. 500
0. 9S3
-1.750
1*. 317
-J 3. 250
-I. 730
-2.239
-2. 31'0
11.
90393.000
3669. 250
0. 900
-3. 250
20.217
-46. 500
-?. 6!J
- 2. 300
-2. 32:":
00
(continued)
-------
TABLE A-54 (continued)
Page 5 of 5
Reading
No.
T. Mill
M. 1b
AT. h
AM. 1b
IATt h
KM, 1b
(fit ""•
(M?). »"
X. Ib/h
Z2.
•;'0457. 'I--.0
:-!»..*". 251.'
1.067
-2. 000
Z.'.: = "
-JO. *.jfl
-1.87:.
-?. 27':'
— "* ""' - ft
23,
905 •'. 000
3665, M..I.!
: . HIMI
-i. .1L-U
- -. •
-------
TABLE A-55 SUMMARY OF DATA FROM TEST NO. 31
1 Of 4
Degreaser B, operating
Solvent: 1,1,1-THchloroethane
Date 1/25/79
FB 1251
Inlet air x
Hot load was used throughout the test
PC x SC
txhaust air x
A
8.
ft/mi
ml n
Ambient air
Temperature 63 *F
Pressure In. Mq
Humidity J?9 I
Reading
No.
T, win
W, 1b
AT, h
AW, 1b
EAT, h
CAW, 1b
(Sf) lb/h
csa ""*
X, lb/h
•::°4C|1.000
•* » & •^Ar^/
21ST7.2DO
.•
tf^l 5"Ofo 0 DO
O 1 ^^ *^t/»v *^^x
89532.000
1.
f?'1; : . ooo
2 "1:. 200
a.
3?»fiJ3. 000
2'?^.9. 400
1 . 000
-3. 300
1.000
-3.300
- 3. 300
-?. 300
::. 300
3.
fi.^.--, npn
*«.*»
1. 31"
• 1 . 200
™i "J < ""'
h. • .' 1 i
-5. 000
-0.91J
-2. 15:-:
- 2. 979
tr
o
-------
TABLE _A-_55 (continued)
2 of 4
Reading
No.
T. «1n
•
U. Ib
AT. h
AM, Ib
CAT. h
CAU. Ib
(ir). lb/h
(IAT). lb/h
X. lb/h
1.
oq- -o Hi
^••.6i/'
o. •?::.:•
- 2. £00
3. J150
--. £01"!
•-- 7?'-'
••I1. ]:']:!:
""' "*i- 1 1
S.
3° •"" : '•'. 000
2?- :-. 8 'Ji.'
O. S50
-..J3CC.
4. 100
-•-<. 400
--.. lit:
_ j -jCl "'
.J.64T'
fc.
2-l.cr,
' . o : "
-L. '!"" '.'
5.1 IT
-,-^n,;
,,--£-
, '. J_ :•
. c . -
' r.
• •-• j " . 0' '0
L.JUO
-2. :'CO
>i. 317
-:-.-co
•-.o0:-
- ;: . i j 1 1
•;. 4-1
8,
,..._ Ofif|
2?',-. 550
0.-83
;. i5«
7. 300
-M.950
-:. :&f
= .04f:
.-•'•!
,B
q .,
:-°5^. 750
"'. SVC'
-'"'. 500
•f. 150
-15. 450
-u. 5 •::•;:
-J.8^.
- ?4^
tn
(continued)
-------
TABLE A-55 (continued)
•age _3 of 4
N>
tr
ts>
Reading
No.
T. «1n
U. 1b
AT. h
AM. 1b
EAT, h
IAU. 1b
(fit «"»
($0. »"•
1. Ib/h
10.
900^2. ooo
2956. lOfi
1.000
-1.650
9. 150
-17. 100
-1.650
-1.86?
-2. 293
11.
qo i »•:. ^. 00" >
£**•''*. 250
1. 181:
-1. S50
10. 3?::
-'S. 950
-1.56;:
-1.834
-?. 24f
12.
°021:.. 000
29':.":, 000
0. :i'67
-1.250
1 1 . 200
-20. 200
-1.442
-1.804
-2. 20^
13.
'PO101?. 00 'i
2T15!, ;:".'•'
1.0S3
-1.750
i::. 203
-21.950
• t . s r;
-1.787
-2. \1Z
14.
9037.'1". 000
2'349. 750
0. 9S3
-1.500
J3.267
-23. 450
-1.525
-1.76?:
-2. 1 J 1
IvS.
•90393.000
29-:?. 800
0. 900
0. 950
14. 167
-24. 400
- i . 056
-1.725:
-2. 1 ! 1
(continued)
-------
TABLE A-55 (continued)
4 of 4
Reading
No.
T, m\n
W. Ib
AT. h
AM. Ib
CAT. h
CAM. Ib
(S). lb'h
GST). lb/h
X. lb/h
16.
91? *™v. -y -.'
2?-'7. 75C
l.O*-:1
-1.070
15.2?::
-25. 450
-0. 98*
-l.*71
-I1. 082.
17.
•: '. ~. '.. in1:
.1"-.-. ' ". n
-. . 0 ;.--.
x • _ _' '.'
ib. -IT1::
-;.r. :.:„;,
-J.857
1.683
2. O1:?
23
•
2,4
•
n 16 Syx U.586 tQ/2 2.145
Slope -1.543 S^ 4.793 r -1.000
Intercept -2.751 Sfi 0.032 Confidence Interval
S... 0.283 1.543 + 0.069
D ~
Sc 0.796
N)
tn
to
-------
TABLE A-56 SUMMARY OF DATA FROM TEST NO. 32
Page i of 7
Degreaser A, operating
Solvent: 1,1,1-THchloroethane
Date 1/28/79
ra 125 %
Inlet air x
Other
PC x SC _x_
Exhaust air x
A 50*
16 ft/min
Ambient'air '
Temperature 69 °F
Pressure - In. Hg
Humidity 'Si t
Reading
No.
Tt mln
H, 1b
AT, h
AW. 1b
EAT. h
CAW. 1b
(S). »*
(if). W
X. Ib/h
94079. ooci
370R. 500
94083. 000
3703. 000
•
94099. 000
3703. 800
1.
9413::. 000
3 702. t-00
^
•_ •
94175.000
3700. 400
0. 700
-2. 200
0. 700
-2. 200
-3. 14::
-3. 14::
-3. 14::
•3.
94193. 000
3697. SOO
0. 300
-2. 600
1.000
-4. SOO
-8. 667
-4. 300
-?. 971
N>
IT
-------
TABLE A-56 (continued)
Page 2 of 7
Reading
No.
T. «in
U. 1b
AT. h
aw, ib
CAT. h
EAW. Ib
(39. ""*
(sft ""•
X. Ib/h
4.
94232.000
3693. 900
0. 650
1. 100
1.650
-3.700
1.69L''
-2. 241:
-3.39!!
5.
94257. 000
3693. 000
0. 417
-0. 900
2. 067
-4. 600
-2. 160
-2. 22t.
-3. 10-::
6.
94298. 000
3696. 500
0. 68-1:
-1.500
2. 750
-6. 100
-2. 19=.
_ o -• i cj
w . «_ 1 •- •
-••• Q~>.
«_ . . »_ *.'
^
i .
94312.000
3696. 100
0.23::
-0. 400
2.98::
-6. 500
-1.7K
-2. 179
-2. 80 J
3.
94346. 000
3695. 600
0. 567
-0. 500
3. 550
-7. 000
-o. ss;:
-1.97;-
-2. 63:-:
9.
94379. 000
3694. 200
0. 550
-1.400
4. 100
-8. 400
-2. 545
-2. 049
-2. 60-
t
ISJ
Ul
en
(continued)
-------
TABLE A-56 (continued)
3 of 7
Reading
No.
T, Bin
U. lb
AT. h
AH. lb
CAT, h
EAU, lb
(1?). ""'
(fir). 1b/h
X. 1b/h
10.
94413.000
3693. 200
0. 567'
-1.000
4. 667'
-9. 400
-1.7S5
-2. 011
-2. 538
11.
94445. 000
3692. 000
o. 53;:
-1.200
5. 200
-10.600
-2. 250
-2. 03$:
~fc. • *T •? C'
12.
94430. nnr.i
•-:Ki:»ri. arm
0. 53::
"- 1.200
5.731!
-11.300
-2. 0571
-2. 040
-2. 447
13.
94500. 000
3690. 000
0. 33':
-0. 300
6. 1 17'
-12.600
-2. 400
-2. 060
-2.415
14.
9-1534. 000
3639. 200
0. 567
-0. 300
6,63::
-13. *QO
-1,412
-2. 00:i
-2. 331
15.
94554. 000
3633. 400
0.33.::
-0. 300
7.017
-14.200
-2. 400
-2. 021
-2. 35?:
SJ
01
(continued)
-------
TABLE AJ>6 (continued)
Page 4 of 1
to
Reading
No.
T. Bin
U. Ib
AT. h
AW.. Ib
EAT. h
EAV. Ib
/AU\
1 UW 1 1 fth * k
I Tr J ID/n
\AT/.
AAW\ lb/h
yaty.
X. lb/h
16.
94533. 000
3633. 000
0. 567
-0. 400
7. 53 ::
-14.600
-0. 70t-
-1.925
~2. ^2C|
17.
94604. 000
3636. 600
0. 267
-1.400
7. 350
-16.000
-5. 250
-2.033
-2. 31 J
13.
94633. 000
3635. 700
0.481:
-0. 900
3. 33'::
-16. 900
-1.36J1
-2. 023
t_ • bl . |
19.
94672. 000
3634. 700
0. 650
-1.000
3.93::
-17. 900
-1. 533
-1.99.::
-2. 277
20.
94694. 000
3634. 100
0. 367
-0. 600
9. 350
-13.500
-1.636
-1.979
-2. 26J1
21.
94747. 000
3632. 400
0. S3'::
-1.700
10.23-::
-20. 200
-1.925
-1.974
-2. 247
(continued)
-------
TABLE A-56 (continued)
Page 5 Of ]_
Reading
No.
T. m\n
U. Ib
AT. h
AH. Ib
CAT. h
CAM. Ib
(ir). lb/h
OAT) lb/h
X. lb/h
22.
94772. 000
36R1 Ano
0.417
-0. 800
10.650
-21.000
-1.920
-1.972:
-2.234
23.
94799. 000
?6fil onn
0. 450
-0. 400
11.1 00
-21.400
-0. 839
-1.92?:
-2. 220
24.
94340. 000
367*. 7nn
0.63::
-1.500
11.78::
-22. 900
-2. 19!!
-1. 94::
-2. 20?:
25.
94330. 000
367R. snn
0. 667
-1.200
12.450
-24. 100
-1.800
-1.93*.
-2. 197
26.
94912. 000
•}677. 250
0.53::
-1.250
12.93-::
-25. 350
-2. 344
-1.95::
-2. 187
27.
94939. 000
3676. 25fi
0. 450
-1.000
13.43::
-26. 350
-2. 22;:
-1.96::
-2. 17?:
00
(continued)
-------
TABLE A-56 (continued)
Page 6 of 7
Reading
No.
Tmim
. •in
U. Ib
AT. h
AM. Ib
I AT, h
EAW. Ib
(QS) Ib/h
vi\i /.
f LAM \ •• ••
I fsrJ '
X. 1b/h
23.
Q4Q7Q nnn
. ^ . 1 . • *JW
3675. 500
0. 667
-0. 750
14. 100
-27. 100
-1. 125
-1.922
-2. 169
29.
94997. 000
3674. 500
0. 300
-1.000
14.400
-23. 100
-3.33::
-1.95J
-2. 16J
30.
95042. 000
3673.250
0. 750
-1.250
15. 150
-29. 350
-1.667
-1.937
-2. 15::
31.
*5iv,:-:. nnn
3673. 000
0.43::
-0. 250
15.58::
-29. 600
-0. 577
-1.899
-2. 145
32.
*5 inr. nnn
3670. 750
0. 650
-2. 250
16.23::
-31.850
-3.46?
-1.96::
-2. 1 39
O -'.
95140. 000
3669. 950
0. 550
-0. 800
16.78.::
-32.650
-1.455
-1.945
-2. 13::
vD
(continued)
-------
TABLE A-56 {continued)
7 of 7
Reading
No.
T, mln
U, 1b
AT. h
AH. 1b
ZAT. h
CAU. Ib
f AU \
• o™ i iw^w
i «— i 1 Df Fi
(fir). lb'h
X. 1b/h
3,.
95179. 000
3668. 750
0. 650
-1.200
17.4?::
-33. 850
-1.846
-1.942:
-2. 127
35.
95208. 000
3663. 500
0. 481:
-0. 250
17.917
-34. 100
-0.517
-1.90::
-2. 121
36.
95233. 000
3667. 300
0. 4 1 7
-0. 700
18. 33':
-34. 800
-1. 68Ci
-1.898
-2. 114
37.
95265. 000
3667. 400
0. 53'::
-0. 400
18.867
-35.200
-0. 750
-1.866
-2. 107
952'3:?. 000
"iK^.K. 7Cifl
95301.000
"if^n. snn
NJ
«T«
O
" 36
Slope -1.854
Intercept -1.099
Swlf 0.466
/*
Sx 5.520
Sa O.U14
O
Sb 0.113
S_ 1.576
2.032
r -1.000
Confidence Interval
1.854 + 0.028
-------
TABLE A-57 SUMMARY OF DATA FROM TEST NO. 32
Page ] of 7
Degreaser B, operating
Solvent: 1,1,1-Trichloroethane
FB 125 *
Inlet air x_
Other
PC x SC
Exhaust air
16~?ten
Date 1/28/79
Ambient air
Temperature 69 °F
Pressure _in. Hg
Humidity j£ %
Reading
No.
T, mln
M1K
« ID
AT. h
AW. 1b
EAT. h
CAW. 1b
(*"} Ih/h
I TT 1 ' D*"
\AT/,
(EAWN lb/h
\ EAT /,
X, lb/h
94079. 000
94092. 000
94101. 000
1.
941 ; 3. 000
~'Q»I "• 1 Tn'i
«1 . -'»!. 1 IJ'.I
^ .
94175. 000
•-•QJ 1 < flfi
o. roo
-1.000
0. 700
-1. 000
-1.429
-1.429
-1. -129
3.
94193. 000
•'^£•0 3iifi
0. 300
-0. SOO
1. 000
-1.800
-2. 6t-7
-1. SOO
- 1. 61 -
-------
TABLE A^57 (continued)
Page 2 of 7
Reading
No.
T. nln
U. 1b
AT. h
AU. Ib
CAT. h
EAU. Ib
00. '«•
(if). »•"•
•
X. lb/h
4.
rt j A • L ,~, A .". ,- .
9423.1. 000
2959. 500
0. 650
-0. SOO
1.650
-2. 600
-1.231
-1.57*.
. -1.601
5.
•3d oc1-1 nnri
r4c j i . UUi.i
2958. 500
0. 4 1 71
-1.000
2. 067
-3.600
-2. 400
-1.74?
-1.637
6.
gj-jqo f|f|f|
- ~ h. . '-' • '-1 '-' '. '
2957. 400
0. 6&::
-1. 100
2. 750
-4. 700
-1.610
-1. 709
-1.651
-7
1 .
•^4~:i "-• nfifi
. T _' 1 t_ • '.' '-' '. f
2957. OOCi
0.23::
-0. 400
2. 93::
-5. 100
-1.714
-1.709
-1. 661
S.
94346. 000
2956. 400
0. 567
-0. 600
3. 550
-5. 700
-1.059
-1.606
-1.65-::
9.
*4?7o. nnri
2954. 600
0. 550
-1.300
4. 100
-7. 500
-.3.27::
-1.329
-1.675
(continued)
-------
TABLE A-57 (continued)
Page 3 of
Reading
No.
T, ntn
U. Ib
AT. h
AU. Ib
CAT, h
£AU. Ib
(3). '«»
(8ft «"*
X, 1b/h
10.
9441-3.000
2953. 900
0. 567
-0. 700
4. 667'
-3. 200
-1.2?*
-1.757
• -1.631
11.
94445. 000
2952. ^00
0.5::;:
-1. 300
5. 200
-9. 500
-2.43?:
-1.827
-1.69*
12.
94430. 000
2951.200
0.58::
-1.400
5. 73 1:
-10. 900
-2. 400
-1. 33*
-1.71ci
13.
94500. 000
2950. 700
0. 330
-0. 500
6. 1 1 7
-11.400
-1.500
-1. 361
-I. 725:
14.
94534.000
2949. 600
0. 567
-1. 100
6. 63::
-12.500
-1.941
-1.370
-1.739
15.
94554. 000
2943. 700
0.33::
-0. 900
7.017
-13.400
-2. 700
-1.910
-1.75J
N)
CT
(continued)
-------
TABLE A-57 (continued)
Page 4 of jr.
N)
Reading
No.
T, min
U. lb
AT. h
AU. lb
EAT. h
CAU. lb
00. lb'h
(fir), lb/h
X. lb/h
16.
94588. 000
2947. 800
0. 567
-0. 900
7. 58::
-14.300
-1.58?:
-1.386
• -1.760
17.
94604. 000
2947. 000
0. 267
-0. 800
7. 850
-15. 100
-3.000
-1.92-1
-1.770
18.
94633.000
2946. 600
0. 48 ::
-0. 400
8. 33::
-15. 500
-0. 82?:
-1.860
-1.775
19.
94672. 000
2945. 000
0. 650
-1.600
8.98::
-17. 100
-2. 46?
-1.901
-I. 78::
20.
94694. 000
2944. 200
0. 367
-0. 800
9. 350
-17.900
-2. is:
-1.911
-1.789
21.
94747. 000
2942. 600
0. 88::
-1.600
10.23'.:
-19.500
-1.811
-1.90*.
-1.795
(continued)
-------
TABLE A-57 (continued)
Page j of 7
Redding
No.
T. win
U, lb
AT, h
aw, lb
EAT. h
EAU. lb
00. "•»
AAUN lb/h
X. lb/h
22.
94772. 000
2941.700
0.417
-0. 900
10.650
-20. 400
-2. 160
-1.915
-1.801
23.
94799. 000
2940. 400
0. 450
-1.300
11. 100
-21.700
-2.839
-1.955
-1.80?:
24.
94840. 000
2938. 300
0. 63:=
.
-1.600
11.78::
-23. 300
-2. 341
-1.977
-1.815
25.
94330. 000
2937. 500
0. 667
.
-1.300
12.450
-24. 600
-1.950
-1.97*
-1.82J1
26.
94912. 000
2936.250
0.53:::
-1.250
12.93::
-25. 850
-2. 34<
-1.991
-1.829
27.
94939. 000
2935. 750
0. 450
-0. 500
13.43]:
-26. 350
-1. Ill
-1.96J1
-1.83-
N>
O-
tn
(continued)
-------
TABLE A-57 (continued)
Page b of 7
Reading
No.
T, win
U. Ib
AT. h
AU, Ib
CAT, h
CAU. Ib
(AT), lb'h
(fir). 1b'h
X, Ib/h
28.
94979. 000
2934. 400
0. 667
-1.350
14. 100
-27. 700
-2. 02S
-1.963
• -1.8-39
29.
94997. 000
29 3'3. 750
0. 300
-0. 650
14.400
-23. 350
-2. 167
-1.969
-1.84.::
30.
95074. 000
2931. 300
1.28::
-2. 450
15.68::
-30.300
-1.909
-1.964
-1.848
31.
95037.000
2932.500
-0. 617
1.200
15.067
-29. 600
-1.94t.
-1.965
-1.851
32.
95107.000
2930. 450
1. 167
-2. 050
16.23:-:
-31.650
-1.757
-1.950
-1.855
33.
95140.000
2929. 500
0. 550
-0. 950
16.78.::
-32.600
-1.727
-1.94::
-1.857
(continued)
-------
TABLE A-57 (continued)
Page 7 of i
Reading
No.
T, mln
U. Ib
AT. h
AW, Ib
CAT, h
EAW, Ib
(Ir). lb/h
(fir). lb/h
X, lb/h
34.
95173.000
2928. 250
0. 550
-1.250
1 7. 33;:
-3'3. 850
-2. 27C:
-1.95::
-1.360
35.
95203. 000
2927. 350
0. 58::
-0. 900
17.917
-34.750
-1.54::
-1.940
-1.36::
36.
95233. 000
2925. 750
0. 4 1 7
-1. 600
13. 33::
-36. 350
-3.340
-1.93::
-1.366
37.
^•=i2h.S. firm
2925. 250
0.53::
-0. 500
13.367
-36.350
-0.937
-1.95::
-1.36*
95238. 000
2925. 000
95329. 000
2925. 050
er
•o
n 36
Slope -2.005
Intercept 0.758
Syx 0.291
$x 5.516
S. 0.009
a
Sb 0.113
S_ 0.667
2.032
r -1.000
Confidence interval
2.005 + 0.018
-------
TABLE A-58 SUMMARY OF DATA FROM TEST NO. 33
Page 1 of j_
Degreaser A, operating
Solvent: 1,1,1-Trichloroethane
n -12S. *
Inlet air
Inle
Other
PC x SC _
x Exhaust air x
A TO X
16 ft/min
Date 1/29/79 .
Ambient'air ' r ~~
Temperature 69 °F
Pressure - in. Ug
Humidity 33 %
Reading
No.
T, mln
H, lb
AT. h
AW, lb
EAT. h
EAN. lb
(sr) lb/h
(Mr) lb/h
X. lb/h
95610. OOD
3794. 3iOO
*SI^K ooo
3790.ODO
QS|:4r OQO
37:38. 21'0
1.
95677. 000
37S6. 000
2.
9573-3. 000
37:34. 300
1.017
-1. 700
. 1.017
-1.700
-1.67:1
-1.67:-
-1.67:-
3.
95752. 000
37S.3. 900
-0. 400
1.250
-2. 100
-1.714
-1.680
-1. 67t-
00
-------
TABLE A-58 (continued)
Page 2 of 7
Reading
No.
T. «fn
y. lb
AT. h
AH. lb
CAT. h
LAW, lb
GO. ">»
(Sft ""'•
X. lb/h
4.
95778. 000
378 3. 000
0.45::
-0. 900
1.681:
- 3. 000
-2. 077
-1.78::
-1, 711
C1
_' •
95797. 000
3782. 600
0. 3 1 7
-0. 400
I1. 000
-3.400
-1.26::
-1. 700
-1. 709
6.
95831. 000
.3731. 500
0. 567'
-1. 100
2. 567
-4. 500
-1.941
-1. 75::
-1. 71:|:
-^
I •
95352. 000
'3730. 600
0. 350
-0. 900
2.917
-5. 400
-2.571
-1.851
-1.740
3.
95389. 000
'3779. 600
0.617
-1.000
3.53::
-6. 400
-1.62::
-1.811
-1.750
9.
95924. 000
3778. 400
0.583
-1.200
4. 117
-7. 600
-2. 057
-1. 846
-1.76::
N)
O>
VO
(continued)
-------
TABLE Ji-53 (continued)
Page 3 of _7_
Reading
No.
T. ain
U, )b
AT. h
Ay. Ib
EAT. h
EAU. Ib
(a) """
VAT/.
(itr). lb/h
X. lb/h
10.
95955. 000
3777. 400
0.517
-1.000
4.63::
-8. 600
-1.93!.
-1.85t.
-1.77::
11.
959:39. 000
3776. 200
0. 567
-1.200
5. 200
-9. SOO
-2. lit:
-1.88!.
-1.7&4
12.
96020. 000
3750. 000
0.517
-26. 200
5. 717
-36.000
-50.710
-6. 297
-2. 194
13.
9604S. 000
3774. 000
0. 467'
24. 000
6. IS::
-12. 000
51.429
-1. 941
-2. 173
14.
960S1. 00 0
3772. 600
0. 550
-1.400
6. 73::
-13.400
-2. 54!.
-1.990
-2. 159
15.
96107. 000
3771. 600
0.43::
-1.000
7. 167
-14.400
-2. 30?:
-2. 009
™ *1 • 1 *T O
O
(continued)
-------
TABLE A-58 (continued)
Page 4 ' of 7
Reading
No.
T. ain
U, Ib
AT. h
AH, Ib
CAT. h
£AU. Ib
GO. ""•
(i?). ""•
X. Ib/h
16.
96145.000
3769. 300
0.63::
-1.800
T. 800
-16. 200
-2. 84J'
-2. or:1
-2. 14::
17.
96177.000
3767. 800
0. 53::
-2. 000
8. 33::
-18.200
-3. 750
-2. 18-
-2. 14t.
18.
96211.000
3766. 250
0. 567'
-1.550
8. 900
-19.750
-2. 7-35
-2.219
-2. 150
19.
96243. 000
3764. 800
0. 53::
-1. 450
9.4.3::
-21.200
-2. 719
-2. 247
-2. 15*.
20.
96271.000
3763.700
0. 467
-1. 100
9. 900
-22. "300
-2. 357
-2.25::
-2. 161
21.
96303. 000
3760. 900
0. 53'::
-2. 800
10.43::
-25. 100
-5. 250
-2. 40t.
-2. 17::
(continued)
-------
TABLE A-58 (continued)
Page 5 of 1
Reading
No.
T. Bin
W, Ib
AT. h
AU. Ib
EAT. h
EAU. Ib
/AW\ .
(—) Ib/h
\AT/,
Aau\ ,
\iSfj,
X. lb/h
22.
96329. 000
3760. 300
0.43::
-0. 600
10. 367
-25. 700
-1.335
-2. 365
-2. is;:
23.
96368. 000
3757. 600
0. 650
-2. 700
11.517'
-23. 400
-4. 154-
-2. 46t.
— ~* 1O^
h. • 1 . .'
24.
96399.000
3756. 300
0.517
-1. 300
12. 03::
-29. 700
-2. Sic.
-2. 46:;:
-2. 207
25.
96425. OOO
3756. 250
0.43::
-0. 050
12. 467
-29. 750
-0. 115
-2. 3 St.
-2.214
26.
96452. 000
3754. 550
0. 450
-1.700
12.917
-31.450
-3.77:i:
-2.435
-^. ^'2.:
27.
96484. 000
3754. 300
0. 53:::
-0. 250
13.450
-31. 700
-0. 469
-2. 357
-2. 22£:
fO
-J
KJ
(continued)
-------
TABLE A-58 (continued)
Page 6 of 7
Reading
No.
T. Bin
y. ib
AT. h
AH. Ib
I AT. h
lay. Ib
(SO. '«•
(M?). »"•
X. lb/h
" O
•_ '»• •
96510. 000
3752. 600
0. 43::
-1.700
13.38::
-33. 400
-3.92-::
-2. 40t.
-2. 23C.-
29.
96549. 000
•3751.250
0. 650
-1. 350
14.53J
-34.750
-2. 077
-2.391
-2.241
30.
96575. 000
3750. 050
0.43::
-1.200
14.967
-35. 950
-2. 76'!'
-2. 40:-
-2. 24t.
31.
96607. 000
3749. 500
0.53::
-0. 550
15. 500
-36.500
-1.031
-2. 35*
-2. 250
32.
96634.000
374S. 300
0. 45-0
-1.200
15.950
-37.700
-2. 667
-2. 364
-2. 25'::
33.
96666. 000
3747. 000
0.53::
-1. 300
16. 48 ::
-39.000
-2.437
-2. 36t.
-2. 257
u>
(continued)
-------
TABLE A^SS (continued)
Page 7 of 7
Reading
No.
T. min
U, Ib
AT. h
AW. Ib
CAT. h
EAU, Ib
(AT) lb/h
(^~\ lb/h
X. lb/h
34.
•? 6 6 96. 000
3745. SOO
0. 500
-1.200
16.93::
-40. 200
-2. 400
-2. 367
-2. 260
35.
96721. 000
3745. 750
0.417
-0. 050
17. 400
-40. 250
-0. 120
-2. 311:
- •' "'h "'
36.
96751.000
3744. 000
0. 500
-1. 750
17. 900
-42. 000
-3.500
-2. 34t.
-2. 261
37.
967S1. 000
3743. 000
0. 500
-1.000
IS. 400
-43.000
-2. 000
-2. 337
-2. 26*.
96809. 000
3742. 500
96825. 000
3746. 000
n 36
Slope -2.406
Intercept 0.524
Syx 4.091
Sx 5.390
S 0.128
O
Sb 0.118
S 12.270
2.032
r -0.988
Confidence interval
2.406 + 0.26U
-------
TABLE A-59 SUMMARY OF DATA FROM TEST NO. 33
Page T of J__
Degreaser B, operating
Solvent: 1,1,1-Trichloroethane
PC
Date 1/29/79
FB 75 I
Inlet air
Other
x SC _
xhaust air x
A
16'
501
fTTSTin
Ambient air
Temperature 69 "F
Pressure - in. l
-------
TABLE A-59 (continued)
2 of 7
Redding
No.
T. m\n
y. ib
AT. h
AM, Ib
I AT. h
LAW. Ib
(30. ">"•
(Mr) lb/h
X. lb/h
4.
95778. 000
2923. 400
0.43::
0. 000
1.63::
-3. 100
0. 000
-1.84J1
-1. 99:-:
5.
95797. 000
2927. 300
0. 317
-0. 600
2. 000
-3. 700
-1. 395
-1.350
-1.961
6.
95331. 000
2926. 700
0. 567
-1. 100
2. 567
-4. 300
-1.941
-1. 870
-1.94-::
i •
95352. 000
2926. 200
0. 350
-0. 500
2.917
-5. 300
-1.429
-1.317
-1.92:-
8.
95399. 000
2924. 700
0.781:
- 1 . 500
3. 700
-6. 300
-1.91=.
- 1 . 83::!
-1.910
9.
95924. 000
2923. 500
0.417
-1.200
4. 117
-3. 000
-2. 380
-1.94C:
-1.914
N>
(continued)
-------
TABLE A-59 (continued)
Pd(,e 3 of 7
Reading
No.
T. Bin
U. lb
AT. h
AW, Ib
£AT. h
LAW. )b
(S). »"
(Mr). ">"•
X. Ib/h
1 0.
95955. 000
2922. 400
0.5 IT1
-1. 100
4.63::
-9. 100
-2. 129
-1.964
-1.920
11.
95989. 000
2921. 2 On
0. 567'
-1. 200
5. 200
-10. 300
-2. ll*
-1.931
-1.92t.
12.
96020. 000
2920. 000
0.5 IT1
-1.200
5.717
-11.500
-2.32::
-2.0K:
-1.934
13.
96048. 000
2919. 200
0. 467
-0. SOCi
6. 18::
-12.300
-1.714
-1.989
-1.938
14.
96081. 000
2918.800
0. 550
-0. 400
6. 7-K-:
-12.700
-0. 727
-l.SSt-
-1.934
15.
96107.000
2918.000
0.43;:
-0. 800
7. 167
-13.500
-1.84t.
-1.884
-1.93J
(continued)
-------
TABLE A-59 (continued)
Page 4. of 7
Reading
No.
T. «tn
y. Ib
AT. h
AU, Ib
EAT. h
EAU. Ib
/au\ ,
(77) Ib/h
V»T/,
fa»\ lh/h
05T;, lb/h
X. lb/h
16.
96145.000
2917.000
0. 63::
-1.000
7. 800
-14.500
-1.579
-1.859
-1.92t-
17.
96177.000
2916.200
0.53::
-0. 800
8. 33::
-15.300
-1.500
-1.83t.
-1.920
18.
96211.000
2915.500
0. 567
-0. 700
8. 900
-16.000
-1.235
-1.79:1:
19.
96243.000
2914.250
0.53-::
-1.250
9.43::
-17.250
-2. 344
-1.829
-1.90?:
20.
96271.000
2913.550
0. 467
-0. 700
9. 900
-17.950
-1.500
-1.8K:
-1.90::
21.
96303. 000
2912.350
0. 53C:
-1.200
10.433
-19. 150
-2. 250
-1.835
-1.900
NJ
«J
00
(continued)
-------
TABLE _A-59 (continued)
Page .5 of 7
Reading
No.
T. Bin
U, Ib
AT. h
AU. Ib
CAT. h
CAM. Ib
/AU\
(IT) lb/h
\AI/.
(iir) Ib/h
X. 1b/h
^. -•
96329.000
2911. 700
0. 4 3 ::
-0. 650
10. 867
-19.800
-1.500
-1.82J1
-l.S9t-
23.
96363. 000
2910. 150
0. 650
-1.550
11.517
-21. 350
-2. 33<-
-1. 354
-1.894
24.
96399. 000
2909. 800
0.517
-0. 350
12.03::
-21.700
-0. 677'
-1.803
-1. 890
•jc;
96425. 000
2909. 350
0.433
-0. 450
12.467
-22. 150
-1.03*
-1. 777
-l.SSt-
26.
96452. 000
2903. 250
0. 450
-1. 100
12.917
-23.250
-2. 444
-1.300
-1.88?
27.
96434. 000
2907. 300
0. 533
-0. 950
1 3. 450
-24. 200
-1.73J
-1.799
-1.879
>J
vC
(continued)
-------
TABLE A-59 (continued)
Page 6 of 7^
Reading
No.
T. «in
y. ib
. • •
AT. h
AU. Ib
EAT. h
EAW. Ib
/AU\ .
(IT) Ib/h
\AI/i
Ciir) lb/h
X. lb/h
28.
96510.000
2906. 600
0.43::
-0. 700
1 3. 88'::
-24. 900
-1.615
-1. 794
-1.87*
29.
96549. 000
2904. 600
0. 650
-2. 000
14.53::
-26. 900
-3. 077
-1.851
-1.87'.
30.
96575. 000
2904. 100
0. 433
-0. 500
14.967
-27. 400
-1. 154
-1.831
-1.87::
31.
96607. 000
290-3. 000
0.53::
-1. 100
15.500
-28. 500
-2.06::
-1.839
-1.87::
32.
96634.000
2902. 000
0. 450
-1.000
15.950
-29. 500
-2. 222:
-1.850
-1.371
33.
96666. OOCi
2900. 500
0. 530
-1. 500
1 6. 48'::
-31.000
-2.812:
-1.881
-1.87J:
N)
09
O
(continued)
-------
TABLE A-59 (continued)
Page 7. of 7.
Reading
No.
T, min
U. Ib
AT. h
AU. Ib
EAT. h
EAU. Ib
/AU\ ....
I 77 1 lo/n
\AT/,
V £A1 J*
• •
x. Ib/h
34.
96691.000
2S99. 50d
0. 4 1 7
-1. 000
16.900
-32.000
-2. 400
-1.89::
-1.S7:-
35.
96721.000
2S9S. 250
0. 500
-1.250
17. 400
-33.250
-2. 500
-1.911
-1.874
36.
96 7 51. 00 0
2897. 250
0. 500
-1.000
17.900
-34.250
-2. 000
-1.9i::
-1.87?
J7.
96751.000
2896. 500
0. 500
-0. 750
IS. 400
-35.000
-1.500
- 1.9 CO
-1.87"..
96809. 000
2S96. 500
9685S. 000
2897. 000
n 36 Syx 0.553 tQ/2 2.032
Slope -1.850 *x 5.38i r -l.QOO
Intercept -0.087 Sa Q.017 Confidence interval
\ 0.118 1.850 + 2.0*9
S,. 0.943
N>
00
-------
TABLE A-60 SUMMARY OF DATA FROM TEST NO. 34
Page 1 of 7
Oegreascr A, operating
Solvent: 1,1,1-THchloroethane
Date 1/31/79
FB 50 %
Inlet air x
Other
PC
SC
Exhaust air
A 50 %
8 ft/min
Ambient 'air
Temperature °F
Pressure in. Hg
Humidity %
Reading
No.
T, m1n
W, 1b
AT. h
AW. 1b
EAT. h
EAW, Tb
(S). "•"•
(Sft '""'
X. lb/h
97314. ooo
3510. ;:00
9734*.oOO
3510. -loo
•'^'•^"l.OOO
3502. ?:0o
1.
•37-Mfi. nnn
3504. 000
?
•— •
97442. 000
3502. 400
o. 53;:
-l.bOO
0.53::
-1.600
-3.000
-3. 000
- 3. 000
3.
974S4. 000
3501.200
0. 700
-1.200
1.231:
-2. 800
-1.714
-2. 270
' -2.635
N)
00
-------
TABLE A-60 (continued)
Page 2 of 7
-------
TABLE A-60 (continued)
Page 3 of 7
Reading
No.
T niin
If ••> I VI
U. 1b
AT. h
AM. Ib
EAT. h
IAU. Ib
GO. 1Wh
(if). ">"
•
X. Ib/h
10.
97693.000
3493.250
0. 450
-1.000
4. 717'
-10. 750
-2. 222
-2. 279
-2. 57=i
11.
97724. 000
3492. 900
0.517
-0. '350
5.23::
-11. 100
-0. 677
-2. 12J
-2.530
12.
97751.000
•3491.600
0. 450
-1. 300
5. 63!:
-12.400
-2. 88?
-2. is::
-2. 49*
13.
•377ft-:. nrin
3-190. 600
0.53::
-1.000
6.217
-13.400
-1.375
-2. 155
-2. 470
14.
97S16. 000
3439. 000
0. 550
-1.600
6. 767
-15.000
-2. 909
-2.217
-2. 450
15.
97341.000
3433. 750
0.417
-0. 250
7. 133
-15.250
-0. 600
-2. 121:
-2. 427
ISJ
00
(continued)
-------
TABLE A-60 (continued)
Page *_ of J^_
Reading
No.
T, nin
U. Ib
AT. h
aw, ib
EAT. h
EAU. Ib
Of). lb/h
(zir) lb/h
X. 1b/h
16.
97381.000
3437. lOfi
0. 667
-1. 650
7. 350
-16.900
-2.475
-2. 15::
-2. 409
17.
97906. 000
3486. 150
0.417
-0. 950
8. 267
-17.350
-2. 230
-2. 159
-2. 39::
13.
97939. 000
'3435. 000
0. 550
-1. 150
8. 317
-19.000
-2.091
-2. 155
-2. 379
19.
97964. 000
3434. 650
0.417
-0. 350
9.23::
-19. 350
-0. 340
-2. 096
-2. 36::
20.
97991. 000
•3433.500
0. 450
-1. 150
9.681:
-20. 500
-2. 556
-2. 117
-2. 350
21.
98024. 000
3482. 400
0. 550
-1. 100
10.23::
-21.600
-2. 000
-2. 11 J
-2.338
ISJ
l/l
(continued)
-------
TABLE A-60 (continued)
Page 5 of 7
Reading
No.
T. nln
U. Ib
AT, h
AU. Ib
CAT. h
CAW. Ib
/AH\
(rr) 1b/h
\AT/t
f LAW \ • . ••
VCATy '
X. Ib/h
98055. 000
3482. 000
0.517
-0. 400
10.750
-22. 000
-0. 774
-2. 047
-2. 324
23.
93032. 000
3430. 600
0. 450
-1.400
11.200
-23.400
-3. 1 1 1
-2. 039
-2. 314
24.
?S 11 2. 000
3479. 550
0. 500
-1.050
11. 700
-24. 450
-2. 100
-2. 090
-2. 30-f
25.
93137.000
3473. 750
0. 417
-0. 300
12. 117
-25. 250
-1.920
-2. 034
-2. 295
26.
93166.000
3478. 250
0. 433
-0. 500
1 2. 600
-25. 750
-1.034
-2. 04«f
-2. 235
27.
98199. 000
3477. 750
0. 550
-0. 500
13. 150
-26. 250
-0. 909
-1.996
-2. 274
ro
00
(continued)
-------
TABLE A-60 (continued)
Page 6 of Z|__
ISJ
00
Reading
No.
T. nin
U. lb
AT. h
AH, lb
EAT. h
CAU. lb
/AU\
(==) lb/h
W/i
(fir). lb/h
X. lb/h
28.
•98224. 000
3476. 750
0.417
-1.000
13.567
-27. 250
-2. 400
-2. 009
-2. 26-'-
29.
98253. 000
3475. 500
0. 480
-1.250
14.050
-28. 500
-2. m.
-2. Q2S
-2. 255
30.
98285. 000
3474. 750
0.53::
.
-0. 750
14.58::
-29. 250
-1.406
-2. 006
-2. 247
31.
98311.000
3474. 250
0. 430
.
-0. 500
15.017
-29. 750
-1. 154
-1.93J
-2. 23S
32.
98344. 000
3473. 000
0. 550
-1.250
15.567
-31.000
-2. 270
-1.991
-2.230
33.
98331.000
3472. 500
0.617
-0. 500
16. 180
-31.500
-0.811
-1.946
-2.221
(continued)
-------
TABLE A-60 (continued)
Page 7 of 7
Reading
No.
T, min
W, Ib
AT, h
AW, Ib
CAT. h
EAU. Ib
/AM\ lh/h
I TT 1 tV/n
\AT/t
(fir). lb/h
X. lb/h
34.
98404. 000
3471.000
0. 383
-1.500
16.567
-33. 000
-3. 9K:
-1.99?
-2.214,
35. .
98436. 000
3470. 650
0.53::
-0. 350
17. 100
-33. 350
-0. 656
-1.950
-2. 20*.
36.
98468. 000
3469. 250
0.53::
-1.400
17.63::
-34.750
-2. 62=:
-1.971
-2. 200
37.
98502. 000
3468. 750
0. 567
-0. 500
13.200
-35.250
-0. 8821
-1.937
-2. r?::
98532. 000
3468. 250
98551.000
3471.950
n 36 Syx 0.561 tQ/2 2.030
Slope -1.885 Sx 5.246 r -1.000
Intercept -1.750 Sa 0.018 Confidence Interval
O
Sfe 0.120 -1.885+0.036
S,. 1.189
N>
00
00
-------
TABLE A^l SUMMARY OF DATA FROM TEST NO. 34
Page 1 of 7
Ocgrcascr B, operating
Solvent: 1,1,1-THchloroethane
FB 50
Inlet air
Other
PC x SC
Exhaust air
Date 1/31/79
Ambient'air "
Temperature _68_
Pressure
- In. Hg
Humidity TlI
Reading
No.
T, mln
M, 1b
AT, h
AW. Yb
EAT. h
EAW. Yb
(*"} Ib/h
1 TI- 1 • «V n
\AI/,
(Mf) lb/h
\EA /.
X. lb/h
97314.000
297S. 000
97340. 000
2977. 000
97-349. 000
2975. SOO
1.
97394. 000
2975. 400
2.
97442. 000
2974. 400
0. SOO
-1.000
0. 800
-1.000
-1.250
-1.250
-1 '-sn
3-
974S4. 000
2973. SOO
0. 700
-0. 600
1.500
-1.600
-0. 357
-1.067
-1 ISf:
00
\o
-------
TABLE A-61 (continued)
of
Reading
No.
T. Bin
U. Ib
AT. h
AM. Ib
CAT. h
CAU. Ib
(39. ""*
(M?). ">"
Xt lb/h
4.
97510. OOCi
2972. 300
0. 43::
-1.500
1.930
-3. 100
-3. 462:
-1.60;:
-1. 307
5.
97536. 000
2971.200
0.43::
-1. 100
2. 367
-4. 200
-2. 53?:
-1.775
-1.424
6.
97568. 000
2970. 800
0.53]:
-0. 400
2. 900
-4. 600
-0. 750
-1.586
-1.456
^
I •
97594. 000
2970. 000
0.43::
-0. 300
3. 33::
-5. 400
-1.84*
-1.620
-1.48::
3.
97628. 000
2969. 050
0. 567
-0. 950
3. 900
-6. 350
-1.676
-1.62?:
-1.50-
9.
97666. 000
2968. 700
0.63::
-0. 350
4.53::
-6. 700
-0. 553
-1.47?:
-1.501
N)
vD
O
(continued)
-------
TABLE A-61 (continued)
Page 3 of 7
Reading
No.
T. *1n
U. Ib
* V A-.
AT. h
AW. Ib
CAT. h
CAU. Ib
/AVA ....
I TV J ID/h
\AT/.
/ J.uM \ ik.jk
1 rTT 1 ID/I!
X. lb/h
10.
97693.000
2967. 800
0. 450
-0. 900
4. 93-1:
-7. 600
-2. 000
-1.525
- 1 . 504
11.
97724. 000
2966. 100
0.517
-1.700
5. 500
-9. 300
-.3. 290
-1.691
-1.52J:
12.
97751.000
2966. 100
0. 450
' 0.000
5. 950
-9. 300
0. 000
-1.563
-1.52*.
13.
97783. 000
2964. 900
0.53::
" -1.200
6. 43::
-10. 500
-2. 250
-1.620
-1.534
14.
97816. 000
2963. 600
0. 550
-1. 300
7.03::
-11.800
-2. 364
-1.67?:
-1.545
15.
97841. 000
2962. 200
0.417
-1.400
7. 450
-13.200
-3.360
-1.77::
-1.561
(continued)
-------
TABLE A-61 (continued)
Page 4 Of 1
Reading
No.
T. «1n
U. 1b
. • *
AT. h
AW, Ib
EAT. h
EAH. Ib
00. ""*
(Sr). »"•
•
X. Ib/h
16.
97831.000
2962. 250
0. 667'
0. 050
8. 11T1
-13 l^fi
A .' • 1 »' '. •
0. 073
-1.620
-1.563
17.
97906. 000
2960. 350
0.417
-1.400
S. 53::
-14 SSfl
1 " . J J L1
-?.. 360
-1.703
-1.574
18.
97939. 000
2960. 050
0. 550
-0. SOO
9. 081:
-is. •••\c,f\
-1.453
-1.690
-1.581
19.
97964. 000
2959. 300
0. 417
-0. 750
9. 500
-16. 100
-1. 300
-1.693
-1.537
20.
97991. 000
295ft. 2'*ifi
0. 450
-1. 100
9. 950
- 1 "• ^fifi
It . *_ L1 '.'
-2. 444
-1.729
-1.594
21.
98024. 000
2957. 150
0. 550
-1.050
10.500
_1 O -^trri
1 •-• . •_ -' '.'
-1.909
-1.735:
-i.6o::
vO
(continued)
-------
TABLE A-61 (continued)
Page J5_ of 7_
Reading
No.
Tmift
. Bin
U. 1b
AT. h
AH. Ib
EAT. h
EAW. Ib
/AU\
1 OW 1 It* fit
17TI ID/n
W/i
(fir) lb/h
X. Ib/h
22.
98055. 000
2956. 400
0.517
-0. 750
11.017
-19.000
-1.452:
-1.725
-1.607
23.
980R2. nnn
2955. 250
0. 450
-1. 150
11.467
-20. 150
-2. 556
-1.757
-1.61'
24.
98112. 000
2954. 500
0. 500
-0. 750
11.967
-20. 900
-1.500
-1.747
-.1.620
25.
931 37. 000
2952. 750
0.417
-1.750
12. 38.::
-22. 650
-4. 200
-1.329
-1.629
26.
•aoiic nnn
• '• 1 O *? • *J '•" .
2952. 250
0. 48::
-0. 500
12.367
-23. 150
-i.03'.
-1. 799
-1.636
27.
oftl^-a. nnn
2950. 900
0. 550
-1. 350
1.3.417
-24. 500
-2. 455
-1.326
-1.64;:
N)
(continued)
-------
TABLE A-61 (continued)
Page j>. of
Reading
No.
T. Bin
U. 1b
AT, h
AM, 1b
EAT. h
EAU. 1b
(*} 1h/h
i 77 1 iD/n
\AT/,
X. Ib/h
2S.
98224. 000
2949. 750
0.417
-1. 150
13.33;:
-25. 650
-2. 760
-1.35^
-1.651
29.
93253. 000
2947. 250
0. 43::
-2. 500
14.317
-23. 150
-5. 17?
-1.966
-1. 66::
30.
93235. 000
2946. 750
0.53::
-0. 500
14.350
-28. 650
-0.93*
-1.929
-1.671
31.
98311. 000
2945. 750
0.43::
-1.000
15.28::
-29. 650
-2. 308
-1.940
-1.680
32.
98344. 000
2943. 750
0. 550
-2. 000
15.83-::
-31.650
-3. 63t-
-1.999
-1.690
33.
93331.000
2942. 000
0.617
-1.750
16.450
-33.400
-2.030
-1.701
rs>
vO
(continued)
-------
TABLE A-61 (continued)
of
Reading
No.
T_i_
t mm
W, 1b
AT. h
AU. 1b
EAT. h
EAU. Ib
Oft «*
OS). """
X, 1b/h
34.
^8404. nnn
2941.000
0. 33::
-1.000
16.83::
-34. 400
-2. 609
-2.044
-1.711
35.
•?ft4::K. nnn
293?. 750
0. 531:
-1.250
17.367'
-35.650
-2. 344
-2. 05C:
-1.721
36.
484 £8. nnn
2939. 000
0.53J
-0. 750
17.900
-36.400
-1.40*.
-2.034
-1.730
::7.
93502. nnn
2938. 250
0. 567-'
-0. 750
18. 467
-37. 150
-1. 324
-2. 01:-
-1.73ft
93° ^ 2. nnn
2937. 750
4ssrft. nnn
2938.000
vO
n 36
Slope -2.082
Intercept 2.370
Syx 1.153
S.. 5.246
Sa 0.037
O
Sb 0.125
S_ 1.140
2.032
r -1.000
Confidence Interval
2.082 + 0.085
-------
TABLE A-62 SUMMARY OF DATA FROM TEST NO. 35
Page 1 of 7
Degreaser A, operating
Solvent: 1,1,1-Trlchloroethane
PC X SC A en*
Exhaust air __% V ig TVmin
Top on Degreaser B left open between each cycle
Date 2/2/79
FB 50 *
Inlet air x
Other
Ambient iir '
Temperature 68 °F
Pressure - in. Hg
Humidity 37 T,
Reading
No.
T, mln
W. 1b
AT. h
AW, 1b
EAT. h
CAN, 1b
(3). """
©. «""
X, 1b/h
1010SO. OOCi
3434. ft^O
101102. 000
34?;:. 300
10 11 -:-:. rififi
343^'. 100
1.
10 lit-1?. 000
3421"-'. SOfi
^
101226. 000
3424. 250
0. 950
-5. 550
0. 950
-5. 550
-5. :34I'
-5. 34?
-5. 34 J1
3.
10125*. 000
3422. 750
0. 500
-1.500
1.450
-7. 050
-3. 000
-4. SK?
-5. ^;-
K>
vO
-------
TABLE A-62 (continued)
Page ? of
Reading
No.
T. win
U. lb
AT. h
AU. lb
EAT. h
EAU. lb
//\y\
1 UI* 1 ik/k
I TV J lo/n
\AV,
(ZAT). 1b/h
X. Ib/h
4.
101286.000
•3420. 900
0. 500
-1.850
1.950
-8. 900
-.3. 700
-4. 564
-5. 039
5.
101316.000
'3419. 250
0. 500
-1.650
2. 450
-10.550
-3. '300
-4. 30t.
-4. 894
6.
101346.000
3418. 250
0. 500
-1.000
2. 950
-11.550
-2. 000
-.3.91}
-4. 69?:
I •
101374. OOO
341 "50
0. 467
-0. 500
3.417
-12.050
-1.071
-3.527
-•*. 50 ::
8.
101407.000
.3415.250
0. 550
-2. 500
3. 967
-14.550
-4. 545
-3. 66?:
-4. 384
9.
101434.000
3413.500
0. 450
-1.750
4. 417'
-16. 300
-3.889
-3. 69J
-4. 297
(continued)
-------
TABLE A-62 (continued)
Page
of
Reading
No.
T. nin
U, lb
AT, h
AU, lb
CAT. h
CAU. lb
(Sf) """
\AT/,
(fir) lb/h
X. lb/h
10.
101469.000
3412. 000
fl 5fl':
•' • •* — *m *
-1.500
5. 000
-17.800
-2.571
-3. 560
-a. 215
11.
101494.000
3411. 250
0. 4 1 7
-0. 750
5.417
-18.550
-1.800
-3.425
-4. 13t-
12.
101542. 000
3408. 600
0. 800
-2. 650
6. 217
-21.200
-3. 31 1:
-3.410
-4. 070
13.
101574.000
3407. 400
n. ^V:
-1.200
6. 750
-22. 400
-2. 250
-3.319
-4. 007
14.
101593. 000
3406. 400
0.317
-1. 000
7. 067
-23.400
-3. 155:
-3.311
-3.95^
15.
101631. 000
3405. 000
0.63-1:
-1. 400
7. 700
-24. 800
-2.211
-•3.221
-3.901
\O
00
(continued)
-------
TABLE A-62 (continued)
Page f of _7_
vD
Reading
No.
T, nin
U, lb
AT. h
AU. lb
CAT, h
IAU, lb
(Sf) ">/"
\AT/,
t 2.QW \ %• *•
V lATJ '
XlK/h
. iD/n
16.
101645.000
3404.300
0.23::
-0. 700
7. 93:::
-25. 500
-3. 000
-3. 214
-3. 856
17.
101683.000
3402. 900
0. 63-::
-1.400
8. 567
-26. 900
-2.211
-3. 140
- 3. 8 1 1
18.
101705.000
3402. 200
0. 367
-0. 700
8.933
-27. 600
-1.909
-3.090
-3. 76?:
19.
101749. 000
3400. 400
0.73::
-1.800
9. 667
-29. 400
-2. 455
-3.041
-3. 72?:
20.
101301.000
3397. 700
0. 867
-2. 700
10.53':
-32. 100
-3. 115
-3.047
-3. 69J1
21.
101839.000
3396. 800
0.63::
-0. 900
11. 167
-33. 000
-1.421
-2. 955
(continued)
-------
TABLE A-62 (continued)
Page 5 of _7_
Reading
No.
T. nln
H. 1b
AT. h
flU, 1b
CAT, h
EAW, lb
\A 1^ •
(HT) lb/h
X. lb/h
22.
101865.000
33*5. ''00
•— ^ • *m* • w • j '_ •
0.433
-1.600
11.600
-34. 600
-3. 69::
-2. 983
• -3.62::
23.
101924. 000
*w onn
0. 933
-1. 900
12.533
-36.500
-1.93J:
-2.901
- 3. 59 ]
24.
101950.000
3391. 900
0.43::
-1.400
13.017
-37.900
-3.231
— "? *3 1 "f
*_ • . Ik.
-3. 561
25.
102003. 000
-•-•*•:. 41-ifi
0. 96T1
-2. 500
1 3. 933
-40. 400
-2. 58*.
-2. 339
-3.53::
26.
102042. 000
^fifi. nno
0. 567
-1. 400
M. 550
-41.300
-2. 471
-2.37::
-3. 507
27.
102069. 000
3331.000
0. 450
-7. 000
15.000
-43. 300
-15. 55*.
-3.253
-3.497
u>
o
o
(continued)
-------
TABLE /V-62 (continued)
Page 6 of 7
Reading
No.
T. min
U. 1b
AT. h
AU. tb
EAT. h
EAU. Ib
/AU\
1 UIf 1 Ik fk
I -rf 1 iD/n
\AT/.
1 I.uN \ ik.*L.
V iST/ '
X. Ib/h
23.
102109. 000
3385. 400
0. 667
4. 400
15. 667'
-44. 400
6. 600
-2. 334
-3.47J1
29.
102133. 000
3384. 200
0. 400
-1.200
16.067
-45. 600
-3. 000
-2. 33?:
-3.450
;sn_
102163.000
3382. 400
0. 500
-1.300
16.567
-47. 400
-3. 600
-2. 361
-3.429
31.
102196.000
3331.800
0. 550
-0. 600
17. 117
-43. 000
-1.091
-2. 804
-3. 409
102227.000
3380. 300
0.517
-1.500
17.63::
-49. 500
-2. 90;:
-2. 807
-3. 339
33.
102251.000
3379. 700
0. 400
-0. 600
18.03::
-50. 100
-1.500
-2. 778
-3. 370
LJ
O
(continued)
-------
TABLE A-62 (continued)
Page 7_ of 7
Reading
No.
T. min
W, Ib
AT. h
AW. Ib
CAT. h
u>
S CAU. Ib
(AW\ lb/h
\AT/,
(IM\ |K/h
Uu lb/h
X. lb/h
34.
102290. 000
3377. 900
0. 65d
-1.800
18.68:::
-51.900
-2. 769
-2. 77?:
35.
102330.i:iui:i
3376. 000
0. 667
-1.900
19.350
-53.800
-2. S50
-2. 7SO
36.
102367. 000
3375. 600
0.617
-0. 400
19.967
-54. 200
-0. 649
-2.715
-3. 318
_• i .
1023:36. 000
3377. 000
0. 317
1.400
20.28::
-52. 800
4. 421
-2. 60 ::
-3.29?:
" 36 Syx 1.330 tQ/2 2.030
Slope -2.553 $x 5.993 r -0.997
Intercept -4.590 S^ 0.038 Confidence interval
d
Sb 0.115 -2.553+0.077
S,. 3.104
-------
TABLE A-63 SUMMARY OF DATA FROM TEST NO. 35
Page \ of 7 _
Degreaser B, operating
Solvent: 1,1,1-THchloroethane
Date 2/2/79
PC x SC
Exhaust air
FB 50 *
Inlet air _^
Other Top was left Qpen for one_half hour between each load cycle
fl -40 *
16 tt/min
Ambient Sir*
Temperature 68 °F
Pressure - in. Hq
Humidity 37 Z
Reading
No.
Tin in
M. 1b
AT, h
AW, 1b
IAT. h
CAW, 1b
(S). '<""
(EAWN lb/h
\EAT/,
X, lb/h
ini 1RO. 000
?C4CJ7 |;e.f|
101202. nnn
2 S 95. 150
101212. 000
1.
1012^2. nnn
259*5.. nnn
hi •
IO^^H.. nnn
2^nn. snn
0. 400
4. 500
0. 400
4. 500
11.250
11.250
11. 250
3.
1 n i "":;K fini'i
2Qnn snn
0. 500
0. 000
0. 900
4. 500
0. 000
5. 000
S. 12=.
U)
o
U
-------
TABLE ^63 (continued)
Page 2 • of 7
Reading
No.
T, nln
U, 1b
AT. h
AH, 1b
EAT. h
EAU. 1b
(3). '*
CM?). »"•
X, 1b/h
4.
101316.000
2899. 900
0. 500
-0. 600
1.400
3. 900
-1.200
2. 78*.
6. 345
5.
101346.000
2S94. 400
0. 500
-5. 500
1.900
-1.600
-11.000
-0.84::
4. 54:1:
6.
101373. 000
2893. 150
0. 450
-1.250
2. 350
-2. 850
-2. 77?:
-1.211:
3. 39-..
•^
i •
101404. 000
2S92. 900
0. 5 1 7
-0. 250
2. 867
-3. 100
-0. 484
-1.081
2. 650
8.
101434. 000
2892. 500
0. '500
-0. 400
?-. 367
-3.500
-0. 800
-1.040
2. 12::
9.
101469.000
2892. 250
0. 58::
-0. 250
3. 950
-3. -50
-0. 42'i'
-0. 949
1.739
(continued)
-------
TABLE A-63 (continued)
3 of 7
u>
o
Reading
No.
T. «in
U. 1b
AT. h
AU, lb
CAT. h
IAU, lb
(SO. "•»
(Bft ">"
X. lb/h
10.
101511.000
2893. 900
n. ?nn
•— • • i ••• •• '
1.650
4. 650
-2. 100
2. 357
-o. 45::
1.495
11.
101540. 000
2393.500
0. 483
-0. 400
5. 133
-2. 500
-0. 32?:
-0. 487'
1.297
12.
101575. 000
2892. 800
0. 5 ft':
-0. 700
5.717
-3. 200
-1.200
-0. 560
1. 12?:
13.
101592.000
2392. 300
0. 28;:
-0. 500
6. 000
-.3. 700
-1.765
-0.617
0.931:
14.
101629. 000
2891.200
0. KIT1
V • *_' A 1
-1. 100
6.617
-4. 800
-1. 78-
-0. 725
0. 85C:
15.
101643.000
2890. 700
Oo^>--
. ._ •-••.'
-0. 500
6. 350
-5. 300
-2. 14:::
-0. 774
0.735
(continued)
-------
TABLE jA-63 (continued)
Page j_ of
Reading
No.
T. «in
U. lb
AT. h
AU. lb
IAT, h
IAU. lb
GO. ">»
(M?). """
X. Ib/h
16.
101631. 000
2890. SOO
0. 63-I:
0. 100
7.43::
-5. 200
0. 15S:
-0. 69?.
0. 64fi
17.
101705. 000
2390. 000
0. 400
-0. 300
7. SSI:
-6. 000
-2. 000
-0. 761
0.55::
13.
101745.000
2389. 300
0. 667
-0. 700
8. 550
-6. 700
-1.050
-0. 784
0.474
19.
101801. 000
2887. 600
0.93::
-1. 700
9.43::
-8. 400
-1.321
-0. S8t.
0. 39 '::
20.
1018?4. 000
2387. 200
0. 550
-0. 400
10.03::
-3. 800
-0. 72"
-0. 877'
0.331
21.
101364.000
2386. 600
0. 50Ci
-0. 600
10.53::
-9. 400
-1.200
-0. 89J:
0. 270
<*>
o
a*
(continued)
-------
TABLE A-63 (continued)
Page 5 of 7_
Reading
No.
T. Bin
H, 1b
AT. h
AU. 1b
EAT. h
EAU. Ib
(^ lh/h
1 77 1 'O/n
VAT/.
(iSr) lb/h
X. 1b/h
22.
101926.000
2835. 400
1.03::
-1.200
11.567
-10.600
-1. 161
-0.916
0.214
23.
101952.000
2884. 600
0.433
-0. 800
12.000
-11.400
-1.84t-
-0. 950
0. 161
24.
102011.000
2334. 300
0. 98 ::
-0. 300
12.93::
-11.700
-0. 301i
-0.901
0. 1 1 •:!
25.
102043. 000
2834. 000
0.533
-0. 300
13.517
-12.000
-0. 563
-0. 888
0. 07.3
26.
102069.000
2833.400
0.433
-0. 600
13.950
-12.600
-1.385
-0. 903
0. 034
27.
102109.000
283 1.200
0. 667
-2. 200
14.617
-14.300
-3.300
-1.013
-0. 007
(continued)
-------
TABLE A-63 (continued)
Page 6_ of 7
Reading
No.
T. win
U. 1b
AT. h
AW, 1b
CAT. h
CAU. Ib
/AW\
1 Ott 1 Ik 4k
1 TV 1 ID/n
\AT/,
(fir). lb/h
X. lb/h
28.
102133.000
2881.500
0. 400
0. 300
15.017
-14.500
0. 750
-0. 966
-0. 042
29.
102163.000
2880. 900
0. 500
-0. 600
15.517
-15. 100
-1.200
-0.973
-0. 075
30.
102196.000
2880. 400
. 0. 550
-0. 500
16. 067
-15.600
-0. 909
-0.971
-0. 106.
102227. 000
2879. 400
0.51?
-1. 000
16.583
-16.600
-1.935
-1.001
-0. 1 36
102251.000
2878. 800
0. 400
-0. 600
16.983
-17.200
-1.500
- 1 . 0 1':
-0. 16«
102290.000
2878. 300
0. 650
-0. 500
17.633
-17.700
-0. 769
-1.004
-0. 191
o
00
(continued)
-------
TABLE A-63 (continued)
Page 7 of 7
Reading
No.
T. min
W. Ib
AT. h
AU. Ib
EAT. h
CAU. Ib
(M\ lh/h
I TT i iD/n
\AT/,
(fir). lb/h
X. lb/h
34.
102330.000
2377. 600
0. 667
-0. 700
13.300
-IS. 400
-1.050
-1.00c.i
.-0.215
35.
102367. 000
2376. 700
0.617
-0. 900
13.917
-19.300
-1.459
-1.020
-0.239
36.
102452. 000
2376. 700
1.417
0. 000
20. 33C:
-19.300
0. 000
-0.949
-0.259
o
vO
n 35
Slope
Intercept
s
s
2.666
1.297
5.906
0.038
0.108
2.891
2.034
r -0.985
Confidence interval
-1.141 + 0.077
-------
TABU A-64 SUMMARY OF DATA FROM TEST NO. 36
Page 1 of 7
Oegreaser A, operating
Solvent: 1.1,1-THchloroethane
2/4/79
FB 50 X
Inlet air
Other
PC x SC
Exhaust air x
A 70 I
V 16 ft/mln
Date
Ambient afr
Temperature °F
Pressure in. Hg
Humidity li
Reading
No.
T, min
W. Ib
AT. h
AW. Ib
EAT. h
EAW. Ib
(S). ""*
(fsr) lb/h
X. 1b/h
1.
104104.000
3514.200
Ll*
104134.000
3512.700
0. 500
1.500
0. 500
1. 500
3. 000
3. 000
3. 000
3.
104159. 000
3511. 800
0.417
0. 900
0.917
2. 400
2. 160
2.616
2. 809
4.
104193. 000
3509. 500
0. 567
2. 300
1.43.::
4. 700
4. 059
3. 169
2. 929
5.
104230.000
3507. 000
0.617
2. 500
2. 100
7. 200
4.054
3. 429
3. 054
6.
104257.000
3505. 500
0. 450
1.500
2. 550
8. 700
3. 33C:
3. 4 1 ;•
3m 1*1.'
-------
TABLE /U64 (continued)
Page 2- of J_
Reading
No.
T. m\n
U. Ib
AT. h
&H. Ib
CAT. h
CAU. Ib
/AU\
1 I 1h/h
\AT/t
(ifr). 1b/h
K. Ib/h
i •
104278.000
3504. 000
0. 350
1.500
2. 900
10.200
4. 236
3.517
3. 191
8.
104311.000
3502. 200
0. 550
1.800
3. 450
1 2. 000
3.27::
3. 478
3. 23?
9.
104341.000
3501.400
0. 500
0. 800
3. 950
12.800
1.600
3. 24 1
3. 233
10.
104373.000
3499. 200
0. 53C:
2. 200
4. 483
15.000
4. 12=.
3. 34t.
•:. 24S
11.
104400.000
3497. 600
0. 450
1.600
4. 93-;:
16.600
3.556
3. 365
3. 257
12.
104436.000
3495. 100
0. 600
2. 500
5.533
19. 100
4. 167
3. 452
3. 27ei
(continued)
-------
TABLE A-64 (continued)
Page 3 of ]_
Reading
No.
T. min
U. Ib
AT. h
AW, Ib
CAT. h
EAU. Ib
00. ™
(M?). »•"•
X. lb/h
13.
10447:-:. 000
34? 3. 400
0. b!7
2. 700
b. 150
21. 300
4. 37:|;
':'.. 54 1.
"-• ~-'^'f\
_• • u. - '•
U.
104495. 000
3491.400
0. 3t.7
1. 000
b. 517
22. 300
>1. i il i
3. 49'!1
:. 313
15.
104520.000
3490. bOO
0. 417
0. 300
•:.. 93".:
23. bQO
1.920
3. 404
I. 31V
It-.
104555. 000
3433. 100
0. 59::
2. 500
7.517
2b. 100
4. 2St.
3. 47I1
j. 33fi
17.
104533. 000
343b. 900
0. 4b7
i . 200
7.93:=
27. 300
2. 57 1
3. 420
3. 335
13.
104617. 000
3434. 500
0. 5b7
2. 400
3. 550
29. 700
4. 235
3. 474
3. 343
OJ
I-"
N>
(continued)
-------
TABLE A-6A (continued)
Page _4_ of 7
Reading
No.
T. ain
U. Ib
AT. h
AU. Ib
EAT. h
EAU. Ib
(30. "•"
(EAT) lb/h
-
X. 1b/h
19.
104647. 000
3483. 400
0. 500
1. 100
9. 050
30. 800
2. 200
3. 40::
-. -.4-
20.
104672. 000
3482. 000
0. 417
1. 400
9. 467
32. 200
3. 360
3. 401
-. -.c-
2 1 .
104704. 000
3480. 000
0.53::
2. 000
1 0. 000
34. 200
3. 750
3. 420
-, -.=;-.
-
tL tl .
104731.000
3478. 500
0. 450
1.500
10.450
35. 700
3. 33::
3. 4 It-
3. 35t.
-i -.
104770. 000
3476. 200
0. 650
2. 300
11. 100
38. 000
3. 53:!:
3.42::
3. 359
24.
104796.000
.3474. 500
0.43::
1.700
11.53'.:
.39. 700
3.92::
3. 44?
3. '36'.:
U)
(continued)
-------
TABLE A-64 (continued)
Page 5 of 7_
Reading
No.
T. oin
W, lb
AT. h
AU. lb
EAT. h
EAU. lb
(|y) Ib/h
AAH\ ,b/h
\IAT/
X. Ib/h
25.
104330. 000
3472. 250
0. 567
2. 250
12. 100
4 1 . 950
3.971
3. 467
3. 367
26.
104863. 000
3470. 5 Oli
0. 550
1. 750
12. 650
•43. 700
3. is:-
3. 4W
3. 3n
il i .
104895. 000
3463. 750
0. 53::
1. 750
13. IS::
i5. 450
3. 281
3. 44;;:
3. 374
23.
104921. 000
3467. 750
0. 43::
1 . 000
13.617
46. 450
2. 30 f:
3. 41]
- t'"^
29.
104953. 000
3465. 850
0.53::
1.900
14. 150
43. 350
3.56::
3.417
3. 377
30.
104985.000
•3463.900
0.5-3::
1.950
14.68::
50. 300
3. 65*.
3. 42t-
3. 37S
(continued)
-------
TABLE A-64 (continued)
Page 6 of 7
Reading
No.
Tnin
, nin
U. lb
AT. h
AU, lb
CAT, h
£AU. lb
(39. ""•
(Mr) lb/h
X. lb/h
31.
10501 1. 000
3462. 500
0. 43:;:
1.400
15. 11 7
51. 70 0
3.231
3. 420
3. 380
32.
insn-T. firm
3461. 100
0.43::
1. 400
15. 550
53. 100
j. 231
3.41!.
3. 331
33.
insfKVi. firm
3459. 000
0. 550
2. 100
16. 100
55. 200
?. Sit:
.3. 429
3. 38J1
3*.
105103. OOCi
3456. 750
0. 550
2. 250
16. 650
57. 450
4. 09)
3. 450
3. 38-
35.
1051 36. 000
3455. 250
0. 550
1.500
17.200
53. 950
2. 727
3. 427
3. 38t-
36.
105163.000
•~t 4 C *™i 1 rt I™ 1
-345 3m 4IJU
0.53::
1.850
1^ ^ •*! ™ 1
i . f :• .•
60. 300
.3. 469
3. 429
3. 387
tJ
(continued)
-------
TABLE A-64 (continued)
Page 7 of 7
Reading
No.
T, min
W, Ib
AT. h
AW. Ib
CAT. h
EAH. Ib
(3). "»*
(Sfl ™
X. 1b/h
:.-t
i 05 194. OOCi
3451. 750
0. 431:
1. b5Ci
13. 167
t. 2. 450
3. 80S:
3. 4:::;:
:•. 3d':
u>
n 36
Slope 3.443
Intercept -0.151
0.311
5.334
0.010
0.115
0.725
t „ 2.032
Q/2
r 1.000
Confidence interval
3.443 + 0.0204
-------
TABLE A-65 SUMMARY OF DATA FROM TEST NO. 37
Page 1 of 5
Degreaser A, operating
Solvent: Methylene chloride
FB 50 « PC
Date 4/1/79
Inlet air
Other
x SC _
xhaust air x
A 50 %
V 8 ft/min
AmbientaTr
Temperature 67 °F
Pressure 29^35 in. Hg
Humidity 62^
Reading
No.
T, min
N. lb
AT. h
AW, lb
IAT, h
EAU, lb
(!r), lb/h
(Mr). lb'h
X, lb/h
1.
184557.000
3504. 200
o
k* •
,54636. 000
3502. 500
1. 317
-1. 700
1.317
-1. 700
-1. 291
-1.291
-1.29J
3.
184679.000
3501. 400
0. 717
-1. 100
2. 03::
-2. 800
-1.53=.
-1. 377
-1.334
4.
184 725. 000
3499. 500
0. 8 1 7
-1.900
2. 850
-4. 700
-2. 327
-1.649
-1. 439
5.
184789.000
3498. 000
1.017
-1.500
3. 867
-6. 200
-1.47"..
- 1 . 60 1:
-1.4 SO
6.
184856. 000
3495. 00 Ci
1. 117
-3.000
4.98.-:
-9. 200
-2. 687
-1.84t.
-1.55;:
w
-------
TABLE A-65 (continued)
Page 2 of _5_
Reading
No.
Tin 4 M
t in in
W, lb
AT, h
AW, lb
EAT, h
LAW, lb
($). lb/h
Cfir) lb/h
X, lb/h
1 •
IOdQ i i nrifi
•-.'". i 1 • U U U
3494. 500
0.917
-0. 500
5. 900
-9. 700
-0. 54S
-1.644
-1.568
8.
184973. 000
3493. 500
1.033
-1. 000
6.933
-10. 700
-0. 96?:
-1.543
-1.565
9.
I'-'CT.n -1 1 Tn'ifi
•-• -iij -• i . ijiji.i
3492. 000
0. 967
-1.500
7. 900
-12.200
-1.552
-1.544
-1.562
10.
185089. 000
3489. 900
0. 967
-2. 100
8. 867
-14. 300
-2. 172
-1.613
-1.568
11.
Ift51=i-:. 000
3488. 000
1.06?
-1. 900
9.933
-16. 200
-1.78J
-1.631
-1.574
12.
185212. 000
3486. 400
0. 983
-1.600
10.917
-17.800
-1.627
-1.631
-1.579
tJ
«-<
00
(continued)
-------
TABLE A-65 (continued)
Page 3 of 5_
Reading
No.
T, m1n
W, lb
AT, h
AW, lb
EAT, h
£AW, lb
GO. ™
(SO. lb/h
X. lb/h
13.
185271.000
3484. 800
0. 983
-1. 600
11. 900
-19.400
-1. 627'
-1. 630
-1.584
14.
1853 30. 000
343-3. 100
0.98::
-1.700
12.88;:
-21. 100
-1.729
-1.63B
-1.58?:
15.
1853S8. 000
3481.400
0. 967'
-1. TOO
1 :•. 850
-22. 800
-1. 759
-1. 646.
-1.592
16.
185447. 000
3479. 600
0. 9S3
-1. 800
14.833
-24. 600
-1.831
-1.65*
-1.59*
17.
185505.000
3475. 200
0. 967
-4. 400
15.800
-29. 000
-4. 552
-1.835
-1.611
18.
185568. 000
347:. 000
1. 050
-2. 200
16. 85(i
-.":!. 200
-2. 095
-1. 85:-
-1. 625
10
(continued)
-------
TABLE A-65 (continued)
Page 4 of _5_
Reading
No.
T, mln
W, lb
AT, h
AW, lb
EAT, h
EAW. lb
f^ Ih/h
1 Tr 1 iD/n
W/,
(fir), lb/h
X, lb/h
19.
18562^. 000
3474. 000
0. 933
1.000
17.333
-30.200
1.01?
-1.693
-1.62?
20.
135634. 000
3470. 500
0. 950
-3. 500
1 8. 733
-3::. 7 fin
*" -• • t1 O^
-1. 794
-1. 638
21.
135744.000
3471. 000
1.000
0. 500
19. 73;:
-33.200
0. 500
-1.67£:
-1.640
~- '•
135308. 000
3469. 500
1. 067
- 1 . 500
20. 350
-34. 700
-1. 40t.
-1.664
-1. 641
23.
135374. 000
3467. 900
1. 100
-1.600
21.950
-36. 300
-1.45!.
-1.654
-1.642
24.
18593;?. 000
3466. 400
0. 933
-1.500
22. 933
-37. Sfifi
» • • V v \ *
-1.52!.
-1.643
-1.6«
OJ
ro
o
(continued)
-------
TABLE A-65 (continued)
Page 5 of _5_
Reading
No.
T, min
W, Ib
AT, h
AW, Ib
EAT, h
EAW, Ib
(EAH\ IL/U
X, lb/h
25.
185988. 000
3464. 900
0.917'
-1.500
£3.850
-39. 300
-1.63*.
-1.648
-1.64:-
186023. 000
3465. 400
186112.000
3465. 300
u>
n 24
Slope -1.71
Intercept 0.427
Syx 1.063
S 7.01b
Sa 0.032
a
Sb 0.178
S. 1.110
t ., 2.074
a/ 2
r -0.999
Confidence interval
1.71 + 0.066
-------
TABLE A-66 SUMMARY OF DATA FROM TEST NO. 37
Page 1 of 5
Degreaser B, operating
Solvent: Methylene chloride
PC
Date 4/1/79
FB 50 I
Inlet air
Other
x SC _
xhaust air x
A
8
50 %
Tin in
Ambient air
Temperature 67 °F
Pressure29.35J". Hg
Humidity bj 1
Reading
No.
T, m1n
W. Ib
AT, h
AW, Ib
EAT, h
EAW. Ib
(S). ">»
(^f) lb/h
X. lb/h
lR4sn~:. nnn
•3004. 500
lR4ci2":. nnn
"ififih.. son
1R4S -:2. nnn
300-:. inn
1.
lft4Shi. nnn
•:nni. grin
2.
lft4K4n. nnn
•:••:» el*. Qfifj
1/31T1
-1.900
1. -31T'
-1.900
-1.44;:
-1. 44-;:
-1. 44!:
3.
Ifi4h.:::":. nnn
2iq<:i7. :::nn
0.717
-2. 600
2.033
-4. 500
-3.*28
-2.213
-1.82B
LJ
N>
N)
-------
TABLE A-66 (continued)
Page 2 of 5
Reading
No.
Tmln
W. Ib
AT, h
AW, Ib
EAT. h
LAW, Ib
(?D. lb/h
AAW\ ....
I "TAT J ID/"
\EATy,
X, lb/h
4.
134731. 000
0. 300
-1. 000
2.33::
-5. 500
-1. 250
-1.941
-1. 8*t.
5.
1847Qi. nnfi
2 * •=>':. son
1.000
-2. 300
3.33!:
-3. -300
-2. 300
- ~' 1 £ Ci
LI 1C1.1
-1.941
b.
Ifi4fi5'3. nnn
1 . 1 33
-2. 900
•». 967
-11.200
-2. 559
-2. 255
-2. 004
I •
Ifl4qi ::. nnn
2qflR. 4nn
0. 900
-2. 200
5. 367
- 1 3. 400
-2. 444
-2. 234.
-2. 050
3.
1 ftd1^"1 ~: fififi
T'QO~* Jflfl
1. 000
-1.000
6. 367
-14. 400
-1.000
-2. 097
-I. 057
'9.
•*
oooGk i nfi
0. 967
-2. 300
7. 333
-16.700
-2. "379
-2. 1.32
-2. 06S
u>
tsj
(continued)
-------
TABLE A-66 (continued)
Page 3 of 5_
Reading
No.
T, m1n
U, 1b
AT, h
AW, 1b
EAT, h
I AH, 1b
$). lb/h
/EAW\ lb/h
VEST/,
X, lb/h
10.
issrifi*. nnn
2932. 400
0. 967'
-2. 700
3. 800
-19.40fi
-2. 79::
-2. 205
-2. 08J1
11.
185153. nnn
2930. 000
1.067
-2. 400
9. 367
-21.300
-2. 250
-2. 209
-2. 094
12.
135212. nnn
2977. 700
0. 933
-2. 300
10. 350
-24. 100
-2. 339
-2. 22)
-2. 106
13.
1R5271. nnn
2976. 300
0. 98::
-1.400
11.33::
-25. 500
-1.424
-2. 155
-2. llfi
14.
Ift^'i'in. nnn
2973. 100
0. 933
-3. 200
12. sir
-28. 700
-3.254
-2. 239
-2. 120
15.
185338. 000
2970. 100
0. 967
-3.000
13.733
-31.700
-3. 103
-2. 300
-2. 133
(continued)
-------
TABLE A-66 (continued)
Page 4 of _5^
Reading
No.
T, mln
M, 1b
AT, h
AW. 1b
EAT, h
ZAW, 1b
(ir) lb/h
AAW\ lb/h
\i5Tj,
X, lb/h
16.
185447. 000
2QhR. 4nri
0. 98::
-1.700
14.767
-33.400
-1.729
-2. 26C1
-2. 14]
17.
13 55ns. nnn
29*5. ftnn
0. 967
-2. 600
15.73^:
-36. 000
-2. 690
-2. 23 8
-2. 151
18.
I855fift. nnn
29^ ::. nnn
1.050
-2. 300
16. 73::
-33.300
— >L . t1 11 '
-2. 31:-
-2. 160
19.
!R^h27. nnn
2'^.n. ftnn
0. 93-::
-2. 200
17.767
-41.000
-2.237
-2. 308
-2. 168
20.
l ft s Aft 4. nnn
'""^sft snn
0. 950
-2. 300
13.717
-43. 300
- '• 4 :' 1
h. • " »- J
- "' ": 1 ":
h. • _• i .•
— -• 1 ^»-
hi • 1 1 •.'
21.
1RS744 nnn
2qcici snn
1.000
- 3. 000
19.717
-46. '300
-3.000
-2. 34?:
-2. 13=.
tJ
N)
(continued)
-------
TABLE A-66 (continued)
Page 5 of 5
Reading
No.
U, Ib
AT. h
AW. Ib
EAT, h
EAU. Ib
(ir). lb/h
(Sf). ^
X. lb/h
22.
Iftssfifi. nnn
2954. 500
1.067
-1.000
20.73::
-47. 3Qd
-0. 937
-2. 27t.
-2. 189
23.
iaci:::74. nnn
2952. 000
1. 100
-2. 500
21. 8 S::
-49. 300
-2. 27'":
-2. 27t.
-2. 19::
24.
1 ft so 3 3. nnn
2949. 900
0. 9ft'":
-2. 100
22. 8*7
-51.900
-2. 1 ::•:.
-2. 270
-2. 19f.
25.
IftSQfifi. nnn
2947. 700
0.917
-2. 200
23.78::
-54. 100
-2. 400
-2. 275
-2. 199
1ft h.n.11 3. nnn
2943. 300
IftMfi-a. nnn
2948. 000
N>
n 24
Slope -2.32
Intercept 0.914
yx
0.574
6.998
0.017
0.177
0.698
t ., 2.074
a/ 2
r -1.000
Confidence Interval
2.32 + 0.035
-------
TABLE A-67 SUMMARY OF DATA FROM TEST NO. 38
Page _1 of 5
Degreaser A, operating
Solvent: Methylene chloride
Date 4/2/79
FB 50 %
Inlet air
Other
PC y SC
x txhaust air x
V 8
50 _?
min
Ambient air
Temperature 67 °F
Pressure 29.62 in. Hg
Humidity 50 %
Reading
No.
Tin 4 n
• in i ri
W. 1b
AT, h
flW, 1b
EAT. h
EAW. 1b
(If). ™
(8ft ">'*
X, Ib/h
186276. 000
3500. 900
1862'? 4. 000
'•.A**, nnfi
1?>. ~:fifi. nnfi
::4?7. "f-OO
1.
lftK':':fi. 000
34?b. 100
-i
w •
!Sb4:;i4. rnjfi
34-?5. 000
1.25 !:
-1. 100
1.23::
-1. 100
-o. s?::
-o. •$.?:•
-o. e?;:
3.
186468.000
3492. 400
1.067
-2. 600
2. 300
-3. 700
-2.437
-1.60?
-1.250
u>
N)
-------
TABLE A-67 (continued)
Page 2 of _«j_
Reading
No.
T, mln
W, lb
AT, h
AW, lb
EAT, h
CAW, lb
(ir). lb/h
(Mr). lb'h
X, lb/h
4.
186527. 000
3490. 100
0. 933
-2. 300
3. 233
-6. 000
• 1* ™* "* Q
«_ • — • -1 j
-1.827
-1.443
5.
186594.000
-3433. 000
1 . 1 1 7
-2. 100
4. 400
-8. 100
-1.881
-1.841
-1.542
6.
186650. 000
3436. 300
0.9? 3
-1. 700
5. 333
-9. 800
-1.321
-1.839
-1.601
i .
186713. 000
3434. Sfici
1.050
-1. 800
6. 383
-11. 600
-1.714
-1.817
-1.637
8.
186763.000
3479. 500
0.917
-5. 000
7. 300
-16. 600
-5. 455
-2. 274
-1. 728
9.
18*6829.000
3479. 500
1.017
0. 000
8. 317
- 1 6. 600
0. 000
-1.996
-1.762
N)
00
(continued)
-------
TABLE A-67 (continued)
Page 3 of 5_
u>
to
Reading
No.
T, mln
W. Ib
AT, h
AW. Ib
LAT, h
EAW, Ib
(AT), lb/h
(fir). lb/h
X, lb/h
10.
186885.000
3477. 800
0.933
-1.700
9. 250
-18.300
-1.821
-1.97?:
-1.786
11.
186944. 000
3476. 000
0. 983
-1.800
10.23-::
-20. 100
-1.83J
-1. 964
-1.804-
12.
187005.000
3473.800
1.017
-2. 200
11.250
-22. 300
-2. 164
-1.982
-1.820
13.
187062.000
3472. 300
0. 950
- 1 . 500
1 2. 200
-23.800
-1.579
- 1 . 95 J
-1.831
14.
187125.000
3470. 200
1.050
-2. 100
1 3. 250
-25. 900
-2. 000
-1.955
-1.840
15.
187183.000
3468. 300
0. 967
-1.900
14.217
-27. 800
-1.966
-1.951J
-1.849
(continued)
-------
TABLE A-67 (continued)
Page 4 of __§_
Reading
No.
T, mln
N. 1b
AT, h
AW, 1b
CAT, h
J-AU IK
c«un y i w
(Sfj. """
X, Ib/h
16.
187244.000
3466. 200
1.017
-2. 100
15.233
-2. 066
-1.963
-1.856
17.
187303.000
3464. 800
0.983
-1.400
16.217
-31. 300
-1.424
-1.930
-1.861
18.
187364.000
3462. 800
1.017
-2. 000
17.233
-33. 300
-1.967
-1.932
-1.865
19.
187429.000
3460. 800
1.08':
-2. 000
18.317
-35. 300
-1.846
-1.927
-1.86?:
20.
187488.000
3459. 000
0. 983
-1.800
1 9. 300
-37. inn
W • • A — »
-1.83J
-1.922
-1.87J
21.
187560.000
3456. 800
1.200
-2. 200
20. 500
-39. 300
-1.833
-1.917
-1.874
u>
o
(continued)
-------
TABLE A-67 (continued)
Page 5 Of 5
Reading
No.
T, mln
W, Ib
AT, h
AW, Ib
EAT, h
EAW. Ib
(S). ">'"
(SO. """
X, lb/h
22.
187A04. 000
3455. 100
0.733
-1.700
21.233
-41.000
-2.31?:
-1.931
-1.87*.
23.
187 Am. firm
3453. Ann
1. 100
-1.500
-. -. -. -. g
-42. 500
-1. 3*4
- 1 . 903
-1.878
24.
187721. 000
3451.400
0. 850
-2. 200
23. 183
-44. 700
-2. 580
-1.928
-1.880
25.
187778.000
3449. 300
0. 950
-1. 600
24. 1 33
-4 A. 300
-1. 684
-1.919
-1.881
187814. 000
3450. 000
187900.000
3452. 100
n 24 Syx 0.724 tQ/2 2.074
Slope -1.94 Sx 7.053 r -1.000
Intercept 0.055 S 0.021 Confidence Interval
a
Sb 0.184 1.94 +_ 0.044
Sc 0.913
-------
TABLE A-6C SUMMARY OF DATA FROM TEST NO. 38
Page i of 5
Degreaser B, operating
Solvent: Methylene chloride
PC x
Exhau
FB 50 %
Inlet air x
Other
_ sc
laust air x
V 8
mn
Date 4/2/79
Ambient air
Temperature 67 °F
Pressure 29J>Zjn7~Hg
Humidity bU %
Reading
No.
T, mln
M, Ib
AT. h
AW, Ib
EAT, h
EAW, Ib
(ir) lb/h
(Mr). lb'h
X, lb/h
186273. OOO
3045. 000
1 362'? 1.000
3033. 30CI
186297.000
3036. 200
1.
186 3 30. 000
3036. 000
,.
136404. 000
3034.600
1.231:
-1. 400
1. 23'.:
-1.400
-1. 13}
-1. 13}
-1. 13}
3.
186463. 00 0
3031. 700
1.067
-2. 900
2. 300
-4. 300
-2.71-:'
-1.370
-1.50J1
u>
-------
TABLE _A-68 (continued)
Page 2 of 5
Reading
No.
T. «1n
U. 1b
AT. h
AW, 16
EAT. h
EAU. 1b
(*} Ih/h
V Tf I iD/n
\AT/,
(fir) lb/h
X. lb/h
4.
186527. 000
0.93::
-1.800
3. 28;:
-6. 100
- 1 . 83 J
-1.858
- 1 . 62 ]
5.
186594. 000
3027. 600
1. 117
-2. 300
4. 4 Oil
-8. 400
-2. 060
-1.909
-1.69::
6.
136650. 000
3026. 300
0.93::
-1. 300
5. '33::
-9. 700
-1. 39::
-1.819
-1.718
,
186713.000
JU^4. U 00
1. 050
-2. 300
6. 38::
-12.0i:ii:i
-2. 190
-1. 880
-1. 745
a.
186768. 000
3022. 600
0.917
-1.400
7. 300
-13.400
-1.527
-1.83t-
-1.758
186829.000
3021. 700
1.017
-0. 900
8. 317
-14.300
-0. 335
-1.719
-1.75;:
UJ
LJ
U)
(continued)
-------
TABLE A-68 (continued)
Page 3 of 5
Reading
No.
T. min
W, 1b
AT. h
AW. Ib
CAT. h
EAU. Ib
(I?), w
(ft?). ">'"
X. Ib/h
10.
18688**. nnn
30 IS. 000
0. 933
-3. 70 Ci
?. 25 Ci
-18. 000
-3.964
-1.94t.
-1. 77!.
11.
lfth.s.14 nnn
* • V m 1 ~ • 1^1 •_! I_I
3016. 500
0. 9 S3
-1.500
10. 233
-19. 500
-1.525
- 1 . 906
-1. 789
12.
1 ':'~Tn~iir. rififi
I •-• i IJU J. IJIJI.I
•3014.000
1.017
-2. 500
11.250
-22. 000
-2. 459
-1.956
-1.S03
I1"' ^ l~l .^ ~l l™i i~l I* I
O i Ut'w. IJIJI.I
3012. 700
0. 950
-1. 300
1 2. 200
-23. 3 00
-1. 366:
-1.910
-1. 812
1,~. ^ 4 — ^ « B •
bi 1^:5. LI iju
3010. 000
1.050
-2. 700
1 3. 250
-26. 000
-2.571
-1. 962
-1.823
187183.000
3008. 000
0. 967
-2. 000
U.217
-28. 000
-2. 061:'
-1. 970
-1.834
LJ
(continued)
-------
TABLE A-68 (continued)
Page 4 of 5
Reading
No.
T. aln
U. 1b
AT, h
AW. Ib
CAT. h
EAU. Ib
(10. »"
(#). "•"•
X. lb/h
16.
187244. 000
.3006. 000
1 . 0 1 T'
-2. 000
15. 2'33
-30. 000
-1.967
-1.969
-1.843
17.
137 3 03. 000
3004. 500
0. 9S3
-1. 500
16.217
-31.500
-1.525
-1.942
-1.S49
18.
1S7364. 000
'3002. 100
1.017
-2. 400
17.233
-.33. 900
-2. 361
-1.967
-1.85*.
19.
1S7429. 000
3000. 300
1.083
-1. 80(i
is. 31 r
-35.700
-1.662
-1. 949
-1.861
20.
137433. 000
2997. 600
0. 983
-2. 700
19. 300
-38. 400
-2. 74t.
-1. 990
-1.368
21.
137560.000
2*^. ::nn
1.200
-2. 300
20. 500
-40. 700
-1.917
-1.935
-1.874
u>
OJ
(continued)
-------
TABLE A-68 (continued)
Page b_ of _5_
Reading
No.
T, min
U, Ib
AT, h
AW. Ib
EAT, h
EAU, Ib
{M\ Ih/h
1 TV I lb/n
\AT/,
(fir). lb/h
X. lb/h
-• -•
187604. 000
J994. 10LI
-1. 200
21. 233
-41. 900
-1.636
-1. 973
-1.879
:. -,
137670. 000
.;**!. 400
1. 100
-2. 700
22. 333
-44. 600
-2. 455
-1.997
-1. 334
24.
137721.000
^990. OOLi
0. 850
-1.400
23. 13::
-46. 000
-1.647
-1.934
-1. 888
25.
137773. 000
j."Ho9. 7 00
0. 950
-0. 300
24. 13::
-46. 300
-0. 3 It-
-1.919
-1. 390
137314. 000
2933. 100
137951. 000
2*39. 000
n 24
Slope -1.96
Intercept 0.854
Syx 0.541
S_ 7.053
Sa 0.016
d
Sfa 0.184
$„ 0.733
2.074
r -1.000
Confidence interval
1.96 + 0.033
-------
TABLE A-69 SUMMARY OF DATA FROM TEST NO. 39
Page
of
Degreaser A, operating
Solvent: Methylene chloride
PC
Date 4/4/79
FB 50 %
Inlet air __*_
Other
x SC
TRaust air x
A 7U *
V 8 ft/min
Ambient air
Temperature 69 °F
Pressure29.45 in. Hg
Humidity 39 %
Reading
No.
Tt mln
W, Ib
AT. h
AH, Ib
EAT, h
EAH, Ib
(S). """
(j*^ lb/h
X. lb/h
188167.000
3449. 500
188173.000
3449. 100
188182. 000
3447. 500
1.
188212.000
3444. 100
2.
188273.000
3440. 300
1.017
-3.800
1.017
-3. 800
-3.738
-3.738
-3. 738
3.
188323.000
3438. 000
0. 83?
-2. 300
1.850
-6. 100
-2. 760
-3.297
-3.518
-------
TABLE A-69 (continued)
Page 2 Of 5_
Reading
No.
T, m1n
W, lb
AT, h
AW. lb
EAT, h
EAW, lb
(tr), lb/h
AAH^ ih/h
I r.T 1 iD/n
\EAT/,
X, lb/h
4.
188384.000
3435. 500
1.017
-2. 500
2. 867
-ft. 600
-2. 45?
-3.000
-3. 34«.
5.
188445. 000
3433.200
1.017
-2. 300
3. 883
-10.900
-2. 262
-2. 807
-3.210
6.
188507. nnn
3430. 100
1.033
-3. 100
4.917
-14.000
-3.000
-2. 847
-3. 138
1 •
188562. 000
3424. 500
0.917
-5. 600
5. 833
-19.600
-6. 10?
-3.360
-3. 17?:
8.
3419. 500
1. 100
-5. 000
6.933
-24. 600
-4. 545
-3. 548
-3. 228
9.
|OO£OC£ fif"ifl
A V *mf V C* _' • * J '•' . '
3420. 500
0. 950
1.000
7.883
-23. 600
1.053
-2. 994
-3. 199
or
(continued)
-------
TABLE A-69 (continued)
Page 3 of J>_
Reading
No.
T, mln
H, lb
AT, h
AW, lb
EAT, h
EAH. lb
(XT) ""•
W/,
(zir) lb/h
X, lb/h
10.
188749.000
3417.200
1.067
-3.300
8. 950
-26. 900
-3. 094
-3. 006
-3. 177
11.
188813.000
3412.700
1.067
-4. 500
10.017
-31.400
-4.219
-3. 135
-3. 173
12.
188865.000
3411.000
0. 867
-1.700
10.883
-33. 100
-1.962
-3.041
-3. 161
13.
188923. 000
3408. 700
0. 967'
-2. 300
11.850
-35. 400
-2. 379
-2. 987
-3. 147
14.
188983.000
3406. 700
1.083
-2. 000
12.933
-37. 400
-1.846
-2. 892
-3. 127
15.
189046.000
3403. 100
0. 967
-3. 600
13.900
-41.000
-3.724
-2. 950
-3. 111
to
W
vD
(continued)
-------
TABLE _A-69 (continued)
Page 4 of __5_
Reading
No.
T, mln
W, Ib
AT, h
AW, Ib
EAT, h
ZAW, Ib
GO. ""
(Sf). ">'"
X, lb/h
16.
lft« ins. nnn
3400. 600
0. 953
-2. 500
14.883
-43. 500
-2. 542
-2. 923
-3. 102
• 17.
189171.00(1
3398. 400
1. 100
-2. 200
15.983
-45. 700
-2. 000
-2. 859
-3. 08
-fc>
o
(continued)
-------
TABLE A-69 (continued)
Page 5 of 5
Reading
No.
T, m1n
U, lb
AT, h
AW, lb
EAT, h
EAW. lb
(£). ">/"
j E An | 1 1* / k
*«AI /,
X, lb/h
22.
189465.000
3387. 700
0. 967
0. 200
20. 883
-56. 400
0. 207
-2.701
-3. 016
23.
189531.000
3384. 900
1. 100
-2. 800
21.98::
-50. 200
-2. 54 «,
-2.69::
-3.001
24.
189590. 000
3382. 400
0. 98::
-2. 500
22. 967
-61. 700
-2. 54?
-2. 687
-2. 98*
25.
189657.000
3381. 800
1. 117
-0. 600
24.08::
-h.2. ::0fi
-0. 5?7
-2. 587
-2.971
189680.000
3382. 100
189760.000
3383. 500
(A)
n 24
Slope -2.59
Intercept -3.038
Syx 1.786
Sy 7.093
A
Sa 0.053
S 0.175
2.074
r -0.998
Confidence Interval
2.59 + 0.110
1.494
-------
TABLE A-70 SUMMARY OF DATA FROM TEST NO. 39
Page J of 5
Degreaser B. operating
Solvent: Methylene chloride
PC
FB 50 %
Inlet air x
Other
x SC
>haust air
70
Tnin
Date 4/4/79
Ambient air
Temperature 69 °F
Pressure29.45 in. Hg
Humidity JJIL %
Reading
No.
T. win
W. lb
AT. h
AW( lb
EAT, h
CAW. lb
(S). ""-
(^11) Ib/h
X. 1b/h
188167. 000
2983. 500
ift ft 17";. nnn
2 9 S2. 300
1:::!:.17r ,-„-„-,
2978. 300
1.
188212. nnn
2973. 000
w •
1 PR 27 3. nnn
2973. 500
1.-017
-J. 500
1.017
-4. 500
-4. 42t.
-4. 42*-'
-4. 42ii-
3.
188323. 000
2970. 200
0.83::
-3.300
1.850
-7. 800
-3. 960
-4. 21*
-4. 32 J
U)
Ifc.
-------
TABLE A-70 (continued)
Page 2 of 5
Reading
No.
T, nln
U. Ib
AT. h
AH, Ib
CAT. h
EAU. Ib
00. '«
(SO. "•"•
X. 1b/h
4.
1853:34. 000
2967. 000
1.017
-3.200
•;• •:•»:•'
•1 > O t' i
-11.000
-3. 14f:
-3.837
-4. 1*0
c;
_' •
188445.000
2962. SOO
1.01T1
-4. 200
3. SS ::
-15.200
-4. 131
-3. ?H
-•i. 095:
t«.
188507. 000
2959. 500
1.031:
-3. 300
4.917
-1=3.500
-3. 194
-.3. 76 ::
-4.031
7.
188562.000
2955. 700
0.917
-3. SOO
5. 8-3-::
-22. '300
-4. 145
1 O •? •*•
i. Oil .'
-3. 997
8.
188628. 000
2952. 000
1. 100
-3.700
b. 93!:
-26. 000
-3. '364
-3. 750
-3.961
9.
188685.000
2948. 700
0. 950
-3. 300
7. 881:
-29. .300
-3. 474
-3.717
-3.931
U)
(continued)
-------
TABLE A-70 (continued)
Page 3 Of 5
Reading
No.
T, nln
W. 1b
AT, h
AU, 1b
EAT, h
EAU. 1b
$). ">"•
(SO. ">"
X. Ib/h
10.
183749. Odd
2944. 900
1.06"
- 3. 800
8. 950
-33. 100
-3. 56'l:
-3. 69t:
-3. 905
11.
18 8 81 3. 000
2941. 800
l.OtT
-3. 100
10.017
-36. 200
-2. 9 0 IT-
'S, b 14
-3. 3"fc
12.
lRRRh.5. nnn
2*--.fi. -:nn
0. 867
-3. 500
1 0. 38 1:
-39. 700
-4.033
-3.643
-3. 35"-
13.
1:3:3923'. 000
2q:*4. =>nn
0. 967'
-3. 400
11.850
-43. 100
-3.517
-3. t-37
-3. S3'1
14.
1:3:39S3. 000
2931. 200
1.033
-3. 700
12.931:
-4b. 800
-3.41}
-3. 619
-3. 320
15.
189046. 000
2927. 900
0. 967
-3. 300
1 3. 900
-50. 100
-3.414
-3.604
-3. 30}
OJ
(continued)
-------
TABLE A-70 (continued)
Page 4 of 5 .
Reading
No.
T, m\n
W. 1b
AT. h
aw, ib
DAT, h
EAH, Ib
60. '«
(80. ">"•
X. lb/h
16.
18? 105. 000
2924. 600
0. 983
-3. 300
14. 883
-53. 400
-3. 35t.
-3. 5S:;:
- 3. 790
17.
189171. 000
2920. 400
1. 100
-4. 200
15.9:33
-57. 600
-3.81Q
-.3. 604
-3. 779
13.
139225. 000
2917. 500
0. 900
-2. 900
It.. 883
-60. 500
-3.222
-3.533
-3. 767
19.
139233. 000
2914.400
1.050
-3. 100
17.933
-63.600
-2. 952
-3. 546
-?. 755
?n_
139347. 000
2910.300
0. 931:
-3. 600
13. 917
-67. 200
-3.661
-3.552
-3.744
?1
189407. 000
2907. 500
1.000
-3. 300
19. 'PIT1
-70. 500
-.3. 300
-3. 540
-3.734
u>
(continued)
-------
TABLE A-70 (continued)
Page 5 of 5
Reading
No.
T, mln
H, lb
AT, h
AW, lb
EAT, h
EAW, lb
(AT) lb/h
(^] lb/h
I V-AT J " **r •'
\EAT/,
X, lb/h
22.
IRCU^. nnn
2903. SOO
0. 967
-3. 700
20. S33
-74. 200
- 3. S28
-3. 725
23.
lfi^53i. nnn
239 8. SCO
1. 100
-5. 000
21.983
-79. 200
-4. 54=;
-3. 603
-3. 720
24.
ifios^n. nnn
2894. 600
0. 9S3
-•*. 200
22. 967
-83.400
-4.271
-3.631
-3.716
25.
is(>he!7. nnn
2S90. 000
1. 117
-4. £00
24. 083
-88. 000
-4. 119
-3.654
-3.713
l s^. fin. nnn
2S90. nnn
lfi3fifi:3. nnn
2890. 600
n 24
Slope -3.55
Intercept -1.120
Syx 0.629
S 7.093
S, 0.018
a
Sb 0.175
S 0.463
t ., 2.074
a/ 2
r -1.000
Confidence Interval
3.55 + 0.037
-------
TABLE A-71 SUMMARY OF DATA FROM TEST NO. 40
Page 1 of 5
Degreaser A, operating
Solvent: Methylene chloride
PC
Date 4/5/79
FB 50 I
Inlet air
Other
x SC
xhaust air
A
8
70 J?
m~in
Ambient air
Temperature 69 °F
Pressure29.45 Jn. Hg
Humidity 40 1
Reading
No.
T, mln
M. Ib
ftT, h
AM, Ib
EOT, h
EAW, Ib
(SI ""*
(S?). ">"•
X, lb/h
190141.000
3512.800
190147.000
3511. 000
1.
190170. 000
3503. 400
•5
•_ .
19024ft. 000
^n^. ri'-in
1. 300
-3.400
1. 300
-3. 400
-2. t-l=.
-2. b!5
-;:. 615
3.
19 03 07. 000
3502. 700
0. 933
-I'. 300
2. 233
-5. 70fi
-2. 339
-2. 496
-2. 5T-6
4.
1903t".b. Odd
3499. 700
0. 933
-3.000
3. 267
-8. 700
-3.051
-2. 663
-2. 592
-------
TABLE A-71 (continued)
Page j_ of _5_
Reading
No.
T. Bin
U. lb
AT. h
AU. lb
CAT. h
EAU. lb
(3D. "•»
GST). lb/h
X. lb/h
5.
190430.000
3497. 100
1.067
-2. 600
4. 333
-11. 300
-2.437
-2. 60£:
-2. 596
6.
190490.000
3494. 600
1.000
-2. 500
5.333
-13. SOO
-2. 500
-2. 588
-2. 594
i •
190554.000
3492. 000
1. 067
-2. 600
6. 400
-16. 400
-2.437
-2. 563
-2. 589
8.
1 90606. 000
3490. 000
0. 867
-2. 000
7. 267
-1:3.400
-2. 308
-2.532
-2.581
9.
190673. 000
34S7. 900
1 . 11 7
-2. 100
8. 3:33
-20. 500
- 1 . 88 1
-2. 445
-2. 564
10.
190731.000
3484. 300
0. 967
-3. 600
9. 350
-24. 100
-3.724
-2. 57B
-2. 56 S
U)
4k
CD
(continued)
-------
TABLE A-71 (continued)
3 of
Reading
No.
T. "in
W. lb
AT. h
AU. lb
CAT. h
CAM. lb
69. «*
dar) lb/h
X. 1b/h
11.
190790. 000
3433. 000
0. 933
-1. 300
10.333
-25. 400
-1.322
-2.458
-2.555
12.
190343. 000
3479. 100
0. 967
-3.900
11.300
-29. 300
-4. 034
-2. 593
-2. 550
13.
190907. 000
3477. 500
0. 933
-1. 600
12. 233
_T;0 Qfjfl
-1.627
-2. 516
-2. 555
14.
190967. 000
3476. 500
1.000
-1.000
1 3. 283
_-, 4 qj-jj-j
- 1 . 000
-2. 402
-2. 543
15.
191026. 000
3473. 100
0. 933
-3.400
14.267
-35. 300
-3. 458
-2. 474
-2. 5?8
16.
191088. 000
3471. 600
1.033
-1.500
15.300
-•":£. fififi
ov. O1.11.1
-1.45::
-2. 405
-2. 52'i'
U)
ife
vO
(continued)
-------
TABLE A-71 (continued)
Page 4 of 5
Reading
No.
T B4n
• 9 M •••
U. Ib
AT. h
aw. ib
I AT. h
£AU. Ib
/AM\ .
1 TT J ib/n
\AT/t
(Mr) 1b/h
X. Ib/h
17.
191146.000
3463. 800
0. 967
-2. 800
1 6. 267
-39.600
-2. 897
-2. 434
-2. 523
18.
191204.000
3466. 800
0. 967
-2. 000
17.233
-41.600
-2. 069
-2.414.
-2.517
19.
191266.000
3464. 000
1.033
-2. 800
18.26?
-44. 400
-2. 710
-2.43)
-2.512
20.
191325. nno
3462. 500
0. 983
-1. 500
19.250
-45. 900
- 1 . 525
-2. 384
-2. 505
21.
191385.000
3459. 000
1.000
-3.500
20. 250
-49. 400
-3.500
-2. 440
-2. 50Z
22.
191445. 000
3456. 500
1 . 000
-2. 500
21.250
-51. 900
-2. 500
-2.442
-2. 499
U)
VI
o
(continued)
-------
TABLE A-71 (continued)
Page 5 of 5
Reading
No.
T. min
M. Ib
AT. h
AU. Ib
EAT. h
EAU. Ib
(fi). ™
(fir). ]b/h
X. Ib/h
23.
191504.000
3454. 900
0.98::
-1.600
22.23-::
-53.500
-1.627'
-2. 40t.
-2. 495
24.
191572.000
3452. 500
1. 13::
-2. 400
23. 367
-55. 900
-2. US
-2. 39C1
-2. 490
25.
191615. 000
3450. 000
0. 88::
-2. 500
24. 250
-58. 400
-2.830
-2. 40:;:
-2. 4:37
191718. 000
3451. 900
190108. 000
3514. 500
U)
n 24
Slope -2.372
Intercept -1.012
'yx
0.569
7.050
0.017
0.185
0.786
t ., 2.074
a/2
r -1.000
Confidence interval
2.372 + n.035
-------
TABLE A-72 SUMMARY OF DATA FROM TEST NO. 40
Page J of 5
Degreaser B, operating
Solvent: Methylene chloride
PC
FB 50
Inlet air
Other
x SC
xhaust air
Date 4/5/79
Ambient 'air'
Temperature 69 °F
Pressure29.4iTin. Hq
Humidity 40 1
Reading
No.
T, mln
U. Ib
AT. h
AW. Ib
EAT, h
CAM. Ib
(*"} Ih/h
I TT 1 •O/n
\AI/t
(™f) 1b/h
X, Ib/h
1901.37. 000
2973. 300
190144. oon
2971. 500
1.
19017Q. 000
2*>7n. wi
2.
190248. 000
2963. 200
1. 300
-2. 100
1. 300
-2. 100
-1.615
-1.615
-1.615
3.
190307. 000
••-366 40fl
0. 98 ::
-1. 800
2.28!:
-3.900
-1.831
-1. 708
-1 . 66 i'
4.
190366.000
2Qfil. QOfl
0.981:
-2. 500
•3. 267
-6. 400
-2. 54::
-1.959
-1.761
to
V
NJ
-------
TABLE A-72 (continued)
Page _2 of 5
Reading
No.
T, nin
U. lb
AT. h
AW, lb
EAT. h
EAU. lb
(AT). lb/h
AAM\ ,b/h
\lSTj,
X. lb/h
5.
190430.000
2961. 100
1.067
-2.800
4.333
-9. 200
-2.625
-2. 123
• -1.85J
6.
190490. 000
2959. 200
1.000
-1.900
5. -333
-11. 100
-1.900
-2.081
-1.897
-
190554.000
2956. 900
1.067
-2. 300
6. 400
-13.400
-2. 156
-2. 094
-1.930
8.
190606. 000
2953.500
0. S67
-3.400
7. 267
- 1 6. 800
-3.92::
-2. 31 £
-1. 985
9.
190673.000
2952. 500
1. 117
-1.000
8. 383
-17.800
-0. 896
-2. 123
-2. 002
10.
190731.000
2949. 100
0. 967
- 3. 400
9. '350
-21.200
-3.517
-2. 267
-2.031
(continued)
-------
TABLE A-72 (continued)
Page 3 of _§_
Reading
No.
T. nin
U. Ib
AT. h
AW. Ib
CAT. h
CAW. Ib
(SO. ""*
f c*uW \ IL.JL.
1 EAT/ '
X. Ib/h
11.
190790. 000
2943. 000
0. 983
-1. 100
10. 333
-22. .300
-1. 119
-2. 150
-2. 044
12.
190343. OOn
2944. 000
0. 967
-4. 000
11. 300
-26. 300
-4. 1 30
-2. 327
-2. 070
13.
190907. nnn
2943. 000
0. 933
-1. 000
12.233
-27. 300
-1.017
-2.223
-2. 033
14.
l^n*^7. nnn
2940. 200
1. 000
-2. 300
1 3. 233
-30. 100
-2. 300
-2. 26>,
-2. 0*7
15.
r-in-'h. nnn
2933. 000
0. 933
-2. 200
14. 267
-32. 300
-2.237
-2. 264
_ ~i 4 i~i A
w • 1 '.' j
1ft
29?5. 500
1.0'33
-2. 500
15.300
-34. 800
-2.41-:'
-2. 275
-2. 120
(continued)
-------
TABLE . A-72, (continued)
Page 4 of 5
Reading
No.
T, win
U. 1b
AT. h
AU, 1b
CAT. h
EAU. 1b
(3). ««
(Mr). '>"•
X. Ib/h
17.
191146.000
2932. 600
0. 967
-2. 900
16. 267
-37.700
-'3. 000
-2.31?:
-2. 1 32
13.
191204.000
2931. "300
0. 967
-1.300
17.233
-39. 000
-1.343
-2. 263
-2. 140
19.
191266. 000
2927. 000
1.033
-4. 300
18. 267
-43. 300
-4. 16J
-2. 370
-2. 153
20.
191325.000
2925. 000
0. 933
-2. 000
19.250
-45. 300
-2.034
-2. .353
-2. 163
21.
191385.000
2922. 200
1.000
-2. 300
20. 250
-48. 100
-2. 800
-2. 37!i
-2. 174
22.
191445.000
2919.700
1 . 000
-2. 500
21.250
-50. 600
-2. 500
-2. 33 J
-2. 134
U)
IT
IP
(continued)
-------
TABLE A-72 (continued)
Page 5 Of J_
Reading
No.
T, min
H. Ib
AT. h
AU. Ib
EAT, h
EAH. Ib
(ir). lb/h
(m\ ib/h
VEAT/.
X. lb/h
23.
191504.000
2917. 300
0. 98.::
-2. 400
22. 23".:
-53.000
-2. 441
-2. 38<-
-2. 19::
24.
1^1^72. nnn
2915.000
1. 13::
-2. 300
2-3. 367
-55. 300
-2. 029
-2. '367
-2. 200
25.
191625. Orifi
2912. 700
0.881:
-2. 300
24. 250
-57. 600
-2. 604
-2. "375
-2. 20?:
l^lftris. nr'ri
2911.000
1-5 run ft n •-,.-,
2976. 200
n
Slope
Intercept
s
s
Confidence interval
-------
TABLE A-73 SUMMARY OF DATA FROM TEST NO. 41
Page 1 of 5
Degreaser A, operating
Solvent: Methylene chloride
Date 4/11/79
FB 125 %
InTet air
Other
PC
x SC
Exhaust air x
A 50 %
V 8 ft/min
Ambient air
Temperature 70 °F
Pressure 29.6 in. Hg
Humidity 36 %
Reading
No.
T, min
W. Ib
AT, h
AM. Ib
EAT, h
CAM. Ib
(AT) 1b/h
(IM\ ]b/h
X, Ib/h
198151. 000
198163. nnn
37£0. 500
1981 6*. non
3778. 000
1.
1 051 94. 000
3777. 000
2.
1Q O t1 ^ c* rt ft fi
- O il . ' _' . U 0 U
3775. 000
1.017
-2. 000
1.01 ;•
-2. 000
-1.967
-1.967
-1.967
3.
1QO ">i^ nnri
- O -• 1 i • UU'.'
3773. 700
1.03]:
-1.300
2. 050
-3. 300
-1.25?:
-1.610
-1.7S:-:
LJ
IP
-------
TABLE JW3 (continued)
Page 2 of 5
Reading
No.
T, min
W, Ib
AT, h
AH, Ib
EAT, h
£&U, Ib
(S). 'Wh
(SO. ">"•
X. lb/h
4.
198377.000
3772. 600
1. 000
-1. 100
3. 050
-4. 400
-1.1 00
-1.44-::
-1.67::
5.
198437.000
3771.600
1 . 000
- 1 . 000
4. 050
-5. 400
-1.000
-1. 33::
-1.5?:::
6.
198497. 000
3769. 400
1. 000
-2. 200
5. 050
-7. 600
-2. 200
-1.50?
-1.57J-
1 •
198557. 000
3768. 600
1. 000
-0. 800
6. 050
-S. 400
-0. 800
-1. 38?:
-1.54J
8.
198617.000
3767. 600
1. 000
-1. 000
7. 050
-9. 400
-1.000
-1.33::
-1.511
9.
198677.000
3766. 400
1 . 000
-1.200
8. 050
-10. 600
-1.200
-1.3171
-1.487
U)
IP
00
(continued)
-------
TABLE A-73 (continued)
Page 3 of 5_
Ul
in
VD
Reading
No.
T, mln
U, 1b
AT, h
AW. 1b
EAT, h
EAW, 1b
(AT) lb/h
(lirj. lb/h
X, Ib/h
10.
198737. 000
3765. 000
1 . 000
-1. 400
9. 050
-12. 000
-1. 400
* • »* kL t •
-1.469
11.
198797.000
-.-.;-. .;,-•,
1.000
-1. 100
!0. 050
-13. 100
-1. 100
-1. 303
-1.453
12.
1988^. nnn
376 1. 700
1. 133
-2. 200
11. is::
-15. •:fifi
-1.94J
-1. 36 f:
-1.445
13.
193917. 000
3761. 100
0. 367
-0. 600
12. 050
-15. 900
-0. 692
-1. 320
-1.434
14.
198975. 000
375?. TOO
0. 96?
-1. 400
13.017
-17. 300
-1. 440
-1. 329
-1.42*.
15.
199034.000
3758. 300
0. 983
-0. 900
14.000
-18.200
-0.915
-1.300
-1.417
(continued)
-------
TABLE j\-73 (continued)
Page 4 of 5
Reading
No.
T, m1n
W, 1b
AT, h
AW, 1b
EAT, h
EAW, Ib
/AU\
1 OI> 1 1 k 1 U
\ Tr J 'Ofn
VAT/,
(fir). lb/h
X, lb/h
16.
199099. 000
3757. 500
1.0S3
-1. .300
15. OS 3
-1*. 500
- 1 . 200
-1.293
-1.409
17.
199157. 000
3756. 300
0. 967
-1.200
16. 050
-20. 700
-1.241
-1.290
-1.402
IS.
199216.000
3754. TOO
0. 9S3
-1. 600
17.033
-22. 300
-1.627
-1. 309
-1. 396
19.
199275.000
3753.600
0. 983
-1. 100
1:3.017
-23. 400
-1. 119
- 1 . 299
-1. 391
20.
199337. 000
3751.700
1.033
-1.900
19. 050
-"•5 ":0fi
w -• • _' '-' •- *
-1.839
-1.-320
-1. 3S7
21.
199397.000
3750. 500
1. 000
-1.200
20. 050
-26. 500
-1.200
-1. 322
-1.384
U)
o>
o
(continued)
-------
TABLE A-73 (continued)
Page 5 of b
•* 1^1 ..
Reading
No.
Tnrin
W, Ib
AT, h
AW, Ib
EAT, h
EAW, Ib
(EAW\ 1W/1,
X, Ib/h
W W •
199458. OOn
3749. 000
1.01 7
-1.500
21.067
-28. 000
-1.475
-1. 329
-1. 38Z
2 3.
199518. nnn
3749. 000
1. 000
-1. 000
22. 067
-29. 000
-1. 000
- 1 . ':! 1 4
-1. 37?:
24.
1^0^70. nnn
3746. 700
1.017
-1. 300
23.083
-30. 300
-1.27V
-1. 313
-1. 37*
25.
l?96ift. nnn
37^5. 700
0. 983
-1.000
24. 067
-31. 300
-1.017
-1. 301
-1. 372
26.
1 9*6.14. nnn
'3747. 200
0. 100
1.500
24. 167
-29. 300
15.000
-1. 2-33
-1. 367
1««713. 000
3747. 800
n 25
Slope -1-29
Intercept -0.627
Syx 0.442
S 7.506
x
S 0.012
d
S, 0.172
S 3.280
2-069
r -1.000
Confidence interval
1.29 + 0.025
-------
TABLE A-74 SUMMARY OF DATA FROM TEST NO. 41
Page
of
Degreaser B, operating
Solvent: Methylene chloride
FB 125 %
Inlet air
Other
PC x SC
Exhaust air
50
ft/m
min
Date 4/11/79
Ambient air
Temperature 70.
Pressure 29.6
Humidity 36 __*
Reading
No.
• _
, mm
W. Ib
AT. h
AH. Ib
EAT, h
EAW, Ib
(*"} Ih/h
I TT j iD/n
\AI/,
X. Ib/h
1i™i §""i 4 C* 4 i~i •"• •" i
r*y 1 .• 1 . 0'Ji.i
3135. 000
198163. 000
3133. 000
19B169. 000
3132. 000
1.
19319-1. 000
3129. 500
2.
193255. 000
3123. 300
1.017
-0. 700
1. 017
-0. 700
-0. 639
-0. 6? 9
?>
193317. 000
3126.600
1.03::
-2. 200
2. 050
-2. 900
-2. 129
-1.415
-1.05:1
u>
N)
-------
TABLE A-74 (continued)
Page 2 of __§_
Reading
No.
T. win
U. Ib
AT. h
AW, Ib
EAT, h
EAH. Ib
GO. lwh
(BO. »"•
X, Ib/h
4.
198 37 7. 000
3125.600
1. 000
-1. 000
3. 050
-3. 900
-1. 000
-1.27*
-!. 127
c-
_'•
198437. 000
3 12 4.0 00
1. 000
-1. 600
•i. 050
-5. 500
-1. 600
-1. 358
-1. 185
6.
198497. 000
3122. 000
1 . 000
-2. 000
5. 050
-7. 500
-2. 000
-1.48!.
-1. 24!.
•*
198557. 000
3121. 300
1 . 000
-0. 700
6. 050
-8. 200
-0. 700
-1. 35!.
-1.263
£•
198617.000
3118.800
1. 000
-2. 500
7. 050
-10. 700
-2. 500
-1.51?:
- 1 . 300
4
198677.000
3116.300
1. 000
-2. 000
8. 050
-12.700
-2. 000
-1.57?:
-1.2-34
CO
tr«
CO
(continued)
-------
TABLE A-74 (continued)
Page 3 of 5
Reading
No.
T. min
U. Ib
M ^ • W
AT. h
AW, Ib
TAT k
LQI , n
CAW. Ib
/AU\
1 U1* 1 1 t> / k
v TT J iD/n
\AT/,
(fir). w
X. 1b/h
10.
193737. 000
3115. 600
1. 000
-1.200
*. nsn
- 1 3. 900
-1.200
-1.53*.
-1.357
11.
193797. 000
3113. 900
! . 000
-1. 700
10. 050
-15.600
-1. 700
-1.552
-1. 376,
12.
193365. 000
•3111. 400
1. 133
-2. 500
11 1 OQ
i 1 I 1OO
-18. 100
-2. 206
-1.610
-1. 398
13.
193917. 000
3110. 200
0. 367
- 1 . 200
1~t ft C" fm
d. 0 50
-19. 300
-1. 385
-1.602
-1.415
14.
198975. 000
310ft. Kflfl
0. 967
-1.600
1 3. 017
-20. 900
-1.655
-1.606
-l.J?0
is.
199034. 000
3106. 700
0. 933
-1.900
14.000
-22. SOO
-1.932
-1.629
-1. 444
u>
(continued)
-------
TABLE A-74 (continued)
Page 4 of 5
Reading
No.
T. fflln
W. 1b
AT. h
AW. 1b
TAT h
Lai ( n
ZAW, Ib
(W\ 1h/h
V Tr J ID/n
w/,
(fifc -
X. Ib/h
16.
144044. nnn
3104. 500
1.033
-2. 200
15.033
-25. 000
-2.031
-1.657
-1.450
17.
199157. 000
3103. 200
0. 967
-1. 300
16. 050
-26. 300
-1. 34S
-1.639
-1.4-0
13.
19921 6. 000
3101. 300
0.93::
-1.900
17. 03::
-28. 200
-1.932
-1.65t.
-1.431
19.
i44"i7c; nnn
* - . »— i -••*_• •„• I. •
3099. 700
0. 98::
- 1 . 600
13. 017
-29. 300
-1.627
-1. 654
-1. 490
20.
1 '^Q ^ ":7 flfifi
i ...'_• i •'.* i_" 1. 1
3093. 000
1. 033
-1. 700
10. n«=;n
-31.500
-1.64=.
-1.654
-1.499
21.
1 49307. nnn
3096. 300
1.000
- 1 . 700
20. 050
-33.200
-1.700
-1.65t.
-1.507
CO
CT>
l/l
(continued)
-------
TABLE A-74 (continued)
Page 5 of 5
Reading
No.
T. min
U. 1b
AT. h
AU. Ib
EAT. h
I AW, Ib
/EAW\ lb/h
\£AT/,
X. lb/h
hi hi, •
1994Sft. nnn
3094. 700
1.017
-1. 600
21.067
-34. 300
-1.574
-1.65*
-1.514
23.
19951ft. 000
"3093. 300
1.000
-1.400
22. 067
-36.200
-1.400
-1.640
-1.519
24.
199579. 000
3091. 100
1.017
-2. 200
23.03::
-38. 400
-2. 164
-1. 664
-1.52*.
25.
199633. 000
3033. 800
0. 981:
-2. 300
24. 067
-40. 700
-2. 339
-1. 691
-1.533
26.
1996-14. 000
3091. 000
0. 100
2. 200
24. IK?
- 38. 500
22. 000
-1.593
-1.535
199827.000
"3090. 900
u>
n 25
Slope -1.71
Intercept 1.211
Syx 0.480
S 7.306
A
Sa 0.013
d
Sb 0.172
S 4.760
2.069
r -1.000
Confidence Interval
1.71 + 0.027
-------
TABLE A-75 SUMMARY OF DATA FROM TEST NO. 42
Page _]_ of J_
Degreaser A, operating
Solvent: Methylene chloride
FB 125 *
Inlet air _x
Other
PC x SC
Exhaust air >
A sn *
V 8 ft/nr
mm
Date 4/12/79
Ambient'air
Temperature 72 °F
Pressure 29.451n. Hg
Humidity 62 t
Reading
No.
T, mln
W, 1b
AT, h
AW. Ib
EAT, h
EAH. Ib
(£). ">"•
(8ft """
X. lb/h
19??lb. OOCi
3746. 200
1??923. 000
3745. 200
199930.000
374 3. 900
1.
199964.000
3745. 400
2m
200026. 000
3742. 700
1.033
-2. 700
1.03::
-2. 700
-2.613
- "> *• i "•
i_. V 1 -.'
- ' A 1 '•
>_• D 1 \.'
3.
200086. 000
3740. 400
1. 000
-2. 300
2. 03.;:
-5. 000
-2. 300
-2. 459
-2. 53t-
10
-------
TABLE A-75 (continued)
Page 2 of g
Reading
No.
T. Bin
W. lb
AT. h
AW, lb
EAT. h
EAU. lb
(ir) lb/h
(ft?). ">">
X. lb/h
4.
20014S. 000
3739. 300
1.033
-1. 100
3. 067'
-6. 100
-1.065
-1.989
-2. 354
5.
200202. 000
3737.000
0. 900
-2. 300
3. 96 T1
-8. 400
-2. 55t-
-2.118
-2. 295
6.
200267. 000
3736.500
i.os::
-0. 500
5. 050
-8. 900
-0. 46?
-1.76::
-2.186
i •
200330. 000
3735.500
1.050
-1.000
6. 100
-9. 900
-0. 95?
-1.62::
-2. 094
S.
200388. 000
3734. 300
0. 967
-1.200
7. 067
-11. 100
-1.24J
-1.57J
-2.019
9.
200447. 000
3732. 600
0. 983
-1.700
8. 050
-12.800
-1.729
-1.590
-1.966
OJ
-------
TABLE A-75 (continued)
Page
Reading
No.
T. «1n
U. 1b
AT, h
AW. 1b
CAT, h
EAU. Ib
(I?). '*
(M?). >""•
X, Ib/h
10.
200506. 000
3731.300
0. 983
-1.300
9.033
-14. 100
-1.32::
-1.561
-1.921
11.
200577. 000
3 729. 800
1. 183
-1.500
10.217
-15.600
-1.268
-1.527
-1.881
12.
200629. 000
3 7 23. 500
0. St. 7
-1. 300
ll.OS::
-16.900
-1.500
-1.525
-1.849
13.
200687. 000
3727. 300
0. 9671
-1.200
12.050
-18. 100
-1.241
-1.502
-1.820
14.
200746. 000
3726. 500
0.981:
-0. 800
13.03::
-18.900
-0.814
-1.450
-1.792
15.
200779. 000
3725. 700
0. 550
-0. 800
13.583
-19.700
-1.455
-1.450
-1.767
U)
O"
vO
(continued)
-------
TABLE A-75 (continued)
Page 4 of 6
Reading
No.
T. aln
U. 1b
AT. h
AU. 1b
EAT. h
EAU. 1b
(S). '"
(ar). lb/h
X, lb/h
16.
200839. 000
3724. 000
1.000
-1.700
14.58-::
-21.400
-1.700
-1.467
-1.747
17.
200900. 000
3723. 100
1.01 T1
-0. 900
15.600
-22. 300
-0. 883
-1.429
-1.727
18.
200960. 000
3721.500
1.000
-1.600
16.600
-23.900
-1.600
-1.440
-1.710
19.
201019.000
3720. 200
0. 98;:
-1.300
17.58::
-25. 200
-1.32::
-1.433
-1.693
20.
201078.000
3718.900
0. 983
-1.300
18.567
-26. 500
-1.322:
-1.427
-1.681
21.
201139.000
3718.000
1.017
-0. 900
19.583
-27. 400
-0. 883
-1.399
-1.667
u>
>J
o
(continued)
-------
TABLE A-75 (continued)
P*9e _5. of 6
Reading
No.
T. «1n
U. Ib
AT. h
AU. Ib
EAT. h
LAW, Ib
/Ay\ .
I TT 1 ib/n
\AT/.
(fir). lb/h
X, lb/h
....
201199.000
3716.700
1.000
-1.300
20. 583
-28. 700
-1.300
-1.394
-1.654
23.
201233.000
3715.900
0. 650
-0. 800
21.233
-29. 500
-1.23J
-1.389
-1.64J1
24.
201293.000
3715.600
0. 9 1 7
-0. 300
22. 150
-29. 800
-0. 327
-1.345
-1.629
25.
201358. 000
3713.900
1.083
-1.700
23.233
-31.500
-1.569
-1. 35t-
-1.618
26.
201409.000
3713.000
0. 850
-0. 900
24. 083
-32. 400
-1.059
-1.345
-1. 607
201436.000
3712.500
(continued)
-------
TABLE A-75 (continued)
Page 6 of 6
OJ
Reading
No.
T. mln
W, Ib
AT. h
AU. Ib
EAT, h
EAU. Ib
(fi). ""*
i 2. AM i i L « L.
1 I Ib/h
\ *• A Y f **»
X. Ib/h
201496. 000
3714. 100
•
n 25 S „ 0.444 t .« 2.069
yx o/t
Slope -1.29 Sx 7.058 r -0.998
Intercept -2.480 5, 0.013 Confidence Interval
Q
SK 0.176 1.29 + 0.027
D —
S^ 0.551
-------
TABLE A-76 SUMMARY OF DATA FROM TEST NO. 43
Page 1 of 6_
Degreaser B, operating
Solvent: Methylene chloride
PC
FB 125 %
Inlet air
Other
x SC
xhaust air
A 50 %
V 8 ft/min
Date _ 4/12/79
Ambient air
Temperature 72 °F
Pressure 29.45in", Hg
Humidity 62 %
Reading
No.
T. niln
W, 1b
AT. h
AW. 1b
EAT. h
CAW. 1b
(If). ">»
(wf\ ib/h
X, Ib/h
14441* nnn
3090. 000
144421. nnn
3088. 400
144427. nnn
308 1-. 000
1.
1444*4. nnn
3082. 100
2m
2nnn2^. nnn
3080. 400
1.03::
-1.700
1.031:
-1. 700
-1. b4"i
-i.b4«;
-:.^.
3.
200086. nnn
"3080. 700
1.000
0. 300
£.03::
-1.40(i
0. 300
-0. *81'
-1. l^T1
-J
OJ
-------
TABLE A-76 (continued)
Page _ of __
Reading
No.
T, mln
W, lb
AT. h
AW, lb
EAT, h
EAW, lb
(jj£\ Ib/h
(fir), lb'h
X 1h/h
A f 1 \Jf II
4.
200143. 000
3079. 900
1.033
-0. 300
3. 0*7
-2. 200
-0. 774
-0.717
-1.017
5.
200202. 000
3032. 900
0. 900
3.«7
0. 800
3. 333
0. 202
-0.71?
*.
2002b7. 000
3033. 300
1.033
0. 400
5. 050
1.200
0. 3b9
0.230
-0. 52^
i •
200330. 000
307 1. 300
1. 050
-b. 500
b. 100
-5. 300
-b. 190
-0. 8b9
-0. 530
O •
200333. 000
307 b. 100
0. 9*7
-fl TlCl
'-' . i ' j '. *
7. Ob 7'
-b. 000
-0. 724
-0. 849
-''I. KUl
9.
200447. 000
3075. 300
0. 933
8. 050
-b. 800
-0.814
-0.84?.
-0. b47
(continued)
-------
TABLE A-76 (continued)
Page 3 of __6_
Reading
No.
T, mln
U. 1b
AT, h
AW, Ib
EAT, h
EAW, Ib
C^\ lh/h
1 -TT 1 ID/n
W/t
(fir). lb/h
X, lb/h
10.
200506. 000
3074. 300
0. 933
-1.000
9.033
-7. 800
-1.017
-0. 863
-0.671
11.
200577. 000
307?. 200
1. 133
-1. 100
10. 217
-3. 900
-0. 930
-0.871
-0.69J
12.
200629. 000
3072. 400
0. 367
-0. 800
11.033
-9. 700
-0. 923
-0. 87S
-0. 700
13.
200637. 000
3071. 300
0. 967
-1. 100
12.050
-10. 800
-1. 138
-0. 896
-0. 723
14.
200746. nno
3071. 000
0. 933
-0. 300
13.033
-11. 100
-0. 30?.
-0. 85?
-0. 733
15.
200779. 000
3070. 500
0. 550
-0. 500
13.533
-11.600
-0. 901!'
-0. 851
-0. 742
LP
(continued)
-------
TABLE A-76 (continued)
Page 4 of _6_
Reading
No.
T, mln
H, Ib
AT. h
AM. Ib
EAT. h
EAH. Ib
(ir) lb/h
(ft ™
X. lb/h
16.
200339. 000
3070. 500
1. 000
0. 000
14.533
-11.600
0. 000
-0. 795
-0. 745
17.
200900. 000
3071. 100
1.017
0. 600
15.600
-11.000
0. 590
-0. 705
-0. 743
IS.
200960. 000
3067. 400
1.000
-3.700
16. 600
-14.700
-3. 700
-0. 836
-0. 751
19.
201019. 000
306£. 2nn
0. 933
-1.200
17.53C:
-15.900
-1.220
-0. 904
-0. 760
20.
20107R. nnn
3066. 000
0.983
-0. 200
18.567
-16. 100
-0. 20?
-0. 867
-0. 765
21
201139 nnn
t V A A w .? • W •• •
7067 inn
V *J *J 1 • J *J I.I
1.017
1.500
19.53?
-14.600
1.475
-0. 746
-0. 76^
(continued)
-------
TABLE A-7b (continued)
Page 5 of e
Reading
No.
T, mln
M. Ib
AT, h
AM, Ib
CAT, h
CAM, Ib
(**} Ib/h
IT? i iD/n
\AT/,
(Sir). lb'h
X, lb/h
22.
201199.000
3066. 000
1.000
-1.500
20. 583
-16. 100
-1.500
-0. 731:
-0. 76!!
23.
201238. 000
3063.200
0. 650
-2. 800
21.233
-18.900
-4. 30?:
-0. 390
-0. 771
24.
201293.000
3062. 900
0.917
-0. 300
22. 150
-19.200
-0. 327
-0. 367
-0. 775
25.
201358.000
3061.700
1.083
-1.200
2?. 233
-20. 400
-1. 10?:
-0. 87?:
-0. 77?
26.
201409.000
3061.30CI
0. 850
-0. 400
24. 08::
-20. 800
-0.471
-0. 864
-0. 783
M
201436.000
3060. 900
(continued)
-------
TABLE A-76 (continued)
Page 6 of 6
-s)
o>
Reading
No.
T. m1n
U. Ib
AT. h
AU. Ib
EAT. h
EAW. Ib
(&} ih/h
I TF I iD/n
W/,
| &.LjN | IK /|«
X. Ib/h
Snis^J. nnn
30-: 2. bOO
n 25 Syx 1.543 t<|/2 2.069
Slope -0.987 S 7.058 r -0.992
Intercept 1-195 5 0.045 Confidence Interval
d
S 0.176 0.897 + O.U93
b ~
1.821
-------
TABLE A-77 SUMMARY OF DATA FROM TEST NO. 43
Page 1 of 5
Degreaser A, operating
Solvent: Methylene chloride
Date 4/9/79
FB 125 %
Inlet air
Other
PC x SC
Exhaust air x"
A 70 %
8 ft/min
Ambient air
Temperature 69 T
Pressure 29.45 in. Hq
Humidity 39 Z
Reading
No.
T, mln
W. 1b
AT. h
AW. 1b
EAT, h
CAW. 1b
(S). """
(Uj£\ ib/h
X. Ib/h
r?K-:4*. nnn
3737. 400
1 '5 K "I^.K. rifin
-.-.-.«r ---
I^K^KJ:. nnn
37R4. nnn
1.
iQi^tjQq nnri
•Z. •
jQfi.4^.4 fififi
::7:::fi ^fifi
i.os::
-2. 000
1.081:
-2. 000
-1.84t-
-1.84t.
-1.34,:.
3.
1 ^£.s "'O nnfi
">.""•-• fCift
0.931:
-1.600
2. 0 1 7
-'3. 60fi
-1.71'
-1.73S
-1.8 It-
u
^J
vO
-------
TABLE A-77 (continued)
Page _£_ of 5
Reading
No.
T. mln
W, lb
AT. h
AW, lb
TAT k
Z.QI , n
LAW, lb
(^ lh/h
i —f i iD/n
\AT/,
(fir). lb/h
X, lb/h
4.
196531. nnn
3777. 300
1.01 7
-1. 300
-4. 900
-1.279
- 1 . 6 1 ?.
-1. 74'i'
5.
196641. nnn
377=;. snn
1.000
-1.800
4. nv:
-6. 700
-l. 300
- 1 . 66 J
_ < -•"•••
6.
1967m. nnn
'•77'-'.. snn
1. 000
-2. 000
•=; nv:
-8. 700
-2. 000
-1.72?:
-1. 7:'7
1 •
l^h7f:.n. nnfi
0. 98::
-1. 000
h n i "
-9. 700
-1.017
-1.61J1
-'••'**
8.
19^R21. nnn
::771. inn
1.01 7
-1. 4nn
7 fi :: ":
-11. 100
-1. .377
-1.57?:
-1.690
9.
l^hfifto. nno
0.93::
-l.SOO
o n i -
-12.900
-1.S3J
-1.609
-1.679
00
o
(continued)
-------
TABLE A-77 (continued)
3 of 5
Reading
No.
T, win
W. Ib
AT, h
AW, Ib
CAT, h
CAW, Ib
69. """
(fir) lb/h
X. 1b/h
10.
196941.000
3763. 300
1.017
-1.000
9. 030
-13.900
-0. 934
-1.539
.-1.664
11.
196993.000
3766. 900
0. 950
-1.400
9. 933
-15.300
-1.474
-1.533
-1.65!
12.
197057.000
3765. 200
0. 933
-1.700
10.967
-17.000
-1.729
-1.550
-1.64;:
13.
197120.000
3762. 800
1.050
-2. 400
12.017
-19.400
-2. 236
-1.614
-1.639
14.
197176.000
3761.300
0.933
-1.000
12.950
-20. 400
-1.071
-1.575
-1.634
15.
197239.000
3760. 600
1.050
-1.200
14.000
-21.600
-1. 143
-1.543
-1.62?:
u> •
00
(continued)
-------
TABLE A-77 (continued)
Page 4 of 5
Reading
No.
T. min
W, 1b
AT. h
AU, 1b
TAT h
Lot , n
EAU, lb
(3D. 'b'h
(fir). lb/h
X. lb/h
16.
19729?. 000
3759. 100
0. 9 S3
-1.500
14. 9S3
-23. 100
-1.525
-1.54J1
-1.62:-
r>
197361.000
3757. 500
1.050
-1. 600
16. 03!:
-24. 700
-1.525
-1.541
-1.6!"
IS.
197420. 000
-:7=-,'=i. Sf.fi
0. 933
-2. 000
17.017
-26. 700
-2.03'
-1.56?
-1. 614
19.
1974 35.- 000
3754. 100
1.031:
-1. 400
18. 100
-23. 100
-1.29J1
-1.55J1
-1.611
20.
197544. 000
3752. 500
0. 933
-1. 600
1'3. nft":
-29. 700
-1.627
-1.55*.
-1.60?:
21.
197602.000
n onf|
0. 967
-1.700
20. 050
-'31.400
-1.75?
-1.56t-
-l.bOt-
00
K>
(continued)
-------
TABLE A-77 (continued)
Page 5 of 5
Reading
No.
T. mln
W. Ib
AT. h
AW. Ib
EAT, h
EAW. Ib
(*"} ih/h
I TV j iD/n
W/t
(fir) lb/h
X. lb/h
-• -i
197660.000
374?. 200
0. 967
- 1 . 600
21.017
--;;:. fififi
-1.655
-1.570
-1.604
23.
197719. 000
3747. 600
0. 933
- 1 . 600
22. 000
-34.600
-1.627
-1.57::
- : . 603
24.
197777. 000
3745. 900
0. 967
-1.700
22. 967
-36. -300
-1.759
-1.5S1
- 1 . 60:1
25.
1*7339. 000
3744. 400
1. 033
- 1 . 500
24. 000
-1.45:-
-1.575
-1.601
197361?. 000
3744. 000
197948. 000
3745. 500
n 24 S 0.310 tQ/2 2.074
Slope -1.550 Sx 7.065 r -1.000
Intercept -0.283 Sa 0.009 Confidence Interval
d
S. 0.178 1.550 + 0.019
D —
S,. 0.333
10
00
-------
TABLE ft-78 SUMMARY OF DATA FROM TEST NO. 43
Page J of 5
Degreaser B, operating
Solvent: Methylene chloride
Date 4/9/79
FB 125 %
Inlet air
Other
PC x SC
Exhaust air x
A 70 %
V 8 ft/min
Ambient air
Temperature 69 *F
Pressure29.45 in. Hg
Humidity 39 I
Reading
No.
Tf m1n
H. lb
AT. h
AW. lb
EAT, h
EAW, lb
(S). """
(m\ lb/h
X. lb/h
19634S. 000
3212. 100
196354. 000
3211.800
196359. 000
320S. 700
1.
196399. 000
3207. 200
2.
196464. 000
3204. 500
1 . OS I:
-2. 700
i.os::
-2. 700
-2. 49:-
-2. 49:-
-2. 49:-
3.
196520. 000
'3202. 700
0.93::
-l.SOO
2.017
-4. 500
-1.929
-2.231
-2. 36:1
U)
00
-------
TABLE A-78 (continued)
Page 2 of _5_
Reading
No.
T. min
U. Ib
AT, h
AW, Ib
EAT. h
CAW, Ib
00. ™
(M?). «/-
X. 1b/h
4.
196581. 00 0
•3201:1. 500
1.01T1
-I1. 200
3.033
-6. 700
-2. 164
-2. 209
-2. 311
,'
1966-11. orifi
3198. 300
1.000
-2. 200
4. 033
-8. 900
-2. 200
-2. 207
_ "• T-OC
fc— . h_ _ .'
h..
196701. 000
':!*£. 'irifi
1.000
-2. 000
5.033
-10.900
-2. 000
-2. 16t.
-2. 261
^
196760. 000
~\ 1 '3 4 -'fifi
0. 933
-2. 000
6. 017
-12. 900
-2.034
-2. 14^
-2. 24 J
q.
196S21. 000
-1 1 'H t' nnfi
:• l r^.. IJI.M.I
1.017
-2. 300
7. 03::
- 1 5. 200
-2. 26J:
-2. 161
-2. 230
<».
196880.000
*5 { f>n -,,-ifi
v5lO7. :• IJ I.I
0. 983
-2. 700
8. 017
-17. 900
-2. 746
-2 •'";•":
C^ . t_*_' .'
- "• ^"-'fl
h.. •_ .» '_•
00
(continued)
-------
TABLE _A_-78 (continued)
Page JJ of 5
Reading
No.
T, mln
U. 1b
AT. h
AW, 1b
EAT, h
EAW. 1b
(S). ""»
(so. '«-
X. Ib/h
10.
1 96*41. nnn
31? 7. 500
1.01?
- 1 . 300
9.033
-1?. 700
-1.770
_ -• i ft i
«_ • i ••.' i
_ -i -i -i C
— tli • h_ w .'
11.
l*6**fi. nnn
3186. 100
0. 950
-1.400
9. 981:
-21. 100
-1.474
-2. 114
-2. 214
12.
l*7nr,7. nnn
3134. 900
0. 983
-1. 200
10. 9t-7
-22. 300
-1.220
-2.03!:
-2. 197
,,'
lC|712n. nnn
31:32.000
1.050
-2. 900
12.017
-25. 200
-2. 762
-2. 097
-2. 189
14.
1*7 17^.. nnn
3179.200
0.933
-2. SOO
12. 950
-23. 000
-3.000
-2. I*;1
-2. 137
15.
1^733-5. nnn
3177. 100
1.050
-2. 100
14.000
-30. 100
-2. 000
-2. 150
-2. 134
Ul '
CD
(continued)
-------
TABLE A-78 (continued)
Page 4 of J
Reading
No.
T, m1n
W, 1b
AT, h
AW. 1b
EAT, h
CAW. lb
GO. «*
(SO. ">'"
X, lb/h
16.
197295. 000
3174.600
0. 933
-2. 500
14.93::
-32. 60Ci
-2. 54J1
-2. 17t.
-2. 134
1"\
197361.000
317?. 500
1.050
-1. 100
lb. 033
-33. 700
-1.04?:
-2. 10J1
-2. 179
13.
197420. 000
'3170.400
0. 933
-3. 100
17.017
-36.800
-3. 153
-2. 163
-2. 178
19.
197435. 000
3168. 100
1.08:8
-2. 300
18. 100
-39. 100
-2. 12^:
-2. 160
-2. 177
20.
197544.000
3166. 100
0. 93 1:
-2. 000
19. 08 1:
-41. 100
-2.034
-2. 154
-2. 17S
21.
197602. 000
3164.000
0. 967
-2. 100
20. 050
-43.200
-2. 17;:
-2. 155
-2. 174
03
(continued)
-------
TABLE A-73 (continued)
Page 5 of 5
Reading
No.
T, min
U. Ib
AT, h
AW. Ib
EAT, h
EAU, Ib
(EAHA lh/h
X. Ib/h
:. -
l*7K*n nnn
UK :> inn
0. 9 67'
- 1 . 900
21.017'
-45. 100
-1.966
-2. 14t-
-2. ir::
2^.
1*771-3. nnn
3lh.fi. jinn
0. 981:
-1.900
22. 000
-47. 000
-1.93::
-2. 1 3t.
-2. 17!
24.
1*7777. nnn
0. 967
-2. 300
22. 967
-49. 300
-2. 379
-2. 147
-2. 170
25.
1 M7S -i*. nnn
-:lSh.. nnn
1.03::
-1.900
24. 000
-51.200
- 1 . 839
-2. 1 3^:
-2. 169
l*7fth*. nnn
":1". 7nn
19fin74. nnn
tJ
oo
00
n 24
Slope -2.14
Intercept -0.170
Syx 0.413
Sx 7.065
Sfl 0.012
Sb 0.178
S^ 0.501
2.074
r -1.000
Confidence Interval
2.14 + 0.025
-------
TABLE A-79 SUMMARY OF DATA FROM TEST NO. 44
Page 1 of 5
Degreaser A, operating
Solvent: Methylene chloride
Date 4/8/79
FB 125 %
Inlet air
Other
PC x SC
x Exhaust air
V 8
70 %
FtTmin
Ambient air
Temperature 70 °F
Pressure 29.16in. Hg
Humidity 45 %
Reading
No.
T, mln
W. Ib
AT. h
AW. Ib
EAT. h
EAW. Ib
(S). """
(2*un i 1 L. f L.
YTrJ lb/n
X. Ib/h
194603.000
3697. 700
194624.000
3695. :: oo
194632.000
3692. t-00
1.
194658.000
'3692. 600
2.
194722.000
3689. 900
1. 067
-2. 700
1.067
-2. 700
-2.531
-2.531
-2.531
3.
194788.000
3688. 200
1. 100
-1. 700
2. 167
-4. 400
-1.54?.
-2.031
-2.281
(A)
9
vO
-------
TABLE A-79 (continued)
Page 2 of 5
Reading
No.
T, mln
U. Ib
AT. h
AU. Ib
EAT, h
EAU. Ib
(ir) lb/h
(air) lb/h
X, lb/h
4.
194840. Odd
3686. 800
0. 867
-1. 400
3.03::
-5. 800
j " J C
-1.91J1
"" bl • 1 .' •«•
5.
19489'?. 000
3685. 400
0. 93::
-1.400
4.017
-7. 200
-1.42*
-1.79::
-2. 06T
b.
1949*4. 000
3684. 100
i.os::
-1. 300
5. 100
-3. 5 Od
-1.200
-1. 667
-1.987
1 •
195019. 000
3682. 500
0. 917
-1. 600
6. 017
-10. 100
-1.74"..
-1. 679
-1. 93"..
»-t
195031. Odd
3681. 600
1.03::
-U. 9 Oil
7. 050
-ll.OOC
-0.371
-1.56C
-1.33:
9.
195138. 000
36 SO. 400
0. 950
-1.200
3. 000
-12.200
1™i " "t
. lib .•
-1.52=.
-1.837
vD
o
(continued)
-------
TABLE J^-79 (continued)
Page 3 of 5
Reading
No.
T, mln
U, lb
AT. h
AW. lb
EAT, h
CAW. lb
(S). «"
(fift. ">"•
X. Ib/h
10.
195200.00 d
3679. 300
1.033
-1. 100
9.03::
-13. 300
-1.06".:
-1.47?
-1.797
11.
195257.000
3677. 600
0. 950
-1. 700
9. 983
-15. OOO
-1.7S9
-1.503
-1.767
12.
195320. 000
3676. 200
1.050
-1.400
11.033
-16.400
-1. 333
-1.4St.
-1.74::
1 3.
195380. 000
3675. 300
1.000
-0. 900
12.03::
-17. 300
-0. 900
-1.430
- 1 . 7 1 1.
14.
195440. 000
3674. 000
1.000
-1. 300
13.033
-13.6011
-1. 300
-1.427
-1.694
15.
195494.000
'3672. 600
0. 900
-1.400
13.933
-20. 000
-1.55*
-1.4-3^.
-1.676
CO
vO
(continued)
-------
TABLE A-79 (continued)
Page * Of 5
Reading
No.
T mln
W, 1b
AT. h
AU. Ib
EAT, h
TAU IK
LuN ( 1 D
(Sft ">/"
\Al/t
(IAT). 1b/h
X. lb/h
1*.
l^sss* noo
^'h.71 son
i.os::
-1. 100
15.017
-"'1 1 l"lfl
._ 1 • 1 I-".1
-1.015
-1.405
-1.65:1:
17.
!C|ir'f:.21. 000
1.03::
-1. 300
16. 050
-1.25*
— 1 ™* '3 h
-1.6.11
18.
lwoe; ,-„-„-,
^Kh.ft. ROfi
1. 067'
-1.400
17. 117
-"•": fti'M'i
-1. 310
-1. 390
-1.62*.
19.
l-a^-iri. 000
•>,h,7. 600
0.917
-1.200
IS. 030
-25. noo
-1.309
-1. 38t.
-1.S13
20.
iqe-l-.5qi ,-„-,,-,
3666. 300
0. 9S::
-1.300
19.017
-1. 32::
-1. 38::
-1.601
21.
195861.000
3664. 600
1.030
-1.700
20. 050
-2S. 000
-1.645
-1.397
-1.591
to
vO
(continued)
-------
TABLE A-79 (continued)
Page 5 of 5
Reading
No.
T, mln
W, Ib
AT, h
AW. Ib
EAT. h
CAW. Ib
Of). ""*
(ffif). """
X, lb/h
22.
195921.000
3662. 800
1.000
-1.800
21.050
-29. 800
-1.800
-1.416
-1.5s:1
23.
195984. 000
3661. 500
1.050
-1.300
22. 100
-31. 100
-1.230
-1.407
-1.571
24.
196043.000
3660. 400
0. 983
-1. 100
23.083
-32.200
™ 1 • 111
-1.39*
-1.567
25.
196100.000
3658. 800
0. 950
-1.600
24.033
- 3'3. 800
-1.684
-1.406
-1.560
196127.000
3658. 300
19"620 1.000
3659. 500
n 24 S x 0.306 tQ/2 2.074
Slope -1-33 Sx 7.069 r -0.999
Intercept -1.628 S 0.009 Confidence Interval
d
Sb 0.179 1.33 + 0.019
S,. 0.358
JU>
sO
-------
TABLE A-80 SUMMARY OF DATA FROM TEST NO. 44
1 of 5
Degreaser B, operating
Solvent: Methylene chloride
Date 4/8/78
FB 125 %
Inlet air
Other
PC x SC _ x
txhaust air x
A 70 %
8 ft/min
Ambient air
Temperature 70 °F
Pressure29J6 in. Hg
Humidity J6 %
Reading
No.
T, min
H, Ib
AT, h
AH, Ib
EAT. h
EAW, Ib
(!T) lb/h
(ZM\ ....
(m). lb/h
X, lb/h
194603. 000
3135.400
194620. OOCi
3134.900
194627. 000
3132.400
1.
194653. OOCi
•3132. 100
^ •
194722. OOCi
3130.400
1.067
-1. 700
1. 067
-1.700
-1.594
-1.594
-1.594
3.
194788.000
•3128.700
1. 100
-1. 700
2. 167
-3.400
-1.54"..
-1.569
-1.58J
U)
vO
-------
TABLE A-80 (continued)
Page
of
Reading
No.
T, m1n
W. Ib
AT. h
AH. Ib
EAT, h
EAU, Ib
/AU\
1 OI* 1 1 k/k
V Tr 1 ID/h
\AT/»
(fir), lb/h
X. lb/h
4.
194840.000
3127. 800
0. 867
-0. 900
3.033
-4. 300
-1.038
-1.418
-1.527
5.
194899. 000
3127.000
0. 983
-0. 800
4.017
-5. 100
-0.814
-1.270
-1.46::
6.
194964.000
3125.900
1.03-::
-1. 100
5. 100
-6. 200
-1.015
-1.2U.
-1.41.::
i .
195019.000
3124.000
0.917
-1.900
6.017
-8. 100
-2.07::
-1. 34t-
-1.40J1
3.
195081. 000
3123. 100
1.03::
-0. 900
7. 050
-9. 000
-0.871
-1.277
-1.384
9.
195138.000
3121.700
0. 950
-1.400
3. 000
-10.400
-1.474
-1. 300
-1.371
OJ
vD
tP
(continued)
-------
TABLE A-80 (continued)
Page 3 of 5
Reading
No.
T, mln
W, Ib
AT, h
AW, Ib
EAT, h
I AW, Ib
(S). ™
(Mr). ">'"
X, Ib/h
10.
195200. 000
3120. 700
1 . 0'3 1:
-1.000
9.03::
-11.400
-0. 968
-1.26:1
-1. 361
11.
195257.000
3119. 700
0. 950
-1.000
9. 98 1:
-12. 400
- 1 . 05 ::
-1.24J1
-1.349
12.
195320.000
311:3.500
1.050
-1.200
11.03::
-13.600
-1. 143
-1.233
-1.339
13.
195380.000
3116.500
1.000
-2. 000
12.03::
-15. 600
-2. 000
-1.29t-
-1. 335
14.
195440. 000
3115.500
1.000
-1.000
13.03::
-16.600
-1.000
-1.27*
-1.330
15.
195494. 000
3113. 900
0. 900
-1.600
13.93 :•:
-IS. 200
-1.778
-1. 306
-1.329
U)
(continued)
-------
TABLE ..A-80 (continued)
Page 4 of j>_
Reading
No.
T, m1n
U, lb
AT, h
AW, lb
EAT. h
CAW, lb
/AU\
1 OW 1 1 L / U
1 TT I iD/n
W/,
(fir). lb/h
X. lb/h
16.
195559.000
3113.200
1 . 083
-0. 700
15.017
-18.900
-0. 64t.
-1.259
-1. 324
17.
195621. 000
3111. 000
1.033
-2. 200
16.050
-21. 100
-2. 129
-1. 315
-1. 323
18.
1956S5. 000
3109. 500
1. 067
-1.500
17. 117
-22. 600
-1.4Q*.
-1.320
-1.323
19.
195740. 000
310:3. 100
0.917
-1. 400
18.033
-24. 000
-1.527
-1. 331
-1.324
20.
195799. 000
3108. 700
0. 983
0. 600
19.017
-23. 400
0.610
-1.230
-1. 319
21.
195861.000
3106. 900
1.033
-1.3 00
20. 050
-25. 200
-1. 742
-1.257
-1. 31t-
U)
vO
(continued)
-------
TABLE .A-80 (continued)
Page 5 Of 5
Reading
No.
T. min
U. Ib
AT. h
AW. Ib
EAT. h
EAW, Ib
(8). """
(EAU \ i L. / L.
jrf ) 'b/n
X. Ib/h
22.
195921.000
3105. 100
1.000
-1.800
21.050
-27. 000
- 1 . 800
-1.280
-1.314
23.
195984.000
3103.300
1.050
-1.800
22. 100
-28. 800
-1.714
-1.303
-1. 314
24.
196043.000
3101.400
0. 98C:
-1.900
23.08::
-30. 700
-1.932:
-1.330
-1.314
25.
196100.000
3100.600
0. 950
-0. 800
24.03'.:
-31.500
-0. 84I1
-1. 311
-1. 314
196127. 000
3100.200
196294.000
3100.800
" 24 S 0.513 t . 2.074
j ** U/ C
Slope -1.29 Sx 7.069 r -l.QOO
Intercept -0.011 S Q.015 Confidence interval
a
Sb 0.179 1.29 ^0. 031
S,. 0.604
U)
vD
00
-------
TABLE _A181 SUMMARY OF DATA FROM TEST NO. 45
Page j of 5
Degreaser A, operating
Solvent: Methylene chloride
PC
Date 3/28/79
SC
FB 50 * ft y M. « 5Q *
Inlet air __x Exhaust air _x V 8 Tt/min
Othcr Lip exhaust at TOO ft3/min per ft2 top opening
Ambient air
Temperature 68 *F
Prcssure29.68 in. Hg
Humidity 49 *
Reading
No.
T, mln
W. 1b
AT, h
AW, Ib
EAT, h
CAN. Ib
(S). ">"•
(S?). "•"•
X. lb/h
1.
178605. 000
•:-3^f! Qrin
2m
173t.74. fJOO
3934. 000
1. 150
4. <=»00
1. 150
4. 900
4.261
4.261
4.261
3.
17:-: 7 IK. nori
3°?0, JOO
0. *•* 7
3. 600
2.017
8. 500
4. 154
4.215
4.2:-"--'
4.
17R71--!?. nnn
3926. "00
1. 117
3. 700
3. 133
12. 200
3. 313
?. 394
4. 123
5.
17::::::ci2. 000
3922. 200
0. 98 3
4. 500
4. 117
16. 700
4. 576
4. 057
4. 107
6.
173915. 000
3917. 500
1.050
4. roo
5. 167
21. 400
4.476
4. 142
4. 114
-------
TABLE A-81 (continued)
Page 2 of 5
Redding
No.
T. Bin
U. Ib
AT. h
Ay. ib
CAT. h
CAM. Ib
(HT). ">"•
I. Ib/h
1 •
17ROA7. nnn
^14 nnn
0. 367
3.500
6.033
24. qnn
4. 03**
4. 127
• 4. 116
3.
17 90 35. 000
3* in. inn
1. 133
3. 900
7. 167
2R. snn
3. 4-M
4. 019
4. in,-:
9.
ir^n^h,. nnn
"v^nn ~:nn
1.017
9. 300
8. 193
3fi. h.nn
o |^ ^i 13
4.717
4. 17?
10.
179151. nnn
-•on-- nnn
0.91^
-1. 700
9. inn
36. 900
- 1 . 355
4. 055
4. l*1^
11.
17q2m. nnn
~-:p,*7. son
0. 367
4. 500
9. 967
41. 4nn
5. 192
4. 154
4. 164
12.
170^^5 nnn
1. 033
4. 200
11.000
4ci Kl~in
4. 145
4. 1-.2
(continued)
-------
TABLE A-81 (continued)
Page 3 Of _5_
Reading
No.
T. «1n
U. Ib
AT. h
AU. Ib
EAT, h
CAW. Ib
GO. »»
(sfli ">"•
•
X. 1b/h
13.
1 79333. 000
3338. 000
1. 1??
5. 300
1-» i -< -*
^.i 1 :• :•
50. 900
4. 676
4. 195
4. 165
14i
179337. 000
3333.500
0. 900
4. 500
n. m?
55. 400
•=;. nnn "
4.251
4. 172
15.
179450. 000
^R7*. nnn
1.050
4. 500
14. OR 3
59. 900
4. 23b
4.253
4. 177
16.
179505.000
387$. 000
0. 9 1 7
4. nnn
15.000
63. 900
4. 364
4.260
4. 1R3
17.
179563. 000
3371. nnn
1 . 050
4. 000
16. 050
67. 900
3.310
4.231
4. 136
18.
179619. 000
3367. 000
0. 350
4. 000
16.900
71.900
4. 706
4.254
4. 190
(continued)
-------
TABLE i.81 (continued)
Page 4 of
Reading
No.
T «in
V f VM • ••
U. Ib
«T k
AT ( n
AU, Ib
CAT. h
CAU. Ib
($). «•
(ft?). "•"•
X, Ib/h
1?.
179683.000
3362. 400
1. 067
4. 600
17.967
76. 500
4.? 13
4. 258
4. 194
20.
179747. 000
3358. 300
1.067
4. 100
19.033
30. 600
3. 844
4.235
4. 1*6
21.
17*snn. nnn
3'354. 300
n. f.fi-\
4. 000
19. 917
84. 600
4. 523
4.243
4. {••--:
? -i
1 r^'-iKS nnn
ii . •_' f _• • •_' _ • _f
f-\c,r\. 700
i n* 3
i • _' >_• _•
3. 600
21.000
83. 200
3. 323
4. 200
4. 199
2"^.
1~" a o "• •> i"i ri it
< r r ii :• . U LI i j
3345. 400
00^ ~*
_ • . b •
5. -300
i
21.967
•=n. snn
5. 433
4. 256
4. 201
24.
i TQQOO nnn
if. .00. UUL'
'3340. 600
1 no 7
1 . 'J •!• O
4. 300
23. 050
93. 300
4. 431
4.265
4. 204
(continued)
-------
TABLE _A-81 (continued)
Page 5 of 5
o
u>
Reading
No.
T. min
U. Ib
AT. h
AM. Ib
EAT. h
CAU, Ib
(AT) 1b/h
(fir). 1b/h
X, Ib/h
25.
1300S3. 000
3336. 900
1.033
3.700
24. 133
102.000
3.415
4.227
4. 205
2 6 -
130076. 000
3335. 400
' 0. 333
1.500
24.517
103.500
3.913
4.222
4. 206
•
n 25
Slope 4.260
Intercept -0.439
Syx 1.057
Sx 7.286
Sa 0.030
d
Sfa 0.173
S 1.751
la/2
2.07
r 1.000
Confidence interval
4.260 + 0.062
-------
TABLE A-82 SUMMARY OF DATA FROM TEST NO. 46
Page 1 of 5
Degreaser A, operating
Solvent: Methylene chloride
PC
Date 3/29/79
FB 50 %
Inlet air x
Other
x SC
xhaust air x
50 %
ft/min
Ambient air
Temperature 73
Lip exhaust at 50 ft^/min per ft^ top opening
Pressure29.65 in. Hq
Humidity 50 %
Reading
No.
Tt mln
W, Ib
AT. h
AW, Ib
ZAT, h
CAW. Ib
(S). ">"
(Sf). ">"•
X. 1b/h
180388. 00 0
SSI?. 600
1S0401. 000
3317. 000
180405. 000
3816. 200
1.
1 304 68. 000
3312.500
TI
wi. •
130528. 000
3808. 60(i
1.000
-3. 900
1 . 000
-3.900
-3. 900
-3. 900
-3. 900
3.
130592. 000
3805. 400
1.06T'
-3.200
2. 067
-7. 100
-3. 000
-3. 43=i
-3. 6-ES:
-------
TABLE A-82 (continued)
Page 2 of 5
Redding
No.
T. mln
U. 1b
AT, h
AW, 1b
EAT, h
EAH, lb
GO. ™
(SO. «"•
X. 1b/h
4.
180647. 000
3802. 000
0.917
-?. 400
2. 933
-10.500
- 3. 709
- 3. 520
-?. 610
5.
13070 5. 000
3 7 9 S. 700
0. 967
-3. 300
3. 950
-13.800
-3.414
-3.494
-3.587
6.
180772. 000
3 7 •=*=;. 5nn
1. 117
-3. 200
5. Ob 7
-17. 000
-2. 86t.
-3. 35=i
-3. 54 J
-^
I •
18082b. 000
3792. 000
0. 900
- 3. 500
5. 967
-20. 500
- ?. 889
- 3. 4 St.
-3.521:
£•
'_' •
I80386. 000
3733. 400
1 . 000
-3. 600
6. 967
-24. 100
-3. 600
-3.459
-3.514
9.
180946.000
'3785. 000
1.000
-3.400
7. 967
-27. 500
-3.400
-.3. 452
-3.506
-------
TABLE A-82 (continued)
Page 3 of 5
Reading
No.
T, min
U. 1b
AT. h
AU. Ib
EAT, h
EAW. Ib
(S). ™
(Sft '*»
X, Ib/h
10.
18 100 5. 000
3731. 800
0. 983
-3. 200
8. 950
-30. 700
-3.254
-3. 430
-3. 490
11.
131061. 000
3779. 000
0.933
-2. 300
9. 833
-33. 500
-3. 000
-3. 390
-3. 4:37
12.
18 11 25. 000
3775. 000
1.067
-4. 000
10. 950
-37. 500
-3. 750
-3. 425
-3.4S1
13.
131184.000
3773. 400
0. 983
-1.600
H.9'33
-39. 100
-1.627
-• -i^-'
— !>. >Z. • i
-3. 464
14.
18 1241?. 000
3769. 300
1.0S3
-4. 100
13.017
-43. 200
- 3. 785
-3. 319
-:=. 453
15.
181313.000
3764. 800
1.067
-4. 500
14.033
-47. 700
-4.219
-3.387
-?. 448
(continued)
-------
TABLE A-82 (continued)
Page 4 of 5
Reading
No.
T, m1n
U. Ib
AT, h
AW. Ib
EAT, h
EAU. Ib
(M\ ....
ITTI lD/n
W/t
(fir), 1b/h
X, lb/h
16.
181365. ooo
3761.400
0. 867
-3. 400
14.950
-51. 100
-3.923
-3. 4 If:
-3. 44h.
17.
1S1424. 000
3757. 000
0. 9S3
-4. 400
15.933
-55. 500
-4. 47C.
-3. 4 S3
-3. 44'!'
IS.
181488. 000
'3752. 100
1.067
-4. 900
17.000
-60. 400
-4. 594
-'3. 553
-3.45=.
19.
1 SI 55 3. 000
374S. 700
1.0S3
-3. 400
13.033
-63. SOO
-3. 138
-3.52?:
-3.459
20.
131606. 000
3744. 900
0. 333
- 3. 800
13.967
-67. 600
-4. 30::
- 3. 564
-3.464
21.
181666. 000
3740. 400
1.000
-4. 500
19. 967
-72. 100
-4. 500
-3.611
-3. 47Z
(continued)
-------
TABLE A-82 (continued)
Page 5 of _5_
Reading
No.
T, fflln
W, Ib
AT. h
AW, Ib
EAT. h
I AW, Ib
(M\ ih/h
1 TT / iD/n
W/,
/EAW\ 1K/h
IEAT;. lb/h
X. lb/h
22.
1 SI 7 30. 000
3737. 100
1.0*7
-3. 300
21.03::
-75. 400
-3.094
-• c r> c
— I'. _''-• .'
-3. 477
2'3.
1 SI 795. 000
^!7-:-:. 5fm
i.os::
-3.600
22. 117
-7-3. nrm
-3.32::
-3.57:-
-3.4:31
24.
181849.000
3729. 900
0. 900
-3.600
23.017
-S2. 600
-4. 000
-3.589
-3.4*,
25.
181910.000
3725. 500
1.017
-4. 400
24.03;:
-37. 000
-4. 32?:
-3.620
-3.49C1
131933.000
3723.900
1'82000. 000
3722. 900
n 24 Syx 1.212 tQ/2 2.074
Slope -3.60 Sx 7.085 r -1.000
Intercept 1.305 Sa u.036 Confidence Interval
a
Sfa 0.177 3.60 + 0.075
Sc 0.671
o
00
-------
TABLE A-83 SUMMARY OF DATA FROM TEST NO. 46
Page 1 of 5
Degreaser B, operating
Solvent: Methylene chloride
Date
3/29/79
FB 50 %
Inlet air
PC _v_ SC -
x Exhaust air x
A 50 *
V 8 ft/min
Ambient air
Temperature 73
Pressure 29. 65 in.
Humidity _5JL I
°F
~"9
Reading
No.
T, m1n
H, Ib
AT. h
AW. Ib
EAT. h
EAH, Ib
(£). »»
(LAN i t L »u
... j 1 ID/h
X. Ib/h
IRn -:sft. non
29b7. 700
180401. 000
1;..ri401_ nof|
29f".4. 100
1.
IftfMh.:-: fififi
2^^1. 5HO
-.
i c-ii^. '••-• rn'ifi
T--5«=i-5 son
1 . 000
-2. 000
1.000
-2. 000
-2. 000
-2. 000
-2. 000
3.
1 f*fbcr*-i~' i~n~iri
loLOc-i . U'JI.I
0. 983
-2. 100
1.983
-4. 100
24 -~i "
. 1 :•£•
-2. 067
-2. 034
o
vO
-------
TABLE A-33 (continued)
Page z of b
Reading
No.
T. min
U. Ib
AT, h
AW. Ib
EAT. h
CAW. Ib
GO. "»»
(SO. "»
X. lb/h
4.
180647. 000
I1 95 5. 500
1. 000
-1. 900
2.98::
-6. 000
-1.900
-2.011
-2. 02*
5.
Iftri7'"'ci. nnri
295?. 300
0. 967
-2. 200
?. 950
-8. 200
-2. 27t.
-2. 07*
-2. 0?9
6.
180772. 000
2QCin. nrifi
1. 117
-3. 300
5. 067
-11.500
-2. 955
-2. 270
-2. 085
i .
180826. 000
294?. 500
0. 900
-1.500
5. 967
-13.000
-1.667
-2. 179
-2. 100
8.
180836. 000
2946. 200
1.000
-2. 300
6. 967
-15. 300
-2. '300
-2. 19t.
-2. 114
9.
T80946. 000
2944. 000
1.000
-2. 200
7. 967
-17.500
-2. 200
-2. 197
-2. 124
(continued)
-------
TABLE A-83 (continued)
Page 3 of _j>_
Reading
No.
T, mln
U. 1b
AT. h
AU Ih
(IN . 1 U
EAT, h
CAW. Ib
GO. Wh
(It?). 1b/h
X. 1b/h
10.
131005. 000
2941. 000
0. 983
- -;. firm
S. 950
-20. 500
-3. 05 J
-2.291
-2. 143
11.
1 81 06 1.000
2*~\*. ::f'fi
0.933
-1. 700
9. 383
-22. 200
-1.321
-2. 24t.
-2. 153
12.
131125.000
'••3~:7 nnfi
h_ . mf 1 • *— * '— ' '. *
i.o6r
-2. 300
10.950
-24. 500
-2. 15t-
-2.237
-2. 161
13.
131134.000
T'-a-c; nnci
k. - _• J • LlfJ L1
0. 933
-•"• nnri
t_ . L11.11.1
11.933
-2>-. 500
-2.031
_ T1 'T1 t1 1
i_ • •_•_ J
-2. lt«.
14.
131249. 000
'••3 ~- ~> Qnri
i- . -•»_. . U'.'
1.033
- ~' i rifi
^.. 1 iJL1
13. 01T1
-23. 600
-1.93?:
-2. 197
-2. Ib?:
1S.
181313.000
•^Q ^n i nfi
cr;-ij. 1UU
l.ObV
"* '"•llfl
^.. o'Ji.i
14.033
-'31.400
-2.625
-2. 230
-2. 173
(continued)
-------
TABLE A-83 (continued)
Page 4 of 5
Reading
No.
T, min
W, lb
AT, h
AW. lb
CAT, h
CAW, lb
/AH\
1 u>i 1 1 l» JW
1 77 I iD/n
\AT/,
(HT). lb/h
X. lb/h
16.
131 3*5. nnn
2923. 500
0. 867
-1. 600
1 4. 950
-33. 000
-1.84*.
-2. 207
-2. 175
17.
131424. 000
2926. 500
0. 933
-2. 000
15.933
-35. 000
-2.031
-2. 197
-2. 17-:.
18.
131433. 000
2924. 600
1.067
-1.900
17.000
-36. 900
-1.781
-2. 171
_.-• « -«.
19.
131553. 000
2922. 600
1. 083
-2. 000
18.033
-38.900
-1.346
-2. 151
-2. 175
20.
181606. 000
2920. 700
0. 333
-1.900
13.967
-40. 300
-2. 151
-2. 151
-2. 173
21.
181671 nnn
A ' J * •»• 1 A • •_' '_' >. •
2918.500
1.083
-2. 200
20. 050
-43. 000
-2.031
-2. 145
-2. 17::
N)
(continued)
-------
TABLE A-83 (continued)
Page 5 of 5
Reading
No.
T, m1n
W, Ib
AT. h
AU. Ib
EAT. h
LAW. Ib
(M\ ih/h
1 -T-ST I ID/n
W/,
(fir). lb/h
X. lb/h
-• ^
131730. 000
2916.500
0. 933
-2. 000
21.033
-45. ooo
-2. 034
-2. 1 39
-2. 170
23.
131795. 000
2914. 400
1.033
-2. 100
22. 117
-47. 100
-1.935:
-2. 130
-2. 169
24.
131849. 000
2912. 500
0. 900
- 1 . 900
23.017
-49. 000
-2. 11 J
-2. 129
-2. 167
25.
131910.000
2910. 100
1.017
-2. 400
24. 033
-51.400
-2.361
-2. 13?
-2.166
13 19? 3. 000
-..-,,-,.., ,.nf|
182116.000
2909. 000
n 24 Suy O.bbO t .. 2.074
yx Q/ c
Slope -2.16 Sx 7.094 r -1.000
Intercept -0.437 S^ 0.016 Confidence Interval
a
Sb 0.177 2.16 +0.033
S,. 0.340
-------
TABLE A-84SUMMARY OF DATA FROM TEST NO. 47
Page 11 of 6
Degreaser B, operating
Solvent: Methylene chloride
FB 50 I PC x SC
Inlet air x Exhaust air
Other
A 50 %
V 8 ft/min
Date 3/28/79
Amblent'air
Tests Numbers 45 and 47 were run simultaneously; crosscurrent test
Temperature 68 °F
Pressure29.687'". H9
Humidity 49 *
Reading
No.
T, m1n
M, Ib
AT. h
AW. Ib
EAT. h
' CAW. Ib
(AT) 1b'h
(is?) 1b/h
X. Ib/h
178475.000
3008. 000
17:3570. 000
3004. 100
173573. 000
3002. 300
1.
173*03. 000
3000. 500 1
2.
173*73. 000
2995. 700
1. 167'
-4. 300
1.167
-4. 300
-4. 114
-4. 114
-4. 114
3.
178721.000
2992. 500
0. 7171
-'3. 200
1.883
-8. 000
-4.4*=:
-4.246
-4. 131
-------
TABLE A-84 (continued)
Page ? of _
Reading
No.
T. min
U. 1b
AT. h
AU. 1b
CAT. h
CAU. tb
00. "">
(fift »"•
X. lb/h
4.
173738. 000
2937. 000
1. 117
-5. 500
3. 000
-13.500
-4. 925
-4. 500
. -4. 287
5.
178349. 000
2* ft 2. nnn
1.017
-5. 000
4.017
-18.500
-4.918
-4. 606
-4. 367
6.
178910. 000
2977. 300
1.01T1
-4. 700
5. 031:
-23.200
-4.62::
-4. 609
-4.41=.
•^
i •
173969. 000
2971. 500
0.981:
-5. 800
6. 017
-29. 000
-5. 398
-4. 820
-4. 48.::
8.
179032.000
?1£.7 Sfifi
fc- - *_• 1 • J >_l '. 1
1.050
-4. 000
7. 067
-'33.000
-3.810
-4. 670
-4.510
9.
179090.000
pQf.'* snn
f. . •_• t_ • .* '.* *.'
0. 967
-5. 000
8. 03::
-33.000
-5. 17::
-4.730
-4. 537
(continued)
-------
TABLE A-84 (continued)
Page 3 of 6
Reading
No.
T. mtn
U. Ib
AT. h
AW, Ib
CAT. h
CAU. Ib
09. »*
(fir) lb/h
X. 1b/h
10.
179143.000
2957. 200
0. 967
-5. 300
9. 000
-43. 300
-5. 483
-4.811
' -4« **
11.
179203.000
2953.000
0.917
-4. 200
9.917
-47. 500
-4. 58::
-4. 790
-4. 590
12.
1 79265. 000
2948. 500
1.03::
-4. 500
10.950
-52. 000
-4. 355
-4. 749
-4. 60-?
13.
179333. 000
2942. 250
1.13]:
-6. 250
12.08::
-58. 250
-5.515
-4.821
-4. 62J-
14.
179387.000
2937.000
0. 900
-5. 250
12.983
-63.500
-5. 333
-4.891
-4. 643
15.
179450.000
2932.500
1.050
-4. 500
14.033
-63. 000
-4. 286
-4. 346
-4. 657
(continued)
-------
TABLE A-84 (continued)
Page A of 5
Reading
No.
T. nin
U. lb
AT. h
AU. lb
EAT, h
ZAU, lb
/AW\
1 u 1 1 ft* JW
ITT) lD/n
\AT/,
(IAT) 1b/h
X. Ib/h
16.
179505.000
2927. 500
0.917
-5. 000
14.950
-73. 000
-5. 455
-4.881:
• -4. 67J1
17.
179568.000
2923.000
1.050
-4. 500
16.000
-77. 500
-4. 28*
-4. 84
-------
TABLE A-84 (continued)
Page 5 of 6
03
Reading
No.
T. mln
U. lb
AT. h
fiW, lb
CAT. h
CAU. lb
(Ir) lb/h
Aaw\ lh/h
\isr). lb/h
X. lb/h
22.
179365.000
2898. 600
i.os::
-5. 700
20. 950
-101.900
-5. 262:
-4. 86
-------
TABLE A-84 (continued)
Page _6_ of 6
Reading
No.
T, min
H, Ib
AT. h
AW. Ib
EAT. h
CAU. Ib
(I AH \ IL. /•.
— . . i iD/n
X. lb/h
180254. 000
2879. 100
n 25 Syx o.494 la/2 2-069
Slope -4.887 sx 7.309 r -1.000
Intercept 0.961 Sfl 0.014 Confidence Interval
sb 0.171 4.887 +0.029
S,. 0.607
-------
TABLE A-85 SUMMARY OF DATA FROM TEST NO. 48
Page 1 of 5
Degreaser A, operating
Solvent: 1,1,1-Trlchloroethane
FB 75 %
Inlet air x
Other
Crosscurrent test
PC x SC
Exhaust air x
V 8 ft/mi
50 JL
in in
Date 6/1/79
Ambient'air
Temperature 74 °F
Pressure 29.75?n- ^9
Humidity 53 %
Reading
No.
T, m1n
V, 1b
AT, h
AW, 1b
EAT, h
CAN, 1b
(S). ">"•
X. lb/h
283426.000
3599. 500
283434. OCX
3602.100
233439.000
3604. OCX)
1.
233430. 000
3602. 600
2.
233544. 000
3598. 500
1.06T1
-4. 100
1.067'
-4. 100
-3.844
-3.844
-3.844
3.
238606. 000
3597. 400
1.03::
-1. 100
2. 100
-5. 200
-1.065
-2. 47t
-3. 160
IS)
o
-------
TABLE A-85 (continued)
Page 2 of 5
Reading
No.
T. *tn
U. lb
AT. h
AU. lb
EAT. h
EAU. lb
(SO 'w
\AI/.
f {.AN \ «» ••
VIA!/ '
X. Ib/h
4.
288664. 000
25*4. inn
0. 967
-3.300
3. 067
-8. 500
-3.414
*"*! • 1 1 £.
-3.031
5.
288724. 000
3591. 900
1.000
-2. 200
4.067
-10.700
-2. 200
-2.631
-2.931
6.
288784. 000
25*n Kfifi
1.000
-1. 300
5. 067
-12.000
-1. 300
-2. 36?:
-2. 818
i •
238852. 000
3 5ft 7. •'inn
1. 133
-3. 300
6. 200
-15. 300
-2. 9K:
-2. 46*
-2. 760
3.
288910.000
3^ft4. ann
0. 967
-2. 500
7. 167
-17.300
-2. »(.
-2. 484
-2. 720
9.
288970. 000
O^OO Ortfi
1.000
-1.600
8. 167
-19.400
-1.600
-2. 376
-2. 677
N>
(continued)
-------
TABLE A-85 (continued)
Page 3 of 5
Reading
No.
T. Bin
U, lb
AT. h
AH, lb
EAT, h
EAH. lb
(3D. "•»
(if). ""•
X. 1b/h
10.
289030. 000
3580. 200
1.000
-3. 000
9. 167
-22. 400
-3. 000
-2. 444
-2.651
11.
239090. 000
3578. 400
1.000
-1.300
10. 167
-24. 200
-1.800
-2. 380
-2.624
12.
239150.000
3576. 400
1.000
-2. 000
11. 167
-26. 200
-2. 000
-2. '34t-
-2. 599
T3.
239210. 000
3572. 300
1 . 000
-4. 100
12. 167
-30. 300
-•i. 100
-2. 490
-2. 590
14.
239270. 000
3569. 200
1.000
-3. 100
13. 167
-33.400
-3. 100
-2.537
-2. 53*.
15.
289? 30. 000
'3566. 000
1.000
-3.200
14. 167
-36. 600
-3.200
-2. 584
-2. 58t.
N>
(continued)
-------
TABLE A-85 (continued)
Page _4r_ of 5
Reading
No.
T. «in
U. lb
AT. h
AU. lb
EAT. h
IAH. lb
/AW\ ]b/h
AaM\
ysrj.
X, Ib/h
16.
289390. 000
3563. 400
1.000
-2. 600
15. 167
-39. 200
-2. 600
-2. 585
-2. 58 1.
17.
289443. 000
3562. 600
0. 967
-0. 800
16. 131:
-40. 000
-0.820
-2. 479
-2. 579
18.
28950'=;. nnn
3561.200
0. 950
-1.400
1 7. 083
-41.400
-1.474
-2.423
-2. 570
19.
2::":icrir:.::::. nnn
3559. 100
1. 050
-2. 100
18. 133
-43.500
-2. 000
-2. 399
-2. 560
20.
2 ft oft 2 R. nnn
3558. 800
1.000
-0. 300
19. 133
-43.800
-0. 300
-2. 289
-2. 54*
21.
289685. 000
3555. 700
0. 950
-3. 100
20. 083
-46. 900
-3.263
-2. 335
-2. 535
IS)
(continued)
-------
TABLE A-85 (continued)
Page 5 of 5
N)
Reading
No.
, mln
U. 1b
AT. h
AU. 1b
EAT. h
EAU. 1b
oa »»
(8ft «"*
X. Ib/h
22.
28*74=;. nnn
3^ei4. hnn
1.000
-1. 100
21. OS'!:
-48. 000
-1. 100
j-i '•>•?-•
C.. £. i i
-•5 Cj-1. -.
ft_ • .!«_.•
23.
'RQRns. nnn
^tssi rnn
1.000
-2. 900
22.081:
-50. 900
-2. 900
-2. 30=.
-2. 5 1C:
24.
2ft^fth^. nnn
"*.c,c,\. nnn
1.000
-0. 700
23.081:
-51.600
-0. 700
-2. 2?5
-2.501
••?=;
t_ .'.
2?.--»*2c>. nnn
3549. 900
1.000
-1. 100
24.08::
-52. 700
-1. 100
-2. 18t:
-2. 48:;:
289955. OOfi
•35-48. 400
23^71. nnn
3547. 600
n 24
Slope -2.236
Intercept -1.941
Syx 1.555
Sx 7.067
S 0.046
a
S. 0.180
D
Sr 1.064
\f
t „ 2.074
a/2
r -1.000
Confidence interval
2.236 + 0.095
-------
TABLE A-86 SUMMARY OF DATA FROM TEST NO. 48
Page i of 5
Degreaser C. operating
Solvent: 1,1,1-Trlchloroethane
Date 6/12/79
Ambient 4ir
FB 75 * PC x SC A 50* Temperature 74 °F
InleTlfF x Exhaust air x V g ft/mln Pressure 29.751n.
Other Humidity 5,3 t
Leakage of water into the degreaser was noted and correctedj test restarted at 2G8348
Reading
No.
T m1n
1 • IV • 1 IV
W, 1b
AT. h
AW. 1b
EAT, h
CAW, lb
(&} Ih/h
1 TT1 I 1 *VFI
\AI/,
(ltM\ ....
1 T7T 1 lO/n
\EflT/.
X. Ib/h
2:33426. 000
346. 700
2:334 36. 000
346. 300
•
I1ft:-I4:::ri. nun
345. 400
.288544. 000
345. 200
233606. 000
344.600
233664. 000
344. 400
N>
tn
-------
TABLE A-86 (continued)
Page 2 of 5
Reading
No.
T. Bin
y, ib
AT. h
AU, Ib
EAT. h
EAU. Ib
CD. »•»
(SO. ">"•
X. 1b/h
2S3724. OOU
343. 700
j.38734. OP i.i
34::. 800
j. ..,•_; «:S2. O'li'J
'J44. 10U
K
:-o;;:j.^ \ f| nnn
1. •».1 l™i . 1 '— * • '— ' *— ' ¥—
343. 700
•31
^:E"3'?70. 000
343. 300
1.000
0. 400
1.000
0. 400
0. 400
0. 400
0. 400
-i
I'm
2RQmn. nnn
343.000
1.000
0. 300
2. 000
0. 700
0. 300
0. 350
0. .350
tb
IS*
(continued)
-------
TABLE A-86 (continued)
Page 3 of 5
Reading
No.
T. Bin
y. lb
AT. h
AW, lb
EAT. h
EAU. lb
II 1k/h
V 77 ] 1 D/ n
\A 1 / ,
(fir) lb/h
X. lb/h
4.
289090. 000
^42. e-nn
1. 000
0. 500
3. 000
1.200
n. snn
0. 400
0. 38':
5.
289150. 000
342. 100
1.000
0. 4. JO
4. 000
1.6 UO
n. 4nn
0. 400
0. 3 •'"::
6.
259210. 000
•:41. ton
1.000
0. 500
5. 000
2. 100
n. snn
0. 420
0. 3^
I •
289270. 000
341. 100
1 . 000
0. 500
6. 000
2. 600
n. snn
0.433
0.401
8.
•18*330. 000
-:40 h.nn
1. 000
n. snn
7. 000
3. 100
n srm
0.443
0. 407
9.
289390. 000
340. inn
1 . 000
0. 500
8. 000
3. 600
n. snn
0. 450
0. 4 1 2
ro
(continued)
-------
TABLE A-86 (continued)
Page 4 of b
Reading
No.
T. «in
U. Ib
AT. h
AU, Ib
CAT. h
I AM. Ib
($). 1b/h
(Kft """
X. Ib/h
10.
239443. 000
•3--;*. son
n. 0^7
0. 300
3. 967
3. 900
0. 310
0.435
0.415
11.
239505. 000
339. 400
0. 950
0. 400
9.917
4. 300
0. 421
0. 434
0. 4 1 6
12.
239563. 000
V-:o. finn
1.050
0. ^00
10. 967
4. "00
0. 381
0. 429
0. 4 1 3
1.3.
239623. 000
339. 000
1.000
0. 000
11.967
4. 700
0. 000
0. 393
0. 4 1 1
14.
239635. 000
338. 300
0. 950
0. 700
12.917
5. 400
0.737
0. 4 1 3
0.416
15.
289745. 000
337. 900
1.000
0. 400
13.917
5.800
0. 400
0.417
0.416
tv>
o>
(continued)
-------
TABLE A-86 (continued)
Page 5 of 5
Reading
No.
T, min
M. Ib
AT. h
AU. Ib
CAT. h
LAW. Ib
(M\ ih/h
ITF) lb/h
\AT/.
(m\ lb/h
X. lb/h
It..
239305. 000
337. 100
1. 000
0. 300
14. 917
t.. bOO
0. 300
0. 442
0.413
17.
23 93 1 -5. 000
33*. 900
1 . 000
0. 200
15.917
t.. 300
0. 200
0. 427
0.41 3
13.
.13 9? 25. 000
3 3 1.. 500
1. 000
0. 4UO
Ib. 91"
7. 200
0. 400
0. 42b
0. 419
239955. 000
335. 900
289971.000
337. 100
n 17 Syx 0.152 tfl/2 2.13
Slope 0.429 Sx 5.016 r 0.999
Intercept -0.041 S^ 0.008 Confidence interval
d
Sfa 0.258 0.429 + 0.017
S,. 0.182
K)
-------
TABLE A-87 SUMMARY OF DATA FROM TEST NO. 50
Page ] of 2
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling _x ; nonboiling )
FB _SU % PC x SC _
Inlet air y Exhaust air x_
Other
A 0 %
V 0 ft/min
Date 2/1C.17/79
Ambient ait-
Temperature
Pressure 30.08in. Hg
Humidity 31 Z
Reading
No.
Tt min
W. Ib
AT. h
AW. Ib
EAT, h
EAW, Ib
(S). ">'"
(fir). lb/h
X, lb/h
121373.000
3597. 400
121398. 000
3597. 400
121406. 000
3597. 600
121413.000
1.
121433. 000
~\c,*~\. inn
2.
121482.000
0. 73::
-1.300
0. 73'l:
-1.300
-1.77;:
-1.77::
-1.77::
U)
o
-------
TABLE A-87 (continued)
Page 2 of 2
Reading
No.
T. mln
U. Ib
AT. h
AU. Ib
EAT, h
EAW. Ib
(fi). '*
VLAT/.
X. lb/h
3.
122257.000
35 fin. nrifi
12.917
-11.800
1 3. 650
-13. 100
-0. 91 <
-0. 960
-1. 36t-
4.
122? 9 7. 000
35 77. 500
2. 331:
-2. 500
15.93::
- 1 5. 600
-1.071
-0. 97*.
-1.23*
5.
122536. 000
3575. 200
2. 317
-2. 300
18. 300
- 1 7. 900
-0. 99!:
-0. 97S:
-i. 17;-
122623.000
3576. 600
n 4 Syx 0.229 tQ/2 4.303
Slope -0.939 $x 7.85b r -1.000
Intercept -0.545 S. 0.017 Confidence Interval
a
Sb 1.050 0.939 + 0.073
S 0.395
i ^*
U)
-------
SUMMARY OF DATA FROM TEST NO. _5Q
Page
of
Degreaser B, Idle
Solvent: -Methylene chloride
(Boiling _x ; nonboiling
FB 50 % PC x SC
Inlet air x Exhaust air x
Other
A 0 %
V 0 ft/min
Date 2/25/79
Ambient air
Temperature 58 °F
Pressure 3Q.U»jn. Hg
Humidity 31 %
Reading
No.
T, win
H. lb
AT. h
AW. lb
EAT. h
CAW. lb
(I?). ">'"
(Mr) 1b/h
X. lb/h
121377.000
2911. 30fi
121402.000
•-••31=; Qnri
121408.000
-••M-: Ki-iO
121417.000
2 * oft. Qfin
1.
1214-iK. 000
....Jfl7 4nf|
2.
121485.000
2«n? 2nn
0. 650
-0. 200
0. 650
-0. 200
-0. 30?:
-0. 30*
-0. 30?:
U)
-------
TABLE A-88 (continued)
Page 2 of 2
Reading
No.
T, m1n
H, Ib
AT. h
AW. Ib
ZAT. h
EAU. Ib
0"). ">'*
(™^ lb/h
X. lb/h
3.
122261.000
2393.400
1 2. 93::
- 1 3. 800
13.58::
-14.000
-1.067
-1.03J
-0. 669
4.
122400. 000
2S90. 100
2.317
-3. 300
15.900
-17.300
-1.424
-1. OSS:
-0. 809
5.
122531.000
2888. 800
2. 18::
-1.300
18.08::
-IS. 600
-0. 595
-1.029
-0. 864
122703.000
2891. 900
Ui
LO
n 4
Slope -1.078
Intercept 0.466
yx
0.551
7.822
0.041
1.042
0.495
ta/2 4.303
r -1.000
Confidence Interval
1.078 + 0.176
-------
TABLE A-89 SUMMARY OF DATA FROM TEST NO. 51
Page . j_ of ?
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling x ; nonboiling )
FB 50 * PC x SC _
Inlet air x Exhaust air x
Other. . . , J
Lid closed
min
Date 2/25/79
Ambient'air
Temperature 67 »p
Pressure29.64 jn. Hg
Humidity 43 t
Reading
No.
T, min
M, 1b
AT, h
AW. Ib
EAT, h
CAN. Ib
(S). '«
(if), -w.
X. Ib/h
1 ^2Q-as. nnri
3730. 300
i
1 ": ^firr^. fififi
371"?. 400
1 33017. 000
3 7 11 1. 800
1 ^n-:':. 000
3724. 500
1 e
133330.000
3720. '?00
-i
_ •
134217.000
3711.800
14.783
-9. 100
19.73;:
-12.700
-0.616
-0.64^
-0. 68*
-------
TABLE A-89 (continued)
Page 2 of 2
Reading
No.
T, min
W, Ib
AT, h
AU, Ib
EAT, h
EAW. Ib
(isj. ">"•
X, Ib/h
134316. 000
3713. 700
•
Syx la/2
Slope -0.644 Sx r
Intercept S Confidence Interval
-------
TABLE A-90 SUMMARY OF DATA FROM TEST NO. b1
Page ' of *
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling x_; nonboiling
FB 50*
Inlet air
Other
PC
Exhau!
SC
aust air
A _g %
V 0 ft/min
Date 2/25/79
Ambient a*ir
Temperature 67
Lid closed
Pressure29.64 in. Hg
Humidity ' 43""*
Reading
No.
T, m1n
W, 1b
AT. h
AW. 1b
EAT, h
EAW. 1b
(ST) lb/h
(f£). ">'"
X, lb/h
1 3 1"?'? 2. 000
2q*l. Si"""'
1 3 3005. 000
2**1. 4 no
1 3301 3. 000
-..-_,,,-, ,nf|
1 33033. 000
.iqc;^ nnf|
X I-
1 33-330. 000
,qe., ftfif.
^1.
134217.000
-••341 snn
14.7:33
-11. 300
19.733
-15.500
-0. 7t-4
-0. 7S5
-o. sir
*>
OJ
-------
TABLE A-9Q (continued)
Page 2 Of _J_
CO
-0
Reading
No.
T. m1n
U. Ib
AT. h
AW. Ib
EAT, h
EAW, Ib
(m\ ib/h
\EAT/,
X. lb/h
134365. 000
2942. 300
•
Syx 'a/2
Slope 0.785 Sw r
Intercept
Confidence Interval
-------
TABLE A-91 SUMMARY OF DATA FROM TEST NO. 52
Page _i_ of ]_
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling x )
FB 50 % PC x SC _
Inlet air x Exhaust air x_
Other
A Q %
V 0 ft/min
. 2/22/79
'air } *~
Date
Ambient
Temperature 70 °F
Pressure 29.51 in. Hq
Humidity '49~t
Reading
No.
T, m1n
W, lb
AT. h
AW. lb
ZAT. h
CAW. lb
(&} Ih/h
i TT 1 iD/n
\Ai/t
(^ lb/h
X. lb/h
1.
1-31228.000
29:11.400
2.
1 32469. 000
2924. 900
20. 683
-6. 500
20. 683
-6. 500
-0. 314
-0. 314
-0. 314
U)
o>
-------
TABLE A-92 SUMMARY OF DATA FROM TEST NO. 52
Page _]_ of 1
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling x )
FB 50 % PC x SC
Inlet air x Exhaust air
Other
A 0 %
V 0 ft/min
Date 2/22/79
Ambient'air '
Temperature ?9 *F
Pressure29.5T "in. Hq
Humidity -W 1
Reading
No.
T, mln
M. Ib
AT. h
AW. Ib
EAT. h
CAW. Ib
(&} Ih/h
i TT i tufn
\AT/,
(fir) lb/h
X. lb/h
1.
131223.000
3483. 100
2.
132469.000
3473.200
20.68::
-9. 900
2fi. hft":
-9. 900
-0. 479
-0. 479
-0. 479
U)
-------
TABLE A-93 SUMMARY OF DATA FROM TEST NO. jl
Page
of
Degreaser A, Idle
Solvent: Methyl ene chloride
(Boiling _ ; nonboiling J^
FB 50 » PC SC
Inlet air x Exhaust air x
Other
)
A 0 %
V 0 ft/min
Lid closed; solvent loss during cooldown period
Date Z/25/79
Ambient 'air '
Temperature 68 °F
Pressure 29.g9uT~Hg
Humidity 41 I
Reading
No.
T, m1n
H. Ib
AT. h
AW. Ib
EAT. h
CAW, Ib
(S). ">'"
(8ft "-"•
X. 1b/h
1.
134316.000
3713.700
•:•
b. •
136? 34. 000
'3699. 400
43. 63::
-14. 300
43. 63-::
-14. 300
-0. 32?:
-0. 32ij:
-0. 31"::
-------
TABLE A'94 SUMMARY OF DATA FROM TEST NO. 53
Page ] of ]
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling x )
FB 50 % PC _^^ SC
Inlet air x Exhaust air
Other
Lid closed
A
0
Q %
mi n
Date 2/25/79
Amb 1 entSTr
Temperature 66 °F
Pressure 29.19 in. Hg
Humidity ^1 «
Reading
No.
Tf m1n
H, Ib
AT. h
AW, Ib
EAT, h
CAN. Ib
(£). ">"•
(i?). '"/"
X. 1b/h
1.
134365. 000
2?42. 300
•^
hi •
1 36937. 000
2931. 900
42. St-71
-10.400
42. 86 7'
-10.400
-0. 241:
-0. 24^:
-0. 241:
-------
TABLE A-95 SUMMARY OF DATA FROM TEST NO. 54
Page 1 of 1
Degreaser A, idle
Solvent: Methylene chloride
(Boiling ; nonbolling _^ )
FB 50 * PC x SC
Inlet air x Exhaust air
Other
ft/mir
x Lxnausi air x V p ft/mln
Lid closed; solvent loss durinq cool down period
Date 2/27.28/79
Ambient'air""
Temperature °F
Pressure fn. Hg
Humidity %
Reading
No.
T, mln
W, lb
AT, h
AH. lb
EAT, h
EAN, lb
(£). """
(SfX «•"•
X. lb/h
136985.000
37*01. 100
137005.000
3693. 500
1 37022.000
3696. 9oo
1.
1 37055. 000
3693. 600
-•
tli •
138322. 000
3686. 500
21. 117
-12. 100
21. 117
-12. 100
-0.57'.:
-0. 57::
-0. 57 'J
ISJ
-------
TABLE A-96 SUMMARY OF DATA FROM TEST NO. 54
Page 1 of 1
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling x )
FB 50 ' t PC x SC _ x
Inlet air x Exhaust air x
othcr Lid closed
Date 2/27,28/79
A 0 %
V 0 ft/mi n
Ambient'air
Temperature °F
Pressure In. Hg
Humidity %
Reading
No.
T. mln
H. Ib
AT. h
AN. Ib
EAT, h
EAN. Ib
(AW\ ,h/h
1 TT 1 • ofn
XtJ'/t
(IAN\ lb/h
VE&V.
X. 1b/h
136936. 000
2932. 300
137001.000
2923. 600
137013.000
2925. 500
1.
1 37065. 000
2926. 900
2.
133324.000
2921. 500
20. 99 ::
-5. 400
20.93::
-5. 400
-0. 257
-0. 257
-0. 257
to
-------
TABLE A-97 SUMMARY OF DATA FROM TEST NO. 57
1 of 2
Oegrcaser A, Idle
Solvent: Methylene chloride
(Boiling _ ; nonboiling x )
FB 50 *
Inlet air
Other
PC x
Exhau
SC
aust air
A
V 0
Date 3/2/79
Ambient air '
0
rtTmin
Solvent loss during cool down period
Temperature 69 °F
Pressure 29.82-in. Hq
Humidity 44.* 1
Reading
No.
Tf mln
W. 1b
AT, h
AW, Ib
EAT, h
CAM. Ib
(S). ""*
(M?). ">"•
X, Ib/h
141045.000
3534. 400
141105.nnn
3533. 700
141167.000
353?. 400
141223.000
35?2. 750
1.
140925.000
3535. 400
2.
140956.000
3535.000
0. 51T1
-0. 400
0. 5 1 7
-0. 400
-0.774
-0. 774
-0. 774
-------
TABLE A-97 (continued)
Page 2 of 2
Reading
No.
T. Bin
U. Ib
AT. h
AW. Ib
CAT. h
EAU. Ib
(SO. '«•
(8ft «"•
X. lb/h
3.
140986. 000
3534. 700
0. 500
-0. 300
1.017
-0. TOO
-0. 600
-0. 68*
-0. 73 J
4.
141045.000
3534.400
0. 98;:
-0. 300
2. 000
-1. 000
-0. 305
-0. 500
-0. 654
5.
141280.000
3532. 100
3.917
-2. 300
5.917
-3. 300
-0. 587-
-0. 55:.;:
-0. 630
6.
142430.000
3522. 100
19. 167
-10.000
25.08::
-13. 300
-o. 52:-
-0.530
-0. 610
tn
n 5
Slope -0.526
Intercept -0.104
-yx
0.109
10.380
0.005
0.311
0.169
t ., 3.182
o/2
r -1.000
Confidence interval
O.b26 + 0.015
-------
TABLE A-93 SUMMARY OF DATA FROM TEST NO. _57_
Page 1 of 2
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling _x )
FB
Inl?
Other
50 I
let air
PC
SC
Exhaust air
A Q %
V _ Q ft/mln
Date 3/2/79
Amb 1 en fair*
Temperature 69 °F
Pressure29.82 In. Hg
Humidity 44T
Reading
No.
T, m1n
H, lb
AT. h
AW, lb
EAT, h
EAW. lb
(Sf). ""*
X. lb/h
141045..000
_ 2839. 100
141105.000
2838. 400
141167.000
2837. 900
141228. onn
2836.750
1.
.140925.000
2840. 100
\
2.
140986.000
283:-'. 600.
1.017
-Q. 500
1.017
-0. 500
-o. 49:-
-0. 49J1
-0. 49L'1
CT>
-------
TABLE A-98 (continued)
Page 2 of 2
Reading
No.
T, min
Ml K
i ID
AT. h
AW, lb
CAT, h
CAW. lb
(ir). lb/h
fuv\ 1K/K
VLul /f
*, 1b/h
3.
4 4 4 ft < C" 1*1 i~i Ti
14104.1. UOiJ
...c....5 inf|
0.98::
-0. 500
2. 000
-1.000
-0. 505:
-0. 49t-
4.
i •! i ""-TI nnfi
1 *T 1 i-'-'U. IJU'.1
2^^^. nsn
3. 9 1 7
-•3. 050
5.917
-4. 050
-0. 779
-n. Afte;
-0. 559
5.
14j>4::'~i. nnn
2819.000
19. lt-7
-17.050
25.03::
-21. 100
-0. 890
-0.841
-0. 629
n 4
Slope -0.366
Intercept 0.704
Syx 0.353
Sx 11.254
S, 0.018
a
Sb 0.440
S 0.198
4-303
r -1.000
Confidence Interval
0.866 + 0.077
-------
TABLE A-99 SUMMARY OF DATA PROM TEST NO. 58
Page 1 of 3
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling x ; nonboiling
FB 50 %
Inlet air
Other
Date 3/1/79
PC y SC
Exhaust air
Ambient 'air*
Temperature 68
Pressure 29.825 in. Hg
Humidity 4b 'f>
Reading
No.
T, m1n
W, Ib
AT, h
AW. Ib
EAT. h
EAW, Ib
(S). """
(Sf). ">"•
X, 1b/h
139441.000
356P. 500
l?94iE.4.00Ci
3571. 250
139474.000
35*6. 000
1.
139503.000
356-A. 500
2.
139555.000
356=!. «;nri
0. StT'
-1.000
0. 867
-1.000
-1. 15^
-1. 154
-1. 154.
3.
1396 IS. 000
}•=;*:.;!. 7cifi
1.050
-1.750
1.917
-2. 750
-1.667
-1.435
-1.294
*>.
00
-------
TABLE_A-99 (continued)
Page 2 of j
vD
Reading
No.
T, nln
U. Ib
AT. h
AU. Ib
I AT, h
EAU. Ib
09. »*
(SOL 1b/h
•
X. Ib/h
4.
139680. OOCi
3562. 400.
1.031:
-1.350
2. 950
-4. 100
-1.306
-1.390
-1.326
5.
139737.000
3561.200
0. 950
-1.200
3. 900
-5. 300
-1.2*::
-1. 359
-1. 33-
6.
139798. 000
3559. 500
1.017
-1.700
4. 917
-7. 000
-1. 67;:
-1.42-
-1. 35?
i .
139855.000
3558. 250
0. 950
-1.250
5. 867
-8. 250
-1.316
-1.40c.
-1. 361
S.
140814.000
3535. 400
1 5. 98;:
-22. 850
21.350
-31. 100
-1.430
-1.42.::
-1. 370
9.
140866.000
3534. 250
0. 867
-1. 150
22.717
-32. 250
-1.327
-1.420
-1.376
(continued)
-------
TABLE A-99 (continued)
Pdgc ^3 of 3_
tn
o
Reading
No.
T. min
U. Ib
•• f IV
AT. h
AW, Ib
EAT. h
EAV. Ib
/EflW\ ....
(jar;. lb/h
X. lb/h
n 8
Slope -
Intercep
..140925.000
.3535.400
1.427
t 0.124
MO^S*;. non
35^. nnn
s
s
s
14098£. 000
3534. 700
„, 0.106
r*
„ 8.885
, 0.005
1
b 0.244
„ 0.187
14104S nnn
A T A * J ^ J • ••• "• -
3534. 400
lo/2 2-
r -1
Confidence
1.427 +0.0
447
.000
interval
12
-------
TABLEA-l00 SUMMARY OF DATA FROM TEST NO. 58
Page 1 of 3
Oegreaser B, Idle
Solvent: Methylene chloride
(Boiling _x ; nonboiling )
FB 50 * PC x SC _
Inlet air x Exhaust air x
Other
A g %
0 ft/min
Date 3/1/79 __
Ambient ^ir'
Temperature 68 °F
Pressure 29.825 in. Hg
Humidity 45 T,
Reading
No.
T, m1n
W. Ib
AT. h
AW, Ib
EAT. h
EAW. Ib
(5). '>"•
fajM\ lb/h
X. lb/h
139441.000
2858.500
139430.000
2857. 250
1.
139503.000
2855. 500
w •
139555.000
2354. 750
0. 367'
-0. 750
0. 867
-0. 750
-0. 865
-0. 865
-0. 36=.
3.
1-39613.000
2854. 250
1.050
-0. 500
1.917
-1.250
-0. 476
-0. 652
-0. 759
4.
1-39680.000
2353.250
1.033
-1.000
2. 950
-2. 250
-0. 968
-0. 763
-0. 760
tn
-------
TABLE A-100 (continued)
Page 2 of jj_
Reading
No.
T. win
U. Ib
AT. h
AU. Ib
CAT. h
CAM. Ib
(AT) 1b/h
(fe 1b/H
X. Ib/h
5.
139737.000
2852. 450
0. 950
-0. 800
3. 900
-3.050
-0. 34?
-0. 78?
-0. 766
6.
139798.000
2852. 000
1.017
-0. 450
4.917
- 3. 500
-0. 443
-0.71?
-0. 755
i •
139855. 000
2851.250
0. 950
-0. 750
5. 867
-4. 250
-0. 789
-0. 724
-0. 750
8.
140814. 000
2841.050
15.983
-10.200
21.850
-14.450
-0. 638
-0.661
-0. 737
9.
140842.000
2840. 250
0. 467
-0. 300
22.317
-15.250
-1.714
-0. 68':
-0.730
10.
140366.000
2340. 000
0. 400
-0. 250
22.717
-15.500
-0. 625
-0. 68?
-0. 725
N>
(continued)
-------
TABLE JU100 (continued)
Page _3_ of 3
Reading
No.
T, min
U. Ib
AT. h
AU. Ib
EAT. h
EAU. Ib
(iir) lb/h
X. lb/h
140925.000!
_„ .284.0. IOC"
14098<5.000
2839. 6000
141045.000
2839. lO'O
•
LJ
n 9
Slope -0.666
Intercept -0.232
s
s
0.203
9.563
0.008
0.240
0.380
t ., 2.365
a/2
r -l.OOU
Confidence interval
0.666 + 0.019
-------
TABLE A-101 SUMMARY OF DATA FROM TEST NO. 59
Page 1 of 1
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling _x_)
FB 50 * PC x SC
Inlet air * Exhaust air
Other
A Q %
0 ft/min
Date 3/3/79
Ambient 'air'
Temperature 69 T
Pressure 29.525 in.Hg
Humidity 45 I
Reading
No.
T, m1n
W, 1b
AT. h
AW. 1b
EAT, h
CAW. Ib
(Sf). ">'*
(££). ">"<
X, lb/h
.142482.000
_ 3522. 300
1.
142493. 000
3522. 100
•%
u. •
145559.000
3500. 750
51.01T1
-21. 350
51.017'
-21. 350
-0.4 IP
-0.41?:
-0. 41P
VI
-------
TABLE A-102 SUMMARY OF DATA FROM TEST NO. 59
Page 1 of _\_
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling _x )
FB 50 % PC x SC
Inlet air x Exhaust air
Other
A _g %
V Q ft/min
Date 3/3/79
Ambient 'air'
Temperature 69 °F
Pressure 29.525 in. Hg
Humidity 45 %
Reading
No.
T, mln
H. lb
AT, h
AW, lb .
EAT, h
EAW, lb
(Ir) 1b/h
(EAW\ lb/h
\TSTjt
X, lb/h
142482.000
,2819.900
1.
1424?8. 000
. 2820. 000
»» •
145559.000
280?. 250
51.017
-It. 750
51.017
-16.750
-0. 32?:
-0. 32?:
-0. 325:
CP
-------
TABLE A-103 SUMMARY OF DATA FROM TEST NO.
Page
of
Degreaser A, idle
Solvent: Methylene chloride
(Boiling ; nonboiling jc )
FB 50 t PC x SC _
Inlet air _x Exhaust air
Other
A Q 1
V 0 TfTmin
3/SZ79.
Date
Ambient Jir
Temperature
Pressure29_J>1 i n. Hg
Humidity 46..5 3
e 69 °f
1.51 m. Hg
Reading
No.
T, min
W. 1b
:>
n
pi
AT, h
AW. 1b
EAT. h
EAW. lb
(S). ">"
(IAT). lb/h
X. 1b/h
14c,K':i. nnn
1.
l4Sh7*. nnn
2.
14^^^. nnn
^4-3in. arm
21.550
-•?. S50
22. 300
-9. 850
-0. 457
-0. 442
-0.221
-------
TABLE A-104 SUMMARY OF DATA FROM TEST NO. 60
Page 1 of i
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling _x )
FB SO Jt PC x SC _
Inlet ai? x Exhaust air x
Other
A
0
min
Date 3/b/79__
Amb i entTa i r
Temperature 69 °F
Pressure29.51 in. Hq
Humidity 46.5 '»
Reading
No.
T, mln
U. Ib
AT. h
AW, Ib
EAT. h
EAW. Ib
(S). ">'"
(isr). 1b/h
X. lb/h
145631. 000
2302. 500
1.
145t-7if.. 000
2799. 000
2.
146969. 000
27*2. 750
21.550
-16.250
22. 300
-19.750
-0. 754
-0. 336
-2.77fr
-------
TABLE A-in5 SUMMARY OF DATA FROM TEST NO. fi1
Page i of
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling x )
FB 50 % PC "SC
Inlet air x_
Other
xnaust air
A
0
0 %
In in
Date 3/6/79
Ambient a"ir
Temperature 69_ °F
Pressure 29.475 in. Hg
Humidity 45 *
Reading
No.
T, min
W. 1b
AT. h
AW. 1b
EAT. h
CAW. 1b
(sr) 1b/ff
/EAWN ....
\m). 1b'h
X, Ib/h
1 46995. 000
3490. 400
1.
147012. 000
3481.400
tZ. •
1 43 354. 000
3470. 000
22. 367'
-11.400
22. 36T1
-11.400
-0.510
-0.510
-0. 510
•
09
-------
TABLE £-106 SUMMARY OF DATA FROM TEST NO. 61
Page 1 of 1
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling _x )
FB 50 % PC SC _
Inlet air x Exhaust air x_
Other
A 0 %
V 0 fVmin
Date J/6/79
Amb 1 ent 'air
Temperature 69 °F
Pressure 29.475 In. Hg
Humidity 4b I
Reading
No.
T, m1n
W, 1b
AT. h
AW. 1b
EAT. h
CAM, Ib
(AT) 1b'h
(fe """
X. Ib/h
146995.000
2784. 000
1.
147012.000
2733.250
2e
148354.000
2772. 600
22. 367
-10.650
22. 367
-10.650
-0. 476
-0. 476
-0. 476
-------
TABLE A-107 SUMMARY OF DATA FROM TEST NO. 62
Page J_ of J__
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling _* ; nonboiling
FB 50 *
Inlet air j
Other
PC x SC
Exhaust air
ft/mil
min
Date 3/7/79
Ambient 'afr'
Temperature 69 °F
Pressure 29.3 In. Hq
Humidity 45 I
Reading
No.
T. min
W, Ib
AT. h
AW. Ib
EAT. b
EAW. Ib
(AU \
ON 1 iL/i,
•TT i " o/"
AT/,
(gjf^ Ib/b
X. Ib/h
14S451. 000
3479. 750
14ftsnn.nnn
3479. 000
143515.000
3479. 250
1.
143546. 000
3473. 000
b. •
14-54RA. nnfi
3461. 100
15.667
-16.900
15.667
-16.900
-1.079
-1.079
-1.079
149536.000
3460. 750
-------
TABLE A-107 (continued)
2 of 2
Reading
No.
T( mln
M, Ib
AT, n
AH, Ib
CAT. h
CAM. Ib
(M} 1K/h
l77/ '°'n
\AT/,
X. Ib/h
149592.000
3460. 000
149653.000
3462. 000
149434. oon
3461. 000
•
tr
Sltpe- 1.079
Intercept
s
s
t
I
r
Confldenrp Interval
-------
TABLE £_]J38 SUMMARY OF DATA FROM TEST NO. 52
Of 2
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling _x ; nonboiling )
FB 50 % PC x r
Inlet air x Exhaust air
Other
Date 3/7/79
SC
ft/mil
min
Ambient 'air
Temperature 69 °F
Pressure 29.3^ 1". Hg
Humidity
Reading
No.
T, min
W. 1b
AT, h
AW, 1b
EAT, h
EAW, lb
(M\ ,h/|k .
i -Tf i iDf n
\tji/i
(m) 1b/h
X. 1b/h
148481.000
2805. 250
1484?7. 000
2804. 650
148515.000
2804. 350
1.
148546.000
*7QQ 'Sfi
o.
14?486. 000
,,ftn 2e;f|
15.667'
-19.000
15.667'
-1?. 000
-1.210
-1.210
-1.210
.
149536.000
(
N)
-------
TABLE £_]Q8 (continued)
Page 2 of 2
Reading
No.
T, nln
W, Ib
AT. h
AU. Ib
CAT. h
CAM. Ib
(Si ""'
f ftA" A | h /t,
X. lb/h
-
149592.000
2778. 600
149658.000
2780. 850
149434.000
2790. 400
.
cr
Slope • 1.213
Intercept
s
s
t
(
r
Confidence Interval
-------
TABLE AJ09 SUMMARY OF DATA FROM TEST NO. 63
1 Of 2
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling x ; nonbolllng )
FB 50 * PC x SC
Inlet air x Exhaust air
Other
V 0
ft/mi
In in
Date 3/8/79
Ambient'air'
Temperature 70 °F
Pressure 29.3 in. Hq
Humidity T1I
Reading
No.
Tt mln
M. 1b
AT, h
AW, lb
EAT. h
SAW, lb
(£). ""*
(if). «>"•
X. 1b/h
149S46. 000
3535. 200
149868.000
3529. 600
1.
149896. 000
3530. 500
^
hi •
149922.000
3529. 450
0.431:
-1.050
0.43::
-1.050
-2.421:
-2.42::
-2.42]:
3.
151097.000
3502. 500
19.58::
-26. 950
20.017
-28. 000
-1. 376
-1.39?
-1.911
4.
151155.000
3501.200
0. 967
-1.300
20.98::
-29. 300
-1.345
-1. 39t-
-1.739
-------
TABLE A-109 (continued)
Page 2 of 2
Reading
No.
T, win
U. 1b
AT, h
AH, 1b
CAT. h
IAW. lb
09. """
(fir). lb/h
X. lb/h
5.
151243.000
349?. 700
1.467
-1.500
22. 450
-30. 300
-1.020
-1.37?
-1.64?:
151274.000
3493. 350
15133*. iWi
n 4
Slope- -1-365
Intercept -0.491
'yx
0.297
10.407
0.016
1.035
0.609
t „ 4.303
a/c
r -1.000
Confidence Interval
1.365 + 0.069
-------
TABLE A-110 SUMMARY OF DATA FROM TEST NO. J£
Page 1 of 2
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling _x ; nonbolling )
FB 50 J * PC x SC
Inlet air x Exhaust air _>
Other
Date 3/8/79
ft/mii
min
AmblentTair
Temperature 60 °F
Pressure 29.3
-------
TABLE A-110 (continued)
Page 2 of _2.
Reading
No.
T, mln
M. 1b
AT. h
AH. 1b
EAT. h
EAU. Ib
(AH\ lb/h
1 -rsr I ID/n
\AT/,
(fir). lb/h
K, lb/h
5.
151243.000
2987. 750
1.467
0. 600
22. 450
-17.350
0. 409
-0.77::
-1.80:;:
151274.000
2987. 500
151336.000
2988. 700
n 4 S „ 1-048 t ., 4.303
yx o/c
Slope- -0.742 $ 10.407 r -1.000
Intercept -1.846
0.058
1.035
2.275
Confidence Interval
0.742 + 0.250
-------
TABLE ^A-lll SUMMARY OF DATA FROM TEST NO. 64
Page 1 of 2
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling _x ; nonboiling
FB 75 * PC x
Inlet air x txhaust air
Other
ft/mil
min
Date 3/10.11/79
Ambient d"ir
Temperature 68 °F
Pressure 29.5T in. Hg
Humidity 42 I
Reading
No.
T mln
ly III 1 11
H. lb
AT, h
AW, lb
.
IAT, h
CAW, lb
(S). ">"••
/TMt\
viar) 1b/h
-
X, Ib/h
1.
152628. 000
3533. 300
3.
152643. 000
3581. 900
0. 3'33
-1.900
0. 33!:
- 1 . 900
-5. 700
-5. 700
-5. 700
•3.
152657. nnfi
3577. 300
0. 150
-4. 600
0. 483
-b. 500
-30.667
-1:3.44:!:
-9. 57-f
4.
152635. 000
3577. 300
0. 467
0. 500
0. 950
-b. 000
1.071
-6. 3U'
-3. 43?:
5.
154024. 000
3561. 100
22.317
-16.700
23.267
-22. 700
-0. 74?:
-0. 976
-6.610
6.
154109.000
3562. 600
1.417
1.500
24. 683
-21.200
1.059
-0. 859
-5. 460
00
-------
TABLE A^VII (continued)
Page 2 of 2
Reading
No.
T, mln
N. 1b
AT. h
AW. Ib
EAT. h
EAU. Ib
(S """
X. Ib/h
•
•
n 5 Syx 2.207 tQ/2 3.182
Slope -0.732 S^ 12.821 r -1.000
Intercept -4.383 S. 0.086 Confidence Interval
a
Sb 0.350 0.732 + 0.274
S_ 13.518
-------
TABLE J\-112 SUMMARY OF DATA FROM TEST NO. _6i
Page i of 2
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling x_; nonboiling )
FB 75 I PC x SC
Inlet air x Exhaust air
Other
0 %
7min
Date 3/10,11/79
Ambient'air
Temperature 68 °F
Pressure 29.5T in. Hg
Humidity 42 %
Reading
No.
T, min
W, Ib
oT. h
flW, Ib
EAT, h
CAW. Ib
(S). ""*
(Sfi ™
X. Ib/h
1.
152631.000
3042. 800
X
••?
k_ •
152645.000
3041.900
0.23;:
-0. 900
0. 23C:
-0. 900
-3.857
-3. 857
-3.857
3.
152653. 000
3038. 300
0. 13::
-3. 600
0. 367
-4. 500
-27. 000
-12.27::
-S. Ot-s
4.
152tS2. 000
3037. 300
0. 43::
-1.000
0. 850
-5. 500
-2. 069
-6.471
-7. 53::
5.
1540 IS. 000
3013.300
22. 267
-24. 000
O-'S 11 "•
>1O. 1 1 I
-29. 500
-1.078
-1.276
-T.. 96^'
6.
1541S9. 000
3014. 100
2. 350
0. 800
25. 967
-28. 700
0. 2SJ
-1. 105
-4. 996
-------
TABLE A-l 12 (continued)
Page 2 of 2
Reading
No.
T, mln
U. Ib
AT, h
AH. Ib
CAT, h
CAU. Ib
$). ">»
(M\ lb/h
X. lb/h
•
n 5 Syx 2.346 tQ/2 3.182
Slope -1.052 *x 13.218 r -1.000
Intercept -3.185 Sfl 0.089 Confidence interval
Ss 0.346 1.052 + 0.283
Sc 11.423
-------
TABLE A-113 SUMMARY OF DATA FROM TEST NO. 65
?aser A, Idle
Solvent: Methylene chloride
(Boiling x ; nonboiling )
FB log* PC x SC A 0 %
Inlet air x_ Exhaust air x V o ft/min
Other
Date 3/11.12/79
Ambient 'air
Temperature 68 '
Pressure 29. bl in.
Humidity "37 X
Page T of 2
Reading
No.
Tf m1n
H, lb
AT, h
AW, lb
ZAT. h
CAW. lb
(S).'"
(Sft 1W
X, lb/h
1.
154243.000
3615. 300
w •
15425b. 000
361 1.500
0.217
-3. SOO
0.2 IT1
-3. 800
-17.53:;:
-17.53?:
-17.53?:
3.
1542ft":. Ofifi
3610. 600
0. 450
-0. 900
0. 667
-4. 700
-2. 000
-7. 050
-12.294
4.
15S5-:':. OilO
3593. 400
20. S 33
-17.200
21.500
-21.900
-0. :32>.
-1.019
-3. 53t-
15560S. 000
5594. 450
1555^5 nnn
3594. 300
-------
TABLE A-113 (continued)
Page 2 of _2_
Reading
No.
T, mln
H, Ib
AT. h
AU. Ib
*» EAT. h
EAW. Ib
(M\ ih/h
1 TT t iD/n
W/t
(IAT) lb/h
X. lb/h
•
n 3
Slope -0.839
Intercept -3.877
Syx 0.370
Sx 12.160
S, 0.021
o
t /9 12.706
a/2
r -1.000 •
Confidence Interval
L 1.106,
o.576
-1
j
9.329
-------
TABLE A-114 SUMMARY OF DATA FROM TEST NO. 65
Page \ of 2
Degreaser B, Idle
Solvent: Methylene chloride
(BojUng _x ; nonboiling )
FB 100 % PC x SC
Inlet air x Exhaust air x
Other
A
0
n in
Date 3/11,12/79
Ambient 'air
Temperature 68 °F
Pressure 29. bl
Humidity 37 \
Reading
No.
Tt min
H, 1b
AT. h
AW, Ib
EAT. h
EAM. Ib
(ir) 1b'h
(Sr) lb/h
X. lb/h
1.
154243.000
3086. 000
2.
154253.000
3035. 700
0. 167
-0. 300
0. 167
-0. 300
-1.300
-1.300
-1. 800
3.
154279. 000
3036. 100
0.43!:
0. 400
0. 600
0. 100
0.92::
0. 167
-0.817
4.
15553-3. 000
3065. 900
20. 900
-20. 200
21.500
-20. 100
-0. 967
-0.935
-0. S5t-
155595.000
3063. 400
155656. 000
3067. 500
-------
TABLE A-l 14 (continued)
Page 2 of 2
Reading
No.
T, m1n
M. Ib
AT. h
AW, Ib
CAT. h
CAU. Ib
(ir) lb/h
X. lb/h
•
» 3 Syx 0.573 la/2 12.706
Slope -0.947 Sx 12.194 r -1.000
Intercept 0.259 Sa 0.033 Confidence interval
O
Sb 0.519 0.947 + 0.419
S,. 1.395
-------
TABLE A-115SUMMARY OF DATA FROM TEST NO. 6b
Page 1 of 1
Degreaser A. Idle
Solvent: Methylene chloride
(Boiling ; nonbolllng x )
FB 100 % PC x SC
Exhaust air
Inlet air x txnausi air x
Solvent loss during cool down period
A 0 %
V 0 ft/min
Date 3/12/79
Ambient
Temperature 69.5 °F
Pressure 29.75 in. Hg
Humidity 37 I
Reading
No.
T, mln
W, Ib
AT. h
AW. Ib
EAT, h
CAW. Ib
(at) 1b'h*
(Mr) lb/h
X. lb/h
1.
155603.000
3594. 450
2.
156870.000
3537. 500
21.03'::
-6. 950
21.03:::
-*. 950
-0. 330
-0. 330
-0. 330
>J
a*
-------
TABLE A-116 SUMMARY OF DATA FROM TEST NO. 66
Page jj of
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonbolling _x )
n inn * PC x SC
Inlet air x Exhaust air
Other
i ft/mi
mln
Date 3/12/79
Ambient "air '
Temperature 69.5 °F
Pressure 29.75 in. Hg
Humidity 37 T,
Reading
No.
T, m1n
W. Ib
AT, h
AW, Ib
EAT, h
EAW, Ib
(***\ IK*,
1 -rr- 1 1 D/n
\AI/,
(**«) lb/h
X. lb/h
1.
155656. 000
3067. 500
tZ. •
156S70. 000
3059. 500
20.23::
-8. 000
20.23^:
-8. 000
-0. 395
-0. 395
-0. 395
-
-
-------
TABLE A-117 SUMMARY OF DATA FROM TEST NO. 67
Page j of 2
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling x ; nonboiling
FB 1QO* PC _ x SC
Inlet air « Exhaust air
Other ~"
-*WJ
ft/mm
Date 3/13/79
Ambient 'air '
Temperature 70 °F
Pressure 29.45 in. Hg
Humidity 37 %
Reading
No.
Tt mln
H. 1b
AT, h
AWV 1b
EAT. h
ZAH. 1b
(S). "•"•
(Si ""•
X. Ib/h
136o??.0oo
3587. ?ft
156912XXX
3536. ^oo
156926.000
3581.oo
1.
156956. OOCi
3531.500
-i
tL •
1570 18. 000
3580. TOO
1 . 03C:
-0. 800
1.03::
-0. 300
-0. 774
-0. 774
-0. 774
3.
158334.000
3565. 000
21.93::
-15.700
22. 967
-16.500
-0.7 If.
-0. 71*
-0. 74t.
it*
^1
09
-------
TABLE A-l 17 (continued)
Page 2 of 2
Reading
No.
T, min
H. lb
AT. h
AH. lb
CAT. h
CAU. lb
(fit 'b»
(£AN i i L / 1.
• ..-• i ib/n
_• g^f m ™ **f *•
X. Ib/h
4.
158400. 000
3564. 500
1. 100
-0. 500
24. 067
-17.000
-0. 455
-0. 706
-0. 73C:
153426. 000
3564. 150
158500. 000
3566. 050
•
153553.000
^S^S. 700
vO
n 3 -
Slope- -0.709
Intercept -0.074
Syx 0.198
sx 12.992
Sa 0.011
Sb 1.094
S, 0.170
r -1.000
Confidence interval
0.709 + 0.140
-------
TABLE A-118 SUMMARY OF DATA FROM TEST NO. 67
Page j of
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling _x ; nonboiling )
FB 10U % PC x SC _x_
Inlet aTF x Exhaust air x
Other
A 0 %
V 0 ft/min
Date 3/13/79
Amblent'air
Temperature 70 °F
Pressure 29.45 in. Hg
Humidity 37 %
Reading
No.
T, mln
W. Ib
AT. h
AW. Ib
EAT, h
CAW. Ib
(S). ""* '
(f£). ">/"
X, Ib/h
13659?.CX)o
3059. 700
156912.000
3057. 700
156926.COO
3054. JOo
1.
156956. 000
3053. 900
2.
157018. 000
305-3. 500
1.03::
-0. 400
1.033
-0. 400
-0. 387
-0. 387
-0. 387
3.
158334.000
3043. 200
21.933
-10.300
22. 967
-10.700
-0. 470
-0. 466
-0. 42t-
o>
o
-------
TABLE A^nc (continued)
Page 2 of 2
Reading
No.
T. n1n
W. Ib
AT. h
AH. Ib
EAT, h
£AU. Ib
(M\ IK/h
1 7T 1 ID/"!
W/»
(Lull i it. gg.
Yj?f ) iD/n
X, Ib/h
4.
15845?.000
3041.200
1.93;:
-2. 000
24. 950
-12. 700
-1.00?:
-0. 501:'
-0. 454
158432.000
3042. 250
153558.000
3042. 900
•
oo
n 3
Slope - -0.496
Intercept 0.155
s
s
0.721
13.273
0.038
1.089
0.337
t ., 12.706
a/2
r -1.000
Confidence Interval
0.496
-------
TABLE A-119 SUMMARY OF DATA FROM TEST NO. 68
Page 1 of 1.
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling _% )
FB 100 %
Inlet air *
Other
PC « SC
Exhaust air
ft/mil
min
3/14/79
Date
Ambient 'air
Temperature 69 °F
Pressure 29.5 in. Hg
Humidity 38 *
Reading
No.
Tf m1n
M, lb
AT. h
AW, lb
EAT. h
EAM, lb
(If). '*
(%). ">'*
X, Ib/h
1.
158500.000
3566. 050
^
k. •
1 59947. 000
'3555. 300
24. 11T1
-10.250
24. 117'
-10.250
-0. 425
-0. 42=.
-0. 42=.
00
ro
-------
TABLE A-120 SUMMARY OF DATA FROM TEST NO. 68
Page 1 of 1
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling _x )
FB TOO * PC x SC
Inlet air x Exhaust air _
Other
A _Q I
V Q ft/mln
Date 3/14/79
Ambient'air
Temperature 69 °F
Pressure .2^5 in. Ha
Humidity .38*
Reading
No.
T, mln
W. lb
AT. h
AW. lb
EAT, h
CAW, lb
(»). '<"*
f •• jkU V
• **O" 1 9 L **-
X. Ib/h
1.
158558.000
3042. 900
2e
15995'3. 000
3029. 300
23.250
-T3. 100
2'3. 250
-13. 100
-0. 560
-0.56::
-0.56::
-
€0
co
-------
TABLE A-121 SUMMARY OF DATA FROM TEST NO. 69
1 of 1
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling *_; nonboiling )
n 125 I PC x SC
Inlet air x Exhaust air
Other
ft/mii
min
Date 3/15/79
Ambient Air
Temperature 68.5 °F
Pressure 30. U9 in. Hg
Humidity 38 %
Reading
No.
T, m1n
W. 1b
AT. h
AW, 1b
EAT, h
CAW, Ib
(*u \
Oil 11, A,
TT i lo/n
Al/,
(™\ 1b/h
X, Ib/h
160026. 000
3643. 350
160050.000
36.39. 000
1.
160075.000
3637. 050
iZ. •
161254. 000
3621. 350
19.650
-15. 700
19.650
-15. 700
-0. 799
-0. 799
-0. 799
161327.000
3623.000
00
-------
TABLE A-122 SUMMARY OF DATA FROM TEST NO. 69
Page i of i
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling j< ; nonboiling
FB 125 I PC x SC
Inlet air x Exhaust air _
Other
Date 3/15/79
Amb i enTTTr
Temperature 6S..5 °F
Pressure 30.09 in. Hg
Humidity 38 I
Reading
No.
T, win
W, Ib '
AT. h
AW( Ib
EAT, h
EAM, Ib
(&} IhTh
i yr i iD/n
\AI/i
X. Ib/h
1 60026. 000
3106. 300
160050. 000
'3100. 750
1.
160075. 000
3100. 750
2.
161254. 000
3076. 750
19.6TO
-24. 000
19. 650
-24. 000
-1.221
-1.22J
161419.000
307S. 500
00
-------
TABLE A-123 SUMMARY OF DATA FROM TEST NO. 70
Page J_ of ]
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling _x )
™ 125 I PC x SC
Inlet air jc Exhaust air x V
Solvent loss during cool down period
ft/m
min
Date 3/16/79
Ambient «Jir '
Temperature 69 °F
Pressure 30.12 in. hg
Humidity 38 *
Reading
No.
T, m1n
W, 1b
AT. h
AW, lb
EAT, h
CAW, lb
(»). ""*
(SOL "•"'
X. Ib/h
1.
161327.000
3623. 000
0
k_ •
162654. OOfi
3616.500
22. 1 1 T1
-6. 500
22. 117
-6. 500
-0. 2?4
-0. 291
-0. 2?
-------
TABLE A-l24SUMMARY OF DATA FROM TEST NO. 70
Page _J_ of J
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling x )
™ 125. * PC x SC
Inlet air x_ Exhaust air
Other
A o %
V o ft/ml n
Date 3/16/79
Ambient 'air
Temperature JJ9_ °F
Pressure 30.12 in. Hg
Humidity 38 ~
Reading
No.
T, mln
W. Ib
AT. h
AN, Ib
EAT, h
CAW. Ib
(S). ">"•
(M?). «""
X, lb/h
1.
161327. 000
307S. 500
•Z. •
1 62654. OOCi
3070. 350
22. 117
-8. 150
22. 117
-3. 150
-0. 36'!'
-0. '369
-0. 3*-:i
3.
165601. 000
.30?0. 400
49. 117
-39. 950
71.23:::
-43. 100
-o. si::
-0. 675
-0. 52J'
00
-------
TABLE A-125 SUMMARY OF DATA FROM TEST NO. 71
Page 1 of 1
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling x )
FB 50 % PC _^^ • SC
Inlet air x Exhaust air
Other
Lip exhaust at 16 ft-Vmin oer ft^ of top opening
I ft/mil
rnin
Date 3/22/79
Ambient 'air
Temperature °F
Pressure in. Hg
Humidity %
Reading
No.
T, m1n
W. lb
AT. h
AW. lb
EAT. h
'EAW, ib
(&} 1h/h
\ TT i *o/n
\AI/f
(IST) lb/h
X, lb/h
1.
170497.000
3598. 700
2.
171342.000
3590. 500
14.08::
-8. 200
14. 08^:
-3. 200
-o. 5s:-
-0. 581:
-0. 5?;1
o>
00
-------
TABLE A-126 SUMMARY OF DATA FROM TEST NO. 71
Page j__ of j_
Oegreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling _x )
FB 50 * PC ___ SC
Inlet air x Exhaust air
Other
Crosscurrent test
An %
V n ft/min
Date 3/22/79
Ambient 'air
Temperature °F
Pressure in. Hq
Humi d i ty %
Reading
No.
Tf min
W, lb
AT, h
AW, lb
EAT, h
CAW. lb
(If). ">"•
(i?). «""
X. Ib/h
1.
170497. 000
2779. *00
:•
k_ •
171342.000
2722. 200
14. Ofi'l:
-57. 400
14. ng::
-57. 400
-4. 07t-
-4. 07t-
-4. 070
CO
vO
-------
TABLE A-127 SUMMARY OF DATA FROM TEST NO. 72
Page ] of 1
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling _x ; nonboiling )
FB _&Q I PC £_ SC A _Q %
Inlet air g_ Exhaust air x V n tt/min
Lip exhaust at 100 ft-Vmin per ft^ of top opening
Date 3/23/79
Ambient Sir
Temperature 69 °F
Pressure 28.81 in. Hg
Humidity 61 I
Reading
No.
Tt mln
H. 1b
AT, h
AW, lb
EAT, h
EAH, lb
(»). i* '
(Sfi ">'"
X, lb/h
171507.000
376-3. 000
171525..00CI,
3762. 000:i
in 535. ooo
3758. 100
1.
171531.000
3755. 700
2m
172357.000
3647. 450
21.2bT1
-1 OS. 250
21.267'
-1 OS. 250
-5. 0?0
-5. 090
-5. 0?0
172910.000
3647. S50
vO
O
-------
TABLE A-128SUMHARY OF DATA FROM TEST NO. 72
1 Of 1
Degreaser B, Idle
Solvent: Methylene chloride
(BofHng x ; nonboiling )
FB 50 I PC x SC _
Inlet air jc Exhaust air x
Other
Crosscurrent test
Ft/mil
min
Date 3/23/79
Ambient 'air
Temperature 69 °F
Pressure 28.81 in. Hg
Humidity 61 _1
Reading
No.
T, m1n
W, Ib
AT. h
AW. Ib
EAT. h
CAW. Ib
(1?). '*'
(M?). "•"•
X. Ib/h
171507.000
2977. 500
171526.000
2973. 000
171535.000
2973. QOO
1.
171 53 1.000
2969. 900
2.
172S57. 000
2793. ?00
21.267
-176.600
21.267
-176. 600
-3. 30<-
-3. 30*-
-8. 30'
172994.000
278S. 250
-------
TABLE A-129 SUMMARY OF DATA FROM TEST NO. 74
Page 1 of 5
Degreaser A, operating
Solvent: Methylene chloride
Date 4/15/79
FB 75 % PC x SC A 50 %
Inlet air x Exhaust air x V 8 ft/mi n
Other
Ambient air
Temperature 7U °F
Pressure 29.6 in. Hg
Humidity _b2~"~*
Reading
No.
T, mln
M, Ib
AT, h
AW, Ib
EAT, h
EAW. Ib
(Atl\ • • •
OW 1 IK/h
xr 1 • vfn
Al/,
(Ml) Ib/h
X, Ib/h
205141. 000
'^72. nnn
~ ™ i ^ • •* •»• •» •
205157. 000
3671. 100
205 it. ?. nnn
':h.K7. ftfn'i
1.
205201. 000
ftl •
205265. 000
1.0*7
-1.000
1.067
- 1 . 000
-0.937
-0.937
-0. 937
3.
205324.000
*> £ £ T« QTifi
O t§ O J* • . U L '
0. 983
-0. 700
2. 050
-1.700
-0.712
-0. 829
-0. 883
-------
TABLE A-129 (continued)
Page 2 of 5
Reading
No.
T, «1n
M. 1b
AT. h
AW, 1b
CAT. h
CAM. 1b
(Sf) ">'"
VAT/,
(IAT). 1b/h
X. 1b/h
4.
205332. 000
3661.500
0. 967
-2. 400
3.017
-4. 100
-2. 43::
-1.359
-1.04C'
5.
205440. 000
3660. 200
0. 967
-1. 300
3.98'.:
-5.400
-1.345
-1. 356
-1. 120
6.
205505. 000
3653. 500
i.os:;
-1. 700
5. 067
-7. 100
-1.569
-1.401
-1. 177
_
205564. 000
3657. 000
0.93::
-1.500
6. 050
-3. 600
-1.525
-1.421
-1.217
3-
205625. 000
3655. 900
1.017
-1. 100
7. 067'
-9. 700
-1.082:
-1. 37::
-1.240
9.
205634. 000
3654. 000
0. 93::
-1.900
3. 050
-11.600
-1.93:-
-1.44J
-1.265
VD
(continued)
-------
TABLE A-l_29 (continued)
3 of 5
Reading
No.
T, nln
U. 1b
AT. h
AU, 1b
CAT, h
CAW. 1b
©. '•*
(IAT), lb/h
X, lb/h
10.
205745. 000
3652. 600
1.017
-1.400
9. 067
-13.000
-1.377
-1.434
-1.234
11.
205804. 000
3651.500
0.98::
-1. 100
10.050
-14. 100
-1. 119
-1.401:
-1.295
12.
205864. 000
3650. 000
1.000
-1.500
11.050
-15. 600
-1.500
-1.41J:
-1. 306
13.
205925. 000
364ft. 800
1. 017
-1. 200
12.067
-16.300
-1. 180
-1.39J1
1 -1.3KI
14.
205935. 000
3647. 300
1. 000
-1.500
1 3. 067
-13.300
- 1 . 500
-1.40J
- 1 . 320
15.
206045. 000
3645. 900
1.000
-1.400
14.067
- 1 9. 700
-1.400
-1.400
-1.326
\D
(continued)
-------
TABLE A-12Q (continued)
Page
Reading
No.
T. »1n
U. 1b
AT. h
AU. Ib
CAT. h
CAU. Ib
(1?). ""*
(sft ">"
X. tb/h
16.
206104.000
3645. 100
0. 983
-0. SOO
15.050
-20. 500
-0. 814
-1.36?
-1.32*
17.
206164.000
3643. 500
1.000
-1. 600
16.050
-22. 100
-1.600
-1. 377
-1.331
18.
206217.000
3642. 600
0. 383
-0. 900
16.933
-23.000
-1.01?'
-1. 358
-1.333
19.
206236. 000
3641. 500
1. 150
-1. 100
18.033
-24. 100
-0. 957
-1. 333
-1.333
20.
206 34 R. 000
3640. 100
1.033
-1. 400
19.11 7
-25. 500
-1. 355
-1. 334
-1. 33::
21.
206401.000
3638. 100
0. 883
-2. 000
20. 000
-27. 500
-2.264
-1.375
-1.335
vD
in
(continued)
-------
TABLfc A-T2_9 (continued)
Page 5 of 5
Reading
No.
T, mln
W. Ib
AT, h
AW. Ib
CAT. h
I AW. Ib
(M\ lh/h
\ TT i iD/n
\AT/,
(fir), lb'h
X, 1b/h
22.
206461. nnn
3637.900
1.000
-0. 200
21.000
-27. 700
-0. 200
-1. 31?
-1.331
^ ^
20652 1. 000
3636. 500
1.000
-1.40fi
22. 000
-29. 100
-1.40CI
-1.32-::
-1.331
24.
206534. nnn
3634. 900
1 . 050
-I. 600
23.050
-.30. 700
-1.521
-i. 33:-
-I. 334
25.
206644. 000
3631. ?nn
1.000
-1.200
24. 050
-31. 900
-1.200
-1.326
-1. 333
206672. nnn
206760. nrin
3634. 000
n 24 Syx 0.529 ta/2 2.074
Slope- -1.336 Sx 7.067 r -1.000
Intercept -0.279 Sfl 0.016 Confidence Interval
Sb 0.179 1.336 + 0.033
S,. 0.480
vO
-------
TABLE A-1JJO SUMMARY OF DATA FROM TEST NO. 74
Page j of
Degreaser B, operating
Solvent: Methylene chloride
Date 4/15/79
FB 75 t
Inlet air x
Other
PC x SC
Exhaust air x
A 50 %
V 8 ft/min
AmblenFair
Temperature 70
Pressure 29.60 in. Hg
Humidity B2 t
Reading
No.
T, mln
W. Ib
AT, h
AW, Ib
EAT, h
CAW, Ib
(**} Ih/h
I TV I • O/n
VA'/t
(i^\ 1b/h
X, lb/h
205141.
3028. (.00
t
205154.
3028. (.00
205161.
3021. 300
1.
205201. 000
3022. 800
w. •
205265. 000
3020. 900
1.0671
-1.900
1.0671
-1.900
-1.781
-1.731
-1.731
3.
205324. 000
30 IS. 300
0. 933
-2. 100
2. 050
-4. 000
-2. 1 36
-1.951
-1.36*.
vD
-------
TABLE A-l30(continued)
Page 2_ of 5
Reading
No.
T. min
U. Ib
AT. h
AW, ib
EAT. h
EAU. Ib
(S). "">
(SO. """
X. Ib/h
4.
205382. 000
3017. 000
0. 967
-1.800
3.0 IT1
-5. 300
-1.8*2
-1.923
•-1.88S
5.
205440. 000
3015.500
0. 967
-1.500
3.98::
-7. 300
-1.55J1
-1.831:
-1 O~"«
1 . O 1 L.
6.
205505. 000
3012.600
1. 08::
-2. 900
5. 067
-10. 20fi
— «z. . t' i i
-2. OK:
-1.900
i .
205564. 000
3010. TOO
0. 93::
-1. 900
6. 050
-12. 100
-i. 93:-
-2. OOCi
-1.917
3.
205625. 000
3009. 000
1.017
-1.700
7. 067
-13.800
-1.67?
-1. 957:
-1.92:-
9.
205684. 000
3007. 000
0. 93::
-2. 000
8. 050
-15.800
-2. 031
-1.96::
-1.927
vO
00
(continued)
-------
TABLE A-130 (continued)
Page 3 of 5
Reading
No.
T. nln
U. 1b
AT. h
AW. 1b
EAT. h
EAU. Ib
GO. "">
(sr) 1b/h
X. 1b/h
10.
205745. 000
?nn5. nnn
1.017
-2. 000
9. 067
-17.800
-1.967
-1.96::
. -1.931
11.
205804. 000
3003. 000
0. 983
-2. 000
10.050
-19.300
-2. 034
-1.970
-1.935
12.
205364. OOfi
3001.200
1.000
-1.800
11.050
-21.600
-1.800
-1.955
-1.937
13.
205925. 000
2«a. 5fifi
1. 017
-1.700
12.067
-23. 300
-1.67?
-1.931
-1.93*
14.
205935. 000
2'5*7. 5flfi
1 . 000
-2. 000
1 3. 067
-25. 300
-2. 000
-1.936
-1.936
15.
206045. 000
ws *nn
1 . 000
-1. 600
14.067
-26. 900
-1.600
-1.912
-1. 935
vO
vD
(contfniied)
-------
TABLE A-130 (continued)
Page 4 of 5
Reading
No.
T, 01n
U, lb
AT, h
AW, lb
EAT, h
CAW, lb
GO. "">
(fir). 1b/h
X, Ib/h
16.
206104. 000
2994. 000
0. 983
-1.900
15.050
-28. 800
-1.93:-
-1.914
. -1.93::
17.
206164. 000
2991. 900
1.000
-2. 100
16.050
-30. 900
-2. 100
-1.925
-1.9-3::
18.
206217.000
299D. SOfi
0.88::
-1.400
16.93::
-32. 300
-1.535
-1. 907
-1. ?3J
19.
206236. 000
2933. 400
1. 150
-2. 100
13.08::
-34. 400
- 1 . 82*.
-1.9CC
-1.930
20.
2063-43. 000
2936. 400
1.03::
-2. 000
19. 117
-36. 400
-1.935
- 1 . 904
-1.92?:
21.
206401. 000
2984. 600
0. 83.::
-1.800
20. 000
-33.200
-3. 038
-1.910
-1.927
o
o
(continued)
-------
in
o
TABLE A-130 (continued)
Page 5 of 5
Reading
No.
T, mln
W. 1b
AT. h
AW. Ib
CAT. h
CAW. Ib
(fi). ™
(Sfl ™
X. Ib/h
00
k» h. •
206461. 000
2982. 600
1.000
-2. 000
21.000
-40. 200
-2. 000
-1.914
-1.927
:••>
i_ _' •
206521. 000
2980. 100
1.000
-2. 500
22. 000
-42. TOO
-2. 500
-1. 941
-1.927
24.
206584. 000
2973. SOn
1.050
-1.800
23.050
-44. 500
-1. 714
-1.931
-1.928
25.
2066J4. 000
2976. 100
1. 000
-2. 200
24. 050
-46. 700
-2. 200
-1.94:-
-1. 928
206672. 000
2975. 700
206845. 000
2977. 000
n 24
Sl-ope- -1.917
Intercept -0.145
syx 0.298
x 7.067
a
s- 0.009
sb 0.179
>,. 0.270
'a/2 2.074
r -1.000
Confidence Interval
1.917 + 0.019
-------
TABLE A-131 SUMMARY OF DATA FROM TEST NO. 75
Page 1 of 5
Degreaser A, operating
Solvent: Methylene chloride
Date 4/17,18/79
FB 75 %
Inlet air x
Other
PC x SC _
Exhaust air x
A
C
50 X
nTin
Ambient'air
Temperature 70 °f
Pressure 29.81 In. Hg
Humidity
Reading
No.
T, mln
H. Ib
AT, h
AW, Ib
TAT, h
CAW, Ib
(W\ rifi.'
1 TT I ID/H
\AI/t
(ffi) Ib/h
X, Ib/h
20723?. OOCi
3642. 700
207247. 000
3642. 000
207255. 000
•^•:ft. -Wi
1.
207270. 000
36 38. 900
2.
207331. 000
i
3637. 300
1. 017
-1. 600
1.017
-1.600
-1.574
-1.574
-1.574
3.
207391.000
3635. 600
1. 000
-1.700
2. 0 1 7
-3. 900
-1.700
-1.63*
-1.60=.
-------
TABLE A-131(continued)
2 of 5
Reading
No.
T. Bin
y. ID
AT. h
AU. 1b
CAT. h
£AU lh
GO. «*
(sft "•"•
X. Ib/h
4.
207451.000
363::. 800
1.0 00
-1.800
3.017
-5. 100
-1.800
-1.691
-1.634
5.
207511.000
3632.700
1.000
-1. 100
4.017'
-h. 2firi
-1. 100
-1.544
-1.611
6.
207571.000
3630. 900
1.000
-1. son
5. 017
-R. nnn
-1.800
-1.595
-1.608
i .
207631. 000
3629. 400
1. 000
-1. 500
6. 017
-o. "inn
-1.500
-1.579
-1. 60 ::
8.
207697. 000
3628. 000
1. 100
-1.400
7. 117
-in. *nn
-1. 27!:
-1.53C:
-1.59::
i
9.
207764. 000
3625. 700
1. 117
-2. 300
8.23::
- 1 ": *nn
-2. 060
-1.60::
-1.594
1/1
o
OJ
(continued)
-------
TABLE A-l31 (continued)
Page 3 of 5
Reading
No.
T. Bin
U, lb
AT. h
AU. lb
EAT. h
EAH. lb
GO. ««•
(fir) lb/h
X. lb/h
10.
207817.000
3624. 700
0. 38::
-I. 000
9. 117
-14.200
-1. 13C-
-1.558
-1.590
11.
207873. 000
3623.800
0. 93::
-0. 900
10.050
-15. 100
-0. 964
-1.502:
-1.581
12.
207938. 000
3620. 500
i.os::
" -3. 300
11. 13::
-18. 400
-3.046
-1.65::
-1.58?:
13.
207996. 000
3619. 500
0. 967
-1.000
12. 100
-19.400
-1.034
-l.bO::
-1.539
14.
203054. 000
3618.200
0. 967
-1.300
1 3. 067
-20. 700
-1. 345
-1.534
-1.589
15.
203113.000
3616.200
0. 98::
-2. 000
14.050
-22. 700
-2.034
-1.616
-1.591
(continued)
-------
TABLE A-131(continued)
Page a of
Reading
No.
T, 0in
U. Ib
AT. h
AH. Ib
CAT. h
CAU. Ib
(xft w
\AT/.
(itr) lb/h
X. lb/h
16.
208173.000
3614.700
1.03-::
-1.500
15. 13::
-24. 200
-1.335
-1.599
-1.591
17.
203237. 000
3613.000
0.93::
-1. 700
16. 117
-25. 900
-1.729
-1.607
-1.59?
13.
203296. 000
3611.400
0.9?::
-1.600
17. 100
-27. 500
-1.627
-1.603
-1.59::
19.
203354. 000
3610. 200
0. 967
- 1 . 200
13.067
-23. 700
-1.241
-1.539
-1. 59::
20.
9
203413. 000
3603. 300
0.93::
-1.400
19.050
-30. 100
-1.424
-1.530
- 1 . 59?
21.
203473. 000
3606. 700
1.000
-2. 100
20. 050
-32.200
-2. 100
-1.606
-1.59::
IP
o
(continued)
-------
TABLE A-131 (continued)
Page 5 of 5
Reading
No.
T. nln
U. 1b
AT. h
AM. 1b
CAT. h
CAW. 1b
(if). «•"•
X. Ib/h
-. ^
203532. 000
3605. 500
0. 983
-1.200
21.031:
-33.400
-1.220
-1.588
-1.593
23.
203593. 000
3 60 3. -500
1.01T1
-2. 000
22. 050
-35.400
-1.967
-1.605
-1.593
24.
.,n.:>.c;.1 nnf|
3602. 000
1 . 000
-1.500
23.050
-36. 900
-1.500
- 1 . 60 1
1 -1.594
25.
20371 3. 000
3600. 400
1. 000
- 1 . 600
24. 050
-38. 500
-1.600
-1.601
-1.594
2n:-:7'5R. nnn
3601. 500
CP
o
a*
n 24
Slope- -1.603
Intercept 0.102
'yx
0.312
7.076
0.009
0.179
0.453
2.074
r -l.OOU
Confidence Interval
1.603 + 0.019
-------
TABLE A-132 SUMMARY OF DATA FROM TEST NO. 75
Degreaser B. operating
Solvent: Methyl ene chloride
FB 75 % PC x SC x A 50 I
Inlet air x Exhaust air x V 8 ft/min
Other
Date 4/17/79
Ambient air
Temperature 70 '
Pressure 29.81 in.
Humidity 4] %
Page l of 5
Reading
No.
T, min
H, Ib
AT. h
AW. Ib
EAT. h
CAW. Ib
(£)>
(far). lb/h
X. lb/h
20723?. 000
3023. 400
207244. 000
302:?. 600
207251.000
3027. 400
1.
207270. 000
3027. 800
2,
207331. 000
3028. 300
1 . 0 1 T1
0. 500
1 . 0 1 7
0. 500
o. 4?;-
o. 4?;:
o. 49:-
3.
2073?!. 000
3026. 500
1.000
-1.800
2.017
-1.300
-1.800
-0. 645
-0. 07t.
in
o
-o
-------
TABLE A-l32 (continued)
Page ? of
Reading
No.
T. nln
U, Ib
AT. h
AW. Ib
CAT. h
EAU. Ib
(XT) ">/"
\Al/.
(lir) lb/h
-
X. 1b/h
4.
207451.000
3025. 300
1.000
-1.200
3.017
-2. 500
-1.200
-0. 829
-0. 327
5.
207511.000
3022. 600
1.000
-2. 700
4.017
-5. 200
-2. 700
-1.295
-0. 569
6.
207571.000
3021.300
1 . 000
-0. 800
5.0 IT1
-6. 000
-0. 800
-1. 19t-
-0. 694
1 •
207631.000
3020. 000
1.000
-1.800
6. 017
-7. 800
-1.800
-1.291-..
-0. 79C-
8.
207697. 000
3020. 400
1. 100
0. 400
7. 117
-7. 400
0. 364
-1.040
-0. 830
9.
207764. 000
3019.400
1 . 1 1 7
-1.000
8.23'.:
-3. 400
-0. 89t«
- 1 . 020
-0. 854
o
00
(continued)
-------
TABLE A-132 (continued)
Page 3 of _§_
Reading
No.
T. nln
U, Ib
AT. h
AW, Ib
CAT, h
HAW. Ib
GO. lb"
(Mr). ">"
X. Ib/h
10.
207817. 000
30 It.. 600
0.881:
-2. 300
9. 1 1 T1
-11.200
-3. 170
-1. 220
-o. 395
11.
207873. 000
3015. 100
0. 931:
-1. 500
10. 050
-12.700
-1.607
-1.264
-0. 93J1
12.
2079™. nnn
3015.700
1.081:
0. 600
11. 131:
-12. 100
0. 554
-1.037
-0. 94t.
13.
2079*K. nrifi
301 3. 900
0. 967
-1. 300
12. 100
-13.900
-1.36:-
-1. 149
-0. 961:
14.
2nan«i4. nnn
3011.700
0. 967
-2. 200
1 3. 067
-16. 100
-2. 27*.
-1.23J1
-0. 934
15.
^nftii^ nnn
3010.500
0. 93 ::
-1.200
14.050
-17.300
-1.220
-1.231
-l.OOJ
(continued)
-------
TABLE A-l32(continued)
Page & of 5
Reading
No.
T. win
U. Ib
AT. h
AU. Ib
EAT. h
EAU. Ib
(*\ lh/h
lirJ io/n
\AV.
AAU\ |b/||
\isr).
X. lb/h
16.
203173.000
3011.000
1.03::
0. 500
15. 130
-16.800
o. 46::
-1. 110
-1.00?
17.
203237. 000
3009. 100
o. 93;:
-1. 900
16. 117
-13.700
-1.93::
-1. 160
-1.01?:
18.
208296. 000
3007. 000
0.98::
m
-2. 100
17. 100
-20. 300
-2. 136-
-1.21t.
- 1 . 030
19.
203354.000
3005. 000
0. 967
-2. 000
18.067
-22. 300
-2. 069
-1.26::
-1.04 ::
20.
20841 3. 000
3003.700
0. 93:-:
-1.300
19.050
-24. 100
-1.32;-
-1.265
-1.054
21.
208473. 000
3004. 100
1.000
0. 400
20. 050
-23. 700
0. 400
-1. 13J:
-1.061
(continued)
-------
TABLE A-132 (continued)
Pagis 5 of 5
Reading
No.
T. mln
W, 1b
AT. h
AM, Ib
CAT. h
CAU. Ib
(1?). ">"
(zir). lb/h
X. lb/h
22.
208532.000
3002. 000
0. 98':
-2. 100
21.03::
-25. ann
-2. 13^-
-1.227
-1.069
i
23.
208593. 000
2999. 500
1.017
-2. 500
22. 050
-'ft ?nn
-2. 459
-1.28:::
-1.07?:
24.
208653. 000
2998. 500
1 . 000
-1.000
23. 050
_,q .^nf|
-1.000
-1.271
-1.087
25.
208713.000
2997. 300
1 . 000
-1. 200
24. 050
-30. 500
-1.200
-1.26:;:
-1.094
208931. 000
2997. 000
n 24
Slope -1.299
Intercept 1.233
Syx 0.835
Sw 7.076
S.. 0.025
a
Sb 0.179
S 1.083
a/2
r -1.000 •
Confidence Interval
1.299 + 0.052
-------
TABLEA-l33 SUMMARY OF DATA FROM TEST NO. 76
Page _i_ of
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling y_; nonboiling )
FB 75 I PC x SC
Inlet air x
Date 4/25/79
ixhaust air
A Q %
V 0 Ft/min
Ambient'air '
Temperature 72
Other Lip exhaust at 50 ft3/min per ft2 top opening
Pressure 29.4 in. Hg
Humidity
Reading
No.
T, mln
W, Ib
AT. h
AW. Ib
EAT. h
EAW, Ib
(S). '*»
(^lf) 1b/h
X. Ib/h
2139?6.0oo
3783. loo
218958.000
3736. :-oo
1.
218966. 000
3780. 500
•:•
h- •
220090. 000
374?. 400
18.73::
-31. 100
13.73::
-31. 100
-1.660
-1. 660
-1. 660
220142. 000
3750. 300
N)
-------
TABLE JUU4 SUMMARY OF DATA FROM TEST NO. 76
Page
of
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling x ; nonboiling )
FB 75 % PC x SC _
Inlet air x Exhaust air x
Other
A Q %
V 0 ft/mln
Date 4/25.26/79
Ambient'air
Temperature 72 *F
Pressure 29.4 jn. Hg
Humidity 66. %
Reading
No.
T, m1n
H, 1b
AT. h
AW, 1b
EAT, h
JAW. Ib
(M\ 1h/h
I TT 1 'ofn- •
\AI/,
(Sr) lb/h
X, lb/h
218936. 000
2954. 200
218954. 000
295::. 600
1.
218963.000
2952. 000
2.
220090. 000
2927. 800
18. 78::
-24. 200
18. 73::
-24. 200
-1. 28?:
-1.23:]:
-1. 23?:
220297. 000
2328. 500
U)
-------
TABLE A-135 SUMMARY OF DATA FROM TEST NO. 77
Page 1 of 1
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling x ; nonboiling )
PC
SC
FB 75. * __
Inlet air x Exhaust air x V
0thCr Lip exhaust at 100 ft3/min per ft2 top opening
A 0 %
0 ft/min
Date 4/26/79
Ambient'air '
Temperature - °F
Pressure Z9.10 in. Hg
Humidity 55t
Reading
No.
T, mln
W. Ib
1
AT. h
AW. Ib
EAT. h
CAW. Ib
(S). ">'"
(far). lb/h
x, lb/h
220347. 000
3747. 000
220378. 000
3746. 500
1.
220389. 000
3742. 100
2.
221529.000
3701.300
19.000
-40. 800
19.000
-40. 800
-2. 147
-2. 147
-2. 147
221606. 000
3701.900
-------
TABLE A-J36 SUMMARY OF DATA FROM TEST NO. 77
Page J of J
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling _x ; nonboiling
FB 75 % PC x SC
.Inlet air x Exhaust air _
Other
Crosscurrent test
A 0 %
V 0 ft/min
Date 4/26/79
Ambient'air
Temperature CF
Pressure 29.10 in. Hg
Humidity 65 *
Reading
No.
T, min
H. lb
AT, h
AW, lb
EAT, h
EAM, lb
(ir). lb/h
(Sf). ">"
X, lb/h
220347. 000
2926. 500
220376. 000
2926. 200
1.
220331.000
2924. 500
2.
221529.000
2330.300
19. 13'J
-94. 200
19. 13;:
-94. 200
-4. 92-::
-4.92::
-4.92::
221735.000
2830. 000
IT
»->
l/l
-------
TABLE A-137 SUMMARY OF DATA FROM TEST NO. 78a
Page 1 of 1
Degreaser A, Idle .
Solvent: Methylene chloride
(Boiling ; nonboiling _g )
FB X PC x SC
Inlet air Exhaust air
Other
Date 5/8/79
min
Lid closed; inlet air was turned on about 3 hours after test started
Ambient air
Temperature 77 °F
Pressure 29.50 in. Hg
Humidity 59 I
Reading
No.
T, min
H. Ib
AT, h
AW, Ib
EAT. h
CAM. Ib
(S). «"•
(LOW 1 f L 1 ft.
TTT-J lO/n
X. 1b/h
1.
237417.000
3607. 100
2.
23S694. 000
3602. 400
21.283
4. 700
21.283
4. 700
,0.221
0.22!
0. 221
-------
TABLE A-138 SUMMARY OF DATA FROM TEST NO. 78a
Page ] of
Degreaser B.'ldle .
Solvent: Methylene chloride
(Boiling ; nonboiling _x )
FB I PC x SC
Inlet air Exhaust air
Other
lid closed
A Q %
V n ft/min
Date 5/8/79
Ambient air*
Temperature 77 °F
Pressure 29.50 in. Hg
Humidity 59 %
Reading
No.
T. mln
W. lb
AT. h
AW, lb
EAT, h
CAW. lb
(S). ">'"
(fir). 1b'h
X. Ib/h
1.
237417.000
2647. 100
2.
238694.000
2642. 000
21.283
5. 100
21.2S3
5. 100
0. 240
0. 240
0. 240
Ul
-------
TABLE A-139 SUMMARY OF DATA FROM TEST NO. 78b
Page
of
Degreaser A, Idle .
Solvent: Methylene chloride
(Boiling ; nonboiling _x )
FB _50__X PC x SC
Exhaus
Inlet air
Other
wust air
l_ ft/mil
mln
Lid closed
Date 5/9/79
Ambient aif
Temperature 60
Pressure 29.5U in. hg
Humidity 75 I
Reading
No.
T( mln
W, lb
AT, h
AW, lb
IAT, h
EAW, lb
(S). """
(lj*\ lb/h
X, 1b/h
1.
238736.000
3602. 400
h_ •
24013S. 000
3Ti?8. 300
23. 367
3. 600
23.367
3.600
0. 154
0. 154
0. 154
00
-------
TABLE A-l40 SUMMARY OF DATA FROM TEST NO. 78b
Page 1 of _]_
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling _x )
FB 50 % PC _^^ SC _
Inlet air Exhaust air
Other Lid closed
V 0 ft/m
0 I
fnin
Date 5/9/79
Ambient air
Temperature 60
Pressure 29.50 in. Hg
Humidity ~~~
Reading
No.
T, min
H. lb
AT. h
AM, lb
EAT, h
EAW. lb
(S). ">'"
(m\ lb/h
X, lb/h
i .
238736.000
Pf4^ |"|j"l
2401 38. 000
?H T.,: ! p.'.
T-.9X,
23. 367
?. ?•?:'
0. 252
u- ^5?
<.'. :-s.'
vD
-------
TABLE A-141 SUMMARY OF DATA FROM TEST NO. 79
Page j of
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling ; nonboiling x_)
FB 125 I PC x SC
Inlet air x txhaust air x"
Other
A 0
V 0 ft/m
X
nfin
Date 5/10/79
Ambient a*ir
Temperature 70 °F
Pressure 29.5U in. Hg
Humidity 75 1
Reading
No.
T, mln
W, 1b
AT, h
AW, lb
EAT, h
CAW, lb
(AW\ 1b/h
1 TT 1 * Vf"
\fll/l
(IAT). lb/h
X. Ib/h
1.
240377. nilfi
3615. 600
kv •
24 1 537. nnn
3605. 500
20. 167
10. 100
20. 167
10. 100
0. 501
0.501
0. 50 L
J5
o
-------
TABLE A-142 SUMMARY OF DATA FROM TEST NO. 79
Page T of 1
Degreaser B, Idle.
Solvent: Methylene chloride
(Boiling ; nonboiling x )
FB I PC x SC _
Inlet air x_ Exhaust air x
Other
V 0 ft/m
Date 5/10/79
Ambient air
Temperature 22 °F
Pressure 29.50 in. Mg
Humidity "75~Ti
Reading
No.
T, mln
H, Ib
AT, h
AW, Ib
EAT, h
CAW. Ib
(AT) lb/h
(EAW\ lb/h
VIST/,
X. lb/h
K
24n3?r. nnn
2R1 1. ftnn
2.
241537. 000
2am. nnn
20. 167
3. 600
20. 167
3. 600
0. 426
0. 426
0. 426
Ol
Is)
-------
TABLE A-143 SUMMARY OF DATA FROM TEST NO. 80
Page \ of J
Degreaser A, Idle
Solvent: Hethylene chloride
(Boiling ; nonboiling x )
n inn * PC x SC
Inlet air x Exhaust air
Other
ft/mil
min
Date 5/11/79
Ambient air
Temperature 70 »F
Pressure 29.46 In. Hg
Humidity
Reading
No.
T, min
W, 1b
AT. h
AW, Ib
EAT. h
EAW. Ib
(S). '""
(if), -w
X. 1b/h
Z4167Z. OOCl
3517.800
245910.000
3486. 300
70. 633
31.500
70. 63?
31. 500
0. 446
0. 4 •:*
0. 440
•
K>
-------
TABLE AjJ44 SUMMARY OF DATA FROM TEST NO. 80_
Page 1 of 1
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling j ; nonboiling _x )
n 100 t PC x sc _
Inlet air x Exhaust air x
Other
V 0
a *
ft/mil
min
Date 5/11/79
Ambient air
Temperature 70 *F
Pressure 29.46 in. Kg
Humidity 70 1
Reading
No.
T, min
H. Ib
AT. h
AW. Ib
TAT. h
CAN. Ib
(&} Ik/h
1 TT 1 • vfn
\AT/,
(^f) Ib/h
X. lb/h
241672.000
2729. 800
24=i?i 0. rinn
2703. 7'00
70. ^.33
26. 300
70.633
26. 300
0. 372
0.372
0. 372
Ul
-------
TABLE A-145 SUMMARY OF DATA FROM TEST NO. 81
Page i of
Degreaser A, Idle
Solvent: Wethylene chloride
(Boiling ; nonbolllng _x )
FB 75 * PC x SC
Inlet air x Exhaust air
Other Lid closed
tt/mli
mln
Date 5/14/79
Ambient'air
Temperature 69 °F
Pressure 29.6b In. Mg
Humidity 53 *
Reading
No.
T, mln
V. 1b
AT, h
AW. 1b
CAT, h
raw, ib
($). ™
(M?). iw
X. Ib/h
1.
246040. 000
3643. 100
2.
247360. 000
3637. 700
22. 000
-5. 400
22. 000
-5. 400
-0. 24?!
-0. 24!!
-0. 24?:
Ut
K>
-------
TABLE A-146 SUMMARY OF DATA FROM TEST NO. 81
Page j__of
Oegreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonbolling _x )
n 75 t PC x sc _
Inlet air x Exhaust air x
Other
Lid closed
V 0
Date 5/14/79
Ambient air '
Temperature 69 °F
Pressure 29.bb'in. Hg
Humidity 53t
Reading
No.
T, m1n
W, 1b
AT. h
AW, 1b
EAT, h
EAN, 1b
(&} ih/h
V TT 1 1 Of"
\Al/.
(I*) ib/h
X, 1b/h
1.
246040. 000
2661.900
2.
247360. 000
2653. 900
22. 000
-8. 000
22. 000
-3. 000
-0. 364
-0. 364
-0. 364
tfl
to
t/1
-------
TABLE A-147 SUMMARY OF DATA FROM TEST NO. 82
of
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling ; nonbolllng _x_)
n 75 *
Inlet air _,
Other
PC * SC
Exhaust air
Date 5/15/79
Ambient'air '
Temperature 22 *f
Pressure 29.74 in. Hg
Humidity sj I
Reading
No.
T, mln
N, Ib
AT, h
AW, Ib
EAT, h
EAW. Ib
(ar) 1b/h
(EAW\ 1b/h
VIST/,
X. Ib/h
247608. 000
3636. 700
248772. 000
3623. 1 00
19.400
8.600
19. 400
8.600
0.443
0.443
0. 443
•
N)
-------
TABLE /^US SUMMARY OF DATA FROM TEST NO. 82
Page IA of i
Degreaser B, Idle
Solvent: Methylene chloride
(Boiling ; nonbolllng _x )
FB 75 t PC x SC
Inlet air x Exhaust air
Other
V 0
ft/mil
ml n
Date 5/15/79
Ambient 'air *
Temperature 73 *F
Pressure 29.74 in. Hg
Humidity ""
Reading
No.
T, nln
N. 1b
AT, h
AW. 1b
EAT. h
CAM, 1b
(S). '«
(SQL ««
X. Ib/h
24760S. 000
2650. 100
248772. nnn
2642. tOO
19.400
7. 500
1?. 400
7. 500
0. 387
0.387
0. 387
M
-------
TABLE A-149 SUMMARY OF DATA FROM TEST NO. 83
Page 1 of 1
Degreaser A, Idle
Solvent: Methylene chloride
(Boiling ; nonbolling x )
n 75 * PC x
Inlet air x Exhaust air
Other
SC
A _n I
V _o_?t/min
Date 5/16/79
Ambient'air "
Temperature 72 BF
Pressure 29.95 in. Hg
Humidity 43~
Reading
No.
T, win
N. 1b
AT. h
AW. 1b
ZAT, h
raw, ib
(.y I • Wf W
(EAWN 1b/f|
VIST/,
X, Ib/h
1.
248831.000
3627. 600
2.
250207. 000
3614.700
22. 93G:
-12.900
22. 93?
-12.900
-0. 563
-0. 56':
-0. 56::
01
ro
o>
-------
TABLE. j\-150 SUMMARY OF DATA FROM TEST NO. 83
Page 1 of
Degreaser B, Idle.
Solvent: Methylene chloride
(Boiling ; nonbolllng _x )
FB 75 t PC x__ SC x
Inlet air x Exhaust air x"
Other
A Q %
V o ft/m1n
Date 5/16/79
Amblent'air'
Temperature 72 *F
Pressure 29.95 in. Hg
Humidity "43~t
Reading
No.
T, mln
W, Ib
AT, h
AW. Ib
IATV h
IAW, Ib
(5). «"•
("*) Ib/h
X, Ib/h
1.
243831.000
2644. 700
2.
250207. 000
2630. 200
22. 93C:
-14.500
22. 933
-14.500
-0. 631:
-0. 632
-0. 63S:
VI
M
(O
-------
TABLE A-151 SUMMARY OF DATA FROM TEST NO. 84
Page i of 5
Degreaser A, 'operating
Solvent: Methylene chloride
Date 5/22,23/79
FB 75 X
Intel' air
PC x SC
Exhaust air
A
8
50 %
Tin In
Other Degreaser A run at 18 kW instead of 24 kW
Ambient air
Temperature 72 _*F
Pressure 29.b6 in. Hg
Humidity 53 1
Reading
No.
T, m1n
W. 1b
AT, h
flW, lb
TAT, h
CAM, lb
(ft «"•
(M?). i".
X, Ib/h
257586. 000
3571.200
257593. OOd
3570. 600
257597. 000
3571.000
1.
257627. 000
3567. 000
2.
257694. 000
3565. 000
1. 117
-2. 000
1. 117
-2. 000
-1.791
-1.791
-1. 791
3.
257752. 000
3563. 000
0. 967
-2. 000
2. 083
-4. 000
-2. 069
-1.920
-1.85*
U1
W
o
-------
TABLE A-l51 (continued)
2 of 5
Reading
No.
T. m\n
U. lb
AT. h
AN. lb
IAT. h
£AU. lb
(£). "•«
Car). lb/h
X. 1b/h
4.
257808. 000
3559. 400
0. 933
-3. 600
3.017
-7. 600
-3. 857
-2.519
• -2. 077
5.
257866. 000
3558. 800
0. 967
-0. 600
3. 98C:
-8. 200
-0.621
-2. 059
-2. 072:
6.
257930. 000
3556. 100
1.067
-2. 700
5. 050
-10.900
-2.531
-2. 15?:
-2. 089
i .
257988. 000
3554. 400
0. 967
-1.700
6.017
-12.600
-1.759
-2. Q9<-
-2. 090
8.
258057. 000
3551. 100
1. 150
-3. 300
7. 167
-15.900
-2. 870
-2.219
-2. 109
9.
258107.000
3549. 100
0. 833
-2. 000
8. 000
-17.900
-2. 400
-2. 23S
-2. 125
Ifl
(continued)
-------
TABLE A-l51 (continued)
Page 3 of 5
u>
Reading
No.
T. «fn
U. 1b
AT, h
AM. 1b
EAT, h
CAM. 1b
1 771 ib/h
\ul/.
Xr»|j\
I. Ib/h
lu.
258170.000
3548. 200
1.050
-0. 900
9. 050
-18.800
-Oi 857
-2. 077
. -2. 119
11.
258228. 000
3546. 800
0. 967
-1.400
10.017
-20. 200
-1.44?:
-2.017
-2. 109
12.
258287. 000
3542. 600
0. 983
-4. 200
11.000
-24. 400
-4.271
-2.21?:
-2. 119
13.
258343. 000
3540. 600
0. 933
-2. 000
11.933
-26. 400
-2. 143
-2.215:
-2. 127
14.
258412.000
3539. 000
1. 150
-1.600
1 3. 083
-28. 000
-1.391
-2. 140
-2. 12?:
15.
258468. 000
3336. 700
0. 933
-2. 300
14.017
-30. 300
-2. 464
-2. 162:
-2. 130
(continued)
-------
TABLE A-151 (continued)
Page 4 of
Reading
No.
T, Bin
U. Ib
AT. n
AH. Ib
CAT, h
CAV. Ib
(ir). lb'h
(isr). lb/h
X. lb/h
16.
258528. 000
3534. 500
1.000
-2. 200
15.017
-32. 500
-2. 200
-2. 164
-2. 133
17.
258585. 000
3532. 900
0. 950
-1.600
15.967
-34. 100
-1.68^
-2. 136
-2. 133
18.
258646. 000
3531.300
1.017
-1.600
16.98C:
-35. 700
-1.574
-2. 102
-2. 13J
19.
258705. 000
3529. 100
0. 98^:
-2. 200
17.967
-37. 900
-2. 237
-2. 109
-2. 130
20.
258773. 000
3526. 600
1. 13?
-2. 500
19. 100
-40. 400
-2. 206
-2. 115
-2. 129
21.
258831. 000
3524. 500
0. 967
-2. 100
20. 067
-42. 500
-2. 172:
-2. 11?:
-2. 12?:
Ut
U)
u>
(continued)
-------
TABLE JU151 (continued)
Page 5 of 5
Reading
No.
T. win
U. 1b
AT. h
AM. 1b
£AT. h
raw, ib
(S) ™
\AI/«
(ifr). lb/h
X, 1b/h
22.
258889. 000
3523. 400
0. 967
-1. 100
21.033
-43. 600
-1. 13S:
-2. 073
-2. 12*.
23.
258998. 000
3520. 800
1.817
-2. 600
22. 850
-46. 200
-1.431
-2. 025:
-2. 12J
24.
259007. 000
3517.900
0. 150
-2. 900
23. 000
-49. 100
-19.333
-2. 13?:
-2. 122:
25.
259070. 000
3516. 500
1.050
-1.400
24. 050
-50. 500
-1.333
-2. 100
-2. 121
259099. 000
3515.700
259131.000
3517.500
•
in
CJ
n 24
Slope. -2.085
Intercept -0.460
Syx 0.763
Sx 7'110
S. 0.022
O
Sk 0.177
2.074
r -1.000
Confidence Interval
2.085 + 0.046
3.631
-------
TABLE A-152SUMMARY OF DATA FROM TEST NO. 84
Page 1 of 5
Degreaser B, operating
Solvent: Methylene chloride
PC
Date 5/22/79
FB 75 I
Inlet air x_
Other
x SC
xhaust air x
A_50 I
V 8 ft/min
Ambient'air
Temperature 72 *F
Pressure 29.66 in. Hg
Humidity b3 I
Reading
No.
T. m1n
M, 1b
AT. h
AW. 1b
CAT. h
CAW. 1b
(??). "*"
(fsr). 1b/h
X. 1b/h
257586.
3063. ZOo
257589.
3063. 2:oo
257595.
3060. 40o
1.
257627. 000
™«i«. -:f.f.
2.
257694. 000
3057. 900
1. 117
-1.400
1. 117
-1.400
-1.254
-1.251
-1.251
3.
257752. 000
snss. *nn
0.967
-2. 000
2.083
-3. 400
-2. 06$
-1.632
-1.443
(II
w
in
-------
TABLE A-152 (continued)
Page 2 of 5
Reading
No.
T. nin
U. 1b
AT. h
AM. 1b
CAT. h
CAM. 1b
(ir). 1b/h
VWA
X. Ib/h
4.
257808. 000
3053. 000
0.933
-2. 900
3.017
-6. 300
-3. 107
-2. 08?:
. -1.65?:
5.
257866. 000
3051.000
0. 967
-2. 000
3. 983
-8. 300
-2. 069
-2. 084
-1.76-1
6.
257930. 000
3048. 900
1.067
-2. 100
5. 050
-10.400
-1.969
-2. 059
-1.823
7.
2579S3. 000
3047. 900
0. 967
-1.000
6.017
-11.400
-1.034
-1.895
-1.835
8.
258057. 000
3044. 800
1. 150
-3. 100
7. 167
-14.500
-2. 696
-2. 023
-1.862
9.
258107.000
3042. 300
0.833
-2. 500
8. 000
-17.000
-3. 000
-2. 125
-1.895
(continued)
-------
TABLE A-1b2 (continued)
Page 3 of 5
Reading
No.
I. »1n
U. 1b
AT, h
AU, 1b
CAT, h
CAU, Ib
GO. ""*
(Sft ">"•
X. Ib/h
10.
258170.000
._ .3042.900
1.050
0. 600
9. 050
-16.400
0. 57 J
-1.81J:
-1.836
11.
253223. 000
...3039.000.
0. 967
-3. 900
10.017
-20. 300
-4. 034
-2. 027
-1.900
12.
253237. 000
._3035. 700
0.983
-3. 300
11.000
-23. 600
-3. 356
-2. 145
-1.92:-
13.
258343. 000
3034. 500
0.933
-1.200
11.933
-24. 800
-1.286
-2. 07?:
-1.935
14.
258412.000
3031.900.
1. 150
-2. 600
13.083
-27. 400
-2.261
-2. 094.
-1.947
15.
258469. 000
3029. 100 .
0.933
-2. 800
14.017
-30. 200
-3. 000
-2. 155
-1.962:
01
w
(continued)
-------
TABLE A-152 (continued)
Page & of
Reading
No.
T. m\n
M. 1b
AT. h
AM, 1b
CAT. h
CAM, 1b
(If). ""*
/fAy\
(IZT) lb/h
j
X. lb/h
16.
258528. 000
3028. 200
1.000
-0. 900
15.017
-31. 100
-0. 900
-2. 07]
-1.970
17.
258585. 000
3026. 100
0. 950
-2. 100
15.967
-33. 200
-2. 211
-2. 079
-1.976
18.
258646. 000
3023. 700
1.017
-2. 400
16.983
-35. 600
-2.361
-2. 096
-1.983
19.
253705. 000
3022. 300
0.983
-1.400
17.967
-37. 000
-1.424
-2. 059
-1.93S
20.
258773. 000
3019.800
1. 133
-2. 500
19. 100
-39. 500
-2. 206
-2. 06?:
-1.992:
21.
.258831.000
...3017.300
0. 967
-2. 500
20. 067
-42. 000
-2. 586
-2. 093
-1.997
in
(continued)
-------
TABLE .A-152 (continued)
Page 5 of 5
Reading
No.
T, mln
W. 1b
AT. h
AW. 1b
CAT. N
CAW. 1b
Of). ""h
(fir). 1b'h
X. 1b/h
22.
258889. 000
3015.300
0. 967
-2. 000
21.033
-44. 000
-2. 069
-2. 092:
-2.001
23.
258948. 000
3013.500
0. 983
-1.800
22.017
-45. 800
-1.83J
-2. 080
-2. 005
24.
259007. 000
3011.200
0. 983
-2. 300
23. 000
-48. 100
-2. 339
-2.091
-2. 009
25.
259070. 000
3009. 100
1.050
-2. 10d
24. 050
-50. 20d
-2. 000
-2. 087
-2.012:
259099. 000
3008. 100
259152.000
3009. 900
n 24 Syx 0.649 *a/2 2-074
Slope- -2.119 *„ 7.059 r -1.000
Intercept 0.642 S. 0.019 Confidence Interval
d
Sb 0.179 2.119 + 0.039
Sr 0.941
c
I/I
u>.
\D
-------
TABLE A-l 53 SUMMARY OF DATA FROM TEST NO. 85
Page _]_ef . 1
Degreaser A, operating
Solvent: Methylene chloride
PC x
Date 5/23/79
FB 75X
Inlet air
Other
SC
Exhaust air
^HW
Test stopped early
fl 50 t
V 8 ft/milt
Ambient air
Temperature *F
Pressure In. Hg
Humidity I
Reading
No.
T, mln
W. 1b
AT. h
AW. 1b
EAT. h
EAW. 1b
(M\ ,b/h
1 TT j tafn
VAT/,
(m) 1b/h
X, 1b/h
259.173.000
3317.200
259186.000
3517.000
259193.000
3513. 100
1.
259247. OOU
3513. 30fi
2.
259309. 000
3511.200
1.033
-2. 100
1.033
-2. 100
-2. 032
-2. 032.
-2. 032
3.
259331.000
3510. 100
0.36?
-1. 100
1. 40f.
-3. 200
-3. 000
-2. 286
-2. 159
VI
Jt*
o
-------
TABLE _A-154SUMMARY OF DATA FROM TEST NO. 35
1 of
Degreaser B, operating
Solvent: 1,1,1-THcMoroethane
Date 5/23/79
n 75 *
Inlel air
Other
PC y SC
txhaust air
Rn *
ft/mi
mln
Ambient 'air
Temperature 71 °F
Pressure 29.43 in. Hg
Humidity "~
Reading
No.
T, mln
N. 1b
AT, h
AV, 1b
CAT, h
CAN, 1b
(Atl\
OW 1 11. /k
IT I i Of ••
01/9
X, Ib/h
259.178.. OOi !
3009. 700.
259183.000
3009. 500
:259189. 00"
3007. 500
1.
259247.00H
3006. 700
2.
259309. 00"
3005. 100
1.033
-1.600
1.033
-1.600
-1.540
-1.540
-1.540
3.
259331.0011
3004. 500
0.367
-0. 600
1.400
-2. 200
-1.636
-1.571
-1.56"
-------
TABLE A-l55SUMMARY OF DATA FROM TEST NO. 86
1 0* 5
Degreascr A, operating
Solvent: 1,1,1-THchloroethane
Date 5/23/79
FB 75 %
Inlet air
Other
PC x SC _
x Exhaust air x
A 50
V 8 ft>nr
Ambient air
Temperature 72 °F
Pressure 29.36 in. Hg
Humidity """'
Reading
No.
t, into
V. 1b
At. h
Atf, It?
EAT» ft
CAW. 1b
(«?)» lb'*
(ir). 1b'h
X. 1b/h
239413._000
3513.600
259417.000
3511*500
259*22. OUtf
3509. 160
1.
259469. OOP
3509. 500
2.
259537e_000
3509. 600 '
i< 133
9s iQt!
h i3l3
0. 100
0.088
0.038
0.038
3.
25?597.< QQC,
3507. 100
1.600
-2- SOC!
1.139
-2. 400
-2. 500
M.12S
-0.518
is)
-------
TABLE A-155 (continued)
Page 2 of 5
u>
Reading
Mo.
T. Bin
K. Ib
AT. h
AU. Ib
EAT. h
IAU. Ib
(AW) 1b/h
AA«\ |b/||
ysr/i
X. 1b/h
4.
259655. 000
3503. 000
0. 967
-4. 100
3. 100
-6. 500
-4.241
-2. 097
-1.045
5.
259727. 000
3499. 500
1.200
-3. 500
4. 300
-10.000
-2.917
-2. 326
-1.365
6.
259787. 000
3497. 000
1.000
-2. 500
5. 300
-12.500
-2. 500
-2. 358
-1.561
7.
259846. 000
?495. 100
0. 98C:
-1.900
6.283
-14.400
-1.932
-2. 292
-1.685
8.
259906. 000
3493. 000
1.000
-2. 100
7.283
-16.500
-2. 100
-2. 265
-1.76?:
9.
259968. 000
3491.500
1.033
-1.500
8.317
-18.000
-1.45a
-2. 164
-1.817
(continued)
-------
TABlt A-155 (continued)
Page 4 of 5_
in
Reading
No.
T. *1n
U. 1b
AT. h
av. 1b
CAT, h
IAW, 1b
IS). •»
(8ft ™
X. Ib/h
10.
260026. 000
3489. 70Ci:i
0. 96?
-1.30CI
9.283
-19.800
-1.862:
-2. 133
-1.85::
11.
;260148.000
3484. 800
2.033
-4. 900
11. 31?
-24. 700
-2.410
-2. 183
-1.885
12.
260212.000
34S3. 300
1.067'
-1.500
12.333
-26. 200
-1.406
-2. 116
-1.906
13.
260278. 000
3481.400.
l.lOOi
-1.900
13.480
-28. 100
-1.727
-2. 08<-
-1.92J
14.
260336. 000
3479. 000
0. 967
-2. 400
14.450
-30. 500
-2. 48C:
-2. Ill
-1.936
15.
260388. 000
=3477. 600
0. 867
-1.400
15.317
-31.900
-1.615
-2. 083
-1.946
(continued)
-------
TABLE A-155 (continued)
Page 3 of 5
Reading
No.
T. «in
Hv Ib
AT. h
AM. Ib
•**V k
CAT, h
CAM. Ib
(ir). 1b'h
(Mr1), "/"
X. Ib/h
i*.
260459. 000
3475. 000
..UK
-2. 600
16.500
-34. 300
-2. 19?
-2. 091
-1.93*.
17.
260511.000
3473. 600
0. 867
-1.400
17.367
-35. 900
-1.615
-2. 067
-1.96C:
18.
260570. 000
3471.200
0. 983
-2. 400
18.350
-33. 300
-2.441
-2. 087
-1.970
19.
260623. 000
3469. 700
0. 967
-1.500
19.317
-39. 800
-1.552:
-2. 060
-1.975
20.
260666. 000
3467.700.
0.633
-2. 000
19.950
-41.800
-3. 133
-2. 095
-1.982
260698. 000
3467. 800
(continued)
-------
TABLE A-155 (continued)
Page _ _5 of 5
Reading
No.
T, ariii
U. Ib
AT. n
AM. Ib
CAT. n
CAM. Ib
(& '""•
X. tb/h
•
260782. 000
3469. 000
n 19 S 1.046 tQ/2 2.110
Slope -2.104 S^ 6.120 r -1.000
Intercept 0.041 S_ 0.040 Confidence Interval
a
S. 0.226 2.104 + 0.084
D —
Sc 0.874
-------
TABLE A-156 SUMMARY OF DATA FROM TEST NO. 86
Page
Of 5
Degreaser B. operating
Solvent: 1.1 ,1-THchloroethane
Date 5/23,24/79
n 75
Inlet air
Other
PC x SC _ x
Exhaust air x
A 50
_
min
Ambient'air
Temperature 72 *F
Pressure 29.36 in. Hg
Humidity "55I
Reading
No.
T, win
W, 1b
AT. h
AW. 1b
CAT, h
EAV. 1b
(Atf\
°W 1 Ik/fc
TT 1 ' Of n
fti/.
(IST). 1b'h
X, 1b/h
259415.000
3006. 000
259426. 000
3002. 600
1.
259469. 000
3003. 600.1
2.
259537. 000
3001.400
1. 133
-2. 200
1. 133
-2. 200
-1.941
-1.941
-1.941
3.
259597. 000
3001. 100
1.000
-0. 300
2. 133
-2. 500
-0. 300
-1. 172:
-1.557
4.
259655. 000
2999. 200
0. 967
-1.900
3. 100
-4. 400
-1.966
-1.419
-1.511
-------
TABLE A-156 (continued)
Page
of
Reading
No.
T, >1n
U. Ib
AT. h
AM, Ib
IAT. h
EAM. Ib
(S). ""*
GST). ib/h
I. Ib/h
5.
1259727. 000
2996. 500
1.200
-2. 700
4. 300
-7. 100
-2. 250
-1.651
• -1.5415,
1
6.
259787. 000
2996. 000
1.000
-0. 500
5. 300
-7. 600
-0. 500
-1.434
-1.524 ;
7.
259846. 000
2994. 500
0.983
-1.500
6.283
-9. 100
-1.525
-1.448
-1.511
8.
259906. 000
2993. 300
1.000
-1.200
7. 283
-10.300
-1.200
-1.414
-1.497
9.
259968. 000
2992. 000
1.033
-1.300
8.317
-11.600
-1.250
-1.395
-1.484.
10.
260026. 000
2990. 700
0. 967
-1.300
9.283
-12.900
-1.345
-1.390
-1.474
o>
(continued)
-------
TABLE A-156(continued)
Page 3 of 5
Reading
No.
T. n1n
M. 1b
AT. b
AM. Ib
CAT. h
CAM. Ib
/AU\
I— I ib/b
\AV,
COT). lb/tl
I, Ib/b
11.
260087. 000
2989. 200
1.017
-1.500
10.300
-14.400
-1.475
-1.39?:
-1.466
12.
260148.000
2988. 500
1.017
-0. 700
11.317
-15. 100
-0. 689
-1.33^
-1.454
13.
260212.000
2987. 300
1.067
-1.200
12.383
-16.300
-1. 125
-1.316
-1.443
14.
260278. 000
2986. 900
1. 100
-0. 400
13.483
-16.700
-0. 364
-1.239
-1.427
15.
260336. 000
2985. 800
0.967
-1. 100
14.450
-17.800
-1. 13?:
-1.232:
-1.413
16.
260388. 000
2984. 000
0.867
-1.800
15.317
-19.600
-2. 077
-1.280
-1.404
(continued)
-------
TABLE A-156 (continued)
.4 of 5
Reading
No.
T. Bin
M. 1b
AT. h
AM. 1b
CAT. h
CAM. 1b
(SO. •*
GST). lb/h
I. 1b/h
17.
._260439. 000
.2982.800
1. 18C:
-1.200
16.500
-20. 800
-1.01*
-1.261
-1.395
18.
260511.000.
2981.700;
0. 867
-1. 100
17.367
-21.900
-1.26*'
-1.26?
-1.3S-'
19.
260570. OOfi
2980. 500
0. 98C!
-1.200
18.350
-23. 100
-1.220
-1.25<«
-1.33H
20.
260623. 000
2979. 000
0. 967
-1.500
19.317
-24. 600
-1.55::
-1.27-
-1.37U
21.
260666. 000
2978. 700
0. 63C!
-0. 300
19.950
-24. 90"
-0. 47*-
-1.240
-1.36?:
260698. 00"
2979..30"
VI
Ui
o
(continued)
-------
TABLE A-156 (continued)
Page S of 5
Ul
Reading
No.
T.wln
H. 1b
AT. h
AH. 1b
CAT, h
CAH. 1b
(ft ""*
(UM\ 1b/h
\Z5T/,
X, Ib/h
^^^^^m^mmA
260782. OOfi
2980. 60fi
n 20 Syx Q.545 *a/z 2.101
Slope -1.201 Sx 5i958 r _1-0r)0
Intercept -1.177 $a Q.021 Confidence Interval
Sb 0.223 1.201 + 0.044
S^ 0.569
-------
TABLE A^S? SUMMARY OF DATA FROM TEST NO. 87
Page ] of 3
Degreaser A, operating
Solvent: 1.1,1-THchloroethane
FB 75 I
InlefaTr
Other
PC x SC
Exhaust air
A 50 *
V 8 ft/min
Date 5/24/79
Ambient*air"
Temperature 71 °F
Pressure 29.39 in. Hg
Humidity b6 *
Reading
No.
Tv mln
W, 1b
AT. h
AN, 1b
EAT, h
EAN, 1b
(S). '*»
f iCM i tt «t
Vr/\T/ 'D'n
X. Ib/h
260985. 000
3468. 900
260994. 000
3468. 700
261000.000
3467. 500
1.
261032. 000
3467. 000
2.
261094. 000
3462. 300
1.03::
-4. 700
1.03:::
-4. 700
-4. 54?:
-4. 54?:
-4. 54f:
3.
261151.000
3459. 200
0. 950
-3. 100
1.9:3::
-7. 800
-3. 26;:
-3.93;:
-4.241
en
in
-------
TABLE A-157 (continued)
Page 2 of 3
Reading
No.
T. win
U. Ib
AT. h
AM. Ib
CAT. h
EAU. Ib
(ir). lb/h
Oft ^
XI k/w
. lb/h
4.
261210.000
3456. 600
0. 933
-2. 600
2. 967
-10.400
-2.64<|
-3. 50t-
-3. 996
5.
261272.000
3454. 100
1.03::
-2. 500
4. 000
-12.900
-2.419
-3. 225
-3. 80::
6.
261332.000
3451.300
1.000
-2. 300
5. 000
-15.200
-2. 300
-3. 040
1 •
261390. 000
3449. 700
0. 967
-2. 100
5. 967
-17. 300
-2. 17J1
-2. 399
-3. 525
8.
261452.000
3447. 000
1.033
-2. 700
7. 000
-20. 000
-2.61-::
-2. 857
-3. 430
9.
261514.000
3444. 800
1.033
-2. 200
3.03::
-22. 200
-2. 129
-2.76::
-3. 34t.
in
IT
U)
(conttnued)
-------
TABLE A-l 57(continued)
Page 3 of 3
in
Reading
No.
T, win
U. Ib
AT, h
AW, Ib
CAT. h
CAU. Ib
(S "*"
X. Ib/h
261551?. 000
3448. 300
•
n d S 0.350 t ., 2.447
yx Q/C
Slope -2.455 S 2.452 r -1.000
Intercept -2.770 Sa 0.054 Confidence Interval
d
S, 0.606 2.455 + 0.132
b
S,. 0.807
-------
TABLE A-158 SUMMARY OF DATA FROM TEST NO. 87
Page i of 3
Degreaser B, operating
Solvent: 1,1,1-Trlchloroethane
n 125 %
Inlet air x
Other
PC x SC x
Exhaust air x"
A 50 %
V 8 ft/min
Date 5/24/79
Ambientf'air
Temperature 71 °F
Pressure 29.39 in. Hg
Humidity 56
Reading
No.
Tt win
V, 1b
AT. h
AW. Ib
EAT, h
CAW, Ib
(S). ">"•'
(SfX """
c
X, lb/h
2609S5. 000
3119.500
•
260996. 000
•3113.000
26 100'3. 000
3113.000
1.
261032. 000
3113.900
tZi •
261094.000
-3113.700
1.03::
-0. 200
1.031:
-0. 200
-0. 194
-0. 194
-0. 194
3.
261151. 000
3112.700
0. 950
-1.000
1.98::
-1.200
-1.05::
-0. 60S
-0. -399
tn
-------
TABLE A-l58(continued)
Page 2 of 3
Reading
No.
T, fiin
U. 1b
AT. h
AH. 1b
CAT. h
CAU. Ib
(ir). 1b/h
(si ib/h
Xlk/h
. iD/n
4.
261210.000
3111.900
0. 98 i:
-0. 800
2. 967
-2. 000
-0. 8H
-0.67^
-0. 491
5.
261272. 000
3112. 100
1.031:
0. 200
4. 000
-1.800
0. 194
-0. 450
-0. 481
6.
261332.000
3111.000
1.000
-1. 100
5. 000
-2. 900
-1. 100
-0. 580
-0. 50 J
1 •
261390. nnn
3103.500
0. 967
-2. 500
5. 967
-5. 400
-2. 53t.
-0. 905
8.
261452.000
3107.400
1.03::
-1. 100
7. 000
-6. 500
-1.065
-0. 929
-0.619
9.
261514. 000
3106. 100
1.03-1:
-1. 300
8.03;:
-7. 800
-1.258
-0. 97 J
-0.661:
in
VI
(contlrfuetf)
-------
TABLE A-158 (continued)
Page 3 of 3
in
Reading
No.
T. win
W. Ib
AT. h
AW. Ib
EAT. h
EAU. Ib
(M"\ Ib/h
I TY" 1 ID/n
\AT/,
X. Ib/h
261585.000
3109. 300
•
n 8 Syx 0.760 tQ/2 2.447
Slope -1.082 \ 2.452 r -1.000
Intercept 1.394 S. 0.117 Confidence Interval
O
Sb 0.606 1.082 +0.286
Sr 0.820
c
-------
TABLE JW159SUMMARY OF DATA FROM TEST NO. 88
Page j of 3
Degreaser At operating
Solvent: 1,1,1-THchloroethane
Date 5/25/79
FB 50 I
Inlet air x
Other
PC x SC _ x
Exhaust air x
A
8
50 X
fin in
Ambient air
Temperature 72 °F
Pressure 29.29 in. Hg
Humidity 52 %
Reading
No.
T, mln
W. 1b
AT. h
AW. 1b
EAT, h
CAW. lb
(zr). 1b'h
(tAW\ ,b/h
VIST/.
X, lb/h
261774.000
335S. 3UU
261787.000
3357.700
•
261795.000
3354. 500
1.
261926. 000
3'351. 300
2.
262000. 000
3349. 100
1.231:
-2. 200
1.23::
-2. 200
-1.784
-1.784
-1.784
3.
262059. 000
•3347.000
0.981:
-2. 100
2.217
-4. 300
~ fc- • 1 -J1 tf
-1.940
-1.86J:
oo
-------
TABLE A-159 (continued)
Page 2 of 3
Reading
No.
T, nln
U. 1b
AT. h
AM. 1b
IAT. h
TAll 111
LAM. ID
(ir) lb/h
(iir) lb/h
X. Ih/h
4.
262118.000
3345. 500
0. 98::
-1.500
3. 200
-5. 800
-1.525
-1.81:::
-1.845
5.
262177.000
3343.900
0. 980
-1.600
4. 18::
-7. 400
-1.627
-1.769
-1.826
6.
262235.000
3339.300
0. 967
-4. 600
5. 150
-12.000
-4. 759
-2. 330
-1.927
I •
262294. 000
3337. 100
0.98::
-2. 200
6. 133
-14. 200
-2.237
-2.315
-1.99:-
8.
262353.000
3335. 300
0. 98 ::
-1.800
7. 117
-16. nnn
-1.83J
-2. 24?:
-2. 02?:
9.
262416.000
3332. 100
1.050
-3. 200
8. 167
-19. 200
-3. 04$:
-2. 35J
-2. 069
IP
IT
\D
(continued)
-------
TABLE A-159(continued)
Page 3 of 3
Reading
No.
T. nfn
N. Ib
AT. h
AM. Ib
CAT. h
CAU. Ib
(M\ lh/h
iTrJ lD/n
\AT/.
(uv\ lh/h
IrTTl I0'"
\IAT/,
X. lb/h
262444. 000
3331.900
2b252T:. nnn
1846.900
•
" 8 S 0.820 t/2 2.447
J "r •
Slope- -2.50* sx 2.415 r -l.QOO
Intercept 1.567 S, 0.128 Confidence Interval
O
Sb 0.661 2.504 + 0.313
Sc 1.078
-------
TABLE A-J60 SUMMARY OF DATA FROM TEST NO. 88
Page i of 3
Degreaser B, operating
Solvent: 1,1,1-Trichloroethane
Date 5/25/79
FB 50 %
Inlet air
Other
PC x_ SC x_ A 50 %
Exhaust air x V 8 ft/min
Ambient air
Temperature 72 °F
Pressure 29.29 in/ Hg
Humidity ~-^*
Reading
No.
T, min
H. 1b
AT. h
AH. 1b
EAT, h
CAW. 1b
($). 1b'h
(rafj. 1b'h
X. Ib/h
•261774.000
2893. 000
261787.000
2892. 000
261795.000
2890. 200
1.
261926.000
2S ft 7. 100
2.
262000. 000
28S4. 600
1 . 23 i:
-2. 500
1. 231:
-2. 500
-2. 02 T1
-2. 027
-2. 027'
5.
262059. 000
2SS2. 200
0.983
-2. 400
2.217
-4. 900
-2.441
-2. 211
_O 1 1 Ci
h» • A 1 .
-------
TABLE AJ60 (continued)
Page 2 °' 3
Reading
No.
T. nin
U. Ib
AT. h
AH. Ib
CAT. h
CAU. Ib
(*"} Ih/h
i -7=- 1 iD/n
\AT/,
GAT) lb/h
X. lb/h
4.
262118.000
2330. 500
0. 980
-1.700
3. 200
-6. 600
-1.729
-2. 06':
-2. 100
5.
262177. 000
2378. 500
0.93::
-2. 000
4. 18::
-8. 600
-2.031
-2. 056
-2. 039
6.
262235.000
2876. 000
0. 967
-2. 500
5. 150
-11.100
-2. 58t.
-2. 155
-2. 10J-
I •
262294. 000
2874. 300
0.98::
-1.700
6. ISO
-12.800
- 1 . 729
-2. 037
-2. 100
8.
262353.000
2871.600
0.98::
-2. 700
7. 117
-15. 500
•"• ~* 1 £
~>L» I Hti
-2. 178
-2. Ill
9.
262416. 000
2369. 600
1.050
-2. 000
3. 167
-17.500
-1.905
-2. 14::
-2. 115
(continued)
-------
TABLE A-160 (continued)
Page 3 of 3
IP
Reading
No.
T. min
W, Ib
AT. h
AU, Ib
CAT. h
I AW, Ib
X. Ib/h
.262444. 000
2869. 400i
262523.000
2871. 100
•
8 Syx 0.24 ta/2 2.447
Stope -2.163 Sx 2.415 r -1.000
Intercept 0.175 Sa 0.038 Confidence interval
a
S. 0.661 2.163 + 0.093
D —
S.. 0.392
-------
TABLE A-161 SUMMARY OF DATA FROM TEST NO. 89
Page i of 2
Degreaser A, operating
Solvent: 1,1,1-Trlchloroethane
Date 5/25/79
T
FB 50 t
Inlet air
Other
PC x SC A 50 *
Exhaust air x V 8 ft/ml n
Ambient 'air
Temperature 71 «
Pressure 29.39 in.
Humidity 51 1
Reading
No.
T, mln
W, Ib
AT h
Ql 9 fl
AV, Ib
EAT, h
EAH, Ib
• .
(Ir) 1b/h
($?). ""*
X. 1b/h
262538. 000
3335. 000
262550. 000
3328. 500
1.
262573. 000
3328. 800i
2.
262637.000
3326. 700
0 QO-.
-2. 100
0.98::
-2. 100
-2. 1 36
-2. 1 3t.
-2. 1 3t-
3.
262698. 000
3324. 600
1 . 0 1 7
-2. 100
2. 000
-4. 200
-2. 06*
-2. 100
-2. 11?:
4.
262758. 000
3322. 500
1 000
X • •— f v •• •
-2. 100
3. 000
-6. 300
-2. 100
-2. 100
-2. lit'
in
-------
TABLE A-161 (continued)
2 of 2
Reading
No.
T, mln
M. 1b
AT, h
AW, 1b
EAT. h
EAU, 1b
(tM\ ,h/h
I TT i iD/n
VAT/,
(m "">
X. lb/h
5.
262813.000
3320. 900
1.000
-1.600
4. 000
-7. 900
-1.600
-1.975
-2. 07?:
6.
262373. 000
3313.700
1.000
-2. 200
5. 000
-10. 100
-2. 200
-2. 020
-2. 066
i •
262933.000
3316. 800
1.000
- 1 . 900
6. 000
-12.000
-1.900
-2. 000
-2. 05J.
8.
262998. 000
3315. 500
1.000
-1. 300
7. 000
-13. 300
-1.300
-1.900
-2. 030
9.
263053. 000
3313. 500
1.000
-2. 000
8. 000
-15.300
-2. 000
-1.913
-2.01?:
263080. 000
3316.300
n 8 Syx 0.242 t^2 2.447
Slepe -1.869 S^ 2.453 r -1.000
Intercept -0.494 Sfl 0.037 Confidence Interval
Sb 0.605 1.869 + 0.090
S,. 0.310
in
-------
TABLE A-162 SUMMARY OF DATA FROM TEST NO. R9
Page j ^of 3
Degreaser B, operating
Solvent: 1,1.1-Trlchloroethane
PC
FB 50 i
Inlel aTF
Other
x SC _
xhaust air x
A 50
8 ~Tt7i
Date 5/25/79
Ambient air'
Temperature
Pressure
Humidity
inTHg
Reading
No.
T, mln
W, 1b
AT. h
AH. 1b
EAT, h
CAW. 1b
(If). 'w»
(M?). «>"•
X, Ib/h
Z6ZT-33. rjrjri
2371.200
2b253S. 000
2S7 1.200
262550. 000
286b. 000
1.
26257ft. 000
2865. 700
2.
262637.000
2363. 400
0. 983
-2. 300
0. 98':
-2. '300
-2. 33?
-2. 339
-2. 339
3.
262693. 000
2361.000
1.01T1
-2. 400
2. 000
-4. 700
-2. 361
-2. 350
-2. 344
-------
TABLE A-ifi?(continued)
Page 2 of
Reading
No.
T. «1n
M. 1b
AT. h
AM. 1b
CAT. h
CAM. 15
©. ""*
(fir). lb'h
X. 1b/h
4.
262758. 000
2859. 300
1.000
-1.700
3. 000
-6. 400
-1.700
-2. 13':
-2. 274
5.
262318. 000
2857. 000
1.000
-2. 300
4. 000
-3. 700
-2. 300
-2. 175
-2. 249
6.
262873. 000
2855. 000
1.000
-2. 000
5. 000
-10.700
-2. 000
-2. 140
-2. 227
i .
262933.000
2353.400
1.000
-1.600
6. 000
-12. 300
-1. 600
-2. 050
-2. 19:-:
8.
262998. 000
2851.500
1.000
-1.900
7. 000
-14.200
-1.900
-2. 029
-2. 174
9.
263053. 000
2848. 700
1.000
-2. 800
3. 000
-17.000
-2. 800
v w • 1 tL .'
-2. 16?:
in
(contfnued)
-------
TABLE A-162 (continued)
Page 3 of 3
Reading
No.
T. nln
N. Ib
AT. h
AH, Ib
s EAT* h
00 IAM. Ib
(ZM\ lb/h
\ i«4J 1 Xtj
• •
X. lb/h
263089. 000
2S52. 300
n 8 Syx 0.290 t^ 2.447
Slope • -2.022 Sx 2.453 r -l.QOO
Intercept -0.442 Sa 0.045 Confidence Interval
Sb 0.605 2.022 + 0.110
S,. 0.396
-------
TABLE A-163 SUMMARY OF DATA FROM TEST NO. 90
Page 1 of 3
Degreaser A, operating
Solvent: Methylene chloride
PC
Date 5/31/79
FB 75 I
Inlet air
Other
x SC _
xhaust air x
A_50j
V 8 ft/m
Ambient air
Temperature 75
Pressure 29.49
Humidity 68 %
Reading
No.
T, mln
W, 1b
ftT, h
AW, 1b
EAT, h
CAW. 1b
(£). ">»
(80. lb/h
X. lb/h
270605.000
3553. 2oo
270618.000
?55i.;:00
270624.0OO
3545. ?Wo
1.
270660. 000
35-i6. 100
-•
t— •
270720. 000
3544. 800
1.000
-1. 300
1.000
-1.300
-1. 300
-1. 300
- 1 . 300
3.
270755. 000
354::. 200
1.03::
-1.600
2. 030
-2. 900
-1.477
-1. 3?:1
-1. 34h.
in
o>
vO
-------
TABLE A-l63 (continued)
Page 2 of 3
vr
^i
c
Reading
No.
T. «in
U. Ib
AT. h
AW, Ib
EAT. h
EAU. Ib
/AU\ .
ITT) iD/n
\AT/,
(TT) 1b/h
X. Ib/h
4.
270843. 000
3540. SOO
0. 967
-2. 400
3. 050
-5. 300
-2. 4S.::
-1.73?:
-1.477
5.
270901.000
3539. 900
0. 967
-0. 900
4.017
-6. 200
-0.931
-1.541
-I. 49::
6.
27096 1. 000
3537. SOO
I. 000
-2. 1 00
5. 017
-8. 300
-2. 1 00
-1.651
-I. 52,
I •
271019.000
3536. 500
0. 967
-1. 300
5.98::
-9. 600
-1. 34S
-1. 604
-1. 53':'
8.
271 OS 3. 000
3534. 700
1. 067
-1. SOO
7. 050
-11. 400
-1.6S7
-1.617
-1. 550
9.
271140.000
3533.400
0. 950
-1. 300
8. 000
-12.700
-1.36S:
-1. 588
-1.55=-
(continued)
-------
TABLE A-163(continued)
Page 3 of
IP
Reading
No.
T, min
U, Ib
AT. h
AU. Ib
CAT. h
CAW. Ib
(ir) lb/h
\,£AT /%
» •
X. lb/h
27114ft. 00.;
I'"l 1~"8. 000
353-i. ftnn
n 8 $„„ 0.296 t ., 2.447
y* o/t
Slope -1.642 Sx 2.439 r -0.999
Intercept 0.217 $a 0.046 Confidence interval
S. 0.617 1.64? + 0.112
Sr 0.494
W»
-------
TABLE £-164 SUMMARY OF DATA FROM TEST NO. 9Q
Page J_ of 3
Degreaser B, operating
Solvent: 1,1,1-THchloroethane
PC
FB 75 %
InleTaT?
Other
x SC
xhaust air
50 I
Tin in
Date 5/31/79
Ambient "air
Temperature 75 °F
Pressure 29.49 in. Hg
Humidity 68 *
Reading
No.
T, m1n
H, 1b
AT, h
AH, 1b
EAT, h
EAH. 1b
(S). "'"•
(•• AU V
**OW ^ • t /•»
X, Ib/h
270605. 000
2872. .300
270618.000
2873. 400
270624. 000
2868. 300
1.
270660. 000
2867. 000
2.
270720. 000
2864. 900
1 . 000
-2. 100
1.000
-2. 100
-2. 100
-2. 100
-2. 100
3.
270785. 000
2863.900
1.031:
-1.000
2. 08':
-3. 100
-0.92!:
-1.48:;:
-1.794
N)
-------
TABLE A-164 (continued)
Page 2 of 3
Reading
No.
T. «in
U. lb
AT. h
AM. lb
CAT, n
IAU. lb
(SO. «<•
(ft?). »•"•
X. Ib/h
4.
270843. 000
2862. 600
0. 967
-1.300
3. 050
-4. 400
-1.345
-1.44:!
-1.677'
5.
270901.000
2861.900
0. 967
-0. 700
4. 0171
-5. 100
-0. 724
-1.270
-1.575
6.
270961.000
2860. 400
1.000
-1.500
5.017
-6. 600
-1.500
-1.316
-1.523
i .
271019.000
285*. 7Hfi
0. 967
-0. 700
5. 98;:
-7. 300
-0. 724
-1.220
-1.471:
8.
271083.000
2858. 500
1.067
-1.200
7. 050
-8. 500
-1. 125
-1.20*.
-1.435
9.
271140.000
2857. 000
0. 950
-1.500
8. 000
-10.000
-1.579
-1.250
-1.411
in
(continued)
-------
TABLE A-l 64 (continued)
Page 3 of 3
Reading
No.
T. win
U. 1b
AT. h
AW. 1b
CAT. h
LAW. Ib
(M\ Ih/h
ITT^J ID/H
\AT/,
X. Ib/h
27114S. 000
285t-. 900
271137. OOfi
2St.l. OOCi
n 8 Syx 0.210 ta/2 2.447
Slope -1.106 \ 2.439 r -1.000
Intercept -0.883 Sa 0.033 Confidence Interval
a
Sb 0.617 1.106 +_ O.P81
S,. 0.475
-------
TABLE .AJ65 SUMMARY OF DATA FROM TEST NO. 91
Page j_ of
Degreaser A, Idle
Solvent: 1,1,1-THchloroethane
(Boiling ; nonboiling jj )
FB 50 t PC SC _
Inlet air Exhaust air x_
Other
Lid closed
A _n X
V 0 ft/min
Date 5/30/79 .
Ambient 'air
Temperature °F
Pressure In. Hq
Humidity t
Reading
No.
T, mln
tf, 1b
AT. h
AW, Tb
TAT, h
CAW, 1b
(M\ lh/h
i XT i iD/n
\AI/,
fUM\ lb/h
\U /.
X. lb/h
1.
269.305. 000
3265. 500
2
270322. 000
3262. 300
16.950
-2. 700
16.950
-2. 700
-0. 15'E'
-0. 151:'
-0. 15?
tfl
-------
TABLE A-l66 SUMMARY OF DATA FROM TEST NO. 91
Page 1 of 1
Degreaser B, Idle
Solvent: l.l.l-TMchloTOethane
(Boiling ; nonboiling _x )
FB 50 % PC SC
Inlet air Exhaust air x~
Other
Lid closed
V 0
Date 5/30/79
Amb i ent'air '
Temperature
Pressure in.
Humidity
Reading
No.
T, m1n
W. 1b
AT. h
AW. 1b
EAT. h
CAM. 1b
(1?). """
(far). 1b/h
X. Ib/h
1.
269305.000
2814.700
%
270-322. 000
2812. 200
16. 950iO
•2. 500
16.950
-2. 500
-0. 147
-0. 147
-0. 147
01
~J
a*
-------
TABLE A-167 SUMMARY OF DATA FROM TEST NO. _92
Page \ of 1
Degreaser A, Idle
Solvent: 1,1,1-TMchloroethane .
(Boiling ; nonboiling x )
FB 50 X PC SC _
Inlet air x_ Exhaust air x
Other
A
0
ft/m1i
m1n
Date 5/29/79
Ambient afr
Temperature 7$ °F
Pressure 29.45 in. Hg
Humidity 59 >
Reading
No.
T, m1n
W, 1b
AT. h
AW, 1b
EAT, h
EAH. 1b
(AW\ 1h/||
1 AT * ' «»f R
\lil/t
(§r). lb'h
X, 1b/h
1.
11T16SOOD
3270. c-nn
0
2*9213.000
^^hS. nnn
20.33.-:
5. 500
20. S3 ?.
5. 500
0.^3
0.263
0.2*3
-------
TABLE A-l68 SUMMARY OF DATA FROM TEST NO. 92
Page i of l
Oegreaser B, Idle
Solvent: 1,1,1-THchloroethane
(Boiling ; nonboiling * )
FB 50 % PC SC _
Inlet air x Exhaust air x_
Other
A 0 I
V 0 ft/min
Date 5/29/79
Ambient air
Temperature 75 «p
Pressure 29.45 in. Hg
Humidity 59 I
Reading
No.
T, mln
W. 1b
AT. h
AW, 1b
EAT, h
CAW. 1b
(S). '»»
(i?). ">"•
X. 1b/h
1.
u:t.rJ
00
-------
TABLE A-l69 SUMMARY OF DATA FROM TEST NO. 94
Page 1 of 1
Degreaser A, Idle
Solvent: 1,1,1-Trlchloroethane
(Boiling ; nonboiling _x_)
FB 75 * PC x SC A
Inlet air x Exhaust air x V p
Primary condensers went off during the test
nln
Date 6/18/79
Ambient air
Temperature 72 «F
Pressure 29.65 in. Hg
Humidity 55 *
Reading
NO.
T, mln
W. 1b
AT. h
AH. 1b
TAT. h
£AW. 1b
(ff). ">'"
(Mr). lb/h
X. 1b/h
i.
3514.600
^
206753. 000
3445. 600
165.567
69. 000
165. 567
69. OU'1
0.417
0.417
0. -i 1 7
vD
-------
TABLE A-l70 SUMMARY OF DATA FROM TEST NO. 94
Page 1 of 1
Degreaser B, Idle
Solvent: 1,1,1-Trichloroethane
(Boiling ; nonboiling _x )
FB 75 * PC x SC
Inlet air
Other
A Q %
V Q ft/min
x Exhaust air j<
Primary condensers went off during the test
Date 6/18/79
Ambient air
Temperature 72 °F
Pressure 29.65 in. Hg
Humidity 55 %
Reading
No.
T. m1n
W. Ib
AT. h
AW. Ib
EAT. h
EAH. Ib
(ff). ™
(ZST). lb/h
X. lb/h
1.
296819.000
337. 600
-.
306753.000
327. 000
165. 567
10.600
165.567
10. 600
0. Oh.4
0. 064
0. n-.J
01
00
o
-------
APPENDIX B
TEST CONDITIONS AND RESULTS
The table given here shows the test conditions and solvent
loss results. Each test run is identified on the left side of the
table in terms of the equipment modifications and other parameters
that were used. Data on solvent loss are given on the right side.
581
-------
TABLE B-l. TEST CONDITIONS AND RESULTS
(test period October 1978 to July 1979)
.
s
Ml
01
1
2
3
4
5
6
7
8
TEST CONDITIONS'
Ol
10
9t
S
A
8
A
B
A
B
A
B
A
B
A
B
A
B
A
B
S
a
5
10/10
10/12
10/16
10/19
10/27
11/3
11/12
11/13
1
**
C
Ol
5
TE
TE
TE
TE
TE
TE
TE
TE
c
Of
ex
o
_J
,
/
J
J
/
/
/
Ol
c
*
c
Ol
*o
I/I
/
/
/
/
s
t_
Ol
Wl
c
01
0
u
i*
^
k.
a.
/
/
/
/
u
^
ec
it.
o
«
l.
fj
3
.O
Ol
U. 4)1
50
50
50
50
50
50
50
50
^
Ol
£
IA
Wl
0.04
0
0
0
0
0 04
0.04
0.04
>t
.
5
f
ss
0.806
0.6B4
0.029
0.029
0.059
0.029
0.034
0 024
0.020
0.015
0.850
0.806
0.737
0.752
0.742
0.688
**
'g
i
u
u
s
UJ
23.68
26.82
NA
NA
NA
NA
NA
HA
NA
NA
NA
NA
23.27
21.47
23.24
20.66
tA
S
•^
i
i
T»
S
ta
0.265
0.180
NA
NA
NA
NA'
NA
NA
NA
NA
HA
NA
0.257
0.163
0.253
0.132
Comments
Ul
oo
(continued)
-------
TABLE B-l (continued)
o
z
w*
Ol
t-
9
10
11
12
13
14
IS
16
TCST CONDITIONS'
i.
Ol
I/I
S
u
Ol
fi
A
B
A
B
A
B
A
B
A
B
A
B
A
B
A
B
01
^
£J
Ol
t-
11/14
11/15
11/15
11/16
11/16
11/17
11 /ZO
11/20
Ol
•J
c
^
5
TE
TE
TE
TE
TE
TE
TE
TE
•
ex
•o
/
/
/
/
/
/
5
i
c
^
3
,
/
/
/
/
/
/
/
~
CL
fc
1 condens
i.
|
b
CL
/
/
/
/
/
/
/
/
.a
u.
ae
/
J
/
/
/
f
<£
"***
o
2
01
Ol
k.
50
SO
SO
50
SO
SO
50
50
.
CL
I/I
r- I/I
0
0
0.04
0
0
0 04
0.04
0
^
41
Ol
L.
_J
0
0
50
0
0
50
50
0
CL
*~
i
Ol
L, Wl
0.1
0.1
0.1
0.1
0.1
0.1
0 1
0.1
0.1
i
cr
1
•V
01
u
•a
c
•— o
0.816
0.426
0.662
1.252
1.325
0.844
0.146
0 975
0.319
0.397
1 510
0.649
0.494
O.S62
0.653
0.549
Wl
SI
** Ol
C 0.
5^
I/I JC
0.586
0.303
0.474
0 894
0.952
0.366
0.063
0.693
0.229
0.283
1.084
0 464
0.356
0.498
0.469
0.391
2
.
!
•o
u
u
I
21.85
19.44
23.07
21.06
23.76
21.03
22.90
20 09
22.98
20 SO
22.64
18.62
21.36
18.38
23.64
21.56
M
L.
01
s
i
1
a
0.278
0.200
0.276
0.180
0.272
0.134
0.278
0.131
0.312
0.141
0.097
0.140
NA
0.112
NA
0.123
Comnents
Results discarded.
Results discarded.
Top was closed one half hour
between each load cycle.
cn
00
to
(continued)
-------
TABLE B-l (continued)
o
z
2
17
18
19
20
21
22
23
24
25
TEST CONDITIONS1
U
Of
tfl
«
Of
sr
o
A
B
A
B
A
B
A
8
A
A
B
A
B
A
A
B
01
a
•o
lA
01
1—
11/21
11/21
11/22
11/26
12/21
12/22
1/15
£
c
01
o
TE
TE
TE
TE
TE
TE
TE
c
i
o
/
/
/
/
/
/
/
?
9
a
c
01
o
I/I
/
/
/
/
,
/
/
a.
t_
01
c
01
1
o
u
u
1
a.
/
/
/
/
/
/
/
u.
oe
/
/
/
/
e
0
4J
C
s
«
01
1.
u. ••
75
75
50
50
75
100
50
•£
«
ex
in
Wl
H
0
0.04
0.04
0.04
0.04
0.04
0.04
<«
—
L.
•a
3
0
50
SO
70
SO
SO
50
ex
•a
«
OJ
IS
0.1
0.1
0.1
0.1
0.1
0.1
0 1
£
cr
u
1
a
Of
u
•o
s
0
9.23
9.23
9.23
9.23
9.23
9.23
c
o
tl
3
«
K
tAt
/
J
J
/
J
/
/
S
u
•o
Of
c
/
T :ST RESULTS
£
5
01
*J
Ul
01
1-
6.97
6.98
6.95
6.90
5.97
5.97
5.93
5.10
5.83
11 83
10.88
10.50
25 83
26.22
s.
I/I C7I
£•"
Ot •
io.
g*^
C •—
Sc
5^
0.485
0 299
0.971
0.816
1.102
1.048
1.281
1.044
0.635
0.835
0.553
0.467
0.807
0.880
2
"g
• 9
ui E
MN «
0 G 'a
*-» 01
c a.
S.C
0.347
0.215
0.698
0.581
0.791
0.747
0.903
0.757
0.454
0.581
0.39S
0.347
0.591
0.620
i.
i
UJ
24.84
22.51
22.64
20.53
22.67
20.99
24.06
20.15
22.88
20.57
21.53
18.85
24.55
20.79
in
•s.
S
—
Tl
C
s
5
(A
-------
TABLE B-l (continued)
s
01
h-
26
27
2b
29
30
31
32
33
34
TEST CONDITIONS1
Ol
Ol
i
A
B
A
B
A
B
A
B
A
B
A
B
A
B
A
D
A
B
01
•a
w
i-
1/18
1/19
1/20
1/21
1/26
1/25
1/28
1/29
1/31
ai
a.
w
I
TE
TE
TE
TE
TE
TE
TE
TE
TE
e
o
Tl
_j
j
J
J
/
/
/
J
/
/
J
J
1
0
2
c
«i
o
*/»
J
/
/
/
/
/
/
/
/
/
/
LJ
k
Ql
C
1
O
u
£
i.
o.
J
/
/
/
/
/
/
/
/
/
/
u_
ae
,
/
/
/
/
/
.
,.
50
50
125
125
125
125
125
100
125
75
50
H
Of
s.
in
H
0 04
0.04
0.04
0.04
0.04
0.04
0.08
0.08
0.08
0 08
0.04
«•
•0
•o
s
70
70
70
70
50
50
50
50
70
50
50
a.
m
g
*oi
t. tn
0.1
0.1
0.1
0.1
0.1
0.1
0.
0.
0.
0.
0.
fi
cr
u
i
c
ai
u
•o
a
O
_l
9.23
9 23
9.23
9.23
9.23
9.23
9.23
9.23
9.23
9 23
9 23
S
£
•— "^
0 630
0.542
0.474
0.781
0.684
0.498
0.435
0.889
0.518
0.610
0.625
0.811
0.562
0 615
0.664
'
1
!
T>
U
1
NA
18.38
NA
NA
24.3
22.07
22.76
19.03
24.33
20 81
23.35
0 32
NA
NA
24.04
21.16
24.64
22.69
Ul
s
•o
c
TJ
l_
W
5
NA
0.134
HA
NA
0.128
0.138
0.190
0.126
0 166
0.128
0.098
0.083
NA
NA
0.080
0.083
0.136
0.080
Comments
Extensive problems with
Degreaser A.
Results discarded.
Results discarded.
I/I
00
1/1
(continued)
-------
TABLE B-l (continued)
t
s
lA
Ol
35
36
37
38
39
40
41
42
TEST CONDITIONS'
i.
Ol
u
Ol
k
S
A
B
A
B
A
B
A
B
A
B
A
B
A
B
A
B
01
•o
Ol
t—
2/2
2/4
4/1
4/2
4/4
4/5
4/11
4/12
a.
-
c
Ol
o
I/I
TE
TE
HC
HC
HC
HC
HC
HC
HC
HC
HC
HC
HC
HC
c
a.
o
5
/
/
/
/
/
/
/
/
/
?
~
£
C
Ol
*o
I/I
/
/
/
/
/
/
/
/
/
a.
i.
Ol
IA
|
8
£*
L.
a.
,
/
/
/
/
/
/
/
/
£
/
/
/
/
^
^
..
50
50
50
50
50
50
50
125
125
£
,,
I
*"
r- I/I
0.08
0.04
0.08
0.04
0.04
0.04
0.04
0.04
0.04
^
i
n
V
•o
ID
O
—I
SO
50
70
50
50
70
70
50
50
.
^"
%
f?
g
01
k IA
0.1
0.1
0.1
0.1
0.1
0 1
0.1
0.1
0 1
^
u
V)
Ol
c
ID
01
•o
3
9.23
2
9.23
9.23
9.23
9.23
9.23
9.23
9.23
c
0
u
IO
3
ID
JC
X
UJ
J
J
/
/
/
/
/
/
/
c
o
k
•J
01
c
/
/
/
/
/
/
/
/
/
TEST RESULTS
f
£
I/I
Ol
1-
20.28
20.33
18.17
23.85
23.78
24.13
24.13
24.08
24.08
24.25
24.25
24.17
24.17
24.08
24.08
*n 171
Ol •
01 —
I/I I/I
c •—
01
> c
r- O
1.157
0.517
1.560
0.776
1.052
0.880
0.889
1.175
1.610
1.075
1.107
0.585
0.776
0.585
0.407
VI
VI (XI
o e
u
c &
V
>.c
*O CJi
1S1 J<
0.796
0.342
1.118
0.557
0.747
0.630
0.591
0.840
1.143
0.771
0.781
0.420
0.562
0.420
0.288
3
i
•o
u
k
•J
UJ
24.07
21.30
24.67
12 00
14.40
13.00
15.36
12.00
14.40
12.99
15.38
12 56
14.42
13 04
15.44
VI
•^
S
•g"
i
•o
3
0.193
0.148
0.187
0 429
0.635
0.410
0.632
0.407
0.623
0.417
0.636
0.432
0.657
0.419
0.638
Comments
Top on Degreaser B left
open between each cycle.
Degreaser B not used.
(.n
CO
(continued)
-------
TABLE B-l (continued)
s
Wl
Ol
1-
43
44
45
46
47
48
49
SO
TEST CONDITIONS'
L.
Ol
Wl
S
1
A
B
A
B
A
B
A
B
A
B
A
C
A
B
A
b
Ol
•5
Wl
Ol
1-
4/9
4/8
3/28
3/29
3/28
6/12
2/16
|
2
5
HC
HC
HC
HC
HC
HC
HC
HC
HC
HC
TE
TE
HC
HC
c
i
•o
,
J
/
/
J
/
/
J
f
•^
c
"o
*/»
/
/
/
J
/
/
/
J
—
—
k
Ol
Wl
C
1
o
u
^
L.
Ob
/
/
/
/
/
/
/
/
a
J
m
|
O
s
1
Of
£
u. M
125
12S
SO
SO
50
SO
75
75
SO
B
5
T)
Ol
**
Wl
r- Wl
0.04
0.04
0.04
0.04
0.04
0.04
0.04
0.04
0
M
^
S
Ol
«
•o
s
70
70
SO
SO
SO
SO
50
SO
0
a
^*
«
^
u
o
>oi
i. Wl
0.1
0 1
0.1
0.1
0.26
0.1
0.1
0 1
£
a
JM
U
S
c
Ol
•o
o
9.23
9.23
9.23
9.23
9.23
9.23
9.23
9.23
9.23
c
0
t.
«
**
X
UJ
J
/
/
/
/
/
/
C
o
1.
*
01
,,
J
J
J
J
/
/
/
TEST RESULTS
*
4!
Ol
•J
Wl
01
^-
24.00
24.00
24.03
24.03
24.46
24.03
24.03
24.46
24.08
16.92
18 60
18.08
1 ^
Wl 01
a?,-;
i-a
Wl.—
Wl Wl
ai
1!
0.703
0.971
0.603
O.S85
1.932
1.633
0.980
2.223
1.016
0.19S
0.426
0.490
Wl
witsj
O E
"~ L.
V
0.503
0.693
0.43S
0.415
1.372
1.172
0.698
1.602
0.713
0.137
0.317
0.3S6
2
.
U
t_
|
UJ
12.19
14.39
12.92
15.33
12.89
12.69
14.14
NA
14.65
4.08
12.41
15.30
Wl
Ol
•
19
C
^
S
s
0.418
0.636
0.419
0.636
0.477
0.464
0.628
NA
0.693
0.142
0.459
0.458
Comnents
Oeg. A: Lip exhaust at
0.50 m3/s per m2 top opening.
Deg. B: Not run.
Oeg. A: Lip exhaust at
0.25 ni3/s per m' top opening.
Deq. B: Crosscurrent test.
Not run.
Crosscurrent test.
Crosscurrent test.
Test of small degreaser.
Not run.
Not run.
IP
CO
(continued)
-------
TABLE B-l (continued)
o
z
VI
Ol
51
52
S3
54
55
56
57
58
TEST CONDITIONS'
k.
Ol
to
Ol
l_
ff
o
A
B
A
B
A
B
A
B
A
B
A
B
A
B
A
B
a
•3
s
2/25
2/22
2/25
2/27
3/2
3/1
£
if
c
01
5
HC
HC
HC
HC
HC
HC
HC
c
Ol
a.
o
B
/
/
/
Ol
c
•^
5
c
Ol
o
I/I
/
/
£•
CL
i.
Ol
IA
C
Ol
o
u
L.
a.
/
/
/
/
/
.a
s
/
/
/
.
IA.
5
C
TJ
L.
i
01
01
50
SO
50
50
50
50
~
^
S
a
IA
H
0
0
0
0
0
0
••
s.
s
u
c-
01 •
u"o7
«— • ex
o
VI •—
M III
c J^
01
> c
OS
0.290
0.358
0.218
0.141
0.150
0.110
0.259
0.118
0.240
0.395
0.649
0.304
IA
VI CM
° E
i.
*-• 01
c a.
Of
> f
5"
0.210
0.254
1.562
1 025
0.107
0.088
0.186
0.083
0.171
1.099
0.464
0.220
2
i
u
*J
UJ
12.35
14.55
0
0
0
0
0.69
0.94
0.79
1.09
12.88
15.27
IA
S
—
•a
i
01
s
5
0.565
0.728
0
0
0.076
0.414
0.505
1.168
0.180
0.493
0.427
0.510
Comments
Solvent lass during cooldowi
period.
Solvent loss during cooldowi
period.
Not run.
Not run.
Not run.
Not run.
Solvent loss during cooldowi
period.
LP
CD
00
(continued)
-------
TABLE B-l (continued)
•
s
IA
Ol
59
60
61
62
63
64
65
66
TEST CONDITIONS9
t_
01
at •
£1£
o
t*2
o o»
c
c *^
Ol
> c
•52
*/» (A
0.191
0.1SO
0.209
0.342
0.231
0.218
0.490
0 549
0.621
0.336
0.331
0 476
0.381
0.431
0.150
0.1B1
in
virvi
o E
i.
£ *
*O Ol
I/I .M
0.132
0.107
0.151
0.244
0.166
0.146
0.347
0.381
0 444
0.249
0 244
0.352
0.269
0.312
0.107
0.127
x
"*
i
E
10
u
"5
s
Ul
0
0
0.82
1.12
0
0
12.30
14.51
12.97
14.91
12.25
14.51
12.34
14.56
0
0
•j..
01
—
E
W
^
2
S
2.52
6.31
2.48
6.65
0
0
6.61
7.44
7.76
9.23
7.76
9.19
7.77
9.19
7.76
9.16
Conments
Solvent loss during cool down
period.
Ul
00
vO
(continued)
-------
TABLE B-l (continued)
I
t/t
01
*~
67
68
69
70
71
72
73
74
TEST CONDITIONS'
u
Ol
IA
01
A
B
A
B
A
B
A
B
A
B
A
B
A
B
A
B
01
a
*~
3/13
3/14
3/15
3/16
3/22
3/23
4/15
Ol
a.
|
3>
HC
KC
HC
HC
HC
HC
HC
•
c
1
•-
•^
,
/
/
/
/
/
J
J
g*
i
c
•V
*o
/
/
/
/
'
u
~
w
I/I
s
^
i.
,
/
/
/
/
V
J
•^
u.
06
,
/
.
e?
*^
0
2
i
Of
w
tfc **
100
100
125
125
50
50
50
50
75
.
^
a,
M
•- wi
X G
0
d
0
0
0
0
0
0
0.04
„
f
s
!S
^
o
ex
^~
^J
I
01
i. IA
0.1
0.1
0.1
0.1
0.43
0.26
0.1
0.1
£
5
u
1
S
u
•o
0
o
0
0
0
0
0
0
0
0
9.23
9.23
c
0
i.
J
01
+J
*u
24.07
24.95
24.17
23 25
19.65
19.65
71.23
71.23
14.08
14.08
27.27
27.27
24.05
24.05
JC
S
^
*-* Q.
g
^
— 0
o «-
1/1 I/I
0.322
0.227
0.193
0.255
0.362
0.553
0.406
0 306
0.264
1 851
2.309
3.765
0.608
0.871
I/I CM
a e
01
> JC
l~ *«^
t/t Jtf
0.229
0.166
0.137
0.181
0.259
0.391
0.293
0.215
0.190
1.323
1.611
2.681
0.435
0.625
2
.
*g
u
u
s
u
12.91
14.74
0.36
1.09
12.35
14.55
0
0
0.35
0
12.90
14.38
12.20
14.38
IA
fc
H
•—
1
1
T)
S
0.469
0.556
0.370
0.579
0.410
0.579
0.286
0.391
0
0
0.491
0.573
0.418
0.635
Comnents
Solvent loss during cooldown
period.
Deg. A: Lip exhaust at 0.08
m3/s per of of top opening;
Deg. B: Crosscurrent test.
Deg. A: Lip exhaust at 0.50
m3/s per of of top opening;
Deg. B: Crosscurrent test.
Not run.
Not run.
cn
vo
o
(continued)
-------
TABLE B-l (continued)
t
o
w
01
t-
75
76
77
76,
781
79
80
(.1
TEST CONDITIONS'
i.
Ol
IA
?
S
A
B
A
B
A
B
A
B
A
B
A
B
A
B
A
B
Ol
4-t
2
4/17
4/25
4/26
5/8
5/9
5/10
5/11
5/14
£
**
Ol
5
HC
HC
HC
HC
HC
HC
HC
HC
c
01
0.
o
•o
/
/
/
/
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/
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c
Ol
5
/
/
/
/
'
£
Ol
M
C
Of
1
g
u
a.
/
/
/
/
J
/
/
/
/
^
oe
/
^
Ub
^^
0
a
"2
•g
c
u. »«
75
7b
75
75
75
50
50
125
100
75
.
•^
Ol
£
i/l
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0.04
0
0
0
0
0
0
0
0
0
M
2.
3
t.
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S
50
r*
*~
%
$
S
*
U Wl
0.1
0.1
0.1
0.26
0.1
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0.1
0.1
0.1
^*
£
i
•a
01
u
•o
s
9.23
9.23
0
0
0
0
0
0
0
0
0
C
0
u
n
*J
I/I
to
£
M
LU
/
/
/
/
J
'
J
/
/
c
o
i.
<0
01
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/
/
/
J
J
'
/
/
/
TEST RESULTS
^
5
g1
01
•J
S
24.05
24.05
18.73
18.78
19.00
19.13
21.28
21.28
23.36
23.36
20.17
20.17
70.63
70.63
22.00
22.00
IA Ol
U "*
Ol •
Q)^-^
o
Vlr—
I/I IA
O
c •—
01
> c
5S
0.726
0.590
0.753
0.585
0.975
2.232
0.100
0.109
0.070
0.114
0.227
0.191
0.202
0.169
0.111
0.165
jh
*-• Of
C 0.
Of
> f
O Ol
I/I JC
0.522
0.415
0 532
0.415
0.693
1.592
0.073
0.078
0.049
0.083
0.161
0.137
0.146
0.122
0.078
0.117
.X
•
?
1
u
c
*J
Ul
12.96
15.35
12.02
14.52
13.11
14.59
0
0
0
0
0
0
0
0
0
0
VI
01
^
^
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c
g
u
s
1.418
(.635
1.428
1.647
1.431
1.418
1.516
1.478
1.515
1.477
1.560
1.581
1.606
1.555
1.587
1.549
Comments
Deg. A: Lip exhaust at 0.25
m3/s per n2 top opening.
Deg. A: Lip exhaust at 0.50
m3/s per m2 top opening;
Oeg. B: Crosscurrent test.
Inlet air was turned on about
3 hours after test started.
en
(continued)
-------
TABLE B-l (continued)
•
£
t
B2
83
84
85
116
U7
88
39
TEST CONDITIONS'
u
41
M
•I
1
A
B
A
8
A
B
A
B
A
B
A
B
A
B
A
B
•i
5
M
5/15
5/16
5/22
5/23
5/23
5/24
5/25
5/25
£
*}
g
1
IK
HC
TE
TE
TE
TE
TE
TE
c
i
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J
J
/
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/
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w
1
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/
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u
a.
i.
S
•i
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L.
a.
/
/
/
/
/
/
/
/
/
JD
U
/
/
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/
/
^
ae
o
i.
^
u
i
ai
u. M
75
75
75
75
75
75
125
50
50
~
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ai
&
w
Wl
0.04
0.04
0.04
0.04
0.04
0.04
0.04
.
i
^
ai
«
1
50
50
50
SO
50
50
50
.
&
a
2f
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o
01
L. VI
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
0.1
f
cr
u
i
c
ai
u
|
0
0
9.23
9.23
9.23
9.23
9.23
9.23
9.23
c
o
t.
c
»- o
O "
4/1 M
0.201
0.176
0.256
0.287
0.953
0.962
1.039
0.712
0.953
0.544
1.161
0.490
1.134
0.980
0.848
0.916
I/I
^O E
""" u
£ *
II
0.146
0.127
0.186
0.205
0.698
0.679
0.742
0.508
0.684
0.405
0.874
0.312
0.767
0.693
0.493
0.654
*
•g
"°
U
*J
S
Ul
0
0
1.07
15.85
18.42
17.14
20.50
20.56
13.61
22.89
21.34
23.12
20 77
20.35
19.80
>*
3
—
•g
3
S
u
41
S
0.581
0.536
0.360
0.536
0.214
0.148
0.214
0.146
0.166
0.135
0.151
0.139
0.150
0.136
0.150
0.134
Cooments
069. A run at 18 kW Instead
of 24 kW.
Test stopped early.
v£>
(continued)
-------
TABLE B-l (continued)
s
VI
Ol
90
91
92
93
94
95
96
97
TEST CONDITIONS'
t.
w
Ml
m
a
A
B
A
B
A
B
A
C
A
C
A
C
A
C
A
C
Ol
*»
M
VI
01
t-
5/31
5/30
5/29
6/18
Ol
a.
|
TE
TE
TE
TE
TE
TE
c
i
•o
/
/
/
/
/
/
j?
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01
/
/
~
—
1.
01
1
u
a.
/
/
/
/
I
.
s
o
z
1
01
s
U.M
75
50
50
50
50
75
75
75
~
XI
01
Ol
CL
III
M
f IA
0.04
0
0
0
0
0
0
0.04
*•
u
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3
bO
0
0
0
0
0
0
0
CL
Jj
£
01
L. M
0.1
0.1
0.1
O.I
0.1
0.1
0.1
0.1
£
o1
u
1
*
zs
O) •
S3.
0
Wlf—
at
•II
l/t Wl
0.744
0.503
0.072
0.067
0.119
0.069
0.189
0.029
0.027
0.004
0.327
0.127
t/l
SI
s£
> JC
— "^
0.427
0.317
0.044
0.049
0.088
0.049
0.137
0.020
0.020
0.016
0.235
0.091
j
•g
1
U
L.
1
UJ
22.90
20.26
0
0
NA
NA
0
0
23.78
4.17
I/I
-
i
Ol
5
0.196
0.136
0
0
0
0
NA
NA
0.185
0.021
CoaiMnts
Hot run.
Primary condenser Mater went
off during test.
Not run.
Not run.
tn
vO
U)
(continued)
-------
TABLE B-l (continued)
i
M
4V
H-
98
TEST CONDITIONS*
t.
M
S
S
D«
Ee
S
Kt
•1
5/17
5/24
01
Solvent
HC
HC
e
Of
.,
'
5
Solvent
o
i.
condens
£•
a.
*j
^
u.
a
k.
Freeboa
X
TJ
Ol
*J
M
« «t
0
0
u
U
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3
0
0
i
01
1. IA
0.1
0.1
7r
I"
U
1
0
0
s
Ml
Exhaust
c
0
i.
01
"c
TEST RESULTS
JC
01
1
165.00
28.03
3™
01
tl
o
-g
C i—
O)
> c
AS
VI
tfifM
*-» U
j:
0.654
0.898
^
•"
c demand
|
UJ
0
0
t
01
i
i
•a
S
0
0
Comaents
en
vO
a Degreaser A and Degreaser B were operated under the same conditions except where differences are noted.
b Refrigerated freeboard chiller.
c Total load for Degreasers A and B: Load coil. 45.4 kg. basket. 22.7 kg.
Total load for Degreaser C: Load cot). 10 2 kg; basket. 2.3 kg.
d Solvent loss values for many of the Idle tests are based on Initial and final weight readings.
e Evaporation test In small containers. Containers D and E had 0.064 n2 and 0.018 m2 top opening area.
NA: Not available.
-------
TABLE B-la. TEST CONDITIONS AND RESULTS IN ENGLISH UNITS
(test period October 1978 to July 1979)
o
z
I/I
Ol
*~
1
2
3
4
5
6
7
8
TEST CONDITIONS' - -
i.
OJ
I/I
s
u
s
A
-
A
B
A
B
A
B
A
B
A
B
A
B
A
B
01
n
TJ
•J
Ul
01
10/10
10/12
10/16
10/19
10/27
11/3
11/12
11/13
A)
a
e
Of
3?
TE
TE
TE
TE
TE
TE
TE
TE
C
i
TJ
,
/
j
j
j
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e
2
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01
V
c
0
u
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,,
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o
.
£
0
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1
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50
50
50
50
50
50
50
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f
P
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i/» El
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0
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8
8
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m.
^
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0
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50
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20
20
20
20
20
20
20
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f.
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I
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a
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9.23
0
0
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9.23
9.23
9 23
c
o
u
ta
g
1
j
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/
c
0
u
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01
/
TEST RESULTS
*
£
1
01
I/I
01
IB. 23
20.95
15.67
15.67
21.83
21.83
19.27
19.27
17.50
17.50
3.07
3.03
24.00
23.91
14.fc7
14 88
1
Wl
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sr^
i. ai
I/I •—
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c
c £
OJ
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2.5U9
2.113
0.096d
0.096
0.179
0.096
0.10S
0.068
0.053
0.049
2.534
1.934
2.270
2.314
2.280
2.130
WIIM
tn w
O •*-
u
01
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oS
0.165
0.140
0.006
0 006
0.012
0.006
0.007
0 005
0.004
0.003
0.174
0.165
0.151
0.154
0 152
0.141
3
.
1
TJ
U
U
1
23.68
26.82
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
23.27
21.47
23.24
20.66
c
^
a
at
•a
i
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u
2
4.20
2.86
NA
NA
NA
NA
NA
NA
NA
NA
NA
NA
4.07
2.59
4.01
2.09
Comments
vO
tn
(continued)
-------
TABLE B-la (continued)
o
z
0>
9
10
11
12
13
14
15
16
TEST CONDITIONS "
t.
Ol
Wl
MB
Ol
k
s
A
B
A
B
A
B
A
B
A
B
A
B
A
B
A
B
S
•o
s
11/14
11/15
11/15
11/16
11/16
11/17
11/20
11/20
Ol
a.
^
|
s
TE
TE
TE
TE
TE
TE
TF
TE
e
Ol
•o
^
'
'
j
'
J
5
£
c
01
o
I/I
_,
'
J
/
/
J
1
J
k
Ol
M
c
01
T9
C
O
U
X
k
k
o.
/
'
'
/
/
/
'
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a
u
u_
cc
/
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/
/
/
,
oe
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^
u
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i
Ol
£
U. It
50
50
50
SO
50
50
50
50
^
^
VI
X *-
0
0
8
0
0
8
8
0
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m
<.
I
8
0
0
50
0
0
50
50
0
Ob
^
JJ
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0
Ol C
> ^
sc
20
20
20
20
20
20
20
20
20
f
A
w
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c
s
u
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2
0
0
0
0
0
9.23
2
2
0
C
o
k
*
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M.
UJ
j
J
'
/
/
/
'
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C
o
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ai
*c
TEST RESULTS
^
^
S
^
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s
7.93
7.92
7.10
7 08
7.05
7.10
7.15
7.20
7.07
6.05
5.72
5.93
8.03
6.33
6.95
6.93
1
1A
ai
Ol »
k ai
*^ a.
o
"~ c
*> 1-
C r-
Ol
5=5
i.ho*
0.940
1.456
2.765
2.920
1.858
0 321
2.149
0.704
0.876
3.330
1.430
1.092
1.237
1.440
1.210
IAOJ
III <->
O *-
w ai
C Ok
01
> f.
•— ^.
0.120
0.062
0.097
0.1B3
0.195
0.075
(0.013)
O.U2
0.047
0.058
0.222
0.095
0.073
0.102
0.096
0.080
3
"g
u
ll
Ul
21. bb
19.44
23.07
21.06
23.76
21.03
22.90
20.09
22.98
20.50
22.64
18.62
21.36
18.38
23.64
21.56
c
£
a
at
1
8
k
-------
TABLE B-la (continued)
i
s
17
18
19
20
21
22
23
24
25
TEST CONDITIONS a
u
01
lit
s
u
o?
a
A
B
A
B
A
B
A
B
A
B
A
B
A
D
A
A
B
S
a
•o
i/i
01
H-
11/21
11/21
11/22
11/26
12/21
12/22
1/15
Ol
•*
c
Ol
o
I/I
TE
TE
TE
TE
TE
TE
TE
c
Ol
B
/
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/
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5
—
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c
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5
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J
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t.
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i/l
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/
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m
ae
u.
o
s
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i
Ol
01
75
75
50
SO
75
100
50
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a.
VI
u E
0
8
8
8
8
8
8
^-
•X
3
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to
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0
50
50
70
SO
SO
SO
a.
£
S-
u
o
*oi c
> F-
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20
20
20
20
20
20
20
.1:
^
w ^
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c
s
u
•o
s
0
9.23
9.23
9.23
9.23
9.23
9 23
§
"
3
£
•— ^
0.071
0.044
0.143
0.119
0.162
0.153
0.18S
0.155
0.093
0.119
0.081
0.071
0.121
0.127
2
?
Tl
U
h
lu
24.84
22.51
22.64
20.53
22.67
20.99
24.06
20.15
22.88
20.57
21.53
18.85
24 55
20 79
c
I
01
i
•o
L.
Ol
•J
S
NA
NA
NA
NA
NA
NA
NA
2.61
6.88
2.45
4.31
1.92
3.85
Z.02
.
Comnents
Not run
Not run
(continued)
-------
TABLE B-la (continued)
o
„
Ol
1-
26
27
28
29
30
31
32
33
34
TEST CONDITIONS'
k.
01
IA
Of
L.
I
A
B
A
9
A
B
A
B
A
B
A
B
A
B
A
B
A
B
Al
«
£
1/18
1/19
1/20
1/21
1/26
1/25
1/28
1/29
1/31
Ol
*•
«
5
TE
TE
TE
TE
TE
TE
TE
TE
c
S
o
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'
/
J
J
/
s
J
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/
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5
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01
5
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/
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J
/
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^
L.
01
s
o
u
X
I
u
&
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/
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/
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a
tf
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/
j
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/
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0
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g
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SO
SO
125
125
125
125
125
100
125
75
50
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I
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W g
S£
8
8
8
8
8
8
16
16
16
16
8
*"
3
i.
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I
70
70
70
70
50
50
50
50
70
50
50
CL
%
2
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s£
20
20
20
20
20
20
20
20
20
20
20
£
0
1
OJ
tl
3
9.23
9.23
9.23
9.23
9.23
9.23
9 23
9 23
9.23
9.23
9.23
C
o
i.
«l
*••
3
ID
UJ
'
J
/
J
/
J
'
J
j
S
u
«
U
'
/
/
/
J
J
*
s
J
TEST RESULTS
JC
S1
01
^
M
24.23
24.20
24.25
24.10
24.26
25.40
26.40
24.07
16.28
18.87
IB 87
18.40
18.40
18.20
18.47
1
1.
i-*o7
•— ex
o
VI M
O
-g
1= "~
>"c *.
5 = 1
1.886
1.676
1.435
2 369
2.122
1.495
1.160
2.259
1.543
1.654
2.005
2.406
1.850
1.885
2 082
WIIM
VI **
*~ U
*> Ol
•1
•— V.
0.129
0.111
0.097
0.160
0.140
0.102
0.089
0.182
0.106
0.125
0.128
0.166
0.115
0.126
0.136
3
i
•o
u
£
Ul
NA
18.38
NA
NA
24.3
22.07
22.76
19.03
24.33
20.81
23.35
0.32
NA
NA
24.04
21.16
24.64
22.69
c
B
Ol
!
"*>
&
**
5
NA
2.13
NA
NA
2.03
2.19
3.01
2.0
2.63
2.03
1.56
1.32
NA
NA
1.26
1.32
2.16
1.26
Comnents
Extensive problems with
Degreaser A.
Results discarded.
Results discarded.
cn
v£>
(P
(continued)
-------
TABLE B-la (continued)
s
**
tn
01
1—
35
36
37
38
39
40
41
42
TEST CONDITIONS'
u
Of
«o
01
u
I
A
B
A
B
A
B
A
B
A
B
A
B
A
B
A
B
01
•S
s
2/2
2/4
4/1
4/2
4/4
4/5
4/11
4/12
01
&
X
c
Ol
s
TE
TE
HC
HC
HC
HC
HC
HC
HC
HC
HC
HC
HC
HC
C
1
E
/
J
J
/
/
/
/
/
5
4-*
1
5
/
/
j
/
/
/
/
/
/
1.
01
wt
c
w
0
u
a.
/
/
J
J
/
/
/
/
/
ae
J
/
/
U.
0
4-*
•o
•*>
I
Ol
01
i.
u. »t
50
50
50
50
50
50
SO
125
125
^.
~-
•o
u
a
M
5^
ZH-
16
8
16
8
8
8
B
8
8
-
^
n
01
i-
•o
s
so
50
70
50
50
70
70
50
50
a.
IO
X
u
y
"a c
* E
20
20
20
20
20
20
20
20
20
£
^
^
C
s
u
1
9.23
2
9.23
9 23
9.23
9.23-
9.23
9 23
9.23
c
o
i.
10
s
10
ul
j
'
/
^
/
/
/
/
/
c
o
1.
a
Ol
j
/
/
'
J
J
J
J
/
TEST RESULTS
£
£
If
ai
1
20.28
20.33
18.17
23.85
23.78
24 13
24.13
24.08
24 03
24.25
24.25
24.17
24.17
24.03
24 08
1
2
ft),—
trt •—
Ul tfl
O
*~ C
«-» •-
c •—
> C f
5^5
2.553
1.141
3.443
1 710
2 320
1 940
1.960
2.590
3.550
2.372
2.440
1.290
1.710
1.290
0 397
WMM
IA *>
O **•
*~ ^
*j ai
c a.
01
> £
0.163
0.070
0.229
0.114
0.153
0.129
0.121
0.172
0.234
0.158
0.160
0.086
0.115
0.086
0.059
3
•a
c
1
W
u
L.
*J
U
Of
UJ
24.07
21.30
24.67
12.00
14.40
13.00
15.36
12.00
14.40
12.99
15.38
12.56
14.42
13.04
15.44
c
-^
8.
"9
^
i_
0)
3
3.06
2.35
2.97
6.80
10.07
6.50
10.02
6.45
9.88
6.61
10.08
6. 85
10.41
6.64
10.11
Comments
Top on Degreaser B left
open between each cycle.
Degreaser B not used.
1C
vC
(continued)
-------
TABLE B-la (continued)
t
£
a
43
44
45
46
47
48
49
50
TEST CONDITIONS'
u
01
s
1
A
B
A
B
A
B
A
B
A
B
A
C
A
B
A
B
Ol
•o
**
Ml
01
1-
4/9
4/8
3/28
3/29
3/28
6/12
2/16
Ol
o.
c
Ol
"o
I/I
HC
HC
HC
HC
HC
HC
HC
HC
HC
tic
TE
TE
HC
HC
£
ex
o
•o
-J
J
J
/
;
/
/
jf
—
5
e
Ol
/
j
/
;
/
/
J
01
c
Of
o
u
a.
,
/
/
j
/
/
J
\
ac.
/
.
e
"•^
0
10
s
J
OJ
ai
u
b_ at
125
125
50
50
50
50
75
75
50
p
£
^C
*« i
o *-*
x **-
8
B
8
8
8
8
8
8
0
.1
S.
s
•a
|
70
70
50
50
50
50
50
SO
0
a.
^
*o
if
9
01 C
u ^
•- *4
20
20
20
20
52
20
20
20
^
i2
U
I
i
u
j
C
o
i.
4-1
Of
/
/
J
/
'
'
J
TEST RESULTS
^
£
Ol
c
—
Ol
h-
24.00
24.00
24.03
24.03
24 46
24.03
24.03
24.46
24.03
16.92
18 60
18.08
1
S
S*A
— a.
o
M M
C £
HI
1.550
2.140
1.330
1.290
4.260
3.600
4 b87
2.236
0.429
0.939
1.078
MCM
IA *J
Ot~
U
C S
a»
> f
0.103
0.142
0.089
0.085
0.281
0.240
0.143
0.328
0.146
0.028
0.065
0.073
2
.
•a
«j
s
12.19
14.39
12.92
15.33
12.89
12.69
14. 1<
NA
14.6!
4. Of
12.41
15.30
c
.i
12
Ol
i
i
^
i
6.63
10.08
6.64
10.0E
7.55
7.3!
9.9(
NA
10.9!
2.2!
7.27
7.26
Comments
Oeg. A: Lip exhaust at 100 ftfymtn
per ft2 top opening.
Deg. B: Not run.
Oeg. A: Lip exhaust at 50 ft3/mtn
per ft2 top opening.
beg. B- Crosscurrent test.
Not run.
Crosscurrent test.
Crosscurrent test.
Test of small degreaser.
Not run.
Not run.
cr>
o
o
(continued)
-------
TABLE B-la (continued)
o
z
I/I
Of
h-
51
52
53
54
55
56
57
58
TEST CONDITIONS"
t_
Ol
3
s
o
A
B
A
B
A
B
A
B
A
B
A
B
A
B
A
B
Ol
V
I/I
Ol
t-
2/25
2/22
2/25
2/27
3/2
3/1
41
a.
c
o
i/i
IIC
HC
HC
KC
HC
HC
PC
HC
c
£
o
/
J
/
Ol
c
i
e
at
o
«/t
,
/
u
at
e
01
o
,
/
^
/
u.
O£
j
/
»
ee
— -
0
•o
fc.
•o
1
01
e
u. »
50
50
50
50
50
50
f
~
1
i/i
e
O *J
0
0
0
0
0
0
•t
3
«
1
0
0
0
0
0
0
£
•~
2
1
*ai e
t!
20
20
20
20
20
20
^
•o
^
1
ot
u
O
0
0
0
0
0
0
c
o
Li
«o
•A
3
,
'
_^
x
/
•^
S
"
01
*c
/
/
/
x
/
J
TEST RESULTS
j.
5
i
4J
I/I
Ol
h-
19.73
19.73
20.68
20.68
43.63
42.87
21 12
20.98
25.08
25 01)
22.72
22.72
1
01
u
£**-!
i. U
o
vt ^~
l/l tA
o
«5
C r-
at
"o »- ^
Irt «!•—
0.644
0.7H5
0.314
0.479
0.328
0.243
0.573
0.257
0.526
0.860
1.427
(1.666
VIIM
I/I *J
*> 01
s11
> JC
Irt •—
0.043
0.052
0.32
0.21
0 022
0.018
0.038
0.017
0.035
0.225
0.095
0.045
2
?
u
^
S
UJ
12.35
14.55
0
0
0
0
0.69
0 938
0.789
1.092
12. 8E
15.27
c
]i
•jj
Ol
1
•o
U
s
s
B.95
11.54
0
0
1.2C
6.SE
8.01
18.51
2.8(
7.8!
6.77
8.0(
Garments
Solvent loss during cooldown
period.
Solvent loss during cooldown
period.
Not run.
Not run.
Not run.
Not run.
Solvent loss during cooldown
period.
(continued)
-------
TABLE B-la (continued)
o
se
fcl
lfl
Ol
H-
59
60
61
62
63
64
65
66
TEST CONDITIONS8
t.
Ol
IQ
Ol
s-
o
A
B
A
B
A
B
A
B
A
B
A
B
A
B
A
B
S
5
•J
l/l
at
h-
3/3
3/5
3/6
3/7
3/8
3/10
3/11
3/12
0*
o.
Zf
*J
c
Of
o
t/l
HC
HC
HC
HC
HC
HC
HC
HC
HC
HC
HC
MC
HC
HC
HC
HC
e
S.
o
•o
/
J
J
J
/
/
/
/
f
—
J
c
Ol
o
I/I
/
/
/
/
k.
Ol
c
if
o
u
*»
^
L.
OL.
/
/
/
/
/
/
/
a
ac
/
/
e?
o
ID
•O
i.
Q
1
SO
so
50
SO
SO
75
100
100
•£
"
'S
£
VI
5§
0
0
0
0
0
0
0
0
.
5
ID
I.
ID
O
_J
0
0
0
0
0
0
0
0
o.
ID
X
u
o
"o c
< «-
20
20
20
20
20
20
20
20
£
U
•o
OJ
c
ID
rj
XI
S
0
0
0
0
0
0
0
0
g
•a
%
m
C.
UJ
/
/
/
/
/
/
/
/
c
o
u
ID
Ol
c
/
/
/
/
/
/
/
/
TEST RESULTS
£
^r
g-
01
I
51.02
51.02
21. 5b
21.55
22.37
22 37
17.43
17.43
22.45
22.45
24.68
25.97
21.50
21.50
21 03
20.03
1
I
at »
"&
M •—
O
c •—
> c £
0.418
0.328
0.4S7
0.754
0.510
0.476
1.079
1.213
1.365
0.742
0.732
1.052
0.839
0.947
0.330
0.395
IflCM
O*-
££
01
> £
•— ^
0.027
0.022
0.031
0.050
0.034
0.030
0.071
0.078
0.091
0.051
O.OS
0.072
O.OS5
0.064
0.022
0.026
3
1
|
U
u
I
UJ
0
0
0.82
1.12
0
0
12.30
14.51
12.97
14.91
12.25
14.51
12.34
14.56
0
0
C
1
o»
i
i
T>
t.
Ol
3
2.52
6.31
2.48
6.65
0
0
6.61
7.44
7.76
9.23
7.76
9.19
7.77
9.19
7.76
9.16
.
Corments
Solvent loss during cooldown
period.
(continued)
-------
TABLE B-la (continued)
s
IA
01
1-
67
68
69
70
71
72
73
74
TEST CONDITIONS'
Of
trt
.
0
*u c
i
l_ ^^
20
20
20
20
84
52
20
20
f
U
W
u
s
0
0
0
0
0
0
0
0
9.23
9.23
c
o
t.
^J
3
X
UJ
/
/
/
'
,/
J
/
e
O
41
01
"c
/
/
/
J
/
J
/
TEST RESULTS
f
£
If
01
VI
Of
h-
14.07
24.95
24.17
23.25
19.65
19.65
71.23
71 23
14.08
14.08
27 27
27.27
24.05
24.05
in
£
Ot •
U «f
I/I M
Sg
** —
c •-
01
> Cf
•~ °~>
O f &
Ifl Mr—
0.709
0.596
0.425
0.563
0.799
1.221
0.89'
0 675
0.582
4.076
5 090
8.304
1.336
1.917
WICM
Ut f
U
*• 01
c a.
OJ
> JC
55
0.047
0.034
0.028
0.037
0.053
0.08
n.nco
0.044
0.039
0.271
0.33
0 549
0.089
0.128
a
i
1
•o
u
UJ
12.91
14.74
0.36
1.09
12.35
14.55
0
0
0.35
0
12.90
14.38
12.20
14.38
C
I
3,
i
i
•o
01
«-»
s
7.44
8.81
5.86
9.18
6.50
9.17
4.53
6.20
0
0
7.78
9.08
6.63
10.07
Comments
Solvent loss during cool down
period.
Deg. A: Lip exhaust at 16 ft3/m1n pe
ft' of top opening; Deg. B: Cross-
current test.
Den. A: Lip exhaust at 100 ft3/m1n p
ft" of top opening; Deg. B: Cross-
current test.
Not run.
Crosscurrent test. Not run.
o
OJ
(continued)
-------
TABLE B-la (continued)
£
ut
01
1-
75
76
77
78a
78b
79
80
81
TEST CONDITIONS1
01
VI
Ol
L.
O
A
B
A
B
A
B
A
B
A
B
A
B
A
B
A
B
Ol
0
•o
01
4/17
4/25
4/26
5/8
5/9
5/10
5/11
5/14
41
CX
C
41
S
HC
HC
HC
MC
HC
MC
HC
HC
c
1
ts
/
J
/
/
£
I
C
41
O
/
^
;
L.
Ol
c
Ol
0
u
_
u
Q.
/
J
J
J
/
/
/
/
/
tt
/
•£
0
*J
HI
t.
•o
1
41
£..
75
75
75
75
75
50
50
125
100
75
X
—
1
VI
c
wi E
O **
X "•-
8
0
0
0
0
0
0
0
0
0
»
^
S
L.
r-
C r-
01
> C JC
»/l irt»-
1.603
1.299
1 660
1 28C
2 147
4.923
0.221
0.240
0.154
0.252
0.501
0.426
0.446
0.372
0 245
0.364
MUM
tn »*
2*"
1^
O JQ
1.07
0.085
0.109
O.OBS
0.142
0.326
0.015
0.016
0.01P
0.017
0 033
0.028
0.030
0.025
0.016
0.024
j
•g
1
£
•a
u
&.
Ul
12.96
15.35
12.82
14.52
13.11
14.59
0
0
0
0
0
0
0
0
0
0
c
I
8.
•
I
-o
L.
41
oVJ
S
6.62
10.06
6.78
10.25
6.83
6.63
8.18
7.57
8.16
7.56
9.50
9.20
9.60
8.80
9.30
8.70
Comments
Deg. A: Lip exhaust at 50
ftJ/mtn per ft2 top opening.
Oeq. A; Lip exhaust at 100 ft3/m1n
per ft' top opening; Deg. B: Cross-
cur'»nt test.
Inlet air was turned on about 3 hours
after test started.
(continued)
-------
TABLE B-la (continued)
s
*>
,2
82
83
84
85
86
87
88
89
TEST CONDITIONS'
i.
Ol
s
1
A
B
A
B
A
8
A
B
A
B
A
B
A
B
A
B
3
•3
*•
*i
01
5/15
5/16
5/22
5/23
5/23
5/24
5/25
5/25
g
w
c
01
MC
HC
TE
TE
TE
TE
TE
TE
c
QJ
O.
O
_J
/
/
J
/
/
/
/
/
/
f
S""
c
Ol
"o
J
/
/
/
/
/
/
01
lA
c
Ol
0
u
o.
/
/
/
/
/
/
/
/
/
a
S
/
/
/
J
m
C?
o
*J
f
S
*ol c
^- 4-1
20
20
20
20
20
20
20
20
20
JC
u
c
"u
1
0
0
9 21
9.23
9.23
9.23
9.?1
9 23
9.23
c
o
i.
*
3
«
£
X
UJ
/
/
/
/
/
/
/
/
/
c
o
u
V
01
c
/
/
/
/
/
/
/
TEST RESULTS
a
JC
S1
Of
1
19.40
19.40
22.93
22.93
24.05
24 05
1.40
1.40
19.95
19.95
8.03
8.03
8.167
8.167
8.00
8.00
1
£
a* •
L. 01
I/I tA
O
"~ c
I1"
III
0.443
0.387
0.563
0.632
2.085
2.190
2 286
1.571
2.104
1.201
2.455
1.082
2.504
2.163
1.C69
2.022
•AN
M **
S*"
"" i.
!£
> j:
0.030
0.026
0 038
0.042
0.143
0.139
0.1<2
0.104
0.140
*
i
1
T>
U
*J
a
UJ
0
0
1.07
15.05
18.42
17. K
29.5
23.56
0.083 |19-6'
0.179
0.064
0.157
0.142
0.101
0.134
22.69
21.3'
23.12
20.77
20.35
19.8
c
1
s.
i
•o
L.
O)
4-1
5
9.20
8.50
5.70
8.50
3.40
2.34
3.39
2.32
2.63
2.14
2.40
2.20
2.38
2.16
2.37
2.12
Comments
Deg. A run at IB kW Instead
of 24 kW.
Test stopped early.
o
1/1
(continued)
-------
TABLE B-la (continued)
as
I/I
a*
t—
90
91
92
93
94
95
96
TEST CONDITIONS3
,.
IQ
Ol
J^
A
B
A
B
A
B
A
C
A
C
A
C
A
C
01
Tl
Ol
t—
5/31
5/30
5/29
6/18
7/19
Ol
5
c
Ol
5
TE
TE
TE
TE
TE
TE
e
Of
A
o
•o
/
/
/
/
/
/
1"
—
i
c
Ol
o
*/»
/
/
i.
lA
C
ft)
1
o
u
t.
ID
E
i
/
/
/
/
u.
K
.
l<
75
50
50
50
50
75
75
75
~
01
c
!£
8
0
0
0
0
0
0
0
f
£
s
•o
s
50
0
0
0
0
0
0
0
a.
•—
r-
e
i. -^
20
20
20
20
20
20
20
20
^
""
•D
C
•g
i
u
01
3.11
2.16
0
0
0
0
NA
NA
2.93
0.33
torments
Not run.
Primary condenser water went
off during test.
-------
TABLE B-la (continued)
t
o
z
*rf
«/l
01
t-
97
98
TEST CONDITIONS"
k.
Ol
<0
Ol
k
en
A
C
oe
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01
^
w
01
5/17
5/24
01
s
c
Ol
o
I/I
HC
HC
c
0.
o
•o
/
0.
*~
s
c
Ol
*o
1/1
i.
s
01
0
u
k.
1
0.
^
oe
.
e
0
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2
•D
O
1,.
>
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1
1/1 c
!§
0
0
.h
i
•V
Ol
«
•o
s
0
0
a
IO
s-
i
01 C
> .-
«c «-
20
20
"*fc
A
\j
•o
i
u
•Q
3
0
0
c
o
L.
•a
3
X
UJ
S
*j
OJ
TEST RESULTS
^
^
en
c
^
i/i
ai
165.00
28.03
i
u
li
o
I/I —
° c
C r-
> c -c
o2£
M(M
Wl *-•
"~ L.
c ex
01
•— ***
0.134
0.184
j*
-o
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•o
u
u
tJ
u
Ol
UJ
0
0
c
.i
S.
1
i
"O
OJ
0
0
Comments
Not run.
8 Oegreaser A and Degreaser B were operated under the same conditions except where differences are noted
Refrigerated freeboard chiller.
c Total load for Degreasers A and B. Load coll, 100 Ib; basket, SO Ib.
Total load for Degreaser C. Load coil, 22.5 Ib, basket, 5 Ib.
d Solvent loss values for many of the Idle tests are based on initial and final weight readings.
e Evaporation ttst In small containers. Containers 0 and E had 0 69 ft and 0.194 ft top area.
NA- Not available.
-------
APPENDIX C
STATISTICAL COMPARISONS BY TEST OF SIGNIFICANCE*
THE TEST OF NULL HYPOTHESIS (TEST OF SIGNIFICANCE)
A null hypothesis is a specific hypothesis about a popula-
tion that is being tested by means of the sample results. A
test of significance is a calculation by which the sample
results are used to throw light on the truth or falsity of a
null hypothesis. A quantity called a test criterion is com-
puted; it measures the extent to which the sample departs from
the null hypothesis in some relevant respect. If the value of
the test criterion falls beyond certain limits into a region of
rejection, the departure is said to be statistically signifi-
cant. Tests of significance have the property that if the null
hypothesis is true, the probability of obtaining a significant
result has a known value, most commonly 0.05. This probability
is the significance level of the test.
Of course, the test of significance is not an automatic
rule for making a decision to either accept or reject a null
hypothesis. Knowledge accumulated through the work should be
added to the evidence of the test.
This analysis is based on standard statistical methods. See
Svedecov, G. W., and W. G. Cochran. Statistical Methods.
The Iowa State University Press, Ames, Iowa, 1967.
608
-------
In this appendix, the test is used to determine the sig-
nificance of differences between the rates of solvent loss from
Degreaser A and Degreaser B, between rates obtained with the use
of refrigerated freeboard chillers, and between rates obtained
with the different solvents.
TEST OF SIGNIFICANCE APPLIED TO DEGREASER A AND DEGREASER B (TWO
SAMPLES TREATED AS INDEPENDENT)
Data Points From Tests Using 1,1,1-Trichloroethane
Data points representing solvent loss are shown in Table
C-l.
Pooled estimate of variance (with samples of same size,
n = 13):
C2 _ ,S!2 + S22t _ (0.436)2 + (0.390)2
s - ( 2 ) - 2
= 0.171
Number of degrees of freedom = 2(n-l) = 2(13-1) = 24
Standard deviation of differences:
¥• =/
2 x 0.171
X! - x2 * n v 13
= 0.162
Student ft' = x* ~ *2 = Tz = 0.488
b U
_
Xi - X2
From statistical tables, it is known that an absolute value
of t = 0.685 is exceeded 50 percent of the time. The test thus
provides no evidence upon which to reject the null hypothesis
that the difference between Degreaser A and Degreaser B in rate
of solvent loss is zero.
609
-------
TABLE C-l. TEST OF SIGNIFICANCE APPLIED TO
DEGREASERS A AND B USING 1,1,1'TRICHLOROETHANE
Test
Group
No.
1
2
3
4
5
24
25
26
27
28
29
30 and 33
31 and 32
Solvent loss rate, kg/h
From Degreaser A:
xl
1.04
1.28
0.97
0.55
1.08
0.82
0.05
0.32
0.05
0.66
0.49
0.12
0.07
From Degreaser B:
x2
1.00
1.04
0.75
0.47
0.96
0.43
0.05
0.40
0.03
0.90
0.30
0.07
0.07
Difference:
Xl"x2
0.04
0.24
0.22
0.08
0.12
0.39
0
-0.08
0.02
-0.24
0.19
0.05
0
No. of observa-
tions (n)
Mean
Std. deviation
d-f
13
= 0.577
= 0.436
12
13
x2 = 0.498
S2 = 0.390
12
Xl"x2 = °'079
S3 = 0.159
610
-------
Data Points From Tests Using Methylene Chloride
Data points representing solvent loss are given in Table
C-2.
Fooled estimate of variance (with samples of same size,
n = 10):
S2 = (0.209)2 + (0.336)2 = 0
xl ~ X2
S = / "\"^'<*t - 0.125
xl ~ X2
Number of degrees of freedom = 2(10-1) = 18
Student 't' = *1 " *2 = "p' = -°-904
xl ~ X2
From statistical tables, it is known that an absolute value
of t = 0.865 is exceeded 45 percent of the time. The test thus
provides no evidence upon which to reject the null hypothesis
that the difference between Degreaser A and Degreaser B in rate
of solvent loss is zero.
TEST OF SIGNIFICANCE APPLIED TO REFRIGERATED FREEBOARD CHILLERS
The test of significance lacks validity in the following
two cases because only two or three data points are available.
It is given here, however, for the limited purpose of comparing
results obtained with refrigerated freeboard chillers.
Table C-3 presents data points from tests using Refriger-
ated Freeboard Chillers I and II.
For d-f = 3, the 't1 values in the critical region at 95
percent confidence level are -3.182
-------
TABLE C-2. TEST OF SIGNIFICANCE APPLIED TO DEGREASERS
A AND B USING METHYLENE CHLORIDE
Test
Group
No.
34
35
36
37
38
43
44
45
46
47
Solvent loss rate, kq/h
From Degreaser A:
xl
0.78
0.61
0.59
1.17
0.70
0.88
0.73
0.59
1.08
0.60
From Degreaser B:
x2
1.05
0.87
0.78
1.61
0.97
0.89
0.59
0.41
1.10
0.59
Difference:
Xl - X2
-0.27
-0.26
-0.19
-0.44
-0.27
-0.01
0.14
0.18
-0.02
0.01
No. of observa-
tions (n)
Mean
Std. deviation
d-f
10
= 0.773
= 0.209
9
10
x2 = 0.886
S2 = 0.336
x^) = -0.113
S = 0.202
612
-------
TABLE C-3. TEST OF SIGNIFICANCE APPLIED TO REFRIGERATED FREEBOARD
CHILLERS I AND II (TREATED AS PAIRED SAMPLES)
Test
Group
No.
16
17
18
20
Solvent loss rate, kq/h
From RFC I:
xl
0.99
0.96
0.68
0.76
From RFC II:
x2
0.92
0.82
0.53
0.66
Difference:
Xl -X2
0.07
0.14
0.15
0.10
Mean 0.848 0.733 0.115
Std. deviation 0.151 0.172 0.037
613
-------
_ Z(xt - Xg) = I(X! - xg)
Sj /•>} n nSj /V n
°-115 = 1.554
4. -
0.037
The computed t = 1.554 is not within the critical region;
therefore, it can be concluded that there is no significant
difference between the two types of chillers at 95 percent con-
fidence limits.
Table C-4 presents data points from tests using RFC II at
the two temperature ranges.
For d«f = 2, the 't1 values in the critical region are
-4.303
-------
TABLE C-4. TEST OF SIGNIFICANCE APPLIED TO REFRIGERATED FREEBOARD
CHILLER II BEFORE AND AFTER CORRECTION (TREATED AS PAIRED SAMPLES)
Test Group
No.
16 and 21
17 and 22
18 and 23
Solvent loss rate (kg/h) from
Refrigerated Freeboard Chiller II
Before
correction:
xl
0.92
0.82
0.53
After
correction:
x2
0.98
0.54
0.49
Difference:
Xl -X2
-0.06
0.28
0.04
Mean 0.76 0.67 0.087
Std. deviation 0.203 0.27 0.175
615
-------
TABLE C-5. TEST OF SIGNIFICANCE APPLIED TO SOLVENTS
1,1,1-TRICHLOROETHANE AND METHYLENE CHLORIDE
IN DEGREASER A
Test Group
No.
1 and 34
2 and 37
3 and 35
5 and 38
16 and 43
17 and 44
18 and 45
20 and 47
24 and 48
30 and 61
Solvent loss rate, kg/h
Using TE:
Xl
1.04
1.28
0.97
1.08
0.99
0.96
0.68
0.76
0.82
0.12
Using MC:
X2
0.78
1.17
0.61
0.70
0.88
0.73
0.59
0.60
0.44
0.20
Difference:
xi - x2
0.26
0.11
0.36
0.38
0.11
0.23
0.09
0.16
0.38
-0.08
No. of observa-
tions (n)
Mean
Std. deviation
d • f
10 10
0.87 x2 = 0.67
0.314 S2 = 0.258
9 9
- x2 = 0.2
S = 0.15
616
-------
Standard deviation of differences:
2S2 _ /2(0.083) _
— - v 10 -
Student 't' = i " 2 = = !-55
x - x
1 2
From statistical tables, it is known that an absolute value
of t = 1.734 is exceeded 10 percent of the time.
Data Points From Tests Conducted On Degreaser B
Data points representing solvent loss are shown in Table
C-6.
Pooled estimate of variance (with ten samples):
S2 = S!2 + S22 = (0.707)2 + (0.758)2 = Q 53?
Number of degrees of freedom = 2(n-l) = 2(10-1) = 18
Standard deviation differences:
c - /2S1 _ 72(0.537)'
b - ~ v— - V n
10
= 0.328
Xj - X2
Student 't' = ' " * = "' = -0.156
xl ~ X2
From statistical tables, it is known that an absolute value
of t = 0.257 is exceeded 80 percent of the time. The test thus
provides no evidence upon which to reject the null hypothesis
that the difference between solvent loss rates using trichloroe-
thane and methylene chloride is zero.
617
-------
TABLE C-6. TEST OF SIGNIFICANCE APPLIED TO
SOLVENTS 1,1,1-TRICHLOROETHANE AND METHYLENE CHLORIDE
IN DEGREASER B
Test Group
No.
1 and 34
2 and 37
3 and 35
5 and 38
21 and 43
22 and 44
23 and 45
19 and 46
20 and 47
24 and 48
33 and 61
Solvent loss rate, kq/h
Using TE:
Xl
1.00
1.04
0.75
0.96
0.98
0.54
0.49
0.86
0.66
0.43
0.07
Using MC:
X2
1.05
1.17
0.87
0.97
0.89
0.59
0.41
1.11
0.59
0.54
0.15
Difference:
Xl - X2
-0.05
-0.13
-0.12
-0.01
0.09
-0.05
0.08
-0.25
0.07
-0.11
-0.08
No. of observa-
tions (n)
Mean
Std. deviation
d • f
11 11
= 0.707 X2 = 0.758
= 0.303 S2 = 0.324
9 9
Xi • x2 = 0.051
S3 = 0.104
618
-------
APPENDIX D
SUMMARY OF COST ANALYSIS
619
-------
TABLE D-l SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
OR RETROFIT Test Group 1
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
50
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:fl
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
0
0
2000
0
0
4000
0
0
6000
0
0
Value in parentheses represents loss or expenditure.
620
-------
TABLE D-2 SUMMARY OF SAVINGS
FROM MODIFICATION OF
OR EXPENDITURES RESULTING
DEGREASER (NEW)
Test Group
Conditions
Solvent
Freeboard ratio (FR), «
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
75
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost. S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
230.00
0
0
230.00
2000
140
dan
33.75
9.20
d.fin
n
n
98.76
338.63
51.20
291.08
1.08
6.12
39.22
8.90
6
4000
280
Qfin
33.75
9.20
d.fifl
n
n
197.53
677.26
149.98
629.70
3.15
13.24
16.32
4.25
6
6000
420
1440
33.75
Q.?n
a. fin
n
n
296.30
1015.89
248.75
968.34
5.23
20.34
10.30
2.79
6
Value in parentheses represents loss or expenditure.
Includes $80.00 for worker platform revisions.
621
-------
TABLE D-3 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 3
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
75
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:3
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
355.00°
2000
140
480
52.10
14.20
7.10
0
0
98.77
338.63
25.37
265.23
0.35
3.61
77.52
14.45
6
4000
280
960
52.10
14.20
7.10
0
0
197.53
677.26
124.13
603.86
1.69
ft. 23
27.71
6.73
6
6000
420
1440
52.10
14.20
7. in
0
0
296.30
1015.89
222.90
942.49
3.04
12. R4
16.87
4.38
6
Value in parentheses represents loss or expenditure.
Includes $80.00 for worker platform revisions.
622
-------
TABLE D-4 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 4
Conditions
Solvent
Freeboard ratio (FR), ",-
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Tnchloroethane
100
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimurr.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, j
300. 00b
2000
980
1060
44.03
i? nn
6. on
n
0
691.37
747.80
629.34
685.77
10.15
11.06
5.50
5.06
12
4000
1960
2120
44.03
12. on
fi.nn
n
n
1382.74
1495.62
1320.71
1433.59
21.29
23.11
.68
2.47
12
6000
2940
3180
44.03
i?.nn
fi nn
n
n
2074.11
2243.42
2012.08
2181.39
32.44
35.17
1.77
1.63
12
Value in parentheses represents loss or expenditure.
Includes $100.00 for worker platform revisions.
623
-------
TABLE D-5 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 4
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
100
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), S/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
450. 00b
2000
980
1060
66.04
iR.nn
q nn
n
n
691.37
747.80
RQR 33
654.76
6.43
7.04
8.49
7.80
2
4000
1960
2120
66.04
iR.nn
Q.nn
n
0
1382.74
1495.62
l?RQ.7n
1402.58
13.86
15.07
4.07
3.75
12
6000
2940
3180
66.04
iR.nn
q.nn
n
0
2074.11
2243.42
1QR1.07
2150.38
21.29
23.11
2.68
2.47
12
a Value in parentheses represents loss or expenditure.
Includes $100.00 for revision of worker platform.
624
-------
TABLE D-6 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 16
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
50
Type I @ 1 to 2°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
3300.00
3300.00
2000
100
484.31
132.00
66.00
0
222.53
70.55
(834.29)
(0.92)
-
0
4000
200
484.31
132.00
66.00
0
222.53
141.10
(763.74)
(0.84)
-
0
6000
300
484.31
132.00
66.00
0
222.53
211.64
(693.20)
(0.77)
-
0
Value in parentheses represents loss or expenditure.
625
-------
TABLE D-7 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 16
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), °*
Others
1,1,1-Trichloroethane
50
Type I
-------
TABLE D-8 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 16
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
50
Type II @ -23 to -32°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
3718.00
0
0
3718.00
2000
160
545.65
148.72
74.36
0
341.44
112.88
-
(997.291
-
(0.90)
_
0
4000
320
545.65
148.72
74.36
0
341.44
225.75
-
(884.42)
-
(0.80)
_
0
6000
480
545.65
148.72
74.36
0
341.44
338.63
-
(771. $&}
-
(0.69)
_
0
a Value in parentheses represents loss or expenditure.
627
-------
TABLE D-9 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 16
Conditions
Solvent
Freeboard ratio (FR), £
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
50
Type II @ -23 to -32°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:3
Minimuir,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3718.00
3622.00
0
7340.00
2000
_
160
1077.22
293.60
Mfi.RO
n
344.44
112.88
.
(1749.18)
—
(0.94)
-
-
0
4000
—
320
1077.??
293.60
146. 80
0
344.44
225.75
(1636.30)
.
(0.88)
-
-
0
6000
—
480
1077.??
293.60
146. RO
n
344.44
338.63
(1523.43)
.
(0.82)
-
-
0
a Value in parentheses represents loss or expenditure.
628
-------
TABLE D-10 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group
17
Conditions
Solvent
Freeboard ratio (FR), 1-
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), i
Others
1,1,1-Tnchloroethane
75
Type I @ 1°C to 2°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), S/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
.•nnn.no
0
0
3300.00
2000
_
180
484.31
132.00
fifi.OO
n
??2.53
126.99
-
(777.85)
.
(0.86)
-
_
6
4000
_
360
484.31
132.00
66.00
0
222.53
253.97
-
(650.87)
.
(0.72)
-
6
6000
_
540
484.31
132.00
66.00
0
222.53
380.96
-
(523.88)
.
(0.58)
-
„
6
a Value in parentheses represents loss or expenditure.
629
-------
TABLE D-ll SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group
17
Conditions
Solvent
Freeboard ratio (FR), «
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), *
Others
1,1,1-Trichloroethane
75
Type I @ 1° to 2°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:3
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
3300.00
700.00
0
4000.00
2000
.
180
586.24
160.00
80.00
n
225.53
126.99
(922.58)
(0.88)
-
6
4000
.
360
586.24
160.00
80.00
0
222.53
253.97
(795.60)
(0.76)
-
6
6000
.
540
586.24
160.00
an. no
n
222.53
380.96
(668.61)
(0.64)
-
6
Value in parentheses represents loss or expenditure.
630
-------
TABLE D-l2 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 17
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Tnchloroethane
75
Type II @-23 to -32°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/y:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, °*
3948. 00b
o
n
3948.00
2000
—
360
579.41
157.92
7R Qfi
n
341.44
126.99
-
(1030.74)
-
(0.89)
-
_
6
4000
—
720
579,41
157.92
7R Qfi
n
341.44
253.97
-
(903.76)
-
(0.78)
-
_
6
6000
—
1080
579.41
157.Q?
7R Qfi
n
341.44
380.96
-
(776.79)
-
(0.67)
-
_
6
a Value in parentheses represents loss or expenditure.
Includes $80.00 for revision of worker platform.
631
-------
TABLE D-13SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 17
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
75
Type II @ -23 to -32°C
Annual operating hours
Solvent savings (loss), k9/yr:a
Minimurr.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
3948. 00b
•}fi?2 nn
7570.00
2000
—
360
1110.97
302.80
151.40
0
341.44
126.99
-
(1779.62)
(0.93)
-
6
4000
—
720
1110.97
302.80
151.40
0
341.44
253.97
-
(1652.64)
(0.87)
-
6
6000
—
1080
1110.97
302.80
151.40
0
341.44
380.96
-
(1525.65)
(0.80)
-
6
a Value in parentheses represents loss or expenditure.
Includes $80.00 for revision of worker platform.
€32
-------
TABLE D-14SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 21
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Tnchloroethane
50
Type II (3 -29 to -40°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimurr.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, c;
3718.00
0
0
3718.00
2000
40
545.65
148.72
74.36
0
341.44
28.22
-
(1081.95)
-
(0.97)
-
_
0
4000
80
545.65
148.72
74.36
0
341.44
56.44
-
(1053.73)
-
(0.95)
-
—
0
6000
120
545.65
148.72
74.36
0
341.44
84.66
-
(1025.51)
-
(0.92)
-
_
0
Value in parentheses represents loss or expenditure.
633
-------
TABLE D-15SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 21
Conditions
Solvent
Freeboard ratio (FR), £
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Tnchloroethane
50
Type II ? -29 to -40°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimurr,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3718.00
3622.00
0
7340.00
2000
40
1077.22
293.60
146.80
0
341.44
28.22
-
4000
80
1077.22
293.60
146.80
0
341.44
56.44
-
(1830.84) 1(1802.62)
-
(0.98)
_
0
-
(0.97)
_
0
6000
120
1077.22
293.60
14fi.RO
0
341.44
R/Lfifi
-
(1774.40)
-
(0.95)
_
0
Value in parentheses represents loss or expenditure.
634
-------
TABLE D-16SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 22
Conditions
Solvent
Freeboard ratio (FR), «
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
25
Type II @-29 to -40°C
0.04
50
Annual operating hours
Solvent savings (loss), k9/yr:a
Minimuir.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. 5:
3948.00
3948.00
2000
900
579.41
157.92
78.96
n
341.44
634.93
(522.80)
_
(0.551
-
6
4000
1800
579.41
157.92
78.96
n
.141.44
IPfiQ 86
112.13
—
0.10
_
107.40
6
6000
2700
579.41
157.92
78. Q6
n
341.44
1904.79
747.06
—
0.65
_
44 m
6
a Value in parentheses represents loss or expenditure.
635
-------
TABLE D-l7SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 22
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Tnchloroethane
75
Type II 0 -29 to -40°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimuir,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
3948.00
3622.00
0
7570.00
2000
—
qnn
1110.97
302.80
151.40
0
341.44
-
634.93
(1271.68)
(n.fi?)
-
_
6
4000
—
iftnn
1110.97
302.80
151.40
0
341.44
-
1269.86
(636.75)
(0.33)
-
_
6
6000
—
??nn
1110.97
302 . 80
151.40
0
341 . 44
-
1Q04.79
(1.82)
0.00
-
_
6
a Value in parentheses represents loss or expenditure.
636
-------
TABLE D-18SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group
18
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
125
Type I G> 1 to 20°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, $
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3660. 00b
0
0
3660.00
2000
720
579.41
157.92
78.96
0
341.44
507.95
-
(590.23)
(0.54)
-
—
17
4000
1440
579.41
157.92
78.96
0
341.44
1015.89
-
(82.29)
(0.07)
-
—
17
6000
.
2160
579.41
157.92
78.96
0
341.44
1523.84
-
425.66
0.39
-
60.11
17
Value in parentheses represents loss or expenditure.
Includes $120.00 for revision of worker platform.
637
-------
TABLED-19 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 18
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
125
Type I @ 1 to 2°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), S/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, 5;
3820. 00b
700.00
0
4520.00
2000
_
720
fifiT ?fi
lan.Rn
qn.an
n
79? ^
507.95
(649.14)
(0.56)
-
_
17
4000
_
1440
fifiT ?fi
lan.an
qn.an
n
???.R3
1015.89
(141.20)
(0.12)
-
_
17
6000
_
2160
fifi3.?fi
i sn. sn
qn.an
n
77?.^-\
1523.84
366.75
0.32
-
72.96
17
a Value in parentheses represents loss or expenditure.
Includes $120.00 for revision of worker platform.
. 638
-------
TABLE D-20 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 18
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), *
Others
1,1,1-Trichloroethane
125
Type II @ -23 to -32°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
4078. 00b
0
0
4078.00
2000
_
940
598.49
163.12
81.56
0
341.44
fifil.lR
—
(521.46)
-
(0.44)
-
_
17
4000
_
1880
598.49
163.12
81.56
0
341.44
•n?fi_3n
.
141.69
-
0.12
-
101.63
17
6000
_
2820
598.49
163.12
81.56
0
341.44
1Qflq.4R
—
804.84
-
0.68
-
42.75
17
Value in parentheses represents loss or expenditure.
Includes $120.00 for revision of worker platform.
639
-------
TABLE D-21 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 18
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), *
Others
1,1,1-Trichloroethane
125
Type II G> -23 to -32°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:3
Minimurr,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, °K
4238.00
3fi??.nn
n
7860.00
2000
„
940
1153.53
314.40
157.20
0
341.44
663.15
-
(1303.42}
-
(0.66)
_
17
4000
_
1880
1153.53
314.40
157.20
0
341.44
1326.30
-
(640.27)
-
(0.33)
_
17
6000
-
2820
1153.53
314.40
157.20
0
341.44
1989.45
-
22.88
-
0.01
-
139.14
17
Value in parentheses represents loss or expenditure.
Includes $120.00 for revision of worker platform.
640
-------
TABLE D-22 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 23
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
125
Type II @-29 to -40°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:3
Minimum
Maximum
Capital cost, $
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3660.00
0
0
3660.00
2000
1020
537.14
146.40
73.20
0
222.53
71Q.RQ
-
(P.RQ.fiR)
(0.27)
-
_
17
4000
2040
537.14
147.40
73.20
0
222.53
1439.18
-
4RQ Q1
0.47
-
57.42
17
6000
3060
537.14
147.40
73.20
0
222.53
2158.77
-
•mq.sn
1.20
-
29.59
17
Value in parentheses represents loss or expenditure.
641
-------
TABLE D-23SUMMARY OF SAVINGS
FROM MODIFICATION OF
OR EXPENDITURES RESULTING
DEGREASER (RFTROFIT)
Test Group 23
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
125
Type II 0 -29 to -40°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimurr,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), S/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximunr,
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3948.00
3fi?? . nn
7570.00
2000
—
1020
1110.97
302.80
151.40
n
341.44
71Q 5Q
-
(1187.02)
-
0.62
-
—
17
4000
—
2040
1110.97
302.80
151.40
0
341.44
143Q.1R
(467.43)
-
(0.25)
-
.
17
6000
_
3060
1110.97
302.80
151.40
0
341.44
P15R.77
252.16
-
0.13
-
102.88
17
a Value in parentheses represents loss or expenditure.
642
-------
TABLE D-24 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 2
Conditions
Solvent
Freeboard ratio (FR), «
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
50
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimuir,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss). S/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, 5;
78.00b
n
n
78.00
2000
(100)
(480)
11.41
3.21
1.56
0
0
(70.55)
(338.63)
(86.68)
(354.76}
(5.37)
(22.00)
-
_
0
4000
(200)
(960)
11.41
3.21
1.56
0
0
(141.10)
(677.26)
(157.23)
(693.39)
(9.75)
(42.99)
-
_
0
6000
(300)
(1440)
11.41
3.21
1.56
0
0
(211.64)
(1015.89)
(227.77)
(1032.02)
(14.12)
(63.43)
-
_
0
Value in parentheses represents lo*s or expenditure.
Additional expenditure required for larger basket over standard basket.
643
-------
TABLE D-25SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 2
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
50
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
242. 00b
0
0
242.00
2000
—
480
35.52
9.68
4.R4
n
0
(70.55)
(338.63)
(120.59)
(388.67)
(2.41)
(388.70)
-
_
0
4000
—
960
35.52
9.68
4.84
0
0
(141.10)
(677.26)
(191.14)
(727.30)
(3.82)
(14.54)
-
_
0
6000
_
1440
35.52
9.68
4.84
0
0
(211.64)
(1015.89)
(261.68)
(1065.93)
(5.23)
(21.30)
-
_
0
Value in parentheses represents loss or expenditure;
Cost of new basket, 20 percent larger than recommended.
644
-------
TABLE D-26SUMMARY OF SAVINGS
FROM MODIFICATION OF
OR EXPENDITURES RESULTING
DEGREASER (NEW)
Test Group
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
125
0.04
70
Annual operating hours
Solvent savings (loss), k9/yr:a
Minimurr.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), S/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, °k
438. 00l
0
0
438.00
2000
(60)
sn
64.38
17.52
8.76
0
0
(42.33)
56.44
(132.89)
(34.12)
(1.47)
(0.38)
-
_
17
4000
(120)
ifin
64.28
17.52
8.76
0
0
(84.66)
112.88
(175.22)
22.32
(1.93)
(0.25)
-
89.36
17
6000
(180)
?dfl
64.28
17.52
8.76
0
0
(126.99)
169.32
(217.55)
78.76
(2.40)
0.87
-
45.60
17
Value in parentheses represents loss or expenditure.
Includes $120.00 for worker platform revisions and $78.00 additional expenditure
required over standard basket.
645
-------
TABLE D-27SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 5
Conditions
Solvent
Freeboard ratio (FR), 5-
Refrig. fraeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
125
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
762. 00b
n
n
762.00
2000
(60)
80
111.83
30.48
15.24
0
0
(42.33)
Rfi 44
(199.88)
(101.11)
(1-27)
(0.64)
-
_
17
4000
(120)
160
111.83
30.48
15.24
0
0
(84.66)
11? RR
(242.21)
(44.67)
(1.54)
(0.28)
-
_
17
6000
(180)
240
111.83
30.48
15.24
0
0
(126.99)
IfiQ 7?
(284.54)
11.77
(1.81)
0.07
-
121.48
17
Value in parentheses represents loss or expenditure.
Includes $120.00 for worker platform revisions and $242.00 for a new larger
basket. 646
-------
TABLE D-28 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 19
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), »
Others
1,1,1-Trichloroethane
50
Type II @ -23 to -32°C
0.04
70
Annual operating hours
Solvent savings (loss), kg/y:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3?Qfi.nnb
0
0
3796.00
2000
_
280
557.10
151.84
75.92
0
341.44
1Q7.F53
_
(928.77)
-
(0.82)
-
—
0
4000
_
560
557.10
151.84
75.92
0
341.44
395.07
_
(731.23)
-
(0.650
-
_
0
6000
_
840
557. in
151.84
75.9?
n
341.44
RQP.fin
_
(533.70)
-
(0.47)
-
.
0
a Value in parentheses represents loss or expenditure.
Includes $78.00 required for larger basket.
647
-------
TABLE D-29 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 19
Conditions
Solvent
Freeboard ratio (FR), '•
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), '„
Others
1,1,1-Trichloroethane
50
Type II @ -23 to -32°C
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3960. 00b
3622.00
0
7582.00
2000
—
280
1112.73
303.28
151.64
0
341.44
197.53
-
(1711.56}
(0.90}
_
-
0
4000
_
560
1112.73
303.28
151.64
0
341.44
395.07
-
(1514.02)
(0.79)
_
-
0
6000
_
840
1112.73
303.28
151.64
0
341.44
592.60
-
(1316.49)
(0.69)
„
-
0
a Value in parentheses represents loss or expenditure.
b Includes $242.00 for a new larger basket.
648
-------
TABLE D-30 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 20
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
125
Type I [ 1 to 2°C J
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, $
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), S/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
3738. 00b
0
0
3738.00
2000
^an
548.59
149.52
74.7fi
0
22?. 53
-
409.18
(586.22)
(0.59)
-
_
17
4000
n fin
548.59
149.52
74.7fi
0
222.53
-
818.36
(177.03)
(0.18)
-
_
17
6000
1740
548.59
149.52
74.7fi
n
222.53
-
1227.54
232.14
"0.23
-
82.51
17
Value in parentheses represents loss or expenditure.
b Includes $78.00 for additional cost of the larger basket over the smaller
one and $120.00 for revision of worker j3atform.
649
-------
TABLE D-31 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group
20
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), »
Others
1,1,1-Trichloroethane
125
Type I P 1 to 2°C
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
4062. 00l
700.00
n
4762.00
2000
—
580
698.87
iqn_4R
Q5.?d
n
777. $1
409.18
(797.94)
_
(0.66)
-
17
4000
—
IT fin
698.87
iqn.4R
PR . 7 d
n
??? R3
818.36
(388.76)
_
(0.32)
-
17
6000
_
1740
698.87
iqn.dR
QR ?d
n
???.R?
1227.54
20.42
_
0.02
_
136.95
17
Value in parentheses represents loss or expenditure.
Includes $242.00 for a new longer basket to replace the old one and $120.00
for revision of worker platform.
650
-------
TABLE D-32 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group
20
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
125
Type II (<> -23 to -32°C
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:3
Minimurr.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
4156.00fc
0
0
4156.00
2000
_
660
609.93
166.24
83.12
0
341.44
465.62
-
f 735. 11)
(0.61)
-
—
17
4000
_
1320
609.93
166.24
83.12
0
341.44
931.23
-
(PfiQ.Rn)
(0.22)
-
_
17
6000
_
1QRO
609.93
166.24
83.12
0
341.44
1396.85
-
IQfi 11
0.16
-
91.94
17
Value in parentheses represents loss or expenditure.
Includes $78.00 for additional cost of larger basket and $120.00 for revision
of worker platform. 551
-------
TABLE D-33SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 20
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1, 1-Tnchloroethane
125
Type II G> -23 to -32°C
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:3
Minimurr.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, °k
4480. 00b
•?fi?? nn
n
8102.00
2000
_
fifin
1189.05
324.08
162.04
0
341.22
465.62
(1550.77)
(0.77)
—
_
17
4000
_
1320
1189.05
324.08
162.04
0
341.22
931.23
(1085.16)
(0.54)
—
—
17
6000
_
1980
1189.05
324.08
162.04
0
341.22
1396.85
(619.54)
(0.31)
.
_
17
Value in parentheses represents loss or expenditure.
Includes $242.00 for replacement of the old basket and $120.00 for worker
platform revision.
652
-------
TABLED-34 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 10
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Tnchloroethane
50
0.08
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimutr.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), S/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
50.00
0
0
50.00
2000
„
(220)
7.34
2.00
1.00
0
0
(1RR ?l )
-
(165.54)
(16. 01)
_
0
4000
.
(44(1)
7.34
2.00
1.00
0
0
(310.41)
-
(320.75)
(31.03)
_
0
6000
.
(660)
7.34
2.00
1.00
0
0
(465.62)
-
(475.96)
(46.04)
_
0
a Value in parentheses represents loss or expenditure.
Cost difference for a new 0.08 m/s hoist over an 0.04 m/s hoist.
fi53
-------
TABLE D-35 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 10
Conditions
Solvent
Freeboard ratio (FR), »
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Tnchloroethane
50
0.08
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimuir,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. j;
finft.7n
i?n.nn
n
728.70
2000
(220)
106.94
29.15
14.57
0
0
(155. ?1)
(305.88)
(2.03)
-
_
0
4000
(440)
106.94
29.15
14.57
0
0
(310.41)
(461.08)
(3.06)
-
_
0
6000
(660)
106.94
29.15
14.57
0
0
(465.62)
(616.29)
(4.09)
-
_
0
a Value in parentheses represents loss or expenditure.
654
-------
TABLE D-36. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 11
Conditions
Solvent
Freeboard ratio (FR), 1-
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Tnchloroethane
75
0.08
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimurr.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, •*
280. 00b
0
0
280.00
2000
-
320
41.09
11.20
5.60
0
0
225.75
-
167.87
2.90
-
17.57
6
4000
-
640
41.09
11.20
5.60
0
0
451.51
-
393.62
6.80
-
8.06
6
6000
-
960
41.09
11.20
5.60
0
0
677.26
-
619.37
10.70
-
5.23
6
Value in parentheses represents loss or expenditure.
Includes $80.00 for revision of worker platform and $50.00 cost difference
between 0.04 and 0.08 m/s hoist speed.
655
-------
TABLE 0-37. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 11
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
75
0.08
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
963. 701
120.00
0
1083.70
2000
-
320
'
159.04
43.34
0
0
-
225.75
-
1.68
-
0.01
-
141.37
6
4000
-
640
159.04
43.34
0
0
-
451.51
-
227.44
-
1.01
-
40.93
6
6000
-
Qfin
159.04
43.34
0
0
-
677.26
-
453.19
-
2.02
-
23.93
6
a Value in parentheses represents loss or expenditure.
Includes $80.00 for worker platform revisions.
656
-------
TABLE D-38. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 12
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
100
0.08
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimurr.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
345. 00b
0
0
345.00
2000
-
180
50.63
13.80
6.90
0
0
126.99
55.66
—
0.78
-
49.05
12
4000
-
360
50.63
13.80
6.90
0
0
253.97
182.64
_
2.56
-
19.58
12
6000
-
540
50.63
13.80
6.90
0
0
380.95
309.63
_
4.34
-
12.23
12
a Value in parentheses represents loss or expenditure.
b Includes $100.00 for revision of worker platform.
657
-------
TABLE D-39. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 12
Conditions
Solvent
Freeboard ratio (FR), 5'
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Tnchloroethane
100
0.08
50
Annual operating hours
Solvent savings (loss), kg/y:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss). S/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
1046.20b
120.00
0
1166.20
2000
-
180
171.15
46.65
23.32
0
0
126.99
_
(114.13)
(0.47)
-
-
12
4000
-
360
171.15
46.65
23.32
0
0
253.97
_
12.84
0.05
-
127.19
12
6000
-
540
171.15
46.65
23.32
0
0
380.96
_
139.84
0.58
-
59.04
12
Value in parentheses represents loss or expenditure.
Includes $100.00 for revision of worker platform.
658
-------
TABLE D-40. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 13
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), »
Others
1,1,1-Trichloroethane
125
0.08
50
Annual operating hours
Solvent savings (loss), kg/y:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
i
410.00b
0
0
410.00
2000
400
60.17
lb.4U
8.20
0
0
?R? 1Q
-
197.42
_
2;33^
-
21.24
17
4000
800
60.17
lb.40
8.20
0
0
564 . 38
-
479.61
_
5.66 n
-
9.58
17
6000
1200
60.17
lb.40
8.20
0
0
846 . 58
-
761.81
_
8.99
-
6.18
17
a Value in parentheses represents loss or expenditure.
Includes $120.00 for worker platform revision.
659
-------
TABLE D-41- SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group
13
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Trichloroethane
125
0.08
50
Annual operating hours
Solvent savings (loss), kg/y:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
1128. 70b
120.00
0
1248.70
2000
-
400
183.26
49. 9b
24.92
0
0
282.19
-
24.01
_
0.09
_
117.00
17
4000
-
800
183.26
49.95
24.92
0
0
bb4 . 38
-
306.20
_
1.19
—
36.52
17
6000
-
1200
183.26
49.95
24.92
0
0
84b.58
-
588.40
.
2.28
_
21.64
17
a Value in parentheses represents loss or expenditure.
b Includes $120.00 for platform revision costs.
660
-------
TABLE D-42.
SUMMARY OF SAVINGS
FROM MODIFICATION OF
OR EXPENDITURES RESULTING
DEGREASER (NEW)
Test Group 14
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
1,1,1-Tnchloroethane
50
0.08
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, £
128.00
0
0
128.00
2000
-
(1040)
18.79
5.12
2.56
0
0
-
(733.70)
-
(760.16)
-
(28.72)
-
-
0
4000
-
(2080)
18.79
5.12
2.56
0
0
-
(1467.40)
-
(1493.87)
_
(56.45)
-
-
0
6000
-
(3120)
18.79
5.12
2.56
0
0
-
(2201.10)
-
(2227.56)
_
(84.17)
-
-
0
9 Value in parentheses represents loss or expenditure.
-------
TABLE D-43. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 14
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), tn/s
Load area (A), %
Others
1,1,1-Trichloroethane
50
0.08
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
850.70
120.00
0
970.70
2000
-
(1040)
142.46
38.83
19.41
0
0
(733.70)
-
(934.40)
-
(4.66)
-
_
0
4000
-
(2080)
142.46
38.83
19.41
0
0
(1467.40)
-
(1668.10)
_
(8.31)
-
_
0
6000
-
(3120)
142.46
38.83
19.41
0
0
(2201.10)
-
(2401.80)
_
(11.97)
-
-
0
Value in parentheses represents loss or expenditure.
662
-------
TABLE D-44. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 15
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), *
Others
1,1,1-Tnchloroethane
125
0.08
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
4R8.nnb
n
n
488.00
2000
.
(100)
71.62
19.52
9.76
0
0
-
(70.55)
-
(171.45)
-
(1.70)
-
-
17
4000
.
(200)
71.62
19.52
9.76
0
0
-
(141.10)
-
(241.99)
-
(2.40)
-
-
17
6000
„
(300)
71.62
19.52
9.76
0
0
-
(211.64)
-
(312.54)
-
(3.10)
-
-
17
8 Value in parentheses represents loss or expenditure.
Includes $120.00 for revision of worker platform.
663
-------
TABLE D-45. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 15
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), *
Others
1,1,1-Trichloroethane
125
0.08
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost. $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
1370. 70b
120.00
1490.70
2000
.
(100)
218.78
59.63
29.81
0
0
-
(70.55)
-
(378.77)
-
(0.25)
-
-
17
4000
(200)
218.78
59.63
29.81
0
0
-
(141.10)
-
(449.32)
-
(0.30)
-
-
17
6000
(300)
218.78
59.63
29.81
0
0
-
(211.64)
-
(519.86)
-
(0.35)
-
-
17
a Value in parentheses represents loss or expenditure.
Includes $120.00 for revision of worker platform.
664
-------
TABLE D-46. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW OR RETROFIT)
Base Case
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
50
0.04
50
Annual operating hours
Solvent savings (loss), k9/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
0
0
U
2000
4000
6000
a Value in parentheses represents loss or expenditure.
665
-------
TABLE D-47. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (HEW)
Test Group 35
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
75
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimuir,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
230. 00b
o
0
230. 00"
2000
340
360
33.75
9.20
4.60
0
0
220.66
233.64
173.10
186.09
3.64
3.91
14.35
13.45
6
4000
680
720
33.75
9.20
4.60
0
0
441.32
467.28
393.77
419.73
8.28
8.83
6.68
6.29
6
6000
1020
1080
33.75
9.20
4.60
0
0
661.98
700.92
614.43
653.37
12.92
13.74
4.36
4.10
6
a Value in parentheses represents loss or expenditure.
Includes $80.00 for revision of worker platform.
€66
-------
TABLE D-48. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 35
Conditions
Solvent
Freeboard ratio (FR), «
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
.Methylene chloride
75
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss). $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
355. 00l
0
0
355. 00*
2000
340
360
52.10
14.20
7.10
0
0
220.60
233.64
147.26
160.24
2.01
2.18
24.09
22.44
6
4000
680
720
52.10
14.20
7.10
0
0
441.32
467.28
367.92
393.88
5.01
5.37
10.72
10.06
6
6000
1020
1080
52.10
14.20
7.10
0
0
661.98
700.92
588.58
627.52
8.02
8.55
6.89
6.48
6
a Value in parentheses represents loss or expenditure.
Includes $80.00 for revision of worker platform.
667
-------
TABLE D-49. SUMMARY OF SAVINGS
FROM MODIFICATION OF
OR EXPENDITURES RESULTING
DEGREASER (NEW)
Test Group
36
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
125
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:3
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, °K
360. 00b
0
0
360.00°
2000
380
560
52.83
14.40
7.20
0
0
246.62
363.44
172.19
289.01
2.31
3.88
21.37
13.54
17
4000
760
1120
52.83
14.40
7.20
0
0
493.24
726.88
418.81
652.45
5.63
8.77
9.62
6.33
17
6000
1140
1680
52.83
14.40
7.20
0
0
739.86
1090.32
665.43
1015.81
8.81
13.65
6.21
4.13
17
Value in parentheses represents loss or expenditure.
Includes $120.00 for revision of worker platform costs.
668
-------
TABLE D-50. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 36
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
125
0.04
50
Annual operating hours
Solvent savings (loss), k9/yr:a
Minimuir,
Maximum
Capital cost, $
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), S/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
520. 00b
0
0
520.00
2000
380
560
76.32
20.80
10.40
0
0
246.62
363.44
172.19
289.01
1.60
2.69
28.95
18.77
17
4000
760
1120
76.32
20.80
10.40
0
0
493.24
726.88
418. 81
652.45
3.90
6.06
13.50
8.96
17
6000
1140
1680
76.32
20.80
10.40
0
0
739.86
1090.32
665.43
1015.89
6.19
9.45
8.80
5.89
17
Value in parentheses represents loss or expenditure.
Includes $120.00 for revision of worker platform.
66-9
-------
TABLE D-51 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (MEW)
Test Group 43
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), °*
Others
Methylene chloride
50
Type I @ 1° to 2°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:3
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
3300.00
0
0
3300.00
2000
(200)
484.31
132.00
66.00
0
222.53
-
(129.80)
-
(1034.64)
_
(1.14)
-
_
0
4000
(4000
484.31
132.00
66.00
0
222.53
-
(259.60)
-
(1164.44)
_
(1.29)
-
_
0
6000
(600)
484.31
132.00
66.00
0
222.53
-
(389.40)
-
(1294.24)
_
(1.43)
-
.
0
Value in parentheses represents loss or expenditure.
670
-------
TABLE D-52. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 43
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
50
Type I @ 1° to 2°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:3
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3300.00
2000
(200)
700.00!
0
4000.00
586.24
160.00
80.00
0
222.53
(129.80)
-
(1179.39)
-
(1.12)
-
_
0
4000
(400)
586.24
160.00
80.00
0
222.53
(259.60)
-
(1309.17)
-
(1.25)
-
_
0
6000
(600)
586.24
160.00
80.00
0
222.53
(389.40)
-
(1438.97)
-
(1.72)
-
_
0
Value in parentheses represents loss or expenditure.
671
-------
TABLE D-53. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 43
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), *
Others
Methylene Chloride
50
Type II @ -29° to -40°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimuir,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3718.00
0
0
3718.00
2000
320
545.65
148.72
74.36
0
341.44
207.68
-
(902.49)
_
(o.sn
_
—
0
4000
.
640
545.65
148.72
74.36
0
341.44
415.36
-
(694.81)
_
(0.62)
_
_
0
6000
960
545.65
148.72
74.36
0
341.44
623.04
-
(487.13)
_
(0.44)
_
_
0
a Value in parentheses represents loss or expenditure.
672
-------
TABLE D-54. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 43
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
50
Type II @ -29° to -40°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/y:a
Minimurr.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3718.00
3622.00
0
7340.00
2000
320
1077.22
293.60
146.80
0
341.44
207.68
-
(1651.38)
-
(1.53)
-
_
0
4000
640
1077.22
293.60
146.80
0
341.44
415.56
-
(1443.70)
-
(1.34)
-
_
0
6000
960
1077.22
293.60
146.80
0
341.44
623.04
-
(1236.02)
-
(1.15)
-
_
0
a Value in parentheses represents loss or expenditure.
673
-------
TABLE D-55. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 44
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
75
Type I @ 1° to 2°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3530. 00b
o
0
3530. OOb
2000
100
518.06
141 .20
70.60
0
222.53
64.90
(887.49)
-
(0.93)
-
-
6
4000
200
518.06
141 .20
70. bU
0
222.53
129.80
(822.59)
-
(0.86)
-
-
6
6000
300
518.06
141.20
70.60
0
222.53
194.90
(757.69)
-
(0.79)
-
-
6
Value in parentheses represents loss or expenditure.
Includes $80.00 for revision of worker platform.
674
-------
TABLE D-56. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 44
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
75
Type I (<> 1° to 2°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/y:a
Minimuir.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), S/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximurr,
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. «
3530. 00b
825.00
0
4355. OOb
2000
100
639.14
174.20
87.10
0
222.53
64.90
(1058.07)
-
.
(0.94)
.
-
6
4000
200
639.14
174.20
87.10
0
222.53
129.80
(993.17)
-
(0.88)
-
6
6000
300
639.14
174.20
87.10
0
222.53
194.70
(928.27)
-
(0.83)
-
6
Value in parentheses represents loss or expenditure.
Includes $80.00 for revisions of worker platform.
€75
-------
TABLE 0-57. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 44
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
Methylene chloride
75
Type II @ -29° to -40°C
0.04
50
3948. 00b
0
0
3948. ODD
2000
980
579.41
157.92
78.96
0
341.44
636.20
-
(521.53)
-
(0.45)
-
-
6
4000
1960
579.41
157.92
78.96
0
341.44
1272.04
-
(114.31)
-
0.10
-
106.87
6
6000
2940
579.41
157.92
78.96
0
341.44
1903.06
-
(750.33)
-
0.65
-
43.89
6
Value in parentheses represents loss or expenditure.
b Includes $80.00 for revisions of worker platform.
676
-------
TABLE D-58. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 44
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
75
Type II @ -29° to -40°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3948. 00b
3747.00
0
7695. 00b
2000
980
1129.32
307.80
153.90
0
341.44
636.20
-
(1296.25)
-
(0.67)
_
6
4000
1960
1129.32
307.80
153.90
0
341.44
1272.04
-
(660.42)
-
(0.34)
_
6
6000
2940
1129.32
307.80
153.90
0
341.44
1908.06
-
(24.40)
-
(0.01)
_
6
Value in parentheses represents loss or expenditure.
Includes $80.00 for revisions of worker platform.
677
-------
TABLE D-59. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 45
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
125
Type I @ 1° to 2°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimurr,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss). $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. ef
3660. 00b
0
0
3660. 00b
2000
380
537.14
146.40
73.20
0
222.53
246.62
(732.65)
_
-
(0.75)
-
-
17
4000
760
537.14
146.40
73.20
0
222.53
493.24
(468.03)
_
-
(0.48)
-
_
17
6000
1140
537.14
146.40
73.20
0
222.53
739.86
(239.41)
_
-
(0.24)
-
_
17
Value in parentheses represents loss or expenditure.
b Includes $120.00 for revisions of worker platform.
678
-------
TABLE D-60. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DE6REASER (RETROFIT)
Test Group 45
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
125
Type I @ 1° to 2°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimurr.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3820. 00b
700.00
0
4520.00
2000
380
663.36
180.80
90.40
0
222.53
246.62
(687.94)
-
-
(0.59)
_
-
17
4000
760
663.36
180.80
90.40
0
222.53
493.24
(441.32)
-
-
(0.38)
_
-
17
6000
1140
663.36
180.80
90.40
0
222.53
739.86
(194.70)
-
-
(0.17)
_
-
17
Value in parentheses represents loss or expenditure.
Includes $120.00 for revisions of worker platform.
679
-------
TABLE D-61. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DECREASER (NEW)
Test Group 45
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
125
Type II @ -29° to -40°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
4078. 00b
o
0
4078.00
2000
1280
598.49
163.12
81.56
0
341.44
830.72
-
(353.89)
-
(0.30)
-
-
17
4000
2560
598.49
163.12
81.56
0
341.44
1661.44
-
476.83
-
0.40
-
59.92
17
6000
3840
598.49
163.12
81.56
0
341.44
2492.16
-
1307.55
-
1.10
-
29.70
17
Value in parentheses represents loss or expenditure.
Includes $120.00 for revisions of worker platform.
680
-------
TABLE D-62. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 45
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
125
Type II @ -29° to -40°C
0.04
50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost. $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
4078.00
3782.00
0
7860.00
2000
1280
1153.53
314.40
157.20
0
341 .44
83U./2
_
(1135.85)
-
(0.58)
-
-
17
4000
2560
1153.53
314.40
157.20
0
341.44
lbbl.44
_
(305.13)
-
(0.15)
-
_
17
6000
3840
1153.53
314.40
157.20
0
341.44
2492 . 1 b
_
525.59
-
0.27
-
29.97
17
a Value in parentheses represents loss or expenditure.
681
-------
TABLE D-63. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 37
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), °*
Others
Methylene chloride
50
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, °*
78.00b
0
0
78.00
-
2000
(1120)
(800)
11.45
3.12
1.56
0
0
(726.88)
(519.20)
(743.01)
(535.33)
(46.06)
(33.19)
-
-
0
4000
(2240)
(1600)
11.45
3.12
1.56
0
0
(1453.76)
(1038.40)
(1469.89)
(1054.53)
(91.13)
(65.38)
-
-
0
6000
(3360)
(2400)
11.45
3.12
1.56
0
0
(2180.64)
(1557.60)
(2196.77)
(1573.73)
(136.19)
(97.56)
-
-
0
Value in parentheses represents loss or expenditure.
Cost of large basket minus cost of small basket.
682
-------
TABLE D-64. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 37
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), '»
Others
Methylene chloride
50
0.04
70
Annual operating hours
Solvent savings (loss), kg/y:3
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
242. 00b
0
0
242.00
2000
(1120)
(800)
35.52
9.58
4.84
0
0
(726.88)
(519.20)
(776.92)
(569.24)
(15.52)
(11.37)
-
-
0
4000
(2240)
(1600)
35.52
9.b8
4.84
0
0
(1453.76)
(1038.40)
(1503.80)
(1088.44)
(30.05)
(21.75)
-
-
0
6000
(3360)
(2400)
35.52
9.68
4.84
0
0
(2180.64)
(1557.60)
(2230.68)
(1607.64)
(44.58)
(32.13)
-
-
0
Value in parentheses represents loss or expenditure.
Cost of new basket.
683
-------
TABLE D-65. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 38
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), »
Others
Methylene chloride
125
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimuir.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, •*
438. nnb
0
n
438.00
2000
140
160
64.28
17.52
8.76
0
0
90.86
103.84
0.30
13.28
0.00
0.15
142.83
105.58
17
4000
280
320
64.28
17.52
8.76
0
0
181.72
207.60
91.16
117.12
1.01
1.29
41.17
34.21
17
6000
420
480
64.28
17.52
8.76
0
0
272.58
311.52
182.02
220.96
2.01
2.44
24.05
20.41
17
Value in parentheses represents loss or expenditure.
Includes $120.00 for revisions to worker platform and $78.00 for premium on a
larger basket. gg
-------
TABLE D-66. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group
38
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
125
0.04
70
Annual operating hours
Solvent savings (loss), k9/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
762. 00b
0
0
762. OQb
2000
140
160
111.83
30.48
15.24
U
0
90.86
103.84
(66.69)
(53.71)
(0.42)
(0.34)
-
17
4000
280
320
111.83
30.48
15.24
0
0
181.92
207.68
24.17
50.13
0.15
0.32
104.30
80.47
17
6000
420
480
111.83
30.48
15.24
0
0
272.58
311.52
115.03
153.97
0.73
0.98
51.22
42.05
17
a Value in parentheses represents loss or expenditure.
b Includes $120.00 for revisions to worker platform and $242.00 for a new
large basket.
S85
-------
TABLE D-67. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 46
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
50
Type I @ 1° to 2°C
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, \
3378.00
0
0
3378.00
2000
(600)
495.76
135.12
67.56
0
222.53
(389.40)
(1310.37)
-
(1.42)
-
-
_
0
4000
(1200)
495.76
135.12
67.56
0
222.53
(778. SO!
(1699.77;
-
(1.84
-
-
_
0
6000
(1800)
495.76
135.12
67.56
0
222.53
(1168.20)
(2089.17)
-
(2.27)
-
-
-
0
a Value in parentheses represents loss or expenditure.
686
-------
TABLE D-68. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 46
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
•Methylene chloride
50
Type I @ 1° to 2°C
0.04
70
Annual operating hours
Solvent savings (loss), k9/yr:a
Minimurr
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, £
3542.00
700.00
0
4242.00
2000
(600)
622.56
159.68
84.84
0
222.53
(389.40)
(1489.01)
(1.35)
-
-
-
0
4000
(1200)
622.56
169.68
84.84
0
222.53
(778.80)
(1878.41)
(1.71)
-
-
-
0
6000
(1800)
622.56
169.68
84.84
0
222.53
(1168.20)
(2267.81)
(2.06)
-
-
-
0
Value in parentheses represents loss or expenditure.
687
-------
TABLE D-C9. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DECREASER (NEW)
Test Group 46
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
50
Type II @ -29° to -40°C
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimurr,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
3796.00
0
0
3796.00
2000
(100)
557.10
151.84
75.92
0
341.44
(64.90)
(1191.20)
-
(1.06)
-
-
0
4000
(200)
557.10
151.84
75.92
0
341.44
(121.80)
(1256.10)
-
(1.11)
-
-
0
6000
(300)
557.10
151.84
75.92
0
341 .44
(194.70)
(1321.00)
-
(1.17)
-
-
0
Value in parentheses represents loss or expenditure.
688
-------
TABLE D-70. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group
46
Conditions
Solvent
Freeboard ratio (FR), «
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), ?,
Others
Methylene chloride
50
Type II @ -29° to -40°C
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimurr,
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, 3;
4038.00
3782.00
0
7820.00
2000
(100)
1147.66
312.80
156.40
0
341.44
(64.90)
~
(2023.20)
(1.03)
-
_
0
4000
(200)
1147.66
312.80
156.40
0
341.44
(129.80)
~
(2088.10)
(LOT)1
-
0
6000
(300)
1147.66
312.80
156.40
0
341.44
(194.70)
~
(2153.00)
(1.10)
-
_
0
6 Value in parentheses represents loss or expenditure.
689
-------
TABLE D-71. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 47
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
125
Type I G> 1° to 2°C
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
3660.00
0
0
3660.00
2000
340
537.14
I4U.4U
73.20
U
222.53
220.66
(758.61)
-
(0.78)
-
_
17
4000
680
537.14
140.40
73.20
0
222.53
441.32
(537.95)
-
(0.55)
-
_
17
6000
1020
537.14
140.40
73.20
0
222.53
661.98
(317.29)
-
(0.33)
-
_
17
2 Value in parentheses represents loss or expenditure.
690
-------
TABLE D-72. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 47
Conditions
Solvent
Freeboard ratio (FR), «
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), »
Others
Methylene chloride
125
Type I ? 1° to 2°C
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
3820.00
700.00
0
4520.00
2000
340
663.36
180.80
90.40
0
222.53
220.66
(936.43)
.
(0.81)
-
_
17
4000
680
663.36
180.80
90.40
0
222.53
441.32
(715.77)
—
(0.62)
-
_
17
6000
1020
663.36
180.80
90.40
0
222.53
661.98
(495.11)
—
(0.43)
-
_
17
Value in parentheses represents loss or expenditure.
691
-------
TABLE D-73. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 47
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), *
Others
Methylene chloride
125
Type II @ -29° to -40°C
0.04
70
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimuir.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
4156.00
0
0
4156.00
2000
940
609.93
166. 24
83.12
0
341.44
610.06
(590.67)
(0.49)
-
_
17
4000
1880
609.93
lbb.24
83.12
0
341.44
1220.12
19.39
0.02
-
136.36
17
6000
2820
609.93
lbb.24
83.21
0
341.44
1830.18
629.45
0.52
-
51.11
17
a Value in parentheses represents loss or expenditure.
€92
-------
TABLE D-74. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 47
Conditions
Solvent
Freeboard ratio (FR), «
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), »
Others
Methylene chloride
125
Type II G> -29° to -40°C
0.04
70
Annual operating hours
Solvent savings (loss), kg/y:a
Minimum
Maximum
Capital cost, S
Purchase of modif icatioi
Installation cost
Engineering and startup
Total
Annual operating cost. S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, 5:
/
4156.00
jyqb.uu
0
8102.00
2000
940
1189.05
324.08
162.04
0
341.44
610.06
(1406.55)
-
(0.70)
-
_
17
4000
1880
1189.05
324.08
162.04
0
341 .44
1220.12
(796.49)
-
(0.39)
-
_
17
6000
2820
1189.05
324.08
162.04
0
341.44
1830.18
(186.43)
-
(0.09)
-
-
17
a Value in parentheses represents loss or expenditure.
693
-------
TABLE D-75. SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 39
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others
Methylene chloride
50
0.04
50
0.25
Annual operating hours
Solvent savings (loss), k9/yr:a
Minimurr.
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), S/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
1330.00
90.00
0
1420.00
2000
(1720)
208.39
56.80
28.40
0
201.67
-
(1116.28)
-
(1650.42)
-
(3.33)
-
-
0
4000
(3440)
208.39
56.80
28.40
0
403.33
-
(2232.56)
-
(2929.49)
-
(4.20)
-
-
0
6000
(5160)
208.39
56.80
28.40
0
605.00
-
(3348.84)
-
(4247.44)
-
(4.73)
-
-
0
a Value in parentheses represents loss or expenditure.
694
-------
TABLED-76 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER RETROFIT
Test Group
39
Conditions
Solvent
Freeboard ratio (FR), «
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), * _
Others - lip exhaust nr/s oer m
Methylene chloride
50
0.04
50
0.25
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
1330.00
90.00
0
1420.00
2000
(1720)
208.39
56.80
28.40
0
201.67
(1116.28)
_
(1611.55)
(3.25)
—
0
4000
(3440)
208.39
56.80
28.40
0
403.33
(??3?_ Rfi)
.
(2929.50)
(4.20)^
—
0
6000
(5160)
208.39
56.80
2R.40
0
605.00
(3348.84)
(4247.440
(4.73)
_
0
Value in parentheses represents loss or expenditure.
695
-------
TABLE D-77 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 40
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others - lip exhaust m/s perm
Methylene chloride
50
0.04
50
0.50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
1330.00
an.nn
n
1420.00
2000
_
(2280)
208.39
56. RO
?d_an
n
4m. 33
(1479.72)
(2176.65)
(3.14)
_
0
4000
_
(4560)
208.39
56. RO.
24. an
n
Rflfi.fi?
(2959.44)
(4056.71)
(3.70)
_
0
6000
_
(6840)
208.39
Rfi.Rfl
?4.an
n
•mn.nn
(4439.16)
(5942.76)
(3.96)
_
0
a Value in parentheses represents loss or expenditure.
696
-------
TABLE D-78SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER RETROFIT
Test Group 40
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), »
Others - lip exhaust m/s perm
Methylene chloride
50
0.04
50
0.50
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximuir,
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
1330.00
90.00
0
1420.00
j
2000
-
(2280)
208.39
56.80
24.40
0
403.33
(1479.72)
(2176.64)
(3.14)
-
—
0
4000
-
(4560)
208.39
56.80
24.40
0
806.67
(2959.44)
(4059.71)
(3.70)
_
_
0
6000
-
(6R40)
208.39
56.80
24.40
0
1210.00
(4439.16)
(5942.76)
(3.96)
_
.
0
Value in parentheses represents loss or expenditure.
697
-------
TABLE D-79SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 41
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Methylene chloride
50
Hoist speea iv;t m/s
Load area (A), %
Others, cross current m/s
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
0.04
50
0.10
b
0
0
n
2000
140
0
0
0
0
0
qn.Rfi
90.86
0.00
b
b
0
4000
280
0
0
0
0
0
Ifil 7?
181.72
0.00
b
b
0
6000
420
0
0
0
0
0
272.58
272.58
o.nn
b
b
0
Value in parentheses represents loss or expenditure.
Since capital cost is zero, this is included.
€98
-------
TABLE D-80SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 41
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others - cross current m/s
Methylene chloride
50
0.04
50
0.1
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost. S
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. °*
n.ob
0.0
2000
_
140
n
n
n
n
0
90.86
gn.Rfi
-
0.00
b
b
0
4000
_
280
n
n
n
n
0
181.72
1R1.72
-
0.00
b
b
0
6000
_
420
n
n
n
n
0
272.58
?7?.5R
-
0.00
b
b
0
Value in parentheses represents loss or expenditure.
Since capital cost is zero, this is undefined.
699
-------
TABLE D-81 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (NEW)
Test Group 42
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), %
Others - cross current m/s
Methylene chloride
50
0.04
50
0.26
Annual operating hours
Solvent savings (loss), kg/y:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss), $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity, %
-o-b
n
n
-0-
2000
„
(2360)
0
0
0
0
(15T1 fid)
(1531.64)
—
0.00
b
b
0
4000
(4720)
0
0
0
0
(infiT ?R)
(3063.28)
_
0.00
b
b
0
6000
(7080)
0
0
0
0
(4«;Q4 Q?)
(4594.92)
—
o.on
b
b
0
a Value in parentheses represents loss or expenditure.
Since capital cost is zero, this is undefined.
700
-------
TABLE D-82 SUMMARY OF SAVINGS OR EXPENDITURES RESULTING
FROM MODIFICATION OF DEGREASER (RETROFIT)
Test Group 42
Conditions
Solvent
Freeboard ratio (FR), %
Refrig. freeboard chiller (RFC)
Hoist speed (V), m/s
Load area (A), »
Others - cross current m/s
1,1,1-Trichloroethane
50
0.04
50
0.26
Annual operating hours
Solvent savings (loss), kg/yr:a
Minimum
Maximum
Capital cost, S
Purchase of modification
Installation cost
Engineering and startup
Total
Annual operating cost, $
Capital charges
Insurance and taxes
Maintenance and labor
Replacement parts
Utilities
Credit (expenditure) due to
solvent savings (loss):
Minimum
Maximum
Net profit (loss). $/yr:
Minimum
Maximum
Ratio of savings (expenditure) to cost:
Minimum
Maximum
Payback period, months:
at minimum solvent savings
at maximum solvent savings
Lost capacity. %
0
0
0
0
2000
—
(2360)
0
0
0
0
0
(1R?1 .64
(1^1 fid)
0.00
b
b
0
4000
.
(4720)
0
0
0
0
0
(3063.2R)
(3063.28)
0.00
b
b
0
6000
—
(7080)
0
0
0
0
0
(4594.92)
(4594.92)
0.00
b
b
0
Value in parentheses represents loss or expenditure.
701
-------