EPA-600/2-77 122
June 1977
Environmental Protection Technology Series
FIELD TESTING: APPLICATION
OF COMBUSTION MODIFICATIONS
TO CONTROL POLLUTANT EMISSIONS
FROM INDUSTRIAL BOILERS -
Phases I and II
(Data Supplement)
Industrial Environmental Research Laboratory
Office of Research and Development
U.S. Environmental Protection Agency
Research Triangle Park, North Carolina 27711
-------
RESEARCH REPORTING SERIES
Research reports of the Office of Research and Development, U.S. Environmental
Protection Agency, have been grouped into five series. These five broad
categories were established to facilitate further development and application of
environmental technology. Elimination of traditional grouping was consciously
planned to foster technology transfer and a maximum interface in related fields.
The five series are:
1. Environmental Health Effects Research
2. Environmental Protection Technology
3. Ecological Research
4. Environmental Monitoring
5. Socioeconomic Environmental Studies
This report has been assigned to the ENVIRONMENTAL PROTECTION
TECHNOLOGY series. This series describes research performed to develop and
demonstrate instrumentation, equipment, and methodology to repair or prevent
environmental degradation from point and non-point sources of pollution. This
work provides the new or improved technology required for the control and
treatment of pollution sources to meet environmental quality standards.
EPA REVIEW NOTICE
This report has been reviewed by the U.S. Environmental
Protection Agency, and approved for publication. Approval
does not signify that the contents necessarily reflect the
views and policy of the Agency, nor does mention of trade
names or commercial products constitute endorsement or
recommendation for use.
This document is available to the public through the National Technical Informa-
tion Service, Springfield, Virginia 22161.
-------
EPA-600/2-77-122
June 1977
FIELD TESTING: APPLICATION
OF COMBUSTION MODIFICATIONS TO CONTROL
POLLUTANT EMISSIONS FROM INDUSTRIAL BOILERS -
Phases I and II
(Data Supplement)
by
S.C. Hunter and H.J. Buening
KVB Engineering, Inc.
17332 Irvine Boulevard
Justin, California 92680
Contract No. 68-02-1074
Program Element No. 1AB014
ROAP No. 21BCC-046
EPA Project Officer: Robert E. Hall
Industrial Environmental Research Laboratory
Office of Energy, Minerals, and Industry
Research Triangle Park, N.C. 27711
Prepared for
U.S. ENVIRONMENTAL PROTECTION AGENCY
Office of Research and Development
Washington, D.C. 20460
-------
Limitations On Application of Data Reported
The data cited in this report are pollutant emissions. These emission
levels are suitable for use in estimating mean emissions from industrial boilers
as a class and are useful in compiling areawide emission inventories. However,
they are not suitable for predicting emissions from any one boiler or as regula-
tory limits or emission standards. Use of emissions as emission standards auto-
matically would place a large proportion of the industrial boiler population
in noncompliance.
-------
TABLE OF CONTENTS
Foreword
INSTRUMENTATION
GLOSSARY
CONVERSION FACTORS
SITE LOCATION NUMBER
1 1
2 40
3 67
4 77
5 92
6 112
7 123
8 137
9 144
10 164
11 178
12 188
13 215
14 231
15 248
16 273
17 281
18 290
19 315
20 368
21 406
22 421
23 429
24 450
25 466
26 470
27 510
28 524
29 537
30 550
31 558
32 564
33 575
34 580
35 587
36 596
37 605
38 613
39 622
ill
-------
FOREWORD
The purpose of this Data Supplement Volume is to document data in greater
detail than was practical in the final reports for this contract. It is intended
to provide the necessary details to other researchers who are interested in per-
forming their own analysis.
Readers are referred to the contract final reports for information as
to objectives, selection of units, measurement procedures, interpretations and
conclusions.1'2
All data presented for gaseous emission concentrations of NO, NO , CO,
X
HC, and SO are expressed in parts per million by volume (ppm) on a dry basis
corrected to 3 percent O by volume (dry) in the flue gas.
The data are arranged in this volume by Location Number for Locations
1 through 39. A location is defined as one company or plant in which one or
more boilers were tested. Each boiler tested at a location is identified by
a unit number. The contract final reports frequently refer only to the test
number when data are discussed. Table 1 presents a cross-reference list of
test numbers and the corresponding location number for the tests conducted
in Phase I. Table 2 presents a similar list for tests conducted in Phase II.
'cato, G. A., et al., "Field Testing: Application of Combustion Modifications
to Control Pollutant Emissions from Industrial Boilers-Phase I," PB 238 920/AS,
EPA-650/2-74-078a, October 1974.
2Cato, G. A., et al., "Field Testing: Application of Combustion Modifications
to Control Pollutant Emissions from Industrial Boilers-Phase II," PB 235 500/AS,
EPA-600/2-76-076a, April 1976.
iv
-------
TABLE 1. INDEX OF TEST NUMBERS AND LOCATION
NUMBERS FOR PHASE I
Test
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25
Location
Number
19
19
15
5
1
7
17
20
18
16
N/A1
1
2
10
9
15
15
11
21
21
18
18
8
9
6
Test
Number
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
41
42
43
44
45
46
47
48
49
50
Location
Number
12
14
14
13
9
13
20
3
23
26
15
5
4
26
23
3
22
22
26
26
24
24
26
25
N/A
Test
Number
51
52
53
54
55
56
57
58
59
60
61
62
63
64
65
66
67
68
69
70
71
72
73
74
75
Location
Number
23
19
19
19
26
26
26
5
N/A
4
N/A
1
2
23
6
1
1
2
2
2
20
20
24
8
12
Test Location
Number Number
76 N/A
77 12
78 12
.79 N/A
80 10
*N/A - test number not assigned.
For Tests 101-212 see Table 2.
KVB 6001-491
v
-------
TABLE 2. INDEX OF TEST NUMBERS AND LOCATION
NUMBERS FOR PHASE II
Test
Number
101-108
109-112
113-121
122-130
131-133
134-139
140-148
149-152
153-155
156-159
160-164
165-168
169
170-175
176-179
180-189
190-206
207-212
Location
Number
1
27
29
28
31
30
32
33
34
13
36
35
31
20
37
38
19
39
For Tests 1 - 80, see Table 1.
KBB 6001-491
VI
-------
For each unit tested, the data supplement contains the following in-
formation:
1. Industrial Boiler Design Data
Design data tabulations include: unit description, installation
date, steam conditions, furnace characteristics, burner type and
spacing, fuels burned, and design temperatures for fuel, air and
stack gas.
2. Boiler Emission Measurements and Control Room Data
Emission measurements tabulated for each test include test type
test load, combustion conditions (excess ©2, CC^), gaseous
emissions (NOX, NO, CO, HC, SOX/ and SO2 all at 3% O2, dry),
total particulates and solid (filterable) particulates,\ boiler
efficiency, Bacharach smoke spot number, and plume opacity.
Control room data tabulated include steam pressure and tempera-
ture, combustion air and stack temperatures, fuel flow, fuel
temperature and pressure, furnace pressure, and burner air
register setting.
3. Cascade Impactor Data
Impactor data include impactor flow conditions, stage collection
weights, and calculated aerodynamic particle size for each size.
The impactor used was a Brink Model B (BMS-11) with the follow-
ing stage dimensions:
Spacing of
Jet No. Jet Dia., in. Jet Opening, in.
1 0.249 0.747
2 0.1775 0.533
3 0.1396 0.419
4 0.0946 0.282
5 0.0731 0.220
4. Emission Data Plots
Plots of gaseous emissions of NOX, HC, CO, and smoke as a function
of excess O at a given load are included.
5. Stack Traverse
Plots of stack traverse data for 02, velocity and temperature as
a function of position in the stack are included.
6. Fuel Analysis
Laboratory reports of fuel analysis are included as received.
Dash marks entered on the data forms indicate that data were not
available. Blacked out areas on certain data forms are deletions of company
names at which boiler tests were conducted.
vii
-------
INSTRUMENTATION
The emission measurements were made with instrumentation contained in
a 2.5 by 9 meter (8 by 27 ft) laboratory trailer. The gaseous emission measure-
ments, except sulfur oxides, were made with analyzers located in the measure-
ment console in the trailer. The particulate concentration, particulate size,
and sulfur oxides concentration measurements were made with instrumentation
prepared in the wet chemistry area of the laboratory and taken to the sample
port. The weighing and titration were done in or near the laboratory.
The emission measurement instrumentation used for the program was
that shown in Table 3. The operation of the instrumentation is discussed
in detail in the contract final reports.
TABLE 3. EMISSION MEASUREMENT INSTRUMENTATION
Emission
Symbol
Measurement Method
Equipment Mfgr S Model
Nitric oxide
Oxides of nitrogen
Carbon monoxide
Carbon dioxide
Oxygen
Hydrocarbons
Sulfur dioxide
and trioxide
Total particulate
matter
Particulate size
Smoke spot
Opacity
NO
NO
x
CO
co2
°2
HC
SO.,,
-3
PM
K
Chemiluminescent*
Chemiluminescent*
Spectrometer*
Spectrometer*
Polarographic *
Flame ionization*
Absorption/
titration
EPA Std. Method 5
Cascade impactor
Reflection
EPA Std. Method 9
Thermo Electron, 10A
Thermo Electron, 10A
Beckman, 864
Beckman, 865
Teledyne, 326A
Beckman, 402
KVB Equipment Co.
Joy Mfg. Co.
Monsanto-Brink, B(BMS-11)
Research Appliance Co.
*Precision, + 1% of Full Scale
KVB 6001-491
Vlll
-------
GLOSSARY OF SYMBOLS USED ON DATA FORMS
Burner Type
Air
ChGrt
Pulv.
Ring
SpStk
Spud
Steam
Test Type
Air Reg
Atom Press
BOOS
Base
BrTune
CombCyc
Damper
HiAir
HiLoad
LowAir
LowLoad
LowNOx
NrmlAir
OFA
SCA
SnglCyc
Steamlnjec
VPH
Viscosity
Air Atomizer
Chain Grate
Pulverizer
Natural Gas Ring
Spreader Stoker
Natural Gas Gun
Steam Atomizer
Test Fuel
Coal
NG
Ref.Gas
NG/#6
#2
#5
#6
PS300
Air Register Adjustment
Burner Atomizing Pressure Adjustment
Burners Out Of Service
Baseline
Boiler Tuneup
Combined Cycle
Air Damper Adjustment
High Excess Air
High Load
Low Excess Air
Low Load
Low NOx Condition
Normal Excess Air
Overfire Air
Staged Combustion Air
Single Cycle
Steam Inj ection
Variable Combustion Air Temperature
Fuel Oil Viscosity
Coal
Natural Gas
Refinery Gas
Mixture, NG and #6
No. 2 Grade Fuel Oil
No. 5 Grade Fuel Oil
No. 6 Grade Fuel Oil
Pacific Standard Fuel
Oil No. 300
IX
-------
CONVERSION FACTORS
SI Unita to Metric or English Units
To Obtain
g/Hcal
106 Dtu
HBH/ft2
Mflll/ft3
Dtu
103 lb/hr» or HUH
Ib/KDtu
ft
in
ft'
.
f tj
Ib
Fahrenheit
pslg
piia
iwg (39.2»F)
10* Btu/hr
GJ/hr
•Ib/hr of equivalent
From
ng/J
GJ
-1 -2
GJ'hr -m
GJ'hr~l.m"3
gn cal
GJ/hr
'ng/J .
m
cm
mJ
^
m3
Kg
Celsius
Kelvin
Pa
Fa
Pa
MM
MM
saturated steam
Multiply By
0.004186
0.948
0.08806
0.02684
3.9685 x 10"3
0.948
0.00233
3.281
0.3937
10.764
35.314
2.205
tF - 9/5(t )+32
F C
tF - l.BK - 460
P • (p ) (1.450X10 )~14.7
PPS 9_ (pPa (1.450X10-*)
piw« "
-------
English and Metric Unita to SI Units
To Obtain
ng/J
ng/J
Cl-hr"1-*"2
GJ'hr"1.*"3
GJ/hr
m
cm
m
n
Kg
Celsius
Kelvin
Pa
Pa
Pa
MM
Ml
*lb/hr of equivalent
From
Ib/MBtU
g/Hcal
HDII/ft2
MBH/ft3
103 lb/hr*
or 106 Dtu/hr
ft
in
ft2
Ib
Fahrenheit
poig
psia
iwg (39.2'F)
106 Btu/hr
GJ/hr
saturated steam
'Multiply By
430
239
11.356
37.257
1.055
0.3048
2.54
0.0929
0.02832
0.4536
tc - 5/9 (tp-32)
tR - 5/9 (tp-32) + 273
V - (Pn»l»)(6-B95X1°3)
pa psia
0.293
0.278
To Obtain
ng/J of
Natural Gas Fuel
CO
IIC
NO or •NOx (as equivalent
S02 or SOx
Oil Fuel
CO
HC
NO or NOx (as equivalent
SO. or SOx
Coal Fuel
CO
IIC
NO or NOx (as equivalent
SO. or SOx
Refinery Gas Fuel (Location 33)
CO
IIC
NO or NOx (as equivalent
SO, or SOx
Refinery Gas Fuel (Location 39)
CO
IIC
NO or NOx (as equivalent
nuj.kj.piy v-oncenirokion
in ppm at 3» O. by
0.310
0.177
0.510
0.709
0.341
0.195
0.561
0.780
0.372
0.213
0.611
0.850
0.306
0.175
0.503
0.700
0.300
0.176
0.506
NOj)
S02 or SOx
0.703
6001-491
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. / Test No. £~ Unit No.eJ
Unit Description _g^ /(^^ra/ ^r^a£tf ty/Off M
Installation Date
Steam Output (103 lb/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
W64
23.0
300
400
Watertube
/5 - £ - 7
535-
7&&
/ 8 f: \A/' /?!&$ $ *£J'<5<3lsr? /4 10107. £?rr?-
A/& f. £r&3
di*ib 'i > e w /
Aisnbiswj
<- 460
Comments:
KVB 6001-491
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location I
Unit 2.
Fuel /{£?/. 606
Test No.
Test Type
Test Load (103 lb/1 r)
Excess 02 (%)
NOX (ppm) •*
NO (ppm) *
CO2 dry (%)
CO (ppm) *
HC (ppm) #
QO f nnm } V
^
SOo (ppm) ^f
•Total Part flb/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Opacity (^>)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
PIIA 1 Pint*/
Fuel Temp. (°F)
Fuel Pros. " (psig)
Furnace Pres. (in.^O)
Register (% open)
s-/
f/ijir
22.0
3.4
7o
67
77
/If
380
A***b-
£"&b
£"60
A*27.
o>6/
O./S'
/#
-------
o
o
o
VO
Location
Unit No.
Test No.
--
—
--
—
~
-
-
-
-
-
-
-
-
-
-
I
i
C
c.
-
-
-
-
1
D
>
-
*"
-
-
1
-
-
-
T t
-
-
-
-
-
n
-
~
-
-
1
—
-
G
j<
i
s
&
-
-
-
^
-
o
s
-
-
-
-
-
2,
O
Z
-
No.
£
-
-
—
-
-
-
-
-
-
-
-
-
/
-
-
-
_
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
—
-
-
-
Load <=3?, •5~&&
Fuel A/af. &&*.
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
/ l,f c?
-
-
Ib/hr
?
-
-
-
-
-
°2
-
/
y
X-
i
A
\
X
-
^
-
s
^5
V
">1
s^
-
••
-
^
•v
"s
— *
s
•«*
V.
=9
-
's
••
@ Smoke
O co
|r»i
*
j
y
-
^
-
t—
s
— -
s
s^
f*
V
-
-
s
^
^
X
/
*•
/
HC
i NOX
s
/
'
1
A
j
(
;X
s
--
--
3 if *
(0
^:
u
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
FUEL ANALYSIS SUMMARY
Gas Fuel
I
a
m
V
4
pr-fnua, i
12
13
14
15
24
25
30
37
38
39
40
41
47
48
49
58
60
67
69
75
77
80
I"
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
o"
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
.6
0
0
0
0
0
0
0
.3
n
9E
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
.1
.1
.1
.1
1.3
1.3
4.6
*r
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88.9
84.1
85.8
85.8
85.8
. 85.8
23.6
23.6
74.0
*Ci
13.2
U2
.A
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
,3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
• °
x *~
A 9
1108
- una
AAVO
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548 .
1129
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. /
Test No. /£.
Unit No. /
unit Description _gju/
Tf/oe
Installation Date
Steam Output (103 Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
W.64
£9.0
300
400
Water-tube
/3-6 - 7
S3&
7&S-
/ e^W- Ring 4 3te0w 4te?"7. &rr7.
#2 0iJ / ^/- *£^
Awb/'etrt
/tm&''
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /
Unit /
Fuel A£?/. £7as
Test No.
Test Type
Test Load (1Q3 lb/h :)
Excess C>2 (%)
NOX (ppm) #
NO (ppm) *
CO2 dry (%)
CO (ppm) *
HC fnnm} 4l
cr) (nnm) •¥
•Total Part (Ib/MBtu)
Solid Part (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Tpmn (°F)
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.F^O)
Register (% open)
18 -ft
A/orm/
A,T
21,0
2.8
70
67
/0.0
/a
b A
'i'ty
/, /j
Lf'C/
o&C/
Awb.
O.(s/,/
O.SZf
/00
S3 -6
A/orrtj/.
Air
tto
/,tr
67
64
//.//
O'/f
/3l
0,1
Jee
&•i*s
toocJ
. 0.0
fc.0
32
30
b.g
&3
/
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /
Unit /
Fuel
Test No.
Test Type
Test Load (103 lb/hr)
Excess O2 (%)
NOX (ppm) 4
NO (ppm) *
CO2 dry (%)
CO (ppm) #
HC fnnm} *L
CJT\ fnnTn^ -it
A
co*^ ^r>nm} ^.
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Cjnolc £» Qr^D t" No
Op3.ci.ty (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp (°F)
Pllp 1 Pi OW
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H20)
Register (% open)
IS '-//
/^«->
^/>
£000
/97
38£~'
A»ib.
Awb.
O.8
o.n
/00
/a -/a
h/0r*n.
Air
us
Afr
£3.0
2.3
7/
68
S0,6
/4
/I ^ /// ^
C/t&ftfg
W7
383~
Ainb,
hft/n
V&&
A*ib,
O.&
o>/6
/ff &ts
dwb.
0'&
O,/6~
/r
es.&
3.t
72
6
& €?&
d*y*iy.
&S4
OJ73~
/0
f£/t
O&f
Am6.
0.S4
0.2
J00
/
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /
Unit /
Fuel A/0J- &£)6
Test No.
Test Type
Test Load (1()3 lb/h ')
Excess O2 (%)
NOX (ppm) *
NO (ppm) ¥
CO2 dry (%)
CD (ppm) *
. .
Hl- IPP"U *
SO (ppm) ^
SOo (ppm) •*£
4, '^ ^-
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No .
OD cit f9-)
yp y
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow .
Fuel Temp. (°F)
Fuel Pres. (psig)
Furnace Pres. (in.t^O)
Register {\ open)
/<2-/0
Sjp Af<-^
_^ ^? ^-**^
C^ ^» • v
/*
6tr
£2
/0.6
M
/^7
306'
J»>b.
£-60
A^rb.
0,6-4
O./f
,00
/i>
_:
/2
O.I
J00
£•£?£} G*
7.f
0.7
/02
te
6.6
/3
, -
*r£>
/+*S
.2Z£T
0-2
S3
Sc?
ve
? J000
/ ^^*
. *f£c>
/^7
38f
A^b,
4-63
A~*b.
J.0S-
0.4
,00
/e-z&'
ffase
23.tr
0.f£-
83
76
/J,2
> 2000
sS
/?7
38o
A*»J>.
£"60
Awb,
0,43
o./j-
/**
KVB 6001-491
8
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit /
Fuel A/at-
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) V
NO (ppm) -X
C02 dry (%)
CO (ppm) *
HC (ppm) *
en fr)nm} *L
*^O« frvr>T?i} -K
Total Part. (Ib/MBtu)
Solid Part (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fue 1 F low
Fuel Temp. (°F)
Fuel Pres. (psig)
Furnace Pres. (in.H2O)
Register (% open)
/u~>
/4,T
Z3.6-
J,tT
84
76
/&&
60
/37
38o
Aw&,
&/6~
S00
/S-27
Mi 4>'r
6'8
o./6
/00
/S-28
fa A,r
£000
37
h a
y.tt
// J. .
Wy
/) /•} 10 £"
s\ sisysi ^
(/ 1 &£/&&
7Q
/v
/^r
380
A*»b-
*62
Awb-
0-61
0J4
J00
/?-3c?
/// Air
'8.0
6.7
77
70
7,8
tea
<*2
/37
320
A»
-------
Location No. /
Unit No. /
Test No.
Load
Fuel
Ib/hr
• Smoke
O CO
X HC
A NO
\
o
o
I
&
CO
•g
(0
o
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
J0
8
Location No. / Fuel A/a/. &06
Unit No. / Load £>£, £~00 Ib/hr
Test No. /
-------
. FUEL ANALYSIS SUMMARY
Gas Fuel
/a
I
4
5
13
14
15
24
25
30
37
38
39
40
41
47
48
49
58
60
67
69
75
77
80
n
8
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
o"
0
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
.6
0
0
0
0
0
0
0
.3
CM
z
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
.1
.1
.1
.1
1.3
1.3
4.6
5
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88.9
84.1
85.8
85.8
85.8
.85.8
23.6
23.6
74.0
#
13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
1*
3«
X
A 9
51
X >
iioa
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
11O8
1548
1548
1129
1 2
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /
Unit /
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) *
NO (ppm) *
C02 dry (%)
CO (ppm) /
HC (ppm) *
SOx (ppm) #
SO2 (ppm) *
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow .
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
6e-/
3& >££
/0.3~
b,
20
0.05-
/0G>
•
<^r,
KVB 6001-491
1 3
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. /
Test No. £6,
Unit No.
Unit Description
&tr_*tOjs& .,_.
Installation Date
Steam Output (10J Ib/hr)
Design Pressur*" (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/
Awbier?!
3^0
286 to 3o£~
Comments:
KVB 6001-491
1 4
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location '
Unit 3
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess C>2 (%)
NOX (ppm) X
NO (ppra) x=
C02 dry (%)
CO (ppm) *
HC (ppm) *
SOX (ppm) *•
SO2 (ppm) X
•Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow {<#af///rj
Fuel Temp. (°F)
Fuel Prcs. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
££-'
Base
£6-4
£e?u9 /4/r
-------
CD
CT>
O
O
Location No. / Load
-
-
-
-
-
~
-
-
-
-
-
-
-
~-
-
-
-
-
-
-
-
c
-
-
-
-
1
D
J
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
_
-
f
-
f
f
-
1
2
-
-
1^
i«i
?
-
r^
-
.-
J
•i
£
-
-
-
~
~
~
1
*
s
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
~
-
-
—
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
t
Ib/hr
-
-
-
--
--,
/
L
-
-
^
-
-
'
-
-
-
^
-
/
-
-
t-
-
-
-
s
-
-
-
f
-
-
-
-
s
-
-
^
—
-
-
s
f
s
• Smoke
O CO
S
L
A
a
—
-
^
-
-
,J
^
«*•
t
t
•«
i
Si
X
A
t-j
-
\
HC
NOX
If
JM
w*
mm
-
••>
^
•w
1
"^
m
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit 3
Fuel Afaf-
/
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) #
NO (ppra) #
C02 dry (%)
CO (ppm) X
vr (nnm) #
cr> fnnm^ •}£
cn« frvDiri^ -al
•Itotal Part. (Ib/MBtu)
Solid Part (Ib/MBtu)
Boiler Ef f iciGncy (% }
Orjar*1! *h\7 (%*}
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Stack Temp. (°F)
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
67- /
fact? £0acS
W.tT
3.0
8
A»" b.
6~7
2,b
80
67-4
0a*s
2 3. 6"
6~7
16
?/
8.4
0
f ~y
V?'Ci
/, 7
LT. f
f) ns) {?£,
S22
3*?/
304-
Awb.
3.4>
J,7j'
80
67-s-
#/4i'r
Air
-------
Dj
V
U
o
o
Location No. /
Unit No. 3
Test No. 67
__
--
--
—
--
--
--
--
-
-
-
-
-
-
-
-
-
c
-
•""
-
-
-
*
D
-
-
-
-
-
-
-
-
-
r
-
-
-
-
-
-
-
-
-
-
-
-i
,
-
-
-
r
/
n
•^
7
-
-
_
**\
J
-
f
^
9
-
-
-
-
-
-
-
-
-
a
^
-
^-
-
w
X-
Sr
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
i
-
*
-
-
-
-
-
i \
-
-
-
-
>
'
Load .
-
j
-
/
/
/
-
-
-
^
-
/
k
-
t
r
\
'
-
/
/"
-
|
-
!•
-
lb/hr
5
.irt
—
1
-
-
-
— •
_
<2 t 6
0.,, %
-
i-
-
-
-
-
-
-
-
-
-
-
• Smoke
O CO
-
-
-
X
A
HC
NOX
i-
-
B
in
A
U
(0
n
rfl
•s
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No. /
Unit No. ^
Test No. ^7-
Fuel X/&/.
Load
Ib/hr
stack Diameter' D,duct .3°"
10
<*
_! c
I
i
1
<"N
)
J
J
f
i
HI
V
f
^
/
/
/
/
s
f
f
f
/
i
m
r
(
»
^
/
,,
/
X'
'
f
/
f
/
f
s
/
-
i
/
'
r
/
^J
i
A
T
i
^
/
£*
*|
(
^
i
2
X
i
/i
/t
.,
\
t
s
S
/
s
^
t
>*
\
y
\
3k
,
X
.
\
\
L
V
1
\
1
[V
\
\
n
i
CJL
Y V
A
T
-\ •
L
5
JL L-
31 aj
'?
r
Su
i
1
f
1
N.
1
i
1 h
\~
-- -^.P/O
^ -?/7/9
1" fJC/C/
I
DQj"
CSO&
JJ
a
u
(0
-p
4J
10
.5
D/D Duct
1.0
KVB 6001-491
19
-------
FUEL ANALYSIS SUMMARY
Gas Fuel
?£
!
*»
I
4
5
12
13
14
15
24
25
30
37
38
39
40
41
47
48
49
58
60
^r "
69
75
77
80
f
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548 .
1129
20
-------
DUPLICATE
REPORT
TRUESDAIL LABORATORIES, INC.
CHEMISTS • MICROBIQLOGISTS - ENGINEERS
RESEARCH - DEVELOPMENT - TESTING
KVB Engineering
CLIENT 17332 Irvine Blvd.
Tustin, California 92680
Attn: Glenn Cats
SAMPLE 1 Fuel Oil - "~~ "Special Oil" Feb. 6, 1974
P.O. No. 1700-43
INVESTIGATION; Analyses as requested.
Tee* 62,
RESULTS
Gravity API @ 20" C
Viscosity @ 40° C, SSU
Flask Point, °C
Carbon Residue, Conradson, %
Aniline Point, °C
Distillation:
Initial Boiling Point, °C
10%, °C
50%, °C
907., °C
End Point, °C
Recovery, %
Carbon, %
Hydrogen, %
Nitrogen, %
Sulfur, %
Ash, 7.
Gross Heat of Combustion, BTU/lb.
Ket Heat of Coobustlon, BTU/lb.
4IOI N. FIQUEROA STREET
LOS ANGELES 9OO6B
AREA CODE 213 • ZZ5-IB64
CABLES TRUELAB8
DATH February 27, 1974
RECEIVED February 8, 1974
LABORATORY NO. 120921
31.1
10$
107
0.071
*
153
241
279
333
372
98
85.94
12.72
0.045
0.40
0.003
19,440
18,280
* The sample was too dark for determining the Aniline
Point by the conventional method described in ASTM-D611.
(continued)
2 1
-------
DUPLICATE
TRUESOAIL LABORATORIES. INC. Page 2
/.... ._ ...... __£/i*Lf.._
The results of the spectrographic analysis are as follows:
Parts Per Million in Oil
Copper 2. 2
Zinc 4.5
Iron 5.1
Tin 1.3
Boron 0.018
Silicon C.69
Manganese 0.11
l.agnesium 0.69
Lead 1.4
Vanadium 0.99
Nickel 1.9
Aluminum 0.18
Calcium 1.2
Titanium 0.069
Silver 0.011
Cobalt 0.060
Strontium trace
Chromium 0.024
Respectfully submitted,
5SDAIL lABORATORIES^-EIC,
Alvin E. Hay
Director of Laboratories
KVB 6001-491
22
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. /
Test No./
300
b<70
\JL/c»1&r1-csbe
/3 -6 -7
&3b~
7S&
} 8$W fr'nff 4 3+
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /
Unit <2
Fuel
Test No.
Test Type
Test Load (103 lb/hr^
Excess O2 (%)
NOX (ppm) *
NO (ppra) #
C02 dry (%)
co (ppm) y
HC fnnm} Jf
cr\ fr>nTnl V
crj frnDirO •*/
•TY-kt-al Part Mh/MRtii)
,
f3f
Awb.
&3f
0.1
/00
to/rg
J/iAir
. /7.f
24
-------
Location No. /
Unit No. c?
Test No. /&/
Load /7,
Fuel
Ib/hr
• Smoke
O CO
HC
A
ro
en
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
FUEL ANALYSIS SUMMARY
Gas Fual
6/W/
T«it HO.
-101 .
104-106
109-110
113-115
122-125
140-14B
149-152
153-155
160- IBS
190-194
207-212
of Cat
Nat.
Nat.
Nat.
Hat.
Nat.
Hat.
Rat.
Mat.
Hat.
Hat.
£:*
CH4
94.52
94.52
90.00
88.11
6B.11
91.0
76.40
93.91
96.99
97.26
48.43
C2»6
4.26
4.26
2.90
4.33
4.33
5.64
5.10
4.37
1.9B
1.82
10.96
•J
0.20
0.20
0,40
0.6Q
0.68
0.51
5.30
0.71
0.10
0.027
1.60
\%
0.062
0.062
fr*c«
0.15
0.15
0.08
0.40
-
0.04
0.06
0.15
C5H12
0.032
0.032
-
0.04
0.04
0.01
0.20
-
0.01
-
0.02
C6»14
0.032
0.032
-
0.02
0.02
0.01
-
-
-
(-i
"
"<
.
-
-
-
-
-
a. 80
0.2S
-
-
35.67
-,
0.35
0.35
Q.10
0.67
0.67
-
1.40
0.74
0.60
0,37
*
«,
0.12
0.12
-
-
-
-
-
-
-
0.01
0.02
"l
0.37
0.37
6.60
5.96
5.96
-
1.60
-
0.26
0.28
2.66
T
0.05
0.05
-
0.04
0.04
-
-
-
-
-
"*
kg/*1'
0.725
0.725
0.746
0.765
0.765
0.720
0.765
0.733
0.710
0.705
0.576
«ity
lb/ft3
0.0447
0.0447
0.0460
0.0472
0.0472
0.0444
0.0472
0.0452
0,0438
0.0435
0.0355
Higher
Heating Value
CJ/n3
0.0306
0.0366
0.0364
0.0373
0.0373
0.0391
0.0391
0.0390
0.0377
0.0381
0.0310
Btu/rt3
1042
1042
976
1000
1000
1050
1050.
1047
1011
1023
631
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /
Unit 2
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) *
NO (ppm)y
C02 dry (%)
CX) (ppm) #
HC (nnm) V
cr> fnnm} ^
A
*ZOn tv>r>m} *£
Tnta\ Part- flb/MRtu}
Solid Part (Ib/MBtu)
Hod. 3.6 3T Ef f iciGncv (%}
SinolcG Spot No
Opacitv (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus Air Temp (°F)
Stack Temp. (°F)
Fuel Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
/#e-/
J/0rw/
Air
//
9.o
bs
?3e
346"
£-30
Amb,
a> 4>'r
M.f
zr
/00
'r
M.f
&/
92
58
//.a
t&8
SSf
396
£20
Aw&,
-------
OD
Location No.
Unit No. <=?
Test No.
Load
Fuel
ib/hr
• Smoke
O CO
NOX
w
A
O
2
*
•g
&
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No. /
Unit No. £
Test No. /£>£ -
Fuel
Load
Stack Diameter,
lb/hr
duct
1.0
Q)
W
M
0)
-P
W
29
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /
Unit £?
Fuel
Test No.
Test Type
Test Load (10^ lb/hr)
Excess O2 (%)
NOX (ppm) *
NO (ppm) y
C02 dry (%)
CO (ppm)#
HC (ppm) X
SOX (ppm)*
SO2 (ppm) X
Total Part . (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
/03-/
Aformi,
Air
/
•
fa)
30
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. /
Test No.
thri*
Unit No. /
Unit Description
Installation Date
Steam Output (10J Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
Wf
23,0
3 GO
400
Watertc/b3 / £t &'/ , //al~ &&$
Awb'ewt
AmbiewS
47e? fo -fga
Comments:
31
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /
Unit /
Fuel A/at-
Test No.
Test Type
Test Load (103 Ib/hrt
Excess 02 (%)
NOX (ppm) #
NO (ppm) #
C02 dry (%)
CO (ppm) *
HC (nnml i(
cr> (nnmi #
Of \JJ£JIUI 7T
CO— (nr>m} ^
Total Part . (Ib/MBtu)
col -i d Part flb/MBtu)
Boiler Efficiency (%)
Smoke Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.I^O)
Register (% open)
tet*~/
J/prn* /•
Ai'r
gtf.O
.7
7£-
7/
/J.a
Mf
O 1
&l
<23^
396
A*>b.
£6G
A*"b.
te.O
&>/£
/&&
/0&-i
tfi Air
*<9
82
7g
J0.4
0
^3f
336
/}*>£>.
&70
A»>b.
&.4
0.JS"
S00
/06-J
tfcr**/.
AiT
-. b>
17,0
e.tf
J00
S06-2
f/ert^t-
*>'r
tf.tr
3.f
84
80
/ff.f
o
'
3
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /
Unit /
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) 4-
NO (ppm) *
C02 dry (%)
CO (ppm) if
HC (nom) ^
co fnnml V
SO^ fryom} -)t
Total Part . (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smolce Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
Fuel Temp. (°F)
Fuel Pres. " (psig)
Furnace Pres. (in.H2O)
Register (% open)
/&7-/
t/0rfr>/.
Air
23.6"
3./
74
7f
/ H
230
3W
Awb.
60G
A wti.
£-3
o./~?
}0&
/07-a
/\/cnwli
A,r
£60
AW&-
38
0./
/06>
J07-4
M' A'~r
fas'
&<9
97
33
/0.6
//-
&G
Attrb.
36
0.J3
S00
&7-£~
tfi Air
/&&
f.S
b.
38
O.M
S00
33
-------
CO
Location No. /
Unit No. /
Test No. J&~7
--
__
--
-
-
r-
c
c
-
D
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1
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n
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-
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6
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-
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\
1
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T
Load /<^ ^T0& Ib/hr
Fuel #g Gil
^
*»
^
**
^
*^
^
J*
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-
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r
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-
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•*
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m
-*
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>|
y-
•«
• Smoke
O CO
-
>-
X HC
A NOX
o_ r %
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No. /
Fuel
Unit No. /
Test No.
(
i
!
1
)
i
|
1 i
{
;
1
. i
i i
1
1
1
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I
1
1
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i
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(
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i i
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t
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i
t
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1
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l
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I
1
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i
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1
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t
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1
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S
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r/f i 1
'
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duct vc-
i ,
l
t
!
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,
1
1
i
i i
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i
1
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1
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/
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1
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5
I
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i
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1
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D/D Duct
~\
1.0
4J
o
(0
cn
cn
35
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /
Unit /
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) *
NO (ppra) *
C02 dry (%)
CO (ppm) *
HC (nom) *
SO (onm) *
A
cr>*N /nmn^ *
• Ttotal Part. flb/MBtu)
Solid Part (Ib/MBtu)
Hoiler Efficiency (%)
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.I^O)
Register (% open)
log-/
j/yrm/-
Air
/Zg'
3.4
80
76
/a*
/se
23&
30
S0&-3
A/
-------
STACK TRAVERSE DATA
Location No. /
Unit No. /
Test No. Jog '3
Fuel #2
Load
-------
REPORT
TRUESDAIL LABORATORIES. INC.
CHEMISTS - MICROBIOLOG1STS - ENGINEERS
RESEARCH - DEVELOPMENT - TESTING
KVB Engineering
CLIENT 17332 Irvine Blvd.
Tustin, California 92680
Attn: Glenn Cats
SAMPLE 1 Fuel Oil - "~ "Special Oil" Feb. 6, 1974
P.O. No. 1700-43
INVESTIGATION Analyses as requested.
41O1 N. FIGUEROA STREE1
LOS ANGELES 9OO6;
AREA CODE 213 • 228-156
CABLE: TRUELAB:
DATE February 27, 197*
RECEIVED February 8, 1974
LABORATORY NO. 120921
RESULTS
Gravity API & 20°C
Viscosity @ 40°C, SSU
Flask Point, °C
Carbon Residue, Conradson, %
Aniline Point, °C
Distillation:
Initial Boiling Point, °C
10%, °C
50%, °C
907,, °C
End Point, °C
Recovery, 7o
Carbon, 7«,
Hydrogen, %
Nitrogen, %
Sulfur, %
Ash, 7o
Gross Heat of Combustion, BTU/lb,
Net Heat of Combustion, BTU/lb.
31.1
106
107
0.071
*
153
241
279
333
372
98
85.94
12.72
0.045
0.40
0.003
19,440
18,280
* The sample was too dark for determining the Aniline
Point by the conventional method described in ASTM-D611
(continued)
38
-------
TRUESDAIL LABORATORIES. INC.
Page 2
The results of the spectrographic analysis are as follows:
Parts Per Million in Oil
Copper
Zinc
Iron
Tin
Boron
Silicon
Manganese
Magnesium
Lead
Vanadium
Nickel
Aluminum
Calcium
Titanium
Silver
Cobalt
Strontium
Chromium
2.2
4.5
5.1
1.3
0.018
0.69
0.11
0.69
1.4
0.99
1.9
0.18
1.2
0.069
0.011
0.060
trace
0.024
Respectfully submitted,
TRIJESDAIL LABORATORIES, INC.
Alvin E. May
Director of Laboratories /
39
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No. J3, 63
Unit No.£
unit Description
/r/<-/c/ Erected
Installation Date
Steam Output (103 Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/3£2>
5-3.2
/60
3S-&
WaterJcsbe
&-/6-/a
/3 £oen -Kino B ^ifforr? at 0*97. ffcsrw&fg
U '
3.33
3.33
Mot. &as £ S*S 300
A»?b.-Jer M&. , /30 J*r £>5 3&O
Am&iewJ
•^ £~*?0 t?ri A/* <&> /~~&~80 0*? P£ 300
Comments:
40
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
location 2
Unit 2
Fuel A/Cif- &&$
Test No.
Test Type
Test Load (103 Ib/hr)
Excess ©2 (%)
NOX (ppm) #
NO (ppm) tf
CO2 dry (%)
CO (ppm) #
HC (ppm) #
. .
* x 'PP ' ""
^O ( \ it
2 »"" ' *
Total Part (Ib/MBtu)
^olid Part flb/MBtu)
Smoke Spot No.
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
If "a> 3% G£ c/ry
J3-*
Air
b7.tr
2.2
I3&
118
/0,2
64$
32
~7O
'&
/ft
3&o
Awb.
tte
Awb.
I.*/
-fr/ty
0/h, /00
J2~2
Hi Air
47,
/5V
3&0
Awb,
Sb.
S>4
-a/6
*2e0o
87
SS3
3&0
di«fb.
648
A»*ti'
2.7
-a.s
#/ 30
Oftf /OO
Sf'6
tfi/**c/
. 63
2.4
126
112
/0J
?2000
36
J£6
34-0
Au*t>.
603
A»rt>.
2.7
-0.28
Oid- IOP
/J-7
""£''
&£
2.2
/0ff
91
/0. /
'?200t&
28
/S2
3S0
Ji~b,
60&
/4w&.
/,66
-
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit S
Fuel Va
Test No.
Test Type
Test Load (103 lb/hr)
Excess O2 (%)
NOX (ppm) X
NO (ppm) •*
C02 dry (%)
CO (ppm) #
HC (ppm) X
en (nnml •*
^O^ (r>E>m^ •*
nv->4- = 1 Part (Ib/MBtu)
c?olid Part (Ib/MBtu)
BoiiGjr Ef f iciGncy (% )
OrjacM f v (%^
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fue 1 F low
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.f^O)
Register (% open)
S3-&
Morm/.
Air
L 37.S-
6.2
/3/
//J
7.8
73
ff
If6
348
/4**b.
S4t?
Ai*tb.
.7
-O.28
#> Jo
ofh. loo
;z~9
A/e>r*n /.
Air
3'r
£&
//,0
/3&
IS6
&.
-------
04
g
30
Location No.
Unit No. £
Test No. /3
\
\_
--
--
\
-
-
I
-
-
-
-
'
'
-
6
1
i
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0.
-
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y
^
/
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V
iX
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^
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6
nl
k
91
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-
-
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^
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>>
-
1
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r?\
—
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-
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-
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c
(
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-4
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-
-
-
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-
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/
-
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^
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r
-
-
-
^
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/
Load 4 7, •**
Fuel A/£)"t>
-
s»
-•
S
-
•*•
,/
-
-
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,•••
-
-
-
-
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/
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-
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«••
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>
x«
0& Ib/hr
-
2s
,>
-
-
M
X*
J
^»
-
-
-
x-
^
-
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<:
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>
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-
-
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\
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t
-
-
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^
-
-
-
-
-
-
-
-
-
-
—
-
-
-
-
r i
-
-
-
-
9 Smoke
O co
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
Y.
4
HC
NOX
-
-
»
)
-
-
-
-
-
-
-
-
~
w
nl
1
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
g FUEL ANALYSIS SUMMARY
f e? Gas Fuel
46. /3
H 8 O* sT 5 tT X$
4
5
12
IFtir-n
£3»TL3
14
15
24
25
30
37
38
39
40
41
47
48
49
58
60
67
69
75
77
80
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
0
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
.6
0
0
0
0
0
0
0
.3
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
.1
.1
.1
> -1
1.3
1.3
4.6
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88.9
84.1
85.8
85.8
85.8
.85.8
23.6
23.6
74.0
13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548 .
1129
44
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location <2.
Unit 2
Fuel P6 300
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) X
NO (ppm) X
C02 dry (%)
CO (ppm) X
HC (ppm) *
c(") / nnm \ *L
A
^O^\ foQin} ^
nv-,4- = l Part flb/MBtu)
CrOi d Part flb/MRtu^
Boiler Efficiency (%}
,
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp.(°F)
Ct-ar^lr Tomr** f°P^
Pnol Plntj a a/ //Jf*
ruei lemp. \ t)
Fuel Pres. ' (psig)
Furnace Pres. (in.I^O)
Register (% open)
63-'
A/e>rn^l.
Air
47,3-
^
31&
//.a
0
/^7
3fo
Awb.
&7O
i sy _.
'30
70
-O.2&
/00
6 3 -a
tcu> Ai'r
40
3, If
420
400
13.8
18
/5T/
SS'O
d»rb.
s~s~n
OO&
/30
7/
-0,t7
/00
63-3
fauj 4 if
48
3,0
t/0 1
382
/3.6
0
/&
3&
d»*&.
/r/jjT"
o 'rA
I *J S}
/
HZ
34**b.
*0
~&.a
/CO
63-6
£e>uJ Ai'r
. t6
a?
63?
/3.0
48
77
S? /9 3 ' O£^
&• c/3 */&
C/t &6/O
flp
oc
W8
33~0
AwJb.
*?3^
JCC?
/»?-?
" 3C
75
-0,/4
/0o
6f-7
ttretf /4ir
47
bf
643
//£
44
74
/40
3&?
d&rb
^•^3^^
<$c:&
&£7O
*rO
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location £
Unit 2
Fuel P6 30O
Test No.
Test Type
Test Load (103 lb/hr)
Excess 02 (%)
NOX (ppm) *
MA firinm^ ^
C02 dry (%)
CO (ppm) *
HC (ppm) *
cf} (ninm} ^
co~ friT>m^ V
Total Part. (Ib/MBtu)
Solid Part (Ib/MBtu)
Boiler Efficiency (%)
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow ga////r,
Fiiol T^amr-* / ° 1«M
Fuel Pres. ' (psig)
Furnace Pres. (in.f^O)
Register (% open)
63-8
/c>u? Ai'r
£/6.~
/00
£3'
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location <5
Unit 8
Fuel P6 3OO
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) X
NO (ppm) X
C02 dry (%)
CO (ppm) *
HC (ppm) *
SO (ppm) ^
X
2 \yy I T\
Total Part. (Ib/MBtu)
«?olid Part (Ib/MBtu)
Boiler Efficiency (%)
, . N
" *
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow 9al /fa
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
63-&
leu, Seacf
as
10.8
608
7,4
6!
61
-, —
/ 3
/43
3£-0
Awb
SZ&-
<2
63-/6
b*> 4,r
47
4,0
667
/3.6
37
48
/s
*D * ^?
400
c/
-------
oo
Location
Unit No.
Test No.
a
%
--
--
6
a
a
*
o
u
-
"^
i
PL 1_
/ 1— -
,
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--
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^
C4
2
X"
u
£
n
3
IX
tl
^1
r
-
-
X
s
No. c.
63
-
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-
^
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-
K
! Load 48, 0.
^
-
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5.
--
^1
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--
K^
t^
-
-
--
r
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
• Smoke
O CO
—
-
—
-
-
-
-
_
-
~
-
-
-
-
-
—
-
-
-
-
X
A
-
-
HC
-
-
~
-
-
-
-
-
-
—
-
-
-
-
-
•
§
u
n>
•C
a
' •*
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No. 3
Unit No. £
Test No.
Fuel P6 3GO
Load 7,
Stack Diameter'
Ib/hr
duct
1.0
0)
V4
O
0)
EH
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No. 60,
Unit No.
Unit Description
&e>;/er
Installation Date
Steam Output <103 Ib/hr)
Design Pressurt (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
W63
6&a
/60
3&6
Watertcsbe
18 '-/£ -J2
/393
3*100
& Co en- tfing £ Steam ctfeHr?. tfcsrwe.^
3.33
2.33
.A/0f. &Q5 ^ P* 300
A>nb. for M&. , /3G> for P$ 300
Awbienf
~5~7O
Comments:
50
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 2
Unit 4
Fuel PS 300
Test No.
Test Type
Test Load (103 Ib/hr)
Excess 02 (%)
NOX (ppm) #
«w ^ppiu; ^
CQ2 dry (%)
CO (ppm) *
HP fr»rm^ V
oo { r^nTTi } _i/
*;o^ (DDIH) v
Total Part (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
CTT»rjV^ ^not" Nn
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
T^llol foTTlT-l f°FM
Fuel Pres. ' (psig)
Register (% open)
.68-*
A/orm/.
Air
5-1
s,&
'w
fr£G
Hero
//.o
O
S~/~ ~7
5t> '
ff/
•3 i} K3
MJ~
343
Amb.
66
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6 '8 '-*/
£
/I
M2
348
A*nb.
T^1^
J C-C-
40
— XJ /O
(s,/(f
/£><**
. t?
7,8
t/8/
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0
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348
Awb*
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je>0
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~CS f/7
/6
343
Ai**ti.
*-ra
^ / o
6*
— ^} IO-
& /&
/
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location £
Unit 4
Fuel PS 300
Test No.
Test Type
Test Load (103 lb/hr^
Excess O2 (%)
NOX (ppra) #
NO (nnm) -i£
C02 dry (%)
CO (ppm) X
HC (DDIH) X
SO foDin) ^
SO-> (opm) X
•Total Part . (Ib/MBtu)
«Jolid Part flb/MBtul
CTnoV^ ^ririt" No
nnanit'v f%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp.(°F)
Stack Temp. (°F)
E*iiol rP^mr> f°T?\
Fuel Pres. ' (psig)
Furnace Pres. (in.I^O)
Register (% open)
68-8
£e«y
Air
S'
W
t/68
II. If
O
M7
34g
A»*b.
S7ctJ>
Air
S3
4,8
470
//. 6
O
M3
340
Awb.
S8o
64
-0./7
JOO
68 '-&
#e.80.
tt&
78
-0,83
#£ o
CtHtfS tOO
60^/3
#4 Goes
. se
4.7
3&V
I/, 6
//O
M0
340
di*tb.
£70
7S
-0.33
#3,4 0
o/h. /0
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 2
Unit 4
Fuel PS 30O
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) X
NO (ppm) *
C02 dry (%)
CO (ppm) X
HC (ppm) #
SOv (ppm) *
X
SO2 (ppm) #
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
6S-/6"
J48&OS
j-a.tr
£-.8
49/
tea
/t.O
0
/47
348
A»>6.
S8<=>
83
-0.26
loo @£ too
o too too
68 ~/6
#4 000&
f/
8.8
£o&
8,3
O
32b,
g-^
66
-o./q
eo eo 90
/oo fc& /oo
68 -/7
#4000$
36
1.8
^&e
7,8
0
137
W0
344
•Avb
£35-
4o
68- /8
MB00&
32
/0.6~
bea
7.a
o
187
S42
3^6
4»,b.
S20
46
-0,10
80 3£~ ?0
/CO JO0 /0O
6S-/.
£-6&
66
-0.3
8O 3S
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 8.
Unit <4
Fuel P5
Test No.
Test Type
Test Load (103 lb/hr)
•
Excess O2 (%)
NOX (ppm) ^
NO (ppm) *
C02 dry (%)
CO (ppm) *
HC (ppm) )(.
SOX (ppm) *
S02 (ppm)^
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.P^O)
Register (% open)
£8-'r
S/,5"
&.6
4
-------
en
en
--
--
-__
__
-
-
-
-
1
c
c
Location No
Unit No. *f
Test No. 6
-
-
1
3
1
i
-
"
-
-
f
-
t
O
A
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4
-
-
V
o
.
'«!
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-
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Load £"2,
Fuel X7^ c
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-
-
-
-
-
-
-
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-
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HC
NOX
-
-
-
-
~
-
-
_
CO
43
O
flj
JS
O
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
BOILER EMISSION MEASJREMENTS
AND CONTROL ROOM DATA
Location
Unit 4
Fuel
Test No.
Test Type
Test Load (103 lb/hr>
Excess O2 (%)
NOX (ppro) •%
NO (ppm) if
C02 dry (%)
CO (ppm) *
HP fnnTn) V
CA f nnm } ^
Cf)« fnDTTl} V
l^>tal Part (Ib/MBtu)
Solid Part (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Ortar"! t*\7 T%^
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
Fuel TenVD (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.f^O)
Register (% open)
6<9-/
6e»4(5
£-3
3,8
10 /
9.4
tea
M7
348
Awb.
3,2
-o,/4
#• & f£~
&fh. J0<*s
Air
&3
3,0
86
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W6
3*8
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#6 J£-
0fb. /£?£?
63-3
tfr 'Air
£-3
4,S
83
4
SB
/4?
3*8
4*tb,
3.2
-0.2
#6 '£~
0th. &0
3%
-------
en
1
-
-
d
-
f-
R
c
c
*
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-
Location No
Unit No. ^
Test No. £'
/,
)
7
J
,
e
-7
^
/•
n
,-
^
-
-
-
i
=
-
k
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— i
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-
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7
-
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-
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S
s
-
-
>
A
Load 6~3, 000
Fuel A/Q~t- £?&£>
^
\
S
v
-
-
-
N,
-
-
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-
2«
-
K
c
-
-
-
-
-
-
•w.
-
-
f-
_
-
-
3
-------
FUEL ANALYSIS SUMMARY
Gas Fuel
*»
O
4
5
12
13
14
15
24
25
30
37
33
39
40
41
47
48
49
58
60
67
75
77
80
8"
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
O
0
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
-6
0
0
0
0
0
0
0
.3
n
Z
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
' .1
.1
.1
.1
1.3
1.3
4.6
g*
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88,9
84,1
85,8
85,8
85.8
. 85,8
23.6
23.6
74.0
O
13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
A 9
O«f-f
•3 «
s >
1103
1103
1103
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
lioa
1103
1548
1548 .
1129
58
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No.
Dnit No.
Unit Description
J3 turner
Installation Date
Steam Output (103 Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/?. tfr*.
P$ 3£>0
~/0V
AHibfevf
^-600
Comments:
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location <£*
Unit &
Fuel PS 300
Test No.
Test Type
Test Load (103 lb/hr%
Excess O2 (%)
NOX (ppm) *
NO (ppm) #
O02 dry (%)
PO f Dnm} -it
HC (DDm) V
'•"•'v ipi"'*/ /r
COx» ^r>DTTl} *£
TVrf-al Par-t flb/MRtu)
Solid Part (Ib/MBtu)
Boilcjr Ef f iciGncy (% )
f>n3r*i 1~\/ f§;l
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
r US 1 r 1OW -
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
70-3
t/orrnf.
Air
100
6.b
33-7
3e/
10.4
0, 0y 3 1
S~l y~i 7 ~7ij
ISr V 3 ' f
~7 "7
wv
348
Aw&
6ff^
Jeo
7s-
6,2
&>
74
74
6'^
£~0
70-4
k?uf Air
/OS
4.6
3/7
308
V.0
/44
348
Ai*"b.
640
/&S~
44
2,2
fc
70-6
A/e>r*+>/-
Air
38
7,2
3fft
334
/0.e
,
&^>
Oc.
/40
344
/4wb.
46'6"
/£?*/
/9.f
/,3
&>
70"?
ft/ormf,
Air
. 8t
7,4
334
3/8
u? Ji'r
J0t
4.6
3$S
307
v.&
~
~7Q
/O
/44
34g
Awb.
660
/20
70
J.8-
£&
60
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 2.
Unit &
Fuel P6 300
Test No.
Test Type
Test Load (103 lb/hr)
Excess ©2 (%)
NOX (ppm) if
NO fntsra) ^
C02 dry (%)
CO (ppm) •V
HC (nom} V
SO (DDHI) ^
CO— /DDIIl) V
Total Part (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No .
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
7<5 O
/0, 4
-If-
/•!?
M£~
30
TO-//
A/ormJi
Air
/00
6,6
383
3./Z. eT
3 o5
/&4
Sto-
3l>8
Awb.
6
/poeV
^
fie:
Me
34V
Aw6.
S/0
/6~7
«6.
S&0
/60
43
£8
go
70-/J-
t/orrni.
Air
#£-
&3
4/f
/M
->/. f
cVa
?/"
J6>
/43
344
dH7&.
£7$
/6O
5-8
4.2
60
6 1
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location <
Unit <£
Fuel P6
Test No.
Test Type
Test Load (103 lb/hr'
Excess ©2 (%)
NOX (ppm) *
NO (ppm) ^
C02 dry (%)
CD (ppm) *
HC (ppm) *
cr\ ( nrxm ^ ^
CQ fDDm) rf
'Total Part (Ib/MBtu)
Solid Part (Ib/MBtu)
Boiler Efficiency (%)
fu~ * *- / Q. \
Opacity i%)
Final Stm Pres. (psig)
Final Stm Temp.(°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
T^ii^l fpciTyiT-* f °f?\
ruei ieiup . v r )
Fuel Pres. (psig)
Furnace Pres. (in.I^O)
Register (% open)
7'r
70.0
2,8
4 3 4
— :
13. if
183
e&
/t/4
3 if*'
A**b.
&80
IS S)
/£>&
t/f
2.3
60
70 -/7
A/crwil-
A if
63
6.4
448
/
-------
STACK TRAVERSE DATA
Location No.
Unit No. ^
Test No.
Fuel
Load
Stack Diameter, D
Ib/hr
'duct
0)
1-1
a
8
(U
0)
EH
O
<0
4J
63
-------
o>
Location No. c5
Unit No. &
Test No. 70
-
-
-
-
-
-
-
!
c
-
-
a
3
_._
- d
/
'
?
u
7
-
w
9
-
-
-
s
~
X
z
t
'
u
—
f
s
-
-
-
s
-
-
-
*
s
S
Load /£>&
Fuel /?£
^
'
1
A-
7^
-
s
s
s
(
^
>, £><=> lb/hr
I
A
T
f
-
• Smoke
O CO
X
A
HC
NOX
0)
I
A
u
2
m
1
2,
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
Location No. 2
Unit No.
Test No. 7O
Load
Fuel
Ib/hr
9 Smoke
O co
HC
CD
C/l
U2' *
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
KVB, INC.
TO: Glenn Cato Tech. Memo R-83
PROM: E. D. GUTH j December 17, 1973
SUBJECT: Fuel Oil Sulfur Analyses
cc: Arlen Bell - R. Brienza Tes-t
The following samples were run to determine weight
percent sulfar.
Sample No. Date % W S
Test 70-20 28 Nov. 73 1.10
33-1 6 Dec. 73 .23
Test 59-1 10 Dec 73 .30"
This is a preliminary report. An .official Test
Report will be sent to you as soon as the forms are available.
EDG:es
66
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. 3
Test No. 33,
Unit No. <£
Unit Description Cle£)vcr
Installation Date
Steam Output (10J lb/hr)
Design Pressure (psig)
Final Steam Tercp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
W6&
/0.O
ts-e
360
.Fire tube
go -/a
sa
38
/ £/<£ai/. -SrlS. ffi'wg <£ &/r tftetr?. gr*v.
Afaf. &QS , #-£ 0'7
At*ib/et"t
AiA*bier>t
^
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 3
Unit 2
Fuel
Test No.
Test Type
Test Load (103 Ib/hr^
Excess O2 (%)
NOX (ppm) /
NO (ppm) H-
C02 dry (%)
HC (ppm) y
SO foom) V
cr)_ ^r^nrn) -^
Total Part (Ib/MBtu)
^olid Part flb/MBtul
Rr*i l^T" P"F"F"i CM t^ncv ( % \
Sinoks Spot No •
OO^fM tv f%^
Final ^tm Tpmo (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow . ga/ ///r.
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Register (% open)
33 -/
j(S0r<**i'
Air
6"
6~.8
' I6&
//l
cry
J5/ ^~
C&S
AW&.
30iT
/go
Awb.
//.J~
BB-S
A/0r* o
o
c. /O
4»t&.
300
/&£
dt^fr.
J0.0
33-3
ft /eae/
7
7,2
/7/
/6~2
9.6'
107
m.
&Y
:3/j
c:V
^>£ <£~
Ci&J
d»*b.
3S3~
/00
dwt?.
J3.S
33-4
Mor\** t,
A>'r
^
^.^
/73
M3
^OQcf
3
&0
/66
148
n
37
J»*&-
—
J&?£>,
33-6
ioap toad
. 3
7.o
l&t
H3
/0
S7
Cs
48
Oft
OV
/7 /,
/ftV
^er/i
CO I
J*»&,
3/0
Jl*r&,
//.j-
33-7
A/ffrt~* /.
Air
3~
376
tra
&2
/#.&
SJ
Cs
27
&S?-
c&
^^>er~
ce?5
Jt**£.
30&~
/80
/4i*t6.
//.3
68
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 3
Unit 2
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) /
NO (ppra) -x
C02 dry (%)
CO (ppm) y
HC (ppm) ^
*?O (onm) V
A
^O« fnmn^ V
TVrt-sl PJ=IT-+- /"IH/MRl-iil
Solid Part (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Register (% open)
33 -a
leus A>r
&
4.8
i&&
'33
//.S
0
3a
$0
862
Awb.
3GO
J86
dmb.
/l.f
33-3
l
-------
I
vj
O
Location No.
Unit No. c?
Test No. 33
--
--
--
--
-
-
-
c
c
-
-
—
\
D
J
-
-
-
£
l
T
.
it,
/
n
JC
$
—
1
-
3
-
»
-
3
H
3
•k
§
z
t"
—
I
A
-
*•
_l
-
_.
A
3
-
k
-
<
-
-
-
-
^
^
-
^
-
Load vT^<
Fuel jf<2
-
<*
*
^
rl
-
,
f
h
-
^
t ±
f
^
/
/
•=
j
^
^
/
'
"
*& lb/hr
O»'/
"j
fs
'
k
^
j
/^
n
1
-
-
-
i-
6
-
-
L-
-
-
-
-
-
-
-
-
-
-
• Smoke
O CO
X
A
HC
NOX
§
0)
M
w
o
«J
Vj
(fl
A
o
s
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No.
Unit No. S
Test No. 33
-t
Fuel
Load S~&0&
Stack Diameter,
Ib/hr
1.0
-U
vj
0)
i1
0)
o
<0
4J
W
7 1
-------
KVB. INC.
TO: Glenn Cato - Tech. Memo R-83
FROM: E. D. GUTH ; December 17, 1973
SUBJECT: Fuel Oil Sulfur Analyses Location . 3
C/w't c?
cc: Arlen Bell - R. Brienza Te^-f A/e?. 33
The following samples were run to determine weight
percent sulfar.
Sample No. Date % W S
Test 70-20 28 Nov. 73 1.10
Test 33-1 6 Dec. 73 .23
Test 59-1 10 Dec 73 .JO
This is a preliminary report. An .official Test
Report will be sent to you as soon as the forms are available.
EDGres
72
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 3
Unit <£
Fuel
Test No.
Test Type
Test Load (1Q3 Ib/hr)
Excess ©2 (%)
NOX (ppm) *
NO (ppm) *
C02 dry (%)
CO (ppm) #
EC (ppm) X
cr> / nnTn ) -^
^U2 *PPra' X
TV»i-a1 PA"H- f Tb/MBt\il
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp (°F)
Comb us. Air Temp. (°F)
Stack TV>mn (°F\
Fuel Flow . //*///r.
Fuel Temp. (°F)
Fuel Pres (psi9)
Register (% open)
4/-/
///• S
3
30
Awb.
tfJ-?
/J,-/V6
Awb-
•7 / . **
•540
22.8
Awb,
M-3
4/e? r*n /•
Air
7
7.£-
*}£
83
7,>
— —
*/- ^
f/or»t /•
Air
3~
8.0
/00
93
7,0
'3
asz
dwb.
3^>£~
jcy
te.0
dfrrb.
—
4/'^
4eee?
£0ac/
3
t/.s
M
100
&$
o
163
~7Q
'&
Awi?.
9.6
A*ib.
4/-6
&ST4
ocG
/9.S
A i+i fr.
^/-7
A/0rm/,
Air
£-
&g
80
76
6.6
O
36-£
OS)
^>£./-)
C eye*/
Ai~b,
3s~)S~i
/a
4l*r£>,
/•? tj -»
ex. y /
-.
3%
73
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 3
Unit 2.
Fuel
Test No.
Test Type
Test Load (103 lb/hr>
Excess ©2 (%)
NOX (ppm) )(
NO (ppm) X
C02 dry (%)
CO (ppm) if
HC (ppm) #
SO (ppm) )(
^Q^ fmanil •*£
• TVii-al Part ( lt>/MBtu)
Solid Part. (Ib/MBtu)
Snioke Spot No *
fYri^rM 1~v (^\
Final Stm Temp (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow •//*/&•
Fuel Temp. (°F)
Fuel Pres (psig)
Register (% open)
ff/-8
Soety Air
3~
0. 7
S3
4 $000
£3a
Awb,
*1f
AVH&.
b/'r
&
6.3
7a
62
7,8
&
e^-r
^)S~) -O
c?C>.<9
^>£s>
c;e>&
Awb.
3o
Aw&.
S) s. ~~y
(/•47
4/-/0
Jenx? S?»r
jr
3.6
66
£a
^>^.a
c?&&
Jwb.
300
/(? 0
dtrtb.
S) /, •?
(s. L/5
-------
Location No. 3
Unit No. <£
Test No.
Load
Fuel
Ib/hr
O Smoke
O CO
X HC
A
x
VJ
en
/c?c?
o
z
0)
10
Vl
(0
•s
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
//is»/<7 3
/ ^
*>
41
1
4
' 5
12
13
14
15
24
25
30
37
38
39
40
47
48
49
58
60
67
69
75
77
80
FUEL ANALYSIS SUMMARY
Gas Fuel
s"
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
^
cf
0
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
.6
0
0
0
0
0
0
0
.3
M
z
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
.1
.1
.1
.1
1.3
1.3
4.6
If
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88.9
84.1
85.8
85.8
85.8
.85.8
23.6
23.6
74.0
^
ct
U
13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3,4
0
13.2
0
3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
Heating
i (Btu/«t3)
m
2%
X >
1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548 .
1129
76
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No. 3&,
Unit No.
Unit Description
Installation Date
Steam Output (10J Ib/hr)
Design Pressure (psig)
Final Steam Ten?) (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner ( °F)
Primary Air Temp (°F)
Stack Temp (°F)
/960
eo
£0O
386"
j&re tub<2
20-/3~
/06
4>7
/
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit ^
Fuel A/a
Test No.
Test Type
Test Load (103 lb/hr)
Excess O2 (%)
NOX (ppra) #
NO (ppra) •*
C02 dry (%)
CO (opm) ¥
HC (ppm) *
co frinni} -i/
co*^ foDin} 4l
OW2 I"""/ *
-TVi-t-al Part flb/MBtul
O/-O •! /? "Da r-f- ^ 1 H /MR-f-n ^
Boiler Efficiency (% )
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp.(°F)
Combus. Air Temp. (°F)
C+-ar*V Tomr» ( °P^
Fuel Temp. (°F)
Fuel Pres. " (psig)
FnTTi^r*^ PT"f><^ fin H«.O^
Register (% open)
38 -t
M'S0e>cf
/&£-
6.3
/*3
?;
7,7
76
/to
3W'
Awb-
£/£?&
Awb.
O.6
38-8
103
88,
7,8
6act
4.5"
#0
If
86
b8
foa
90
zsa
/4»*6.
d^b.
e.76~
3S'£-
4/Or***/-
Air
M0
7.2
M
/Ol
7,3
78
/S3~
3fg
d**fb.
dw^.
0,63
38-6
fcus /4/r
. M.0
£.0
"
78
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location v
Unit 4
Fuel
Test No.
Test Type
Test Load (10 3 Ib/hr)
Excess O2 (%>
NOX (ppm) *
NO (ppm) X
C02 dry (%)
HC (ppm) X
cn f nnm \ •»£
SO** fDDm) -^
Tt>tal Part. (Ib/MBtu)
^olid Part ( lb/MRtu^
Hoiler Efficiency {%)
.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in H^O)
Register (% open)
3g-g
£0KJ dlf
W.0
• 7
7*9
7S.
/a 3
*i&G
&
/3S
360
A"*b.
A^b.
Q,66~
38'?
A/orwl.
Air
?..
Awb.
0.66'
38 -to
M- Air
£3S
C*7&
W
/3tT
J&&
Ai**&-
4w£>.
0.66"
38 -S3
Afartr?/'
Air
. M.0
7.3
W
&
0.4'0
-------
Location No.
Unit No. 4
Test No. 38
Load 9,0e>&
Fuel
Ib/hr
• Smoke
O CO
HC
oo
o
o
X
-------
GO
&O-
I
ft
7/7 —
» / V —
CJ
K
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
1
(
C
Location No. <,
Unit No. */
Test No. 38
-
-
ii
3
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
:
-
-
-
-
-
-
-
i
r
-
/
C,
"
f.
O
-
-
—
-
•
c
-
X
f
t
-
-
-
-
-
•^
X
V
-
A
Q
-
-
—
-
-
-
-
-
:
-
-
-
e
3)
ft
-
:
._
-
k
Or-
Z|-
-
-
-
-
-
-
-
-
-
-
-
-
-
--
-
-
-
-
-
-
-
-
.—
-
/
-
-
-
-
-
-
a
_
.-
Load /4
Fuel /
t,
-
-
^
-
^x
-
=
>
-
-
-
Mt
-
-
-
-
-
-1
-
-
/
^<
ft
-
-
^
^
-
^
>
-
?
S
/
/
— j
/-
--
<^-
^
j
-
^
-
-
-
—
-
-
-
• Smoke
O CO
-
-
X
A
-
HC
NOX
-
--
--
--
°
2' *
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
u
(!)
M
-P
O
O
rH
-------
fy FUEL ANALYSIS SUMMARY
Gas Fuel
38
41
t>
4
5
12
13
14
15
24
25
30
37
39
40
41
47
48
49
58
60
67
69
75
77
80
n
O
U
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
n
O
0
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
.6
0
0
0
0
0
0
0
.3
z
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
.1
.1
.1
.1
1.3
1.3
4.6
6*
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85,8
95.6
88.9
84.1
85.8
85.8
85.8
.85.8
23.6
23.6
74.0
<£
X
n
U
13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
-C 9
2?
a >
1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548 -
1129
83
-------
KVB. INC.
TO: Glenn Cato Tech. Memo R-83
FROM: E. D. GUTH : December 17, 1973
SUBJECT: Fuel Oil Sulfur Analyses
cc: Arlen Bell - R. Brienza
The following samples were run to determine weight
percent suliar.
Sample No. Date % W S
Test 59-1 10 Dec 73 .30 >
• ,f
This is a preliminary report. An .official Test
Report will be sent to you as soon as the forms are available.
EDG:es
84
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No.
Unit No.3
Unit Description Cle
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit 3
Fuel Wai,
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) X
NO (ppm) X
C02 dry (%)
CO (ppm) /
HC (ppm) #
SOX (ppra) *
SO2 (ppm) ^
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow .
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.J^O)
Register (% open)
6e-/
tformt.
J,Y
/0
/,$-
J&6
i00
10. 6
<&.
A«»b.
0.4
0$
86
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit *t
Fuel #<
Test No.
Test Type
Test Load (103 Ib/hr)
Excess 02 (%)
NOX (ppm) )(
NO (ppm) *
C02 dry (%)
CO (t>ran) •)(
HC (ppm) x
cn f nnTTi J -rf
cr)^ foDin) V
-TV-kt-^l P^y-h fTH/MRhn^
Solid Part (Ib/MBtu)
Rrt-J 1 or fff i r^T ^nr^ir /&\
Sinolce Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp (°F)
Corabus. Air Temp.(°F)
Stack Temp (°F)
Fuel Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Register (% open)
^-/
BG6£
9,3
&.S
190
181
//.o
$6
1 ~7"3
I/O .
IS &
loo
/) rt ^ Q /
O, Vc&l
/) SJ/£j£~
Cf' f / T"i5
O £T
03
A™k>-
ZOiT
•j'Yo
78
/7
&*?'*-1
M- 4>r
9,3
6.&
143
/8a
/0.O
£4
Aw&.
78
/7,&
S'r
/#.j~
6.2
183
176
10. *f
3f
dw£.
70
/r~*/.
A-'r
. /4
78
/9
*>'
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location V
Unit 4
Fuel #2 Oif
Test No.
Test Type
Test Load (103 Ib/hr)
Excess 02 (%)
NOX (ppm) *
NO (ppm) *
C02 dry (%)
CO (ppm) #
HC (ppm) y
SOX (ppm) #
SO2 (ppm) #
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow .
Fuel Temp. (°F)
Fuel Pres. '(psig)
Furnace Pres. (in. 1^0)
Register (% open)
£-
-------
Location No. y
Unit No. £
Test No. £
1
(
fc
f
»-
it
-
-
-
~
-
-
V
O
n f
L
-
T
't
-
L
L-
/t
:
?
-
-
-
-
-
-
-
-
-
-
1
X
g
-
_
-
^-
-
-
-
-
_
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
J
J
\
*
O 1 £
k
\
-
-
-
-
-
/
I —
\
-
—
~
-
/
Load 9, 3e.
Fuel ^f
v
-•
--
1
)
/
»
\
:/
V
3
•^
-
-
-
/
-
^
—
-
y
\
-
-
r
-
\
-
f
*\
_
/
y
s
i
- i
^
J
s
?o
Qi'r
*
kr
.
f
-
-
^
/
/
-
f
lb/hr
A
-
—
f
-
:
-
°2
t--
^t
f
--
\^
-
-
-
-
-
-
-
-
0
O
-
Smoke
CO
-
-
-
-
X
A
HC
NOX
-
-
-
-
-
-
-
— •
-
-
-
-
-
-
1
on
1
T)
0)
0)
7
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No.
Unit No. 4
Test No. ^~
-------
FUEL ANALYSIS SUMMARY
Gas Fuel
Test
8
•
c
4
S
12
13
14
15
24
25
30
37
38
39
40
41
47
48
49
58
67
69
75
77
80
n
8
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
2
0
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
.6
0
0
0
0
0
0
0
.3
n
X
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
.1
.1
.1
.1
1.3
1.3
4.6
5*
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88.9
84.1
85.8
85.8
85.8
. 85.8
23.6
23.6
74.0
X
c«
U
13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
n
•
a a
1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548 -
1129
9 1
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No.
Unit No. 7/6'-
Unit Description
Installation Date
Steam Output (10J Ib/hr)
Design Pressuia (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner ( °F)
Primary Air Temp (°F)
Stack Temp (°F)
/*£-«'
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location .5"
Unit 7/6-3
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) #
NO (ppm) *
C02 dry (%)
CO (ppm)*
HC (ppm) X
SO (pom) #
J3VJ2 VPP"1/ *
Total Part (Ib/MBtu)
Cnl i r? Payt- MV»/MTH-r^
Boiler Efficiency (%)
Smo)te Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Register (% open)
4-/
Hi Soac/
O. OC/3CS
0, 00 /3
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77
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7.4
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66
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344
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398
dw&-
£-.6'
4-<6
A/erml.
Air
. £0
S3
9.4
37&
4/
//
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location £~
Unit 7/6 ' 3
Fuel Mai-
Test No.
Test Type
Test Load (103 Ib/hr)
Excess ©2 (%)
NOX (ppm) •/
NO (ppm) /
C02 dry (%)
CO (ppm) X
HC (onm) -if
SO fooro) •)(
co^ fmDinl if
• TY^i-al Part flb/MBtu)
^not" No
Oriar*! t*V f%}
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Flie»1 Plow Sf3///f
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Register (% open)
4-8
£oc*j Ji'r
/3.f
6.7
80
76
7,C
&
J&8
3bb
At*i h
4
iaaJ
AV8
4&$~
4,4-
4-/Z
£0l*S
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4.1
6&
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8.8
o
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JCs
//7
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4Sf
4.6'
4-/S
//,- 4,r
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6^,8
80
77
7.8
O
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//7
3*0
466
4.6"
4-/4
J/0rw/.
Air
//,&
8.1
se
73
&
70
- .
//
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location S"
Unit 7/6 '3
Fuel /!/«/-
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) *
NO (ppm) -X
C02 dry (%)
CO (ppm) -X
HC (ppm) *
CO tornn) i.'
SOo fDDm) -t-al Part- nb/MRtu)
^olid Part db/MBtu}
Boiler Efficiency (%)
Smolce Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow . {J3///r
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres (in H-^O)
Register (% open)
T
I/.0
7,0
7V
71
7,2
O
31
1/8
348
AkW&B
466
-/6
6t?tx?
/fir
//.0
6.3
67
65
7,6
O
-------
CO
O5
0,
Location No. £~ Load /<£, 0OO lb/hr
Unit No. 7/6-3 Fuel X^?/. &>Q6
Test No. ^
--
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-------
CO
I
ft
u
Location No. S Load //,&£>&
Unit No. 7/6-3 Fuel V&i. &Qi
Test No. <^
30-
-
-
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-
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-
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-
-
-
-
-
-
-
-
X
A
-
-
HC
NOX
-
--
--
8
°
'2'
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No. £~
Unit No. 7/6 -3
Test No.
Fuel
Load
Stack Diameter, D
Ib/hr
duct
1.0
98
-------
7/6 -v
FUEL ANALYSIS SUMMARY
Gas Fuel
A/0.
14
5
12
13
14
15
24
25
30
37
38
39
40
41
47
48
49
58
60
67
69
75
77
80
n
8
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
O
0
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
.6
0
0
0
0
0
0
0
.3
z
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
.1
.1
.1
.1
1.3
1.3
4.6
6*
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88.9
84.1
85.8
85.8
85.8
. 85.8
23.6
23.6
74.0
to
13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
f!
a 5
1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1103
1108
1103
1108
1548
1548
1129
99
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. >£>
Test No. 37
Unit No.
-3
Unit Description
3fo*?c/0re/ ,
Installation Date
Steam Output (10J Ib/hr)
Design Pressui 3 (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
W68
/ao
30
270
Ft re tf&ts
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location £~
Unit
10, C/
,-7
/O /
37-3
Air
s
7,0
£-r> /-?
c^C/,^
._,
/ f Cs
/) S~)"7
is, (*/ I
37-S-
//r/00
C?(/i &
/7&
/ /tX
f? S7<3
is. C/7
37-6
"jfr
. 8
/.
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location ~S
Unit lid Part (Ib/MBtul
Boilcjr Ef f icicncv (% )
SinolcG Spot No
On^r*! t*v ( %i\
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
mn (°F^
T**itol Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H-jO)
Register (% open)
37-8
Base-
8
S.f
S6>
S3
84
<7
/^
/n *-)sn ^C 2
C/, CJcs & o
&* c/C/jtf
£0.£~
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An*6.
O fZ"
c 76
/}w6>.
0.06
37-.
O.Otf
30/0 Os
\ 02
-------
o
CO
a
--
--
--
-
-
-
-
Location No. >
Unit No. £?4g
Test No. 37
-
a.
ft
ft
o
u.
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
f
V
~f
a
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-
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if
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-
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HC
NOX
-
-
--
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
o
HI
w
4J
g
rH
Q)
0
10
-M
W
Location No. -6
Unit No. c?^g-3
Test No. 37- g
Fuel
Load &, e>e?G>
Stack Diameter,
Ib/hr
10
8
CNL
O L
X
IS
i ' i
! i i
'
A'
-ia.
i i
5
^\
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V
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t I I
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i rr
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st
42
ZtZ
•aeo
-S70
^
.5
D/D Duct
1.0
b
o
X.
O
(0
4J
W
*J
CO
1 04
-------
Test
3~7
FUEL ANALYSIS SUMMARY
Gas Fuel
I
4>
m
a
t>
4
5
12
13
14
15
24
25
30
38
39
40
41
47
48
49
58
60
67
69
75
77
80
*
n
8
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
»
n
O
0
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
.6
0
0
0
0
0
0
0
.3
«
n
2
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
.1
.1
.1
.1
1.3
1.3
4.6
^
5*
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88.9
84.1
85.8
85.8
85.8
.85.8
23.6
23.6
74.0
*
to
X
n
U
13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
•5
•
X 3
I?
1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548 -
1129
1 05
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No. S8
Unit No.
Unit Description
Installation Date
Steam Output (10J Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
8.0
30
270
-F/'re t(sb<°
2D -<9
66
31
/ /3it5
Awb>'er?t
Ai^&ieirtf
"- <23O
Comments:
1 06
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit
Fuel /\/oi.
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppra) *
C02 dry (%)
CO (ppm)#
HC (ppm)#
SO f DDm) -if
SOo (ppm) y
Total Part (Ib/MBtu)
i*J
£e?e*cf
4.8
//.I
63
61
4.4
0
4i
12.0
o.oa
3~8-4
£0ttS
£
£000?
/,6
/S.0
s£-
G.of
f&-7
£e>c*J?
4,'r
6.4
&<>-
5-3
sa
8.5
H6-
25^
/3,o
0,04
Oz
1 07
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm) *
NO (ppm) X
C02 dry (%)
CO (ppm) -X
HC (ppm) *
SOX (ppm) X
SO2 (ppm) #
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No. -
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow .
Fuel Temp. (°F)
Fuel Pres." (psig)
Furnace Pres. (in.H2O)
Register (% open)
6~8 -8
*"*%-
6. if
3.2
47
33
9.4
>20c? otf
O- OO£*f
J2.0
Awb.
stq
A^b.
•
08
-------
Location No. £~
Unit No. £b8 -f
Test No. &Q
c?C>o -
IOO-
S 1
CD
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-
-
-
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1
-
-
-
-
-
-
-
-
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-
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-
-
-
£
3.
3!
3
L-
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-
-
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0
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CO
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-
-
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-
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-
X
A
-
HC
k NOX
-
-
-
-
__.
--
ID
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
Location No.
Unit No.
STACK TRAVERSE DATA
Fuel
Load
Ib/hr
o
i
t-i
0)
?"
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o
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-------
j- FUEL ANALYSIS SUMMARY
-/ Gas Fuel
It
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4
5
12
13
14
15
24
25
30
37
38
39
40
41
47
48
49
60
67
69
75
77
80
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0
0
0
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0
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2.5
2.5
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4.6
4.6
4.6
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4.6
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6.3
3.9
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3.9
6.3
8.4
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1.3
1.3
4.6
6*
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88.9
84.1
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85.8
85.8
. 85.8
23.6
23.6
74.0
to
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13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
3.4
6.7
1^5
X J • £•
13.2
13.2
13.2
69.7
69.7
20.6
x ~~
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£ a
x >
1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548 -
1129
1 1 1
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. & Test No.7 &r**s.
4
0
A/oi- &&& / # <2 &
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit 3
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
-NOX (ppm) -#"
NO (ppm) *
C02 dry (%)
CO (ppm) *
HC (ppm) *
SO (Dem) ^
SO-i (ppm) it
•Total Part. (Ib/MBtu)
Solid Part (Ib/MBtu)
Boiler Efficiency (%)
Smok*1 Spot No .
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Comb us . Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow //y//- X /O3
Fuel Temp (°F)
Fuel Pres. " (psig)
Furnace Pres. (in.J^O)
Register (% open)
c?-£T-/
/#?/•*•*/.
A,T
8&
/4.&~
/8V
/
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit ^
Fuel
Test No.
Test Type
Test Load (103 lb/h^ )
Excess O2 (%)
NOX (ppm) if
NO (ppm) y
C02 dry (%)
CO (ppm) #
HC (ppm) /
CO fririin) *£
•^^v V_Kr*m' T*
CQ— frynm) ^
•TVif-al PAT-*- M Vi/MRtn)
<^n1 1 ri Part- fib /MR tu)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow .//•*/& */03
tSicil T*£iniT-» /O"P\
Fuel Pres. ' (psig)
Furnace Pres. (in.^O)
Register (% open)
2£~-8
tou? 4,r
120
//*
a^3
243
b~.G
38
<37
2go
tee'
3/S
<26Q
U8
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212
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////"
. //f
///
268
268
<*.
-------
en
Location No. 6
Unit No. 3
Test No.
Load //&,
Fuel A/at.
Ib/hr
• Smoke
O co
X HC
A NOS
I
ft
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
o
0)
CO
+J
M-l
>1
-P
-H
O
O
•-I
0)
^
u
«J
-U
w
Location No.
Unit No. s3
Test No.
Fuel A/at-
Load
stack Diameter,
Ib/hr
•'
^^
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0)
M
3
0)
0)
H
0
03
w
+j
w
1.0
1 1 6
-------
''0t4 &
3
4/p.
11O8
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548 .
1129--
1 1 7
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit 3
Fuel
Test No.
Test Type
Test Load (103 lb/hr^
Excess O2 (%)
NOX (ppm)*
NO (ppra)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
SOX (ppm)*
SO2 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow go/, ///r.
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.J^O)
Register (% open)
**'-/
&asc
HS-
£-2
18^
Soo
7.7
//
//cd7
8b
f
/00
6^-6
tf*-r
. /
-------
CD
a
o
Location No. <£ Load /3C> lb/hr 9 Smoke
Unit No. 3 Fuel & g &>/ O CO
Test No. ^"^T
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--
--
--
°2' %
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
NJ
CD
I
04
u
Location No. <=
Unit No. 3
Test No. ££~
—
--
--
--
--
_._
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Fuel Xc7 <=?'y
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^
/£>
//
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No.
Unit No. 3
Test No.
Fuel /«?
-------
REPORT
TRUESDAIL LABORATORIES, INC.
CHEMISTS - MICRQBIOLOGISTS - ENGINEERS
RESEARCH — DEVELOPMENT — TESTING
HJENT
SAMPLE
P.O. No.
INVESTIGATION
KVB Engineering
17332 Irvine Boulevard
Tustin, California 92680
Attention: Mr. Glenn Cato
3 oil samples - EPA SN-60
1700-43
Analyses rnd tests as requested
RESULTS
Sample identification:
No. 1
4101 N. FIQUEROA BTREt
LOB ANGELES 9OO«
AREA CODE 213 • 228-ISt
CABLES TRUELAB
DATE February 27, 1974
RECEIVED February 4, 1974
LABORATORY NO. 120913
Unit #3, Test #65-1, January 2, 1974
Carbon, 7.
Hydrogen, 7.
Nitrogen, %
Ash, 7.
Carbon Residue, 7. (Conradson)
API Gravity at 20°C
Viscosity at 40°C, SSU
No. 1
86.05
13.14
0.018
0.005
0.066
33.4
35
V ' •-•• -V
W w -' rj
.A
Respectfully submitted,
TRUESDAIL LABORATORIES, INC.
A. W. ZneiS M.S.
Chief C>emist
1 22
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. 7
Test No.
Unit No. 3
Unit Description B W
Generator. Contract
Installation Date
Steam Output (10^ Ib/hr)
Design Pressure (psig)
Final Steam Temp (CF)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
jq&o
0&-
3oo
420
W&ter + ube
W-M -8
840
/S70
fy J3$U/ 3team aforrr, £?'/ qw5
S'- 7"
#£-&!/
J72
•^240
«- £34
Comments:
1 23
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 7
Unit 3
Fuel #6~
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 7
Unit 3
Fuel tf 6~ (?•'/
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
CQ fnnml*
ov vpf1"/
CQ_ fnnirO*
Ttotal Part (Ib/MBtu)
Solid Part (Ib/MBtu)
Boiicjr Kf f iciGncy (% )
SiuolcG Spot No
Or};ar«i i~v f%^
Final Stm Pres. (psig)
Final Stm Temp. (°F)
f*oniV>n^ AT y T^mri ( °P^
Stack Temp. (°F)
Fuel Flow .qa/ /**<'*
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H20)
Register (% open)
6-0
A/e?r>~tl-
Afr
&6
7.6
336>
3S-8
fo,0
27
e*t
8
2se
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 7
Unit 3
Fuel # £~ 0'f
Test No.
Test Type
Test Load (103 lb/hr'
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
or) fnnm)*
ov-> vpjjm/
•TVrt-al Part flb/MBtu)
cinl -id Part- (Ib/MBtu)
Boiler Efficiency (%)
Oriafi t~v (%}
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Stack Temp. (°F)
Fuel Flow .qal/i*iiii*
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
6-/s
/ft /7 1 9
£j /*
/0.3
340
36iirt
C"ts
287
7,6
/7Z
3
6"
-0./S-
00
<£-<=>/
#4300$
30
/2.<9
338
34a
6.4
44
46-
227
336
.3/jS)
C^ts
270
3.S"
/£*?
te~
-0J7
/?0
at 3% O dry
1 26
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 7
Unit 3
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
KOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
en (nnnO*
i3VJ VHP"'/
CO /DDITI}*
TV>tal Part flb/MBtu)
Solid Part (Ib/MBtu)
Boiler Efficiency (*fc )
QrnoVf* 4ff*0S
4
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 7
Unit 3
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess ©2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
CQ fnom)*
CQ*% ftJOm}*
• *TYi-f-al Par~t- /TH/MRt-ii^
Solid Part (Ib/MBtu)
Ori^fi "f-v f%^
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow .&a/. /#?'*?
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.J^O)
Register (% open)
6-29
P/B00S
3W
/a^
e
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 7
Unit 3
Fuel # 5" <
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
SO (tram)*
SO-. (DDirO*
-•total Part (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boilsx Ef f iciGncy (% )
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow . 6a/./mtw
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
6-36
#3£5
63
6.0
174
174
I/, 4
24
7
a/
S00
6-39
#3000$
£-*/
#/e0&5
. 4/
&f
243
.248
/o.o
28
21
£40
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 7
Unit 3
Fuel
Test No.
Test Type
Test Load (10 3 lb/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
SO (ppm)*
A
co« fnom}*
•TYji-al Part flb/MRtu)
Solid Part. (Ib/MBtu)
^Tnr»Vf» ^not* No
Onapit'v (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow G>al./*r*ir>-
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.I^O)
Register (% open)
^-^5
#/ff
-------
30-
u
a:
Location No.
Unit No. 3
Test No. £
—
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—
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Tr
--
--
—
--
6
a
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
Location No. 7
Unit No. 3
Test No. £
Load
Fuel # S
Ib/hr
• Smoke
O co
X HC
A NOV
£0 1
u
O
2
O
a
u
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
Location No. 7
Unit No. 3
Test No. <<
Load
Fuel
Ib/hr
//
9 Smoke
O co
X HC
A NO,
,. 4O-
co
._ o
u
Bl-
ft1.
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Emissions for Industrial Boilers as a Function of Excess Oxygen
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Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
REPORT
TRUESDAIL LABORATORIES, INC.
CHEMISTS - MICROBIOLOGISTS - ENGINEERS
RESEARCH — DEVELOPMENT — TESTING
KVB Engineering
17332 Irvine Boulevard
Tustin, California 92680
SAMPLE Attention: Mr. Glenn Catb
3 oil samples - EPA SN-60
T.O. No. 1700-43
INVESTIGATION ind tests as requested
3
M?
Sample identification:
RESULTS
4101 N. FIGUEROA STREE
LOS ANGELES 9 O 06
AREA CODE 213 • 22B-IEi
CABLE! TRUELAB
DATE February 27, 1974
RECEIVED February 4, 197A
LABORATORY NO. 120913
j Boiler #3, Test No. 6, January 8, 1974
Carbon, %
Hydrogen, %
Nitrogen, 7.
Ash, %
Carbon Residue, 7. (Conradson)
API Gravity at 20°C
Viscosity at 40°C, SSU
No. 2
85.65
12.06
0.32
0.010
3.27
21.0
228
4
4>
-
Respectfully submitted,
TRUESDAIL LABORATORIES, INC.
AU 7s*fin*vr M ^
• w » tyiiincjr j in. o *
Chief C>eniist
1 36
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No. 23, 74
Unit No.
unit Description
Installation Date
Steam Output (103 Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/9W
HO
a$o
45-0
Wa+ertisb
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 8
Unit 10
Fuel
4 8%
Test No.
Test Type
Test Load (1Q3 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
cry (onm)*
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Ttotal Part. (Ib/MBtu)
Solid Part (Ib/MBtu)
Rni 1 p*Y" Pf "F"i r*i pncv ( % ^
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Final Stm Pres. (psig)
Final Stm Temp. (°F)
Stack Temp. (°F)
1
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Fuel Pres. ' (psig)
Furnace Pres. (in.I^O)
Register (% open)
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-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location S>
Unit /0
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Test Type
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NOX (ppm)*
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en (nnm)*
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Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No. S Fuel #<6~ 0'/ $ tfcji'very £?aj
Unit No. /O Load £*?, 70 O lb/hr
Test No. 23 -]£ stack Diameter, Dduc<_ £3"
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-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 8
Unit /o
Fuel
Test No.
Test Type
Test Load (103 Ib/hr
Excess 02 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
SO (DOTI)*
cry_ /nnml*
aw2 »Pi^'"'
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Solid Part. (Ib/MBtu)
RrjT 1f»T" ff £ ici_
-------
RUESDAIL LABORATORIES. INC.
HEMISTS - MICRDBIDLOGISTS - ENGINEERS
CSEARCH - DEVELOPMENT - TESTINO
4IOI N. FIGUEROA STREET
LOB ANGELES 9OO66
AREA CODE 213 • 225-1564
CABLE! TRUELABB
IIENT
iMPLE
KVB Engineering
17332 Irvine Boulevard
Tustin, California 92680
Attention: Mr. Glenn Cato
3 oil samples - EPA SN-60
.0. No. 1700-43
iVESTIGATION Analyscs and tests as requested
8
766+
Sample identification:
RESULTS
DATE February 27, 1974
RECEIVED February 4, 1974
LABORATORY NO. 120913 .
No. 3
Boiler #10, Test #23, January 11, 1974
Carbon, 7.
Hydrogen, 7.
Nitrogen, 7»
Ash, 7,
Carbon Residue, 7. (Conradson)
API Gravity at 20°C
Viscosity at 40°C, SSU
No. 3
85.83
13.22
0.16
0.017
3.26
30.0
272
T
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Respectfully submitted,
TRUESDAIL LABORATORIES, INC.
.
. W. Zaifmer, M.S.
VvW'v
«2-<
I 4 3
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No. /5"
Unit No.
Unit Description
Installation Date
Steam Output (103 Ib/hr)
Design Pressui * (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/'"
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess ©2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
tip fnrvmA*
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Opacity (%)
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Final Stm Temp. (°F)
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Stack Temp. (°F)
Fuel Flow .(JJ3///r.Jjf&
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.I^O)
Register (% open)
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218
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4
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 9
Unit gC -/
Fuel
Test No.
Test Type
Test Load (103 lb/hrs
Excess ©2 (%)
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STACK TRAVERSE DATA
Location No.
Unit No. 3£
Test No. Xf"-
Fuel
Load
Stack Diameter, D
Ib/hr
duqt
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600
\ 4 8
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
-------
FUEL ANALYSIS SUMMARY
Gas Fuel
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5
12
13
14
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37
38
39
40
41
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48
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67
69
75
77
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85.8
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13.2
13.2
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20.6
20.6
20.6
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20.6
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13.2
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13.2
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13.2
13.2
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69.7
69.7
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1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
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964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548
1129
1 50
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (Doml*
SO (com)*
co_ fnmn}*
Total Part. (Ib/MBtu)
^nli d Part- fTh/MRtu}
Rni 1 f»T" Fffi r*i pnr*v ( % }
Smoke Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Tf>mn /°F1
Fuel Flow [-(i3/ Mr. )*&
Fuel Temp (°F)
Furnace Pres. (in.H2O)
Register (% open)
24 -'
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&*»-*,
£4 _ ~7
Sou, /t,r
/3*r
2.6
33
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit 8£-
Fuel A/at/,
Test No.
Test Type
Test Load (103 lb/hr^
Excess 02 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC fnnm}*
Cfl / nnm \ *
'S^JV \etrUl'
SO2 (ppm)*
•1V»i-al Pa>-+- M H/MRi-ii}
Colic? Part flb/MBtu)
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
C-f-aolr ToTTir\ ( °V\
Fuel Flow {jJ3/Atr.)x&
Piiol Tomr» f °F^
Fuel Pres. ' (psig)
Furnace Pres. (in.^O)
PoOl
-------
en
co
Location No.
Unit No. 8C
Test No.
m*f
j
M—
-
Load /3£~/ O&&
Fuel A/&f/» £r
-
-
-
-
-
~
z.
-
-
-
-
-
-
5
(
—
-
i
•*
4
-
-
5-
y
-
$
-
-
»-i
-
-
-
<
-
4
-
-
-
-
p-
-
*
-
-
-
-
-
**•
-
-
-
-
-e
>
-
^
~
...
—
k
-
-
-
-
-
\
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
_
lb/hr
36
-
-
-
-
-
-
-
-
-
-
-
-
-
-
—
_
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
._
-
-
-
-
—
-
-
--
—
-
-
-
-
-
-
-
-
-
-
-
-
® Smoke
O co
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
_
-
-
-
-
-
-
-
-
-
_
—
-
X
4
-
HC
i N0x
-
-
-
~
-
-
-
-
-
-
-
--
--
--
--
--
2'
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
FUEL ANALYSIS SUMMARY
Gas Fuel
a
m
V
H
4
5
12
13
14
15
25
30
37
38
39
40
41
47
48
49
58
60
67
69
75
77
80
*
M
8
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
n
O
0
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
.6
0
0
0
0
0
0
0
.3
CM
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
.1
.1
.1
.1
1.3
1.3
4.6
g*
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88.9
84.1
85.8
85.8
85.8
. 85.8
23.6
23.6
74.0
0*
13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
e <•
11
X
JB J3
» >
1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548
1129
1 54
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No.
Unit No.
- /
Unit Description
Furnace ,
? PF/-3/38
Installation Date
Steam Output (10"* Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/77/
3 4/00
<- eeo
Comments:
1 55
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location $
Unit VA -I
Fuel A/at/.
Test No.
Test Type
Test Load (1Q3 ib/hr^
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
en (nnm)*
co_ fnnml*
•Total Part (Ib/MBtu)
Solid Part (Ib/MBtu)
Roilpr Efficiency (%)
fViar»-i +*V f%l
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow {MSZFH)
Fuel Temp (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.l^O)
Register (% open)
3&-/
A/crrm /.
/4/r
/
£93
b&
Z.tT
I7J
168
to,t
a<*
20
&2
JS4
40/
?
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 9
Unit VA - /
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NO foom)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
qr\ fnran}*
SO** fntsinl*
•Total Part (Ib/MBtu)
'Solid Part fTh/MRtti}
Roilt*!" Kf f*T fi f^npv f*k)
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow (M6CFMJ
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
30-8
M A,r
/#4
4,3
P/in
Soo
/T**f ^>
47
47
74
30-3
ttJif
/8fy
S,O
IGt?
i"t)
I9b"
rn* /,
A,r
. /43
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit V4-I
Fuel A/a//-
Test No.
Test Type
Test Load (103 Ib/hr'
Excess 02 (%)
NOX (ppm)*
NO (ppm)*
002 dry (%)
CO (ppm)*
HC (ppm)*
C A / r*»T-»TTl ^ *
»ux ippm;
°*J2 "JfJf1"'
•TVifal Par-t flb/MBtu)
Qol i A P^-rt- f Ih/MRtuJ
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow .(MSCFH)
PMol Tomr* ( °F\
Fuel Pres. " (psig)
Furnace Pres. (in.I^O)
Register (% open)
J<7-/5~
tea? di'r
2^^
$.3
/
/
ry/j
07
sia
5-Sf
3r
/
28?
2"?tS
&06~
Z
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location v
Unit I/A - /
Fuel 4/a//-
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (t>t>m)*
en fonml*
SQ-v (DDin}*
•Total Part (Ib/MBtu)
/
>S1
/&
/00
30-^3
4/0 r*M/'
Air
2/0
2,3
182
183
/0. 4
tf
/)
Cs
2s?£j
•DC/1/
£-/, y
5 V3
2 a -2
303
^2tT7
/
J04.
2.2
7 SI
3.9
/0&
3&-t>
S/6
2,0
/. rt
4-8
ec
3
J/C
&S4
2 &&
J&&
Jss
c6t>
230
6.1
/, /y
y. 7
00
30-27
/3 ffoos
.t?^
28
/
S60
O/i
aV
US
O'/
/"'s—/
S^^/
20-7
JO f
•3 -7s-,
C '0
ez
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit \/A -
Fuel
Test No.
Test Type
Test Load (103 lb/hr}
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
SOX (ppm)*
SO2 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow {M£cFtfJ
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
30-
-------
Location No. *?
Unit No. l/A'f
Test No. 3c>
Load
Fuel
Ib/hr
• Smoke
O co
X HC
A NO
1
ft
o2, %
Emissions for Industrial Boilers as a Function of Excess Oxygen
£
0)
CO
o
IB
<3
O
id
CO
-------
STACK TRAVERSE DATA
Location No. *?
Unit No. I/A- '
Test No.
Fuel 4/a//
Ib/hr
Stack Diameter, D
l.o
1 62
-------
0 FUEL ANALYSIS SUMMARY
VA -1 Gas Fuel
f>
frt
4
5
12
13
14
15
24
25
te^ao
37
38
39
40
41
47
48
49
58
60
67
69
75
77
80
n
8
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
n
O
0
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
.6
0
0
0
0
0
0
0
.3
n
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
.1
.1
.1
.1
1.3
1.3
4.6
g*
85.8
85.8
85.8
85.8
74.0
74.0
74. 0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88.9
84.1
85.8
85.8
85.8
. 85.8
23.6
23.6
74.0
o
n
U
13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
P
ll
1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548
1129
163
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No.
Unit No.
Unit Description
U/hee/er
Installation Date
Steam Output (103 Ib/hr)
Design Pressur •. (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner ( °F)
Primary Air Temp (°F)
Stack Temp (°F)
/
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /O
Unit 4
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (DOTH)*
CO ( T-ii-rtn ^ *
£>u ^ppm;
Total Part . (Ib/MBtu)
^olid Part flb/MRtu)
Boiler Efficiency (%)
CmriV^ ^nnt* No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp (°F)
Stack Temp. (°F)
Fuel Flow [HSCFHJ
Fuel Temp (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
/4-/
Ba6<5
fas'
s,e
/W
13
43
0
/4-
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit 4
Fuel
Test No.
Test Type
Test Load (103 Ib/hr
Excess C>2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (r>nm)*
of* frmm}*
au ipjjiuy
cr>_ ^nDm)*
Total Part (Ib/MBtu)
Col i r\ Par-t- MVi/MR-hn^
Boiler Efficiency (%)
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow (MSCFH)
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.I^O)
Register (% open)
M-0
A/0rHS /•
Air
3^-^'
7.3
90
86-
7,6
O
/7<3
380
A*y*b.
bZo
Sff.6
Avb,
a.b
/.s-
/
-------
en
Location No. /O
Unit No. fy
Test No. /4/
B
*.
o
K
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
—
-
-
-
-
-
i
c
c
-
-
=
£
3
)
-
-
ft
31
*••
Lf
*
-
-
Pt
n
-
-
_
-
-
-
-
L
-
-
-
-
-
-
-
-
-
-
_
-
-
-
-
-
-
-
—
,
-
-
-
-
-
-
-
--
-
-
$
-
•A
-
£
-
_
~
f
L5
D
-
-
~~
...
-
\
v-
—
_
-
-
-
-
V
_
"
_
...
s
-
._
-
-
s
_
-
-
-
-
V
-
-
-
-
-
-
-
-
-
-
^
-
-
•>
«•"
-
•V
>••
Load */•»
-
-
-
-
-
I
—
-
-
-
~
O Smoke
O CO
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
—
-
—
-
—
-
-
-
—
-
X Hc
A NOX
-
-
-
-
-
-
-
-
-
-
-
-
-
-
Bacharach Smoke No.
6
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
location No. /£
Unit No. ^
Test No. /^ -/
Fuel
Load
Stack Diameter, D.
Ib/hr
Soo
boo
-------
FUEL ANALYSIS SUMMARY
Gas Fuel
I
•
4
5
12
13
feSP-14
15
24
25
30
37
38
39
40
41
47
48
49
58
60
67
69
75
77
80
n
8
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
Q«
0
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
.6
0
0
0
0
0
0
0
.3
n
se
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
.1
.1
.1
.1
1.3
1.3
4.6
5
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88.9
84.1
85.8
85.8
85.8
. 85.8
23.6
23.6
74.0
\o
X
ct
u
13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
3 «
X
1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
1103
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548
1129
1 69
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. JO
Test No.
Unit No.
Unit Description
6erioi
7Q
80,'fcr .fyfff A.
Installation Date
Steam Output (10^ Ib/hr)
Design Pressur : (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft }
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
7^5
//0
3oo
*/
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location IO
Unit .5"
Fuel
Test No.
Test Type
Test Load (IO3 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HP ( r>nm \ *
CQ fnnm)*
A
SOo (ppm)*
TC>tal Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boilsr Efficiency (% )
Smoke Spot No .
ODJar*! +-\» (&}
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus Air Temp (°F)
Stack Temp. (°F)
Fuel Flow Y/Vf^/Vy
Fuel Temp (°F)
Fuel Pres. ' (psig)
Fuimarp> Pr<^e fin H n}
Register (% open)
8a-/
t/ar*n/-
Afr
££-
7,8
96
?/
7.6
o
180
37£-
A t->
A*n O.
tf£3~
83.S
4. . A
Aw &•
£.7
/ s~>
Ac/
ys o&
8&-<2
iouy Air
6ff
6.a
120
//*
8.2
O
176-
37S
b£~0
8?.£-
2.7
/,,
liC?
&0-3
iot*y Air
£&
f.6
I3£-
/2 /jir
60
2,3
/&
M3
/0.&
38
/80
37S
434
82,f
27
S) Q
&*&
/tst - £j ~7
tJt/ Y /
&&-S-
tcuj Air
60
3.3
/&
t*f7
48
O
#0
37£-
447
&
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit &
Fuel
Test No.
Test Type
Test Load (103 lb/hr'
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HP fnnm^*
cr\ fnnm)*
SOo (ppm)*
Total Part. (Ib/MBtu)
Solid Part (Ib/MBtu)
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow (M6CFMJ
Pnol Tomr-i i°V\
Fuel Pres. ' (psig)
Regis tear (% open)
Be -8
Mori** 1.
A,'r
4/
£.4
' l?tf
f/8
40
o
/80
37f
/t f^C/t
*//£>
t/?.£T
AL** fa
AM* is*
/,4
S) ±3
O-S.
ff8
6.?
/24
#6
8.4
0
~f£~
76
~
/0f
37£-
6~£0
8£-
^ &
c.c
<9T- /Off
#0-/?
A/or **/,
Air
86-
8.0
/G7
/0S
7,0
O
— MBH^.HW
/8 z> •
^•t:
£ff-70
at 3% O dry
1 72
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /&
Unit S"
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HP tr\r\m\*
HU i ppm;
on (nnm}*
O1 Tp>mr> f°P^
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
£?SJ ~ / £^
^y(^ f^p
£& ' (JL} ^y/^
ef
7,4
/O 7
/&2
8.2
c
/&&
37^
A h
ri *** O ,
f/0
//4,&
A J-,
/IH^? &•
7.0
3.2
60- 6&
go-/6
fcuj Jir
86
64
U6
///
8.6
0
/8&
37J-
&>&
SM.£
7.0
2.0
ss-6
-------
I
Ck
Location No. /^
Unit No. S"
Test No. go
—
—
--
--
--
--
-
-
1
-
-
-
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-
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c
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1
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-
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1
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a
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Load 87,000
Fuel A/af/. (Zras
-
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-
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-
-
-
-
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s
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s
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-
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-
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\
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Ib/hr
-
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-
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-
-
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-
-
-
-
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-
-
-
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-
-
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-
-
-
-
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• Smoke
O CO
-
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-
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-
-
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-
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-
-
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-
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-
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X
A
-
-
-
-
-
-
-
-
-
-
HC
NOX
_
-
-
-
-
-
-
-
-
-
-
-
-
_
-
-
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_
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~
-
-
-
—
-
-
-
-
-
-
:
-
-
- -
--
--
--
--
__
o2, %
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
en
Location No. /<^
Unit No. A"
Test No. 8
-------
STACK TRAVERSE DATA
o
w
\
*J
4J
•H
O
O
U
rd
c/i
Location No. /&
Unit No. 5"
Test No. go -//
Fuel
Load
Stack Diameter,
Ib/hr
&OO
^ 76
-------
FUEL ANALYSIS SUMMARY
Gas Fuel
A/0.
4J
f>
H
4
5
12
13
14
15
24
25
30
37
38
39
40
41
47
48
49
58
60
67
69
75
77
k»-ao
n
8
.9
.9
.9
.9
0
0
0
.9
0
.9
.9
.8
.5
.9
.5
.8
.8
.9
.9
.9
.9
2.5
2.5
0
o
0
0
0
0
.3
.3
.3
0
.3
0
0
.6
0
0
0
.6
0
0
0
0
0
0
0
.3
CM
.1
.1
.1
.1
4.6
4.6
4.6
.1
4.6
.1
.1
6.3
3.9
.1
3.9
6.3
8.4
.1
.1
.1
.1
1.3
1.3
4.6
B*
85.8
85.8
85.8
85.8
74.0
74.0
74.0
85.8
74.0
85.8
85.8
88.9
95.6
85.8
95.6
88.9
84.1
85.8
85.8
85.8
.85.8
23.6
23.6
74.0
B
V
13.2
13.2
13.2
13.2
20.6
20.6
20.6
13.2
20.6
13.2
13.2
3.4
0
13.2
0
3.4
6.7
13.2
13.2
13.2
13.2
69.7
69.7
20.6
c >^
"a $
3s.
X
Si 9
(71 r-l
K >
1108
1108
1108
1108
1129
1129
1129
1108
1129
1108
1108
964
966
1108
966
964
967
1108
1108
1108
1108
1548
1548
1129
1 77
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. //
Test No. /&
Unit Ko. /
Unit Description
Installation Date
Steam Output (103 lb/hr)
Design Pressv -e (psig)
Final Steam Ten?) (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/25c?
/ZS'
S~00
470
Waterfube
/7- // - S3
'€ W '/
-^ t/tt
Comments:
1 78
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location //
Unit /
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess 02 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (pom)*
SO (onm)*
SO 9 (opm)*
"Stotal Part (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (% )
OnarM t"v (%^\
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus Air Teinp ( °F)
Stack Temp. (°F)
Fuel Flow
Fuel Temp (°F)
Fupl Pf£»<5 ' foc-irr^
Furnace Pres. (in.H2O)
Register (% open)
I8'f
A/0rt+*l,
Air
8&
8.0
330
383
//4
28
£>a
cl
bfo
t/£0
. ,
/v**» Oi — ]
tes"
A,^, fa
fllsn L>.
-' Afr
/0e
6.0
367
367
/
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit /
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
SO foDrn)*
co« fnnni}*
rrv>*-=j1 Pa-r-fr- M V»/Mm~11 J
<;olid Part flb/MBtu)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus Air Temp. (°F)
Stack Temp. (°F)
Fuel Temp. (°F)
Furnace Pres. (in.H2O)
Register (% open)
J8- 8
I/O r v<* 1,
A>r
}06
6.3-
379
365-
/2.8
7V
n
4&S~
460
^ iji^t fa
Jj rrr&t
*S67
Ai^ fa
-0.22
&•
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location //
Unit I
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%}
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
SOX (ppm)*
SO2 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow .
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H-,0)
Register (% open)
/8 ~/6~
1003 d>r
7f
£.&
ss-q
s^q
I3.o
O
0
4sy
te*
A ^ /,
A i*i&.
bet?
i , /, _
Jt*rt&- —
-0J7
'8-te
i'0a? /}ir
73
8.1
37 (/
Itt
II.&
O
O
t/ss-
4>6
40&
~0.s '6
;0'2.2
SS
80
4£-'r
//G
£.£*
385-
379
/2,7
Se
&J~£?
460
t/5&
-0./2
at 3% O dry
1 8
-------
STACK TRAVERSE DATA
o
0)
w
4J
U-l
JJ
•rH
O
O
o
id
in
Location No. //
Unit No. /
Test No. /g
Fuel foal
Load /A?/ COO
Stack Diameter,
lb/hr
duct
$00
1 82
-------
Location No.
Unit No. /
Test No.
Load
Fuel
7, e?&
-------
Location No. //
Unit No. /
Test No. /g
Load
Fuel
Ib/hr
• Smoke
O CO
X HC
A NO,
oo
-Ci.
a
a
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
REPORT
IRUESDAIL LABORATORIES. INC. /\
== [j[P I
^ I ^[| I 4IDI N. FIGUEROA STREET
THEMISTS - MICROBIOLOBISTS - ENGINEERS \^^^x^ LOB ANGELES 9 o o & &
RESEARCH - DEVELOPMENT - TESTING * AREA CDDE 2I3 * 22B-IB64
CABLE: TRUELABB
KVB Equipment Corp.
XIENT 17332 Irvine Blvd. DATE May 23, 1974
Tustin, Calif. 92680
Attn: Glenn Cato RECEIVED May 1, 1974
SAMPLE 5 Coal Samples and 2 Fuel Oil Samples, as shown. LABORATORY NO. 122116
.0.: 1700-43
INVESTIGATION Analysis and tests as requested
RESULTS
SAMPLE IDENTIFICATION:
1. Coal - Test
The results of the coaj Analysis are as follows:
NO. 1
As Received:
Moisture, % 5.96
Carbon, 7, 70.02
Hydrogen, J* 5.34
Nitrogen, 7. 1.40
Sulfur, 7. 2.94
Ash, 7. 4.77
Oxygen, 7. 9.57
(by difference)
(Continued)
1 85
-------
"RUESDAIL LABORATORIES. INC.
NO. 1
Heat of Combustionj
Gross, BTU/lb 12,690
Net, BTU/lb 12,190
Dry Basis:
Carbon, 7. 74.46
Hydrogen, 7. 5.68
Nitrogen, 7. 1.49
Sulfur, % 3.13
Ash, 7. 5.07
Oxygen, 7. 10.17
(by difference)
Heat of Combustion:
Gross, BTU/lb 13,490
Net, BTU/lb 12,960
Page 2
LAB. NO. 122116
Respectfully submitted,
TRUESDAIL LABORATORIES, INC.
l^nas Bandziulis
Supervisor, Air Pollution Testing
1 86
-------
REPORT
LABORATORIES. INC.
EMISTS - MICROBIDLOGISTS - ENGINEERS
,EARCH - DEVELOPMENT - TESTING
KVB Engineering
ENT 1?332 Irvine Blvd.
Tustin, CA 92680
Attn: Hans Buening
1PLE 4 Coals previously submitted for other analyses
marked as shown
. No. 6000
fESTIGATION Determination of density
RESULTS
4IOI N. FIGUEROA STREET
LOS ANGELES 9OO65
AREA CODE 213 • 22O-J664
CABLE: TRUELAB8
DATE August 7, 1974
RECEIVED August 1, 1974
LABORATORY NO. 1052
Density (g/ml.)
Test No. 18-4
, 3/6/74 1.278
Respectfully submitted,
TRUE SD AIL LABORATORIES-INC
Alvin E. May
Director of Laboratories
1 87
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. /£
Test No.
Unit No.
Unit Description C£ Corner P,recJ
Installation Date
Steam Output (103 Ib/hr)
Design Pressui i (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner ( °F)
Primary Air Temp (°F)
Stack Temp (°F)
/
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /3
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess 02 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
FC\ ( nrsm ^ *
HC (ppm)*
en friT-im^*
i>U vPP1"/
en** frmm}*
•lY-it-al P^-rt- (1 Vi/MRf-n \
Cr\1 i A T>;a r-f- ( 1 K /P^TOt-n ^
^Tnr>k*a ^rsrit" Nr»
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Stack Temp. (°F)
Fuel Flow (H6CFH)
Fuel Temp (°F)
Fupl PK^»C: * /T-jcirr^
Furnace Pres. (in.H2O)
Register (% open)
7J--/
A/ort^/.
A,r
Igf
6.0
/7/
I6&
m
^
c/'&5 7
c/'0y&>
S6S-
7/0
3bo
&6
A ' : /->
/) lsn&,
-4,3
7S-Z
£e?<*S
£e>ac/
/33
7S~-3
4/ori~>l,
A,r
/<&-
&ff
/ri+'l,
/>>'r
r
. /go
6.4
£o
/w'
-0.7
at 3% O dry
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location A?
Unit
Fuel
Test No.
Test Type
Test Load (1Q3 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (nom)*
HC (ppm)*
QA fr-irim^*
£>w \ppm/
CO— fnDnO*
TY-i-f-al Pav+ MH/MRt-ii^
u? /)ir
J8£r
£3
/9O
8
&Z£~
7/2
s: ///}
& yc/
3f/2
/70
/&
-0<3
7S-/&
t/i Jir
S0£
7,4
Stt
536
e.a
9
&65~
7/2
£//a
& vt?
3£&
/70
/^
/^
-o.£
7&~-//
tec** 4'f
'85
s:*
/73
m
w
/a
S70
7/£-
34f
/70
~
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /S
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)* '
C02 dry (%)
CO (ppm)*
HC (ppm)*
en fnnml*
ow \ppiu;
^O~ frjnm^*
tV->l-a1 Pa>-+- MVi/MPt-n^
Cril i f\ P» t-f- MVl/MHR•f-^^^
Boiler Efficiency (%)
Sinokf* ^nof Nn
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow (M6CFM)
Fuel Temp (°F)
Fuel Pres (psig)
Furnace Pres. (in.H2O)
Register (% open)
^r-xr
/fir &?£>.
!$&
. £.6
16 a
IS?
8.6
It,
£-70
7 SO
6&
3S«
J75-
A , J-i
/fi^tO.
-0.*t
&~~/6
Jir 8s ff.
103-
6.1
l£~7
IW
0.8
IB
at.
07
£~7G
7
-------
CO
NO
a
CJ
a
Location No. /
Unit No. e?ty
Test No. 7g~
--
T
- —
—
--j
--
—
-
-
-
-
-
-
-
_
-
-
-
-
-
-
s
&
ft
c
c
-
_
-
D
J
-
-
-
-
-
-
-
-
-
-
-
-
-
r
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
~
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-
-
-
-
-
-
X
-
[~
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-
7
^
tc
-
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-
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n
1
A
t-
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ft
x
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-
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:
-
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-
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-
-
-
-
-
-
-
f
-
-
-
—
-
-
-
>
-
c? Load Jff^ £?&0
Fuel A/a//- £?&
-
-
-
-
:
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
1
4-
0r
T
-L
7*
-
•*•
-
-
•f
-
-
-
-
-
-
-
f
-
-
A
T
_
-
-
-
**
-
-
-
i
«
-
,-
L
?
-
— '
^
-
-
-
1
-
-
-
-
LX
lb/hr
^
-
-
-
-
•*
f
*>
~
-
-
-
-
-
-
-
-
1
-
-
-
X
-
-
-
-
-
-
-
—
-
-
1-
_
-
-
-
• Smoke
O co
-
-
-
-
-
-
-
X
A
HC
NOX
-
-
-
--
u
<0
n
(0
A
U
a
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No.
Unit No.
Test No.
/<£?
Fuel
Load /&6~~,
Stack Diameter, D
_
duct
Ib/hr
/£
-------
TENNESSEE GAS PIPELINE COMPANY
GAS SAMPLE ANALYSIS
PRODUCE}'.: ALABAMA-TENN. NAT. GAS CO.
LOCATION: CORINTH MISSISSIPPI SALES
STATION NO,(COLS 1-6) 2- 58-1
ANALYSIS DATECCOL 61-66) 9 6 73
COMPOSITE CODEC COL 7)
ANALYSIS
CARBON DIOXI
NITROGEN
OXYGEN
METHANE
ETHANE
PROPANE
I SO- BUTANE
N-BUTANE
I SO-PENTANE
N-PENTANE
HEXANES PLUS
KEYPUNCH
COLUMN
DE 8-11
12-15
16-19
20-23
24-27
28-31
32-35
36-39
40-43
44-47
48-51
TOTAL
MOL
FRACTION
0.0092
0.0023
o.oooo
0.9581
0.0242
0.0039
0.0011
0.0007
0.0003
0.0002
o.oooo
1 .0000
GPM
14-69SPSIA
AT 60 F
16.273
0.622
0.109
0.037
0.023
0-012
0.008
o.ooo
17.081
SP.GR. AT 60 F
C/UR=1>
0.0141
0.0022
o.oooo
0.5317
0.0253
0.0060
0.0023
0.0014
0.0008
0.0005
o.oooo
0.5843
COMPOSITE CODES
1-GREEN BRANCH LINE 4-261N VALLEY LINE 7-DELTA LINECV-516 TO V-C6C
•2-16IN VALLEY LINE 5-AK LINE 8-MAIN LI NEC ST.1 TO ST.87)
3-DEANC1+2) 6-KP LINE 9-TOTAL SYSTEM
FIELD DATA
PRES. 717.0PS1 TEMP 82.OF
H20D.P. 0. F AT 0. PSI .
TAKEN BY WEDGEWORTH DATE
SP.GR. 0.5860 BTU 0.
HYD.D.P. 0. F AT 0. PSI
8 22 73 BOMB NO
LAD DATA
SP.GR.CDAL.) 0-5S30
ANALYSIS NO 68716
ANALYSIS BY LEWI S
SP.GR.CCALC.) 0.5843 *BTUCDRY> 1034.
DEV.TEST NO. 0- 0 *BTUCWET> 1016
REMARKS: ABOVE 2EHOS INDICATE DATA NOT AVAILABLE
*}JTU / CU FT AT 14.73 PSI A AT 60F
QUAKTERLY ANALYSIS**
AR
1 94
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
002 dry (%)
CO (nom)*
HC (ppm)*
cr\ fnnml*
aw ipjjui^
SO-^ (tJDinl*
•TV^t-al Part flb/MRtnl
•;o3if5 Part Hh/MRtu)
Bo"* ler Efficiency (%)
Smoke Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp.(°F)
Stack Temp. (°F)
PUP! Plow ///»////•/
Fuel Temp. (°F)
Pijpl "Prfsc ' /r>cirr\
Furnace Pres. (in.H?O)
Register (% open)
(?£-/
Base.
/8/
&3
383
B6£r*r~
c&So
.O/jA -7
C&Lf /
n /•
o£>
S6S-
7S0
64£-
368
c?C?f C? /&
/70
-0.3
et-e
loco /}>'r
/83
4.J-
36
66^
73ri*t /,
4,r
/7
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (1Q3 lb/hr^
Excess C>2 (*)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO fonm)*
HC (ppm)*
SO (DDm)*
SOo (ppin)*
• TY^t-al Part MVj/MRtu)
C«l -i A "Dra-r-f- M Vi/MR+-n\
On^r*i i~v f%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Temp. (°F)
Furnace Pres. (in.I^O)
Register (% open)
.
Air
/gey
&0
382
370
/*/.
f.8
b&5~
3
f6£~
?t
S00
s:i
370
J64
/£
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess ©2 (%)
NOX (ppm)*
NO (ppm)*
002 dry (%)
CO (ppm)*
HC (ppm)*
SOX (ppm)*
S02 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow .
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
26 -Iff
Air geg.
/0&
£•,
-------
Location No.
Unit No.
Test No.
Load
Fuel
lb/hr
• Smoke
O co
X
A
SO-
CO
00
G
S1
04
O
u.
w-
ftL
XL
7
°2' %
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No
Unit No.
Test No.
Fuel
Load /7£~,
Stack Diameter, D.
lb/hr
o
1
-P
•H
O
O
i-l
X
o
(0
-p
tn
Soo
3
JJ
0)
EH
o
(0
en
1.0
1 99
-------
REPORT
TRUESDAIL LABORATORIES. INC.
" .HEMISTS - MICROBIOLOGISTS - ENGINEERS
RESEARCH — DEVELOPMENT — TESTING
KVB Equipment Corp.
CLIENT 17332 Irvine Blvd.
Tustin, Calif. 92680
Attn: Glenn Cato
SAMPLE 5 Coal Samples and 2 Fuel Oil Samples, as shown.
P.O.: 1700-43
INVESTIGATION / lalysis and tests as requested
4101 N. FIGUEROA 8!
LOB ANGELES vc
AREA CODE 213 • 22!
CABLE: TRUE I,
DATE May 23, 1974
RECEIVED May 1, 1974
LABORATORY NO. 122116
RESULTS
SAMPLE IDENTIFICATION:
3. Coal - Part. Test...#26-i.;
Boiler #24. 3-19-74
The results of the coaj/«=analysis are as follows:
As Received:
Moisture, %
Carbon, %
Hydrogen, 7*
Nitrogen, %
Sulfur, %
Ash, %
Oxygen, 7.
(by difference)
NO. 3
7.42
65.44
4-20
9.36
7.26
(Continued)
20.0
-------
THUESDAIL LABORATORIES. INC.
Heat of Combustion;
Gross, BTU/lb
Net, BTU/lb
Page 2
LAB. NO.
122116
NO. 3
11,430
10,980
Dry Basis:
Carbon, 7.
Hydrogen, 7»
Nitrogen, 7.
Sulfur, 7.
Ash, 7.
Oxygen, 7»
(by difference)
Heat of Combustion:
Gross, BTU/lb
Net, BTU/lb
70.68
5.
1.
.31
.51
4.54
10.11
7.85
12,350
11,860
Respectfully submitted,
TRUESDAIL LABORATORIES, INC.
*-7&/lt24, vb&'Jlffj&tltii,
t-gnas Bandziulis
Supervisor, Air Pollution Testing
20 1
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. /£ Test No. 77, 7<& Unit No.
Installation Date
Steam Output (103 Ib/hr)
Design Pressur ; (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
-
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/3^
326-
6
-------
BOILER EMISSION MEASUREMENTS
i
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppra)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
cr> {nnm}*
QfVm (nnm^*
Total Part. (Ib/MBtu)
r &ff.
e7o
j><>~
567
S68
13
o
'3
S7
&-3G
37?
J7S
-0.3
&-/S
Air #&$
.
-------
BOILER EMISSION MEASUREMENTS
i
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (103 lb/h^
Excess O2 (%)
NOX (ppra)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
or) (nnml*
CO*, ^T!SDTn^*
•TY-it-al Par-t- flh/MRtu)
\d 1 VI r\\ T //• / l/t*
Fuel Temp. (°F)
. . .
Furnace Pres. (in.l^O)
Register (% open)
70 -/
Base
260
5,8
tes-
473
//.£
0
10
1 s yo
i>o~so
I-2I/:
/• O'O
#6
S70
740
6.3
sjy
6*01
/3
0
6
£~70
70 8
13.2
O
. q
'
—
. _._.
—
33-0
700
640
360
yy y^LO
o Of 3 GO
>7£-
-asf
7#-7
toco <4''r
£=><$/
4.0
4
700
6V0
3tt
/7f
-0,36"
at 3% O2 dry
204
-------
ro
O
en
u
X
Location No. /£ Load £<£,&, &&& lb/hr
Unit No.
--
-
-
-
)
-
i
-3
'
-
-
-
-
-
-
-
3
1
-
«
-
-
-
!--
C
-
-
-
-
-
•5
-
-
"%
-
-
-
-
i_
-
-
fe
-
-
-
-
~
-
-
-
-
-
-
-
~
-
i.
-
-
-
-
-
-
-
-
-
-
-
A
-
-
-
-
-
-
-
~—
~
wr
-
-
-
-
-
•-
-
••
-
1^*
-
:
-
1^*
-
— «
-
-
-
-•
-
-
-
/
-
-
-
-
-
-
-
-
r
-
-
-
•a
-
-
-
-*
-
4
-
-
-
f-
f]
-
-
-
-
SS
-
~
•*
-
~
-
-
••
-
-
"
-
-
h
-
^
-
-
-
-
-
^
-
-
-
-
^
-
-
-
-
-
*>
-
-
^
-
^
-
-
^
-
f
I
—
-
—
-
-
*
L-
-
-
_
-
-
-
-
-
-
-
-
-
-
i-
-
-
-
-
-
-
-
-
—
-
-i
_
-'
-
-|
-
_,
-
-
-
-
-
-
-
-
-
-
-
t-
-
0 Smoke
O co
-
-
-
-
-
-
-
-
-
X
A
-
HC
-
-
r--
--
£
7
8
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
u
0)
tn
.u
••H
U
O
4J
cn
Location No
Unit No.
Test No.
Fuel
Load
Stack Diameter, D.
lb/hr
206
-------
— ~ KdPGRT
RUESDAIL LABORATORIES, INC.
HEMISTS - MICROB1OLQGISTS - ENGINEERS
- DEVELOPMENT - TESTINQ
KVB-Equipment Corp.
LIENT 17332 Irvine Blvd.
Tustin, Calif. 92680
Attn: Glenn Cato
3AMPLE 5 Coal Samples and 2 Fuel Oil Samples, as shown.
0.: 1700-43
NVESTIGATION Analysis and tests as requested
Test 70
41DI N. FICUEROA STREET
LOB ANGELES 9OD6B
AREA CODE 213 • 22S-IS64
CABLEl TRUELABB
DATE May 23, 1974
RECEIVED May 1, 1974
LABORATORY NO. 122116
RESULTS
2. Coal -
3-14-74
The results of the co?l analysis are as follows:
NO. 2
As Received:
Moisture, %
Carbon, %
Hydrogen, 76
Nitrogen, %
Sulfur, 7.
Ash, 7.
Oxygen, 7.
(by difference)
8.19
62.28
4.70
1.34
2.74
11.58
9.17
(Continued)
207
-------
rRUESDAiL LABORATORIES. INC.
Heat of CombustionJ
Gross, BTU/lb
Net, BTU/lb
NO. 2
11,160
10,720
Page 2
LAB. NO. 122116
Dry Basis:
Carbon, ?„
Hydrogen, %
Nitrogen, %
Sulfur, 7.
Ash, 7.
Oxygen, 7.
(by difference)
Heat of Combustion:
Gross, BTU/lb
Net, BTU/lb
67.84
5.12
1.46
2.99
12.61
9.98
12,160
11,680
tfis.'f-
Test- 78
Respectfully submitted,
TRUESDAIL LABORATORIES, INC.
ignas Bandziulis
Supervisor, Air Pollution Testing
208
-------
BOILER EMISSION MEASUREMENTS
i
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
S0x (ppm)*
SO2 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow ///.^^/yy
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
77- /
j/or**it.
A.T
il,
Air
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
qo (nnm)*
j\
QO— /rvrMTi^*
° 2 »J^*r '
• TVi-hal P^r-t f Ib/MBtu)
<•(-.! •; J D = T+- M Vi/lYTR-t-ii^
Rnil^l" P f f i c* "i f^Tl cv f%)
/%« • *. /a. \
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow (M6ZF//J
Fue>l Temo f°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.I^O)
Register (% open)
77-8
t/c?r<**l,
Air
260
ff.s-
270
267
£-
36-0
36&
/7
-0.f
77-/3
/ou3 Air
.— *
8&
^70
700
640
3&o
36&
J7
-0.4
77-/t
M- Jir
365-
/7
-^4^
at 3% 0 dry
2 \ 0
-------
BOILER EMISSION MEASUREMENTS
i
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX -(ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC (ppm)*
S0x (ppm)*
S02 (ppm)*
Tot-al Part flb/MBtu)
Cr\T •? A T>a>-+- M V» /MT*+-n1
Boiler Efficiency (%)
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
Piiol Tomo f°Pl
Fuel Pres. (psig)
Furnace Pres. (in.H2O)
Register (% open)
77- AT
M- A>r
Ztt
6.2
3&8
344
8.6
O
7
£-7
-------
Location No. /£ Load
Unit No.
-------
STACK TRAVERSE DATA
o
o>
tn
M-l
>t
-P
•H
O
O
Location No.
Unit No.
Test No.
Fuel //a//.
Load
lb/hr
Stack Diameter, D, -,
. , duct... 7,
-------
TENNESSEE GAS PIPELINE COMPANY
GAS SAMPLE ANALYSIS
PRODUCER: ALABAMA-TENN. NAT. GAS CO.
LOCATION: COKINTH MISSISSIPPI SALES
STATION NO,(COLS 1-6) 2- 58-1
ANALYSIS DATECCOL 61-66) 9 6 73
COMPOSITE CODEC COL 7)
ANALYSIS
CARBON DIOXI
NITROGEN
OXYGEN
METHANE
ETHANE
PROPANE
I SO-BUTANE
N- BUTANE
I SO-PENTANE
N-PENTANE
HEXANES PLUS
KEYPUNCH
COLUMN
DE 8-11
12-15
16-19
20-23
24-27
28-31
32-35
36-39
40-43
44-47
48-51
TOTAL
MOL
FRACTION
0.0092
0.0023
o.oooo
0.9581
0.0242
0.0039
0.001 1
0.0007
0.0003
0.0002
o.oooo
1 .0000
GPM
14.695PS1A
AT 60 F
16.273
0.622
0.109
0.037
0.023
0-012
0.008
o.ooo
17.081
SP.GR. - AT 60 F
-------
INDUSTRIAL BOILER DESIGN DATA
Location No
Test No. 29, 3J
Unit No.
Unit Description
Installation Date
Steam Output (103 U>/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
W67
£•00
/GffO
$&&
]K/aterj-c^ije
<3e-e/-87
<26
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /3 •
Unit £///r.
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
3i-i
ffaJg
4oo
3
&78
&M
/c
0
&
/6,/
•
• -
at 3% O2 dry
2 1 6
-------
Location No.
Unit No. 2
STACK TRAVERSE DATA
Fuel
Load
lb/hr
Test No. 3/-/ Stack Diameter, Dduct ft?"
0
t ^
1
I
!
|
i
i
j
j
f
l
r £
i
i
I
>^xl^: i
^
i
1
i
i
|
i
|
i
i
•^
PS^
1
*s
1 .
i t
i
1
i
i
i i
r
i i i
k
i
1
^
^
•s,
|
i i
1
I
;
(
i
I
i
l
1
•s^ 1
X
^
•m
\
i
i ; t
'
i
i
i
i
1 t
t
i
i i
i
'K
l
i
i
N
i i »
J
c
>
^
5°2
; v
T
k st
1
1
|
1
1
1
[
j
I
1
V
A
i
|
t t
1
^
M^"
1
^
i
! i
1 i i
! I
i
1
I 1
1 !
i i
1
i
D-rT
i *
0 .5
D/D Duct
i 1 i
1 '< i
t
1
i
!
i
1
i
f
j
!
* i
!
1 !
1 !
i i '
t
i 1
1
i !
<
i
*
! I <
i
l | .
i ' i
: l
! !
1 ', '
, \
1
1 | _lj^
^— 1^
1 1
'
[ !
1 ) i
i
1.
-1 -
»g Uj
s ^
TC4_, Stack Temperature, °F
0
2 1 7
-------
TRUESDAIL LABORATORIES, INC.
4101 N. FIGUEROA STR[
THEMISTS - MICROBIDLOGISTS - ENGINEERS \. .^ LOS ANGELES 9oos
RESEARCH - DEVELOPMENT - TEST,NO ^^® AREA CODE 2'3 ' ZZ6^
CABLES TRUELAI
KVB Equipment Corp.
CLIENT 17332 Irvine Blvd. . DATE May 23, 1974
Tustin, Calif. 92680
Attn: Glenn Cato RECEIVED May 1, 1974
SAMPLE 5 Coal Samples and 2 Fuel Oil Samples, as shown. LABORATORY NO. 122116
P.O.: 1700-43
INVESTIGATION Analysis and tests as requested
Test
RESULTS
SAMPLE IDENTIFICATION:
4. Coal --Test #31, ~ Unit 2,"3-28-74 #£ * 17
The results of the coal-^analysis are as follows:
NO. 4
As Received:
Moisture, 7. ) 7-28
Carbon, 7. 63.76
Hydrogen, % 4-26
Nitrogen, 7. 1.35
Sulfur, 7. - 1-68
Ash, 7. 17-37
Oxygen, 7. , 4-30
(by difference)
(Continued)
2 1 8
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /3
Unit t-al Part (Ib/MRtuI
<;r>1 i r\ f>f\i-t- f 1 H/MRt-nJ
ROT 1 f*Y" ff f i r*"i f^n r^/ ^4^
Sinoke Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow (6a/. /#,'*.}
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
£r^,i.
Air
4eo
0-3
2/2
?<7
6.
/<7
840
8SS
44o
440
74
e^s
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /3
Unit 2
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (oDm)*
HC (ppm)*
SO foom)*
CQ_ fnonO*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Onafit'V (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow £>a//W*t.
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.^O)
Register (% open)
£7
^
-------
Ni
ro
o
33
10 -
o-
Location No. /
Unit No. c?
Test No. e?-
-
i
-
-
-
-
-
-
-
,
,
7*i
-
y
_
-
-
-
-
-
"*\
_
-
-
-
J*
-
;<'../
-
1
• 6t-
n.
-
r-
-
p 1
ft
X
O
-
-
-
r
-
-
r-
*
-
i
-
/
&
-
-
/
t
'd
-
-
-
-
;
-
X
-
-
t
-
-
—
-
-
-
s
-
-
-
-
-
-
? <;
Load 40&, &&& Ib/hr
Fuel f&a/ <£ /1~ 7 7e?t*s ///r. &
-
-
-
~
^
-
£
-
[s
-
-
A
-
-
i
-
-
s
-
-
-
^
-
-
^
i»-
-
^
&.
1 10 II
-
-
#
-
-
-
•**
-
-
-
-
~l
-
-
--i
-
\
-
-
-
-
-
-
-
-
-
• © Smoke
^^ O CO
-
-
-
-
-
-
-
h
-
-
-
-
-
-
-
-
-
-
-
-
-
-
_.
-
-
-
-
-
-
-
-
-
-
-
_
-
-
-
-
-
--
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
-
_
-
-
-
-
-
-
-
-
-
-
-
X
4
-
-
-
NOX
-
-
-
-
-
~
-
_
-
-
-
-
-
-
-
-
-
-
-
—
_
-
—
-
_
-
-
-
-
__
—
--
--
--
--
'2
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
o
0)
01
-p
i
4J
•H
O
O
r-l
0)
.*
o
(0
-p
w
Location No.
Unit No.
-------
TRUESDAIL LABORATORIES, INC.
41OI N. FIOUEROA STREET
"HEMISTS - MICRDBIOLOBISTS - ENGINEERS X\~x'X L ° s ANGELES 9 O O 6 B
BESEARCH - DEVELOPMENT - TEBTINQ ^^* AREA CODE 213 • 22B-IS-S4
CABLE! TRUELAB8
KVB Equipment Corp.
CLIENT 17332 Irvine Blvd. DATE May 23, 1974
Tustirx, Calif. 92680
Attn: Glenn Cato RECEIVED May 1, 1974
SAMPLE 5 Coal Samples and 2 Fuel Oil Samples, as shown. LABORATORY NO. 122116
P.O.: 1700-43
INVESTIGATION Analysis and tests as requested
a
RESULTS
SAMPLE IDENTIFICATION:
6. Oil -Test #29, " 3-29-74
SAMPLE ANALYSIS
(Continued)
223
-------
.RUESDAIL LABORATORIES, INC.
Page 2
LAB. NO. 122116
Heat of Combustion?
Gross, BTU/lb
Net, BTU/lb
Dry Basis:
Carbon, 7.
Hydrogen, %
Nitrogen, %
Sulfur, %
Ash, 7.
Oxygen, 7.
(by difference)
Heat of Combustion:
Gross, BTU/lb
Net, BTU/lb
The results of the oil analysis are as follows;
NO. 6
Carbon, 7.
Hydrogen, '/,
Nitrogen, %
Sulfur, 7o
Ash, 7o
Oxygen, 7.
(by difference)
Carbon Residue, 7.
(Conradson Carbon)
Heat of Combustion:
Gross, BTU/lb
Net, BTU/lb
API Gravity at 20°C
Viscosity, SSU, at 40°C
85.54
11.00
0.46
2.43
0.12
0.45
9.55
18,330
17,330
13.6
7560
Test
Respectfully submitted,
TRUESDAIL LABORATORIES, INC.
ignas Bandziulis
Supervisor, Air Pollution Testing
224
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. 13
Test No.
Unit No.
Unit Description
8 £ (A/
ffoi/er
Installation Date
Steam Output (103 Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/^7
S0o
/0<£TO
^00
\A/a / ff r / of b 6
86 - eo -eo
7360
3V,
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /
Unit (ppm)*
HC (ppm)*
SOX (ppra)*
SO2 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow .
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
JS6 -/
Hi
Air
4oo
9.4
bo£
386
9.o
0
30
#30
880
430
430
/S0
-0,11
tis- 7?-4A~
o-t-r~ts-\
JS6~e
Base
40o
8.6
363
337
8.6
Z9
2.6^
2.61
76
9
/oo
£30
8*to
420
^20
Ma
-cf
460
8.6
381
364
9.6
63-
78
9
I0O
840
030
436~
43£-
/fe?
-0.093-
/&7-fy
///• Jir
. 40G>
/O.I
b/o
430
S.4
0
9
loo
£32
870
430
43^"
JS0
-o.te
/&8-I
fact? 4>'r
390
S.I
247
330
10.0
/40
79
830
880
440
tes-
J£&
-a?£
at 3% O dry
226
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location 13
Unit
8006
^IO
va
3S~1 .
3^0
e.a
o
T/
'6
8.S~
9o
83l - £9 a/
/gc? - Me?
&£•
-o-l
iif-7S-'tff
&R. -rf-68
/S?-s
8OO&
400
8.9
3o2
-------
CASCADE IMPACTOR DATA
Test No.
location No.
Fuel Type
Burner Type
Test Load (Ib/hr x 10 J)
Stack Temp (°F)
Stack Press, (in. HO)
Impactor AP (in.H^O)
Gas Volume (cm )
Impactor Flow (cm • -s )
Sample Time (sec)
Orientation
D_ Cyclone (pm)
«W
o
o o
in 2
O
O
rH CD
a n)
•g *J
4J en
u
<
Cyclone, Stage,
& Filter Catch
1 (pm)
2 (Via)
3 (urn)
4 (urn)
5 (pm)
Cyclone (mg)
Stage 1 (mg)
Stage 2 (mg)
Stage 3 (mg)
Stage 4 (mg)
Stage 5 (mg)
Filter {mg)
Total Catch (ing)
Comments
/&6 -G>O
36o
/^^"
«/5
^// ^'^c'
£~J.fy
/e&o
t/on'20wt:
J0.t/
-------
fo
ft
»
Location No.
Unit No. £
Test No. /£~&
- -
--
—
--
__
—
__
-
-
-
-
-
-
-
-
-
i
(
c
-
-
-
-
-
1
D
-
-
-
-
I
-
-
-
i,
I**
-
-
-
-
-
-
-
-
s
-
•J
3
-
-
-
*•'
r*
CJ
-
tL
o
-
-
-
B
&
O
z
h
-
-
-
-
7
/3
-
^
-
^
-
i
-
\
^
i
»-
k,
>
-
(^
puf
4r
JL
-
5
P^-
m
i_
tf
\
Load •* 4&&/ &&&
Fuel
-------
to cat tor?
(Suit £
Test A/o.
FUEL ANALYSIS SUMMARY
Coal and Oil Fuels
Test No.
102-103
107-108
111-112
116-121
126-130
131-133
134-139
-156-159
-159
160-164
165-168
169
170-175
176-179
186-189
195-206
Type of
Fuel
If 2 Oil
«2 Oil
PS 300
(1/5 Oil)
16 Oil
16 Oil
Coal
Coal
Coal
06 Oil
12 Oil
Coal
Coal
16 Oil
«6 Oil
86 Oil
«6 Oil
*
* 3 *
1 5 g
1 i . '5
O * 0?* O +
85.94 12.72 0.89
85.94 12.72 0.89
86.46 10.31 1.07
85.95 10.21 0.22
No Fuel Sample Obtai
62.50 5.21 12.51
68.30 4.70 11.01
69.89 4.67 8.10
85.44 11.35 0.002
87.14 12.71 -
63.42 4.84 9.85
62.50 5.12 12.51
86.60 10.94 0.31
86.17 11.55
85.10 11.10 3.12
86.68 12.16 0.65
s
G
• P<
•H M ui «j rtj
S
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No.
Unit No. /
Unit Description C£
Jcrsa,
Installation Date
Steam Output (103 lb/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/^£>
/6~0
Z&o
8rectc/
-------
BOILER EMISSION MEASUREMENTS
i
AND CONTROL ROOM DATA
Location
Unit /
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess ©2 (%)
NOX (ppm)*
NO (ppra)*
C02 dry (%)
CO (ppm)*
HP fnnm^*
SO (nom)*
cr\_ frvDYTi^*
TVit-al PaTt f Ib/MBtu)
^olid Part flb/MBtu)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Pl1*»l Plnt«7 //l ////"
P*i i o 1 To mr* / ° P ^
Furnace Pres. (in.I^O)
Register (% open)
£7-1
8&6G
/20
10, 3
SS&
fare
1.8
0
JZP^J
/•3£ty
1 y r\^
t aOc
3 7 y^—"
cr, 31$
^ f^ /S
C.Ot&
Q 1
& 1
8gr
/as
s.i.
4ir
70
/3.4
6Tjq
J-07
7,2
&
0*3-
774
-* 3ff&
-0.1
at 3% O dry
232
-------
BOILER EMISSION MEASUREMENTS
i
AND CONTROL ROOM DATA
Location
Unit /
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
SO (ppm)*
S02 (PPm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
<57-8
fau> /ff
i /_,
AMP,
-0.1
r
/20
//,B
47
-------
CO
Location No. /^ Load /£
-------
STACK TRAVERSE DATA
Location No.
Unit No. /
Test No. d3/-'
Fuel
Load /, 000
stack Diameter,
Ib/hr
°F
-------
K V B ENGINEERING. INC.
17332 IRVINE BLVD.
TUSTIN. CALIFORNIA 926BO
(714) 032.6020
CHEMICAL LABORATORY REPORT
CLIENT:
KVB, Inc.
Tustin, CA
Attn: G. Cato
SAMPLES : 2 Coal Samples
KVB CHARGE NO. : eooo
INVEST.I GAT I ON: AS Requested
Sample Identification:
No. I Test No. 27-1;
DATE: 8/5/74 .
RECEIVED: 7/16/74
ANALYZED: 7/24/74
LABORATORY NO: 74121-c
Boiler #1, 4/15/74.
No. 1
Carbon, % 73.02
Hydrogen, 7. 5.50
Ash, T. 7.99
Moisture, % 3.55
Carbon Residue, T, 61.07
Heat of Combustion:
Gross, BTU/lb. 13,110
Net, BTU/lb. 12,600
Sulfur, % 1-58
Nitrogen, % -1.33
Oxygen, % (by difference) 7.03.
236
-------
KVB
// '
/
Parts Per Million in Coal
Silicon
iron
Aluminum
Magnesium
Calcium
Titanium
Barium
Boron
Manganese
Lead
Gallium
Tin
Nickel
Beryllium
Vanadium
Copper
Sodium
Silver
Potassium
Zirconium
Cobalt
Strontium
Chromium
Ho. 1
29,000
7,000
13,000
960
2,400
660
140
37
37
40
14
26
14
6.3
14
24
730
trace
trace
22
7.3
210
30
Respectfully submitted,
.R,
A.R. Brienza
Laboratory Director
237
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No.
Unit No.
Unit Description
Installation Date
Steam Output (103 Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft }
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (CF)
Primary Air Temp (°F)
Stack Temp (°F)
JC?G>
/56SS~
£ ffi Jey 3fyrec»c/&r ^toUett
3
£00'
/QwJbi'ewJ-
d^b/'ertf
•^ 37t?
Comments:
238
-------
BOILER EMISSION MEASUREMENTS
i
AND CONTROL ROOM DATA
Location
Unit fy
Fuel
Test No.
es-e
Test Type
Test Load (103 Ib/hr)
JS2
_2C
Excess
(%)
M3
NOX (ppm)
NO (ppm)*
C02 dry (%)
9.8
8.8
fa 3
CO (ppm)*
EC
.(Ib/MBtu)
Solid
Boiler Efficiency (%)
Smoke Spot No.
Opacity
Final Stm Pres. (psig)
Final Stm Temp. (°F)
700
770
770
730
Combus. Air Temp.(°F)
Awe?.
Stack Temp. (°F)
380
360
Fuel Flow .
Fuel Temp. (°F)
Furnace Pres. (in.H2O)
-a,/
-0J?
Register (% open)
at 3% 02 dry
239
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit fy
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess ©2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
up fnnmt*
nv~ ippui;
cr\ /nnml*
ovj vppm/
cn^ /DDm)*
.cjy.4--.-i pav-t Mh/MRtll^
Cr»1 -i rl Pa vt- M K/WTRf-n^
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Coinbus AIJT TGinp (°F)
Stack Temp. (°F)
P*ii o 1 Tonm t ° P ^
Furnace Pres. (in.H2O)
Register (% open)
o
#£&
74<7
Sf W&,
330
A . h
/)W0,
-&.n
Z&?
3&?
-0.S6
eg-/*
4/£
3-38
£oa
10, a
0
#£>e
7&O
3£ OVViJ
s) 2 y t**\
C/> o3IO
#60
746
33~C?
-0./^
at 3% O2 dry
240
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit fy
Fuel
Test No.
Test Type
Test Load (10^ Ib/hr)
Excess ©2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (Dom)*
cr) (nnm)*
QO-. frmin}*
Total Part (Ib/MBtu)
Solid Part flb/MRtul
Roi If^T" T** f ~F i r* "i f*n r*v ( 4 ^
CrnriVo ciori-f- Nr\
OOApi i-\7 f a \
Final Stm Pres. (psig)
Final Stm Temp. (°F)
ComHliQ AT T T^mn f OP^
Stack Temp. (°F)
Plies 1 T^lr\t*T
Fuel Temp (°F)
Fuel Prp«5 " fnc=-io\
Furnace Pres. (in.H?O)
Register (% open)
eg-te'
So«7A&*
Wf
/Z.&
383
3&**C>.
-0J3
-------
I
04
Location No. /
Unit No. ty
Test No. c?g
...
__
--
-
-
\-
-
-
1
ft
c
t
-
D
Jl
-
-
-
-
-
-
-
-
-
-
-
f
-
•J
f
t*
Jt
3
-
-
...
-
n
V(
•n
71
7
-
-
-
?
7
?
-
_.
-
-
-
--
•-
-
i
&
X
O
s
-
-
1-
•—
-
-
-
-
-
*.
-
_
*
-
-
-
/*
(
V Load X^Ttf^^
Fuel £~e?c)/
-
-
-
-
•**
-
^
-
4!
-
-
-
-
-
*
*
-
i+
-
•*
*'
T
A
\
-
'
-
-
-
*•
-
^
-
A\
T
jf
T
-
J(
A
T
"
-
-
^^
Ib/hr
-
-
-
*
(<•
i
4
x
x
X
1-
^
-
^
!«•
«•
• Smoke
O co
1
A
^
^
««
X
A
HC
NOX
•rx
a
10
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
o
in
4J
4J
•H
o
0
Location No
Unit No. ^
Test No.
Fuel
Load
Stack Diameter, D &
0)
M
3
4J
0)
I
0)
4J
w
01
1.0
243
-------
CLIENT:
KVB, Inc.
Tustin, Calif.
Attn: G. Cato
KVB ENGINEERING. INC.
17332 IRVINE BLVD.
TUSTIN. CALIFORNIA 92GQO
(7)4) O32-9O2O
CHEMICAL LABORATORY REPORT
DATE: 7/17/74
SAMPLES: 5 Coal Samples
KVB CHARGE NO,: 6000
INVESTIGATION: As Requested
Sample Identification:
No. 1 Test No. 2802;
No. 2 Test No. 28-18; '
April 19, 1974
RECEIVED: e/ie/74
ANALYZED: 6/25/74
LABORATORY NO: 74119C
April 17, 1974
Boiler 4, Low NOx firing,
No. 1
No. 2
73.83
5.20
0.86
1.80
10.36
7.95
1.53
52.37
13,320
12,840
70.51
5.16
0.82
1.29
15.55
6.67
1.76
48.11
11,850
11,370
Carbon, %
Hydrogen, %
Sulfur, %
Nitrogen, %
Ash, %
Oxygen (by difference)
Moisture, %
Carbon Residue, %
Heat of Combustion:
Gross, Etu/lb
Net, Btu/lb
The results of a spectrographic analysis for trace metals will be reported
as soon as available.
Respectfully submitted,
J- George'Setter
Laboratory Director-
2-4 4
-------
RUESDAIL LABORATORIES, INC.
IEMISTS - MICROBIDLDGISTS - ENGINEERS
SEARCH - DEVELOPMENT - TESTING
LENT
MPLE
D. No.
KVB Engineering
17332 Irvine Blvd.
Tustin, CA 92680
Attn: Hans Buening
4 Coals previously submitted for other analyses
marked as shown
6000
4101 N. FIGUERQA STREET
LOS ANGELES 9OO65
AREA CODE 213 • 2Z5-1G64
CABLE: TRUELABS
DATE August 7, 1974
RECEIVED August 1, 1974
LABORATORY NO. 1052
VESTIGATION
Determination of density
£0
RESULTS
Density (g/ml.)
Test No. 28-2;
Boiler #4, 4/17/74
1.349
•• r
r ••
Respectfully submitted,
TRUE SDAIL LAB ORATORIE S INC.
Alvin E. May
Director of Laboratories
24 5
-------
K V B ENGINEERING. INC.
17332 IRVINE BLVD.
TUSTIN. CALIFORNIA 92GBO
(7I4> O32-OO2O
CHEMICAL LABORATORY REPORT
CLIENT:
KVB, inc.
Tustin, CA
Attn: G. Cato
DATE! 7/19/74
SAMPLES! 5 Coal Samples
KVB CHARGE NO,: eooo
INVESTIGATION: Spectrographic Analysis of Coal -
Supplement to 741190
RECEIVED: e/is/74
ANALYZED: 6/25/74
LABORATORY NO: 741190
Sample Identification:
"No. 1 Test No. 28-2;
No. 2 Test No. 28-18;
Boiler No. 4, April 17, 1974
S.C./ Boiler 4, Low NOx firing, April 19, 1974
Parts Per Million In Coal
Silicon
Aluminum
Iron
Calcium
Magnesium
Titanium
Copper
Barium
•Beryllium
Boron
Manganese
Lead
Nickel
Tin
No. 1
29,000
16,000
3,600
1,200
940
730
18
100
1.8
13
40
37
14
37
No.. 2
50,000
19,000
5,300
1,100
1,400
1,000
16
120
1.6
30
48
trace
14
14
ND = not detected
24 6
-------
Vanadium
Silver
Sodium
Cobalt
Zirconium
Strontium
Potassium
Chromium
fesf
No. 1
KVB
Parts Per Million In Coal
No. 2
14
ND
660
6.8
26
120
740
33
19
ND
590
8.9
33
110
trace
39
ND = not detected
This completes the laboratory report for the five coal samples.
Respectfully submitted,
J. George Setter,
Laboratory Director
-------
INDUSTRIAL BOILER DKSIGN DATA
Location No
Test No.
Unit No.
Dnit Description
Installation Date
Steam Output (103 ll»/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Teirp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/948
/fb'drtJ
^600
Comments:
248
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
S0x (ppm)*
S02 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow (<£a/.///r)
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.F^O)
Register (% open)
3''
/far** /•
Afr
/
/SZ
20
0./J
2-7
A/0rt^ /,
J,T
?,2
;/.&
£03
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit
Fuel
t~ No
Onaoitv f%^
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combxis. Air Temp. (°F)
Stack Temp. (°F)
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Fhim^r1^ Pfpc; fin H«O\
Register (% open)
3-0
A/tyri»*l>
A,r
/0.7
10,2
231
zej
&tf
o
SS&
3&~
dwb,
6/f
/27
-------
STACK TRAVERSE DATA
Location No. /^
Unit No. f
-------
TRUESDAIL LABORATORIES, INC.
THEMISTS - MICROBIDLOGISTS - ENGINEERS
RESEARCH - DEVELOPMENT - TESTING
KVB Equipment Corp.
CLIENT 17332 Irvine Blvd.
Tustin, Calif. 92680
Attn: Glenn Cato
SAMPLE 5 Coal Samples and 2 Fuel Oil Samples, as shown.
P.O.: 1700-43
INVESTIGATION Analysis and tests as requested
RESULTS
4IOI N. FIGUERQA 8TREE
LOS ANGELES 9 O O 6
AREA CODE 213 • Z25-JSI
CABLE: TRUELAB
DATE May 23, 1974
RECEIVED May 1, 1974
LABORATORY NO. 122116
SAMPLE IDENTIFICATION:
7. Oil - Test #3,
~ , Boiler #1, 4-9-74
see F
SA-MPL6 R-6SULT3
(Continued)
252
-------
.RUESDAIL LABORATORIES. INC.
Page 2
LAB. NO.
122116
The results of the oil analysis are as follows:
NO. 7
Carbon, 7. 84.42
Hydrogen, 7. 11.68
Nitrogen, 7. 0.26
Sulfur, % 1.59
Ash, 7. 0.065
Oxygen, 7. 1.99
(by difference)
Carbon Residue, 7. 6.92
(Conradson Carbon)
Heat of Combustion:
Gross, BTU/lb 18,730
Net, BTU/lb • 17,660
API Gravity at 20°C 21.9
Viscosity, SSU, at 40°C 292
Respectfully submitted,
TRUESDAIL LABORATORIES, INC.
Bandziulis
Supervisor, Air Pollution Testing
253
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. /£~ Test No. /£ Unit No. 3
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /5"~
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess ©2 {%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC fnom)*
S0x (ppm)*
SO2 (ppm)*
•Total Part (Ib/MBtu)
^olid Part- Hb/MBtu}
Crnr>]f o ^nnt" No
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow . Xlb./f-/f.
Pii t* 1 T^mr* { ° p \
Furnace Pres. (in.H2O)
Register (% open)
/<*-/
A/0rn* 1,
Air
47
7,3-
331
311
11.6,
O
S4o
&3
4/2
7/0'
80
466~
6.3
AWO,
-0.0$
/6~e
£0uJ>
Air
47
6.0
cf?7
£86-
13.4
O
*//
70 icil
Ji'r
4*
£7
e?e
zse
I/.8
o
4/0
7/0
7&
4s&
£3
-0,07
S6-3-
A/orme?f
Air
s/
Zf
tee
178
/o.o
o
4/0
6?a
76'
40a
•^r
48
7,f
<2
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
'Location
Unit
Fuel
Test No.
Test Type
Test Load (K)3 lb/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC fnDin)*
cr> fnnml*
ov^ i£j£uuy
•TVrt-al Part ( Ib/MBtu)
Solid Part. (Ib/MBtu)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow HibJMf.
Fuel Temp (°F)
. . . .
Furnace Pres. (in.H2O)
Register (% open)
S6~8
#i* ^ooe/
60
&.'
•3 1*3
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /$""
Unit 3$-SO
Fuel
Test No.
Test Type
Test Load (1Q3 Ib/hr)
Excess 02 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
SOX (ppm)*
2 *JrP"1'
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
^moV^ ^nfit" Mr*
Oo a r» i_ t v ( % }
Final Stm Pres. (psig)
Final Stra Temp. (°F)
Combus. Air Temp.(°F)
Stack Temp. (°F)
Fuel Flow K/b./#f,
Fuel Temp. (°F)
piipl PT~^Q ' /r»Qifi^
Furnace Pres. (in.H2O)
Register (% open)
/6 -/tr
}Jbrn*l.
Air
32
3,0
eo7
/
-------
cn
oo
Location No. /5 Load c? Ib/hr
Unit No. 3c?-/0 Fuel
-------
TRUESDAIL LABORATORIES. INC.
CHEMISTS - MICROBIOLOGISTS - ENGINEERS
RESEARCH — DEVELOPMENT — TESTING
KVB Equipment Corp.
CLIENT 17332 Irvine Blvd.
Tustin, Calif. 92680
Attn: Glenn Cato
SAMPLE 5 Coal Samples and 2 Fuel Oil Samples, as shown.
P.O.: 1700-43
INVESTIGATION Analysis and tests as requested
i / 32 '
RESULTS
41OI N. FIDUERDA STREET
LOB ANGELES POD6E
AREA CODE 213 • Z25-1564
CABLE: TRUELABS
DATE May 23, 1974
RECEIVED May 1, 1974
LABORATORY NO. 122116
SAMPLE IDENTIFICATION:
5. Coal -.Test #16^
Boiler ^10 & 13, 4-5-74
The results of the coaV=aaalysis are as follows:
As Received:
Moisture, %
Carbon, 7»
Hydrogen, 7»
Nitrogen, 7.
Sulfur, 7.
Ash, 7.
Oxygen, 7.
(by difference)
NO. 5
10.54
67.48
4.51
1.40
0.86
9.51
5.70
(Continued)
259
-------
RUESDAIL LABORATORIES. INC.
Heat of Combustionj
Gross, BTU/lb
Net, BTU/lb
Page 2
LAB. NO.
122116
NO. 5
11,610
11,190
Dry Basis:
Carbon, %
Hydrogen, %
Nitrogen, 7.
Sulfur, 7.
Ash, 7.
Oxygen, 7.
(by difference)
Heat of Combustion:
Gross, BTU/lb
Net, BTU/lb
75.43
5.04
1.56
0.96
10.63
6.38
12,980
12,510
Test
Respectfully submitted,
TRUESDAIL LABORATORIES, INC.
tgnas Bandziulis
Supervisor, Air Pollution Testing
260
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No. /7
Unit No. 3-MC{l>i0ts6& (JtfcJerJ.ee/ ^takers
Ceaf
$ 1^1 biew t
/)wbier?t
•«• t/00
•
Comments:
26 1
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
Hf (nnml*
SO fDnml*
co_ (DDTTI^*
Total Part (Ib/MBtu)
C/-i1 i i^ T>»>-+- M V> /MRl-ii^
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow H !&/ f/f
Flip 3 Tpmn (°F}
Furnace Pres. (in.I^O)
Register (% open)
,'7-f
A/of"-' <•
A,r
47
/0. 6
a %
292
/O
O
4,<
47
/0.0
337
3S2
O
407
7SO
68
foe
4.6
-0.1
/7-3
Seus /4,'r
46
4,r
46
8.7
286
27
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location £
Unit 32-J3
Fuel C~i*J
<£oacf
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit ^c? -
Fuel -4- MV-^/MR•^-n^
Solid Part. (Ib/MBtu)
Boiler Efficiency (%}
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus- Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow /('/£>.////-.
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.I^O)
/7- XfT
/fu^ /4>f
46
7.3
^o^
136
/.
4g
-------
Location No.
Unit No. 3
Test No. /?
Load
Fuel
Ib/hr
• Smoke X HC
O CO A NO.
CD
cn
u
O
u
,;<£<=
*«
B
S4''
ft(
X
o-
Sr
5
J±
F
:ui:
/£>
°2'
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
TRUESDAIL LABORATORIES, INC.
.HEMISTS - MICROBIOLOGISTS - ENGINEERS
RESEARCH - DEVELOPMENT - TESTING
KVB Equipment Corp.
CLIENT 17332 Irvine Blvd.
Tustin, Calif. 92680
Attn: Glenn Cato
SAMPLE 5 Coal Samples and 2 Fuel Oil Samples, as shown.
P.O.: 1700-43
INVESTIGATION Analysis and tests as requested
32 -'3
. /7
C/L, , /
Test
RESULTS
41QI N. FIGUCROA BTREr
LOS ANGELES 9OOI
"• AREA CODE 213 • 225-IS
CABLES TRUELAG
DATE May 23, 1974
RECEIVED May 1, 1974
LABORATORY NO. 122116
SAMPLE IDENTIFICATION:
_ 5. Coal - Test #16,
. Boiler #10 & 13, 4-5-74
The results of the coal^analysis are as follows;
As Received:
Moisture, 7,
Carbon, %
Hydrogen, 7»
Nitrogen, %
Sulfur, 7.
Ash, 7.
Oxygen, 7,
(by difference)
NO. .
10.5
67.4
4.5
0.£
5.7
(Continued)
266
-------
. RUESDAIL LABORATORIES. INC.
Heat of Combustion
Gross, BTU/lb
Net, BTU/lb
Page 2
LAB. NO.
122116
NO. 5
11,610
11,190
Dry Basis:
Carbon, °L
Hydrogen, %
Nitrogen, 7.
Sulfur, 7.
Ash, 7.
Oxygen, %
(by difference)
Heat of Combustion:
Gross, BTU/lb
Net, BTU/lb
75.43
5.04
1.56
0.96
10.63
6.38
12,980
12,510
Te6t
' '3
Respectfully submitted,
TRUESDAIL LABORATORIES, INC.
l^nas Bandziulis
Supervisor, Air Pollution Testing
267
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. /5~ Test No. 36 Unit No. «?-/
Unit Description / • r- ^ •/*/•?; ,^ —
r -jcs K> e <~ i & r risri'j&c0
S33
182
/ Jvpcn'er teSarr
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /5~
Unit £?-/
Fuel A/6 f - O
Test No.
Test Type
Test Load (1C)3 lb/hr)
Excess 02 (%)
NOX (ppm) *
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (com)*
qo fnnm}*
SO-> (DDIH)*
Total Part (Ib/MBtu)
Solid Part. (Ib/MBtu)
Rnil^f T** f f i r* i pn r*\7 (^^
Smoke Spot No .
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp.(°F)
Conibus . Air Temp. (°P)
Stack Temp. (°F)
PUG! Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Register (% open)
3& -/
/0ay /0£k/
/z
9.0
3
-------
KVB ENGINEERING. INC.
17332 IRVINE ULVO.
TUSTIN. CAUrONNIA 026BO
(714) O3Z-9O20
CHEMICAL LAEORATC.1Y REPORT
CLIENT:
KVB, Inc.
Tustin, CA
Attn: G. Cato
DATE: 7/22/74
SAMPLES: 8 Fuel Oil Samples
KVB CHARGE NO,: eooo
INVESTIGATION,' Spectrographic Analysis
Supplement to Lab No. 741190
RECEIVED: 6/26/74
ANALYZED: 7/13/74
LABORATORY NO:' 741190
Sample Identification:
No. 8 Test 36;
April 11, 1974.
Soiler #1, Bldg. 2,
5*6 E
SAMPLE 12.6SOL.T5
270
-------
e?
. KVB
/>.//
No. 8
Carbon, % 85.78
Hydrogen, % 11.90
Ash, % ' 0.055
Carbon Residue, % 7.38
Flash Point, °C 108
Aniline Point, °C *
Heat of Combustion:
Gross, Btu/lb. 18,830
Net, Btu/lb. 17,740
API Gravity 23.3 at 70°F
Nitrogen, % -28
Sulfur, % 1-72
Oxygen, % -27
Viscosity at 40°C 175
* Sample Oil too dark to determine Aniline Point
** To be turned in at a later date
Respectfully Submitted,
I'-Z'M^r
Js^/3 J. George Sotter
2 7 1 Laboratory Director
-------
KVB
Parts Per Million in Oil
Vanadium
Nickel
Iron
Tin
Magnesium
Silicon
Manganese
Lead
Aluminum
Calcium
Molybdenum
Copper
Sodium
Zinc
Titanium
Cobalt
Strontium
Chromium
Barium .
Phosphorus
Silver
12) » not detected
*There vas insufficient ash for a spectrographic analysis.
No. 8
200.
8.8
6.6
1.5
13.
14.
0.36
3.1
: 1.6
6.6
0.12
0.04 A
6.6
9.4
0.18
0.10
NO
0.72
KD
31.
KD
Respectfully submitted.
272
IY George SorJter
Laboratory Direct
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. /& Test No. /& Unit No. £
Unit Description /kjfer g^-fe,. K/?r(Ss farrt&Ce. Typ e te» tf
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit 2
Fuel 3?
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
en fnrwtit*
&W Vppiuy
SO»> foDml*
Total Part. (Ib/MBtu)
Cnl i A Pa-rt- MH/MRt*n\
Smoke Spot No.
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.I^O)
Register (% open)
/o-/
***"''
se
3,7
/8o
/78
/3
O
-J;r
^_y ff ^2
i£t* f
eio
2oq
ts.o
0 '
330
4/0
422
/00
4*~
-0,2
/0-6
Air''
. 33,3-
7.6
2?
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit 2
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
EC (ppm)*
X
S02 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
/ff-8
A/or»l.
45-
6.O
^/o
'aw
/M
o
400
. :
fll/tfLs,
boo
J0o
tt/
-0.&-
6f'£S-
/&- *r
;0~/o
A,r
fJ
&s
ej?
-------
CD
u
Location No.
Unit No. (Dr-
iest No.
Load" j'c°y &&& ib/hr
Fuel # £ &• /
• Smoke
O co
X HC
A NOV
o2, %
I1'-• KSJ ons for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No. /6
Unit No. <3
Test No. SO-/
Fuel
Load
Stack Diameter,
Ib/hr
D
duct
fa
o
JJ
(0
Q)
E-i
U
(0
-P
277
-------
K V B ENGINEERING. INC.
17332 mVINE BLVD.
TUSTIN. CAUFOMNIA 026BD
D32-9O2O
CHEMICAL LAEORATCEY REPORT
CLIENT:
KVB, me.
Tustin, CA
Attn: G. Cato
SAMPLES: 8 Fuel Oil Samples
KVB CHARGE NO, : 6000
I N VE ST I G AT I ON : spe .trographic Analysis
Supplement to Lab No. 741190
Sample Identification:
No. I Test 10;
, April 22, 1974
DATE: 7/22/74
RECEIVED: 6/26/74
'ANALYZED: 7/18/74
LABORATORY NO : 741190
Bid. 501.
PA6-E
278
-------
Te* / /o
Carbon, %- 85.89 ,
Hydrogen, % ' 11.87
Ash, % 0.043
Carbon Residue, % 5.23
Flash Point, °C 138
Aniline Point, °C *
Heat of Combustion:
Gross, Btu/lb. 18,930
Net, But/lb. 17,850
API Gravity 20.5 at 70 °F
Nitrogen, % .29
Sulfur, % **
Oxygen, % **
Viscosity at 40°C, SSU 240
* Sample Oil too dark to determine Aniline Point
** To be turned in at a later date
Respectfully Submitted,
-KT/2
J. George Setter
27 Q
' J Laboratory Director
-------
KVB
Ko. 1
Vanadium
Nickel
Iron
Tin
Magnesium
Silicon
Manganese
Lead
Aluminum
Calcium
Molybdenum
Copper
Sodium
Zinc
Titanium
Cobalt
Strontium
Chromium
Barium
Phosphorus
Silver
140
15.
23.
€.«
11.
6.0
0.36
0.95
0.77
22.
0.11
0.056
23.
2.0
0.56
0.43
0.47
0,60
KD
HD
KD
Parts Per Million In Oil
ND «• not detected
280
(continued)
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No. 7
Unit No. / -&
Unit Description
Installation Date
Steam Output (10J Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F) ffi*£atef
/?6 7
no
J° I
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /7
Unit T- 6
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC (nom)*
en fnnm^*
cr) fr>nm^*
fn-t-al Part flb/MBtu)
CD! i A Part (Ib/MBtu)
Boiler Efficiency (%)
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)j^/^
Fuel Flow Gial./Mi't'/.
T>ii£il Tornr-* f°T-M
Fuel Pres. ' (psig)
Furnace Pres. (in.l^O)
Register (% open)
7~l
X^-/.K-^ •
4-'r
38
S.3
M
isq
11,8
o
M2
36o
3eo
S3c
/0.V
A /-.
/7fc*/£7.
£-&
S.o
fasi *• /SjSJ
7~
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location / 7
Unit T- 8
Fuel /
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
S0x (ppm)*
SO2 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp.('F£3££r
Fuel Flow 5*{?.
6&
J,tT
/co-/0 /.
/4,r
8s-
f.f
t8
/-;z
AIT faff.
83
£.2
/06
/03
S/,4
O
Ma
3&c
3?o
^3o
/0.S'
^"7
0.0
70 -/&&
r~/s
/4/r fee?.
. 8e
6.6
W
M
Me
0
/te
36&
3f Kcff,
8S-
6.2
/a*
&&
0.0
/oo -TO
at 3% O dry
283
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /~/
Unit T- &
Fuel / 6
4i'r £»<•&.
80
6&
6
-------
ro
CO
en
6
a
Location No. /
Unit No. T- 8
Test No. 7
Load
Fuel
e?e> c Ib/hr
• Smoke
O co
X HC
A NOV
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No. J7
Unit No. r-8
Test No. 7
Fuel
Stack Diameter, D
,duct
Ib/hr
se"
l.o
286
-------
K V B ENGINEERING. INC.
17332 IRVINE BLVD.
TUSTIN. CALirONNIA 026BO
(7M> 032-9020
CHEMICAL LABORATORY REPORT
L1ENT: KVB, inc.
Tustin, CA
Attn: G. Cato
DATE: 7/22/74
>.iviPLES: B Fuel Oil Samples
/B CHARGE NO, : 6000
t'VESTIGATION: Spectrographic Analysis
Supplement to Lab No. 741190
RECEIVED: 6/26/74
ANALYZED: 7/18/74
LABORATORY NO: 741190
Sample Identification:
Ho. 2 Test 7;
April 29, 1974.
SAMPC5
7
287
-------
KVB
7-0
Test 7
Carbon, %
Hydrogen, %
Ash, %
Carbon Residue, %
Flash Point, °C
Aniline Point, °C
Heat of Combustion:
Gross, Btu/lb.
Net, But/lb.
API Gravity
Nitrogen, %
Sulfur, %
Oxygen, %
Viscosity at 40°C, SSU
No." 2
87.22
12.31
0.004
0.033
93
51.6
19,340
18,220
r 33.2 at 70°F
.01
.18
.28
34.2
288
Respectfully Subraitt-ed,
J. George Sotter
Laboratory Director
-------
KVB
*/*//'/ / - S
Af^/ 7
Vanadium
Nickel
Iron
Tin
Magnesium
Silicon
Manganese
Lead
Aluminum
Calcium
Molybdenum
Copper
Sodium
Zinc
Titanium
Cobalt
Strontium
Chromium
Barium
Phosphorus
Silver
Parts Per Million in Oil
No. 2 '
0.15
0.15
25.
0.015
0.076
1.4
0.20
0.14
0.039
0.040
ND
0.056
ND
ND
0.034
ND
KD
0.048
ND
ND
ND
ND » not detected
289
(continued)
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No.
Unit No. <£>
Unit Description
Installation Date
Steam Output (103 lb/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner ( °F)
Primary Air Temp (°F)
Stack Temp (°F)
/^36"
/
^ Ambt /
^ 700
Comments:
290
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit <£
Fuel #
Test No.
Test Type
Test Load (1Q3 lb/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC fonml*
CQ loom)*
SOn (ppm)*
Tr^t-^T Pa>-+- M"K/MRt-ii^
Solid Part (Ib/MBtu)
Smoke Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp (°F)
Stack Temp. (°F)
Fuel Flow . fo/J/r.
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
9- )
Base
7/
7,4
Z46
S^3
J&7
O
£•3
f>2
Jr w. /.
Aif
67
0,7
' /a*cf
7
70
~0J6
/O0
-g
00
3Z4
43&
6<7o
b?3S-
e/e
73-
-0./&
100
9-7
tf> Jir
7
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /&
Unit 2
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
up fnnm)*
SOV (ppm)*
CO fnriTn^*
2 ' ™&
TV^l-al P^yf- M K/MR1~n \
Soli d Part ( Ib/MBtu)
Rni I^T "P^^ir*! f»nr*v ( % )
On^r1! t^v f %)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
PomVinc: AT T TPTTID f°P^
Stack Temp. (°F)
Fuel Flow /£.///r.
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pros. (in.I^O)
Register (% open)
3-8
A/tyr vt* /.
^ti-
ro
Zo
43G
>A t^* Jn _
70O
ttrs'
J#tT
7;
-&.I6
/GO
OC-.
350
430
6&8
43^
Mf
96
-
-------
1
u
Location No. f& Load /f, &&& Ib/hr • Smoke X HC
Unit No. c? Fuel ^^ &>/ O CO A NO
Test No. <7
~
-
-
-
-
i
t
!
\
i
I
:
-
-
_
-
.
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;
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Hi
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-
-
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— i
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-
._
r
-
-
-
-i
-
-
-
-
r ,
"H
P
>t
C
5
»
-
-
3
^
ft
O
z
t-
•"
~
-
-
>
:
^
*
-
-
-
-
s
-
-
-
-
-
s
:
-
/
-
-
-
-
;
-
:
-
-
-
-
-
—
-
-
7
~
-
-
-
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-
-
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*>
T
i
-
-
-
-
-
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:
-
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-
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-
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-
*
-
-
:
-
-
—
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:
-
-
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:
-
-
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i
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:
-
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:
-
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1
-
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z
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m
r-y—
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i
ip
-
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-
-
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_
-
:
q:
i;
— —
~i~
' i
J-H-j-
e
02,
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
o
OJ
w
-------
K V B ENGINEERING. INC.
17332 IRVINE BLVD.
TUSTIN. CAUIrONNIA 0268O
<7M) O32-9OZO
CHEMICAL LABORATORY REPORT
CLIENT:
KVB, Inc.
Tustin, CA
Attn: G. Cato
SAMPLES! 8 Fuel Oil Samples
KVB CHARGE NO, : 6000
INVESTIGATION: Spectrographic Analysis
Supplement to Lab No. 741190
Sample Identification:
DATE: 7/22/74
RECEIVED: 6/26/74
ANALYZED: 7/18/74
LABORATORY NO: 741190
2
No. 4 Test 9-8;
May 9, 1974.
, Boiler No. 2,
irC(L
F£u<_0t
-------
,* KVB
L^ /£$
^
NO. 4
Carbon, %- 86.34
Hydrogen, % " 12.18
Ash, % . > 0.031 •
Carbon Residue, % ' 5.89
Flash Point, °C , 129
Aniline Point, °C *
Heat of Combustion:
Gross, Btu/lb. 18,420
Net, But/lb. 17,310
API Gravity it 70°F 21.8 at 70°F
Nitrogen, % .26
Sulfur, % 1.04
Oxygen, % .15
Viscosity at 40°C, SSU 198
* Sample Oil too dark to determine Aniline Point
** To be turned in at a later date
Respectfully Submitted,
<4- 'JJ- Ct
/s J. George Sotter
Laboratory Directo
-------
/&
KVB
^
9
Vanadium
Nickel
Iron
Tin
Magnesium
Silicon
Manganese
Lead
Aluminum
Calcium
i
Molybdenum
Copper
Sodium
Zinc
Titanium
Cobalt
Strontium
Chromium
Barium
Phosphorus
Silver
Parts Per Million in Oil
No. 4
90.
16.
8.4
4.6
13.
13.
0.53
2.0
3.1
ii.
0.099
0.13
15.
1.3
0.24
0.22
0.43
0.84
KD
trace
0.002
1ID » not detected
297
(continued)
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No.
Unit No. 3
Unit Description
Q
Installation Date
Steam Output (103 Ib/hr)
Design Pressure (psig)
Final Steam Ten?) (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
»
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner ( °F)
Primary Air Ten^> (°F)
Stack Temp (°F)
Comments:
Burner A/u»/£>erj
W/6
/c>s~
3?o
b3o
Waterfvbe.
/s -/csrt?e'S3
3-83
4
#6 &;'
^e/&
•^ boe?
^^25-
0 ©
298
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /Q
Unit 3
Fuel # <£"
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppra)*
NO (ppra)*
C02 dry (%)
CO (ppm)*
HO fnnm}*
or) ( nnm \ *
OW VPPUI/
Tnf-^ 1 P^yf- f 7 H/MR1-11 1
Solid Part Hh/MRt-ii)
UniloT" P'ffrir>ip»n r*\r f 5- ^
Smokp ^nnt" No
On^r-i f-\r f %}
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
J^uel Flow /6./A/r.
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
r
gc
7,&
2V
287
10.8
O
S"S1£~
5 &S
/i S3 S~
y&3
381
430
4ec
446-
Sgfe
,2/6
7?
-0,2 j
/ae
e/'2
A/on*, /.
J.r
3~ I.
A,r
t/6
7.7
zeo
aii
lo,3
O
320
^3o
370
Stt
337^
^&6
£-3
-as
/&&
e/-Q
/0u2 /oacf
37
8.7
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit 3
Fuel # £ &,/
Test No.
Test Type
Test Load (103 lb/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (nnm)*
SO (DDITI)*
j\
co« /nnm)*
Total Part (Ib/MBtu)
c;n1 i rJ P^rf (Ib/MRtuI
On^r*i t~v f%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow /£, //-/r
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Reoister (% open)
'r
79f&
£,f
ees"
C?c?5~
//5
O
O£T
oy
3n
tJ3&
4tf
435-
&?&£>
go
-0./6
/oo - icey
70 -70
£;-;/
#3 £fc&5
77.6-
6.2
2b£>
£ift
M£f
O
,
3/8
436>
fr
e/-/<2
#3ffo&S
76
£.0
; ~tc>o
ej'/j
#-3&£-
//£
o
3/8
430
bsc?
^2&
^475'
(?&e
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit 3
Fuel #
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppra)*
C02 dry (%)
CO (ppm)*
HP fooml*
en (rrom)*
cr\ fnr>Trn*
Tnt-^l Par"h MH/MRi-n^
Col i rl PA ft- MK/MR-t-n^
Rr> 1 "\ f^r Ffrf:iri'i<=>n r"\7 ^ §: }
Smoke Spot No
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow /6///r.
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
goos
7&
6.3
231
^2o
//,£'
o
38C
^3&
4/0
43o
^438
W/
&7
-a,/?
/oo - Je?c?
joe> - O
<2/-;6
/4 £005
76
6,6
217
e/tf
11,2
o
3^o
430
4/0
t>3&
£4
7 ~3~0
^J-/&
f&
/
&
j
at 3% O dry
30 1
-------
a
CO
O
Location No.
Unit No. -3
Test No.
Load &
-------
STACK TRAVERSE DATA
Location No.
Unit No. 3
Test No.
J8
Fuel
Load &£?,
Stack Diameter,
Ib/hr
duct
^00
0)
M
4J
10
M
0)
0)
EH
JJ
to
10
303
-------
K V B ENGINEERING. INC.
17332 IRVINE BLVD.
TUSTIN. CALIFORNIA 0268O
C32-9020
CHEMICAL LAEORATCr-Y REPORT
CLIENT: KVB, inc.
Tustin, CA
Attn: G. Cato
SAMPLES: 8 Fuel Oil Samples
KVB CHARGE NO,: eooo
INVESTIGATION: Spectrographic Analysis
Supplement to Lab No. 741190
Sample Identification:
DATE I 7/22/74
RECEIVED: 6/26/74
ANALYZED: 7/18/74
LABORATORY NO: 741190
^/
No. 3 Test 21;'
, Unit 3, May 2, 197A.
F" O LL OOI f NJ £-
/2_£TSOLT5
304
-------
KVB
(/<**•/•
Test
Carbon, %-
Hydrogen, %
Ash, %
Carbon Residue , %
Flash Point, °C
Aniline Point, °C
Heat of Combustion:
Gross, Btu/lb.
Net, But/lb.
API Gravity
Nitrogen, %
Sulfur, %
Oxygen , %
Viscosity at 40°C, SSU
No. 3
85.72
11.95
0.032
5.41
129
18,910
17,820
22.9 at 70°F
.26
1.03
1.01
195
* Sample Oil too dark to determine Aniline Point
** To be turned in at a later date
Respectfully Submitted,
305
/s J. George Setter
Laboratory Director
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. /g Test No. cr^? Unit No. fy
unit Description f?,-/e~ Boiler, 6^ria/ A/0. 34?-?
/ '
Installation Date
Steam Output (103 Ub/hr)
Design Pressure (psig)
Final Steam Temp ( °F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
WtS"
/6G
520
b^o
\(/aterfub
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /&
Unit 4
Fuel # r-im ^ *
t>ux ippm;
CO^ fnnml*
Tnt-al Pa-rt- MH/MR-H-^
c<-»1 -i ft T>aT-+- MVi/MR4-ii^
SrnoJce Spot No
Opacity (*•)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow /6.///r.
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
es-/
Bose
/30
6.8
242
ess
H,0
O
S—f, "}
3v3
£~">O
JdV
S3 /
O6
3J4
43G
&0
40f
7?3&
20r
&
9o
-o./6
c?£>- 7
4/e?ri~it.
/}>'f
/So
7^
237
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /&
Unit 4
Fuel / £ Oi/
Test No.
Test Type
Test Load (103 lb/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC (com)*
CQ loom)*
«Q /DDm)*
2 \¥f /
TVit-al Part- n V>/MRi~ii)
Solid Part (Ib/MBtu)
' 1 Ff f" ' enc CM
y i °/
, „
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow /£>///r.
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H-,0)
Register (% open)
ez-8
Sou* /f,r
120
6,5-
236
227
fl.O
O
3/o
43&
•5~fy<2
bofy
?
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /Q
Unit fy
Fuel / £ &>'/
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
S0x (ppra)*
S02 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu) "
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow tb/Mr.
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
^-/s
fZgCOS
tee
9,7
'
-------
CO
O
I
a
u
K
Location No
Unit No. ^
Test No.
Load /J"£?,
Fuel ^<<
Ib/hr
• Smoke
O CO
X HC
A NOV
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
STACK TRAVERSE DATA
Location No. 18
Unit No. ^
Test No. c?c?-/6
Fuel
Load
Stack Diameter,
,
duct
Ib/hr
/> 7 "
^ '
0)
^
4J
IT)
^
0)
a
e
0)
4J
W
3 1 1
-------
K V B ENGINEERING. INC.
17332 IIIVINC BLVD.
TUSTIN. CALIrOF
-------
' / i c1 c*
Vu.-f
-------
KVB
6
^^.
Vanadium
Nickel
Icon
Tin
Magnesium
Silicon
Manganese
Lead
Aluminum
Calcium
Molybdenum
Copper
Sodium
Zinc
Titanium
Cobalt
Strontium
>
Chromium
Barium
Phosphorua
Silver
Parts Per Million in Oil
Ho. 3
100.
9.9
12.
1.5
11.
8.0
0.38
2.4
0.77
10.
0.077
0.17
24.
IS)
0.15
p. 096
trace
0.20
KD
KD
KD
!ZD «• not detected
3 1 4
(continued)
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No. /
Unit No. /
unit Description
-/ -
&0*'/er fy/oe
Installation Date
Steam Output (10 Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner ( °F) .
Primary Air Temp (°F)
Stack Temp (°F)
/?7
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit /
Fuel
Test No.
Test Type
Test Load UO3 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (DDID)*
c;O ^nnm}*
ou \ppm/
A
Tot-al Part flb/MBtu)
c;o1 \ <\ Pflrt- Ob/MRtu}
Boil GIT Ef f i cioncy (% )
Smoke Spot No
Final Stm Pres. (psig)
Final Stm Temp. (°F)
fVimHnt: Air T^mo f °F^
O+- =a*-V Tomr^ ^ °P ^
Fuel Flow /5 /7/r/
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.F^O)
Register (% open)
/-/
/// x^/r
/4-S
b*f
t*?3
4/7
&8
O
M0
37£^ X^//-
/S"
Z-3
33g
332
/4.7
<LLP rfi f
w.s
/.6
276
?7/
M.6
e33
/£-&
37&
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit /
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
CO 2 dry (%)
CO (ppm)*
un (nrim^*
n^ ^ ppm ;
SO (nnm)*
Cnrt frinTrO*
2 \PPI[1/
Total Part (Ib/MBtu)
^nl i ri P^vt- f 1 H/MRt"n^
Srnoko Spot No
ODAPI ^-\r ( % }
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus Air Temp (°F)
'^fflr'V Tomr-i I°V\
J^uel Flow (&PtfJ
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
/-8
it&aj /0&C/
S.7
//,0
<^<2&
4//
8.2
o
/^?
37C
/I lst-J&.
G.gS
/g7
37
O
/0-
3 7
86
^3
3?&
• /),r
. /&#
4.4
385-
374
/2£~
0
•7 ,
•J '
MP
37&
?.&
Ss~
/&
M'J.T
/3.7
5-g
&4C/
l/36
//,&
O
^5
/^^
37&
*"
J>,6
e&/
77
C>,^ 7
/'&&
at 3% o dry
3 1 7
-------
CO
DO
ft
Qt
Location No.
Unit No. /
Test No. /
Load
Fuel
Ib/hr
• Smoke
O CO
X HC
A NO,
Emissions for Industrial Boilers as a Function of Excess Oxygen
-------
Location No.
Unit No. /
Test No. /-//
STACK TRAVERSE DATA
Fuel
Load
Stack Diameter, D
duct
Ib/hr
30"
4-1
fl
^1
0)
I-
o
u
(0
4J
D/D Duct
3 1 9
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No. <£
Unit No. /
Unit Description
Installation Date
Steam Output (10 Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft }
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Tenp at Burner ( °F)
Primary Air Temp (°F)
Stack Tenp (°F)
/r
# ^ <^//
c'OC
/)wbi<2tft
4g
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit /
Fuel #
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO ( nnm \ *
HP (nnm^*
SO (onm}*
SO- (nnm^*
Total Part (Ib/MBtu)
^nlir? P.a vt- M H /MR t-Ti^
Boiler Efficiency (% )
Opacity (^)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus . Air Temp (°F)
Stack Temp (°F)
Fuel Flow (& PrfJ
Fuel Temp. (°F)
Fuel Pres. (psig)
_Furnace Pres. (in.H2O)
Register (% open)
2~/
t/i Air
M.2
£.6
bea
33S
//<£
r K-/ '
Ai'r
#.7
4.3
333
33S
12.8
/-\
u
J&o
37&
-
60 >*,e
S4.7
4.4
333
336
12.3
/^
V
/•% -7(2
/ 3 /&
1 "2 s^S]
'Ob y
C j£~
0$
/£&
37
-------
STACK TRAVERSE DATA
o
-<£>
Fuel
Load
Stack Diameter, D
Ib/hr
duct
*80
4<7o
46o
322 .
-------
CO
N3
CO
a,
u
Location No.
Unit No. '
Test No. £
Load
Fuel
"<' Ib/hr
>&'7
• Smoke
O co
X HC
A NO^
for Industrial Boilers as a Function of Excess Oxygen
-------
K V B ENGINEERING. INC.
»7332 II1VINC fcUVD.
TUSTIN. CAUIFOHNIA C.26BO
O32-9O2O
CHEMICAL LAEORATCP.Y REPORT
CLIENT: KVB, inc.
Tustin, CA
Attn: G. Cato
SAMPLES! 8 Fuel Oil Samples
KVB CHARGE NO, : eooo
INVESTIGATION: Spectrographic Analysis
Supplement to Lab No. 741190
Sample Identification:
DATE: 7/22/74
RECEIVED: 6/26/74
ANALYZED: 7/18/74
LABORATORY NO: 741190
/
No. 5 Test 1-10;
Unit 1, May 13, L97A,
.v • L fl ~ o L c.
^ J c5- P A £- e~
324
-------
KVB
'//^x A?
/ /
No. 5
Carbon, % '86.08
Hydrogen, % 10*37'
Ash, % 0.044
Carbon Residue, % 11.43
Flash Point, °C 134
Aniline Point, °C *
Heat of Combustion:
Gross, Btu/lb. 18,280
Net, Btu/lb. 17,340
API Gravity 11.3 at 70°F
Nitrogen, % .44
Sulfur, % **
Oxynen, % **
Viscosity at 40°C 688 (at 60°C)
* Sample Oil too dark to determine Aniline Point
** To be turned in at a later date
Respectfully Submitted,
4i.-/2 J. George Setter
325 Laboratory Director
-------
KVB
(St.t-f /
T
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No.
Unit No. /
Unit Description
Hoc/?/
Installation Date
Steam Output (103 Ib/hr)
Design Pressure (psig)
Final Steam Temp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit /
Fuel #
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
C02 dry (%)
CO (ppm)*
HC (ppm)*
CQ fnom)*
•*•
Total Part (Ib/MBtu)
Cr>1 T H PAi-t- Mh/MRt-ii^
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Comb us . Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow (^/?rfj
Fuel Temp. (°F)
Fuel Pres. (psig)
Furnace Pres. (in .I^O)
Register (% open)
&?-/
Afar*-' '•
Ait
/-6~
Base
/?
3.6
66
6S
/2,6
&e
&2
54
6>.0378
&• &6 3<-f
&S
/5V
37
-------
STACK TRAVERSE DATA
Location No.
Unit No. /
Test No.
Fuel
Load
Stack Diameter, D
Ib/hr
duct
1.0
Q)
EH
O
rt
4J
in
to
329
-------
co
cu
o
I
Location No. /
Unit No. /
Test No. £'
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No. S3
Unit No. /
Unit Description
&&i'/er
Installation Date
Steam Output (10J Ib/hr)
Design Pressure (psig)
Final Steam Teirp (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft }
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner ( °F)
Primary Air Temp (°F)
Stack Temp (°F)
/?7<7
/7.£T
ego
t/06
]t/&tertub&
V'g-8
327
33 a
/ fa her 4ir /We>w//??>o/ tfc/rwer
#bi
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /v
Unit '
Fuel # ? &,
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC (ppm)*
S0x (ppm)*
S02 (ppm)*
Total Part (Ib/MBtu)
col i d Part (Ib/MBtu)
Boiler Efficiency (%)
On^r-i t\7 (%>}
Final Stm Pres. (psig)
Final Stm Temp. (°F)
PrrniViiic: Air T<=>mr> f°F}
Stack Temp. (°F)
Fuel Flow (& pfij
Fuel Temp. (°F)
Fuel Pres. (psig)
Furnace Pres. (in.H20)
Register (% open)
S3-1
&&6Z1
/3. 8
3.0
9/
6
/*0
37&
/ii^fty.
3~00
/•,g
/03
le/
J2.<2
O
tj
/36
37&
4g
-------
STACK TRAVERSE DATA
u
o
w
\
-p
in
>1
4J
•rH
u
o
rH
X
O
(0
4-1
w
Location No.
Unit No.
Test No.
Ib/hr
Stack Diameter, D,
duct
0)
M
jj
m
Vj
0)
U
<3
4J
1.0
333
-------
o,
o
Location No. /
-------
INDUSTRIAL BOILER DESIGN DATA
Location No.
Test No.
Unit No. /
Unit Description
-/ -
Installation Date
Steam Output (10J Ib/hr)
Design Pressure (psig)
Final Steam Ten?> (°F)
Furnace Type
Furnace Size L-W-H (ft)
Furnace Area (ft )
Furnace Volume (ft )
Burner Description
Horiz. Burner Spacing (ft)
Vert. Burner Spacing (ft)
Test Fuel
Fuel Temp at Burner (°F)
Primary Air Temp (°F)
Stack Temp (°F)
/?7
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit /
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC (ppm)*
SO (ppm)*
A
S02 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No .
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow / (
-------
CO
CO
a
o
X
Location No.
Unit No. /
Test No.
Load
Fuel
Ib/hr
-------
STACK TRAVERSE DATA
u
0)
w
-U
•H
0
0
Location No.
Unit No. /
Test No.
Fuel
Load
Stack Diameter, D
Ib/hr
duct
338
-------
K V B ENGINEERING. INC.
17332 IRVINE bLVD.
TUSTIN. CALIFORNIA 026BD
C7I/.) 032-9O2O
CHEMICAL LABORATORY REPORT
IENT: KVB, inc.
Tustin, CA
Attn: G. Cato
..MPLES: 8 Fuel Oil Samples
B CHARGE NO,: 6000
VEST I GAT I ON.1 Spectrographic Analysis
Supplement to Lab No. 741190
Sample Identification:
DATE : 7/22/74
RECEIVED: 6/26/74
-ANALYZED: 7/18/74
LABORATORY NO: 741190
/
/>//
No. 6 Test 52-5;
Unit 1, May 16, 197A,
Fo /? :J A N^ PL (L
339
-------
Carbon, %
Hydrogen, %
Ash, %
Carbon Residue, %
Flash Point, °C
Aniline Point, °C
Heat of Combustion:
Gross, Btu/lb.
Net, Btu/lb.
API Gravity
Nitrogen, %
Sulfur, %
Oxygen, %
Viscosity at 40°C
No. 6
87.38
12.44
0.001
0.036
88
54.4
19,470
18,340 '
1 34.8 at 70'
.006
.06
.12
33.0
340
Respectfully Submitted,
J. George Setter
Laboratory Director
-------
KVB
/
S3, S3,
Parts Per Tiillion in Oil
No. 6
Vanadium *
Nickel
Iron
Tin
Magnesium
Silicon
Manganese
Lead
Aluminum
Calcium
Molybdenum
Copper
Sodium
Zinc
Titanium
Cobalt
Strontium
Chromium
Barium .
Phosphorus
Silver
KD = not detected
vae Insufficient ash for a spectrographic analysis.
Respectfully submitted,
X? >^
Q • J^Ti^^^U^^
JY George Setter
341 Laboratory Director
-------
INDUSTRIAL BOILER DESIGN DATA
Location No. /^ Test No. /93~-
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit £?
Fuel #
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC (ppm)*
X
S02 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow &f*r/
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
/&TV
3o*e
/4
3.1
/6
A/or u-t '.
/fy
2.2
/77
/77
13 J
e
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit r>
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC (ppm)*
X
SO2 (ppm)*
Total Part. (Ib/MBtu)
Solid Part.(lb/MBtu)
Boiler Efficiency (%)
Smoke Spot No .
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow 6Pr-i
Fuel Temp. (°F)
Fuel Pres. (psig)
Furnace Pres. (in.H2O)
Register (% open)
/atr. g
f 7 ^J g>
£& i*~?
tf.g
-^ *7
J /7 /f
/#4
I ^ "O
0
0
3.*
£..
w
3.0
M-J
M 7
/3
0
0
2
/S0
V&
f&8
£3
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit .&
8<2
/
o
0
e.s
&
/tt
#£-
S°4
3
4
/~
-5
/£&
/W
403
as
/*
&4
•'
407
#
. M.I
/,3
MS
S30
/4
3s
&
4
/• —
^
&e
/
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit 2
Fuel
Test No.
Test Type
Test Load (1C>3 Ib/hr)
Excess Q>2 (%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC (ppm)*
SO (onm)*
^"^2 »PP'n'
Total Part Hh/MRtu)
C/-\1 i /3 Oavf- MH /Mn-hil ^
. n -c*ff ' /Q. \
Final Stm Pres. (psig)
Final ^tm Tpmn ( °F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow &Pn
Fuel Temp. (°F)
Fuel Pres. (psig)
Furnace Pres. (in.f^O)
Register (% open)
W7-&
F&R
M.fy
3.
0
s-~
£
&0
/GO
^00
<=>,/
Za^
43
0,3
66
ws ~e
SCA
W
S
66
W0-*
5CA
/3.0
a/
136
126
/3
o
o
/~- ."
& ,&
J5~&"
/0&
s&y
'
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit £
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC (ppm)*
S0x (ppm)*
SO2 (ppm)*
Total Part. (Ib/MBtu)
Solid Part. (Ib/MBtu)
Boiler Efficiency (%)
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Final Stm Temp. (°F)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow ~,&M
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H-,0)
Register (% open)
we - 7
$CA
/3.6~
3
e2.2
0
fa
0.027
a.caj
i^J r^
(t
f
/*-/
& ^
^2 ' J ' £/
e.3
&a
4s~
G.36~
66
/0*
'.'6
ass
£6
at 3% O dry
347
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit £?
Fuel
Test No.
/
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit e
Fuel
Test No.
Test Type
Test Load (1Q3 Ib/hr)
Excess O2 {%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC (ppm)*
Q/-V fr-iniM*
ou^ ippmj
CO /T-*T~»TTt^*
Total Part (Ib/MBtu)
Cr-\l -i /} Da v-J- M V* /MQ-f-ii ^
Boiler Efficiency (%)
Smoke Spot No.
. / 0 \
Opacity (-s)
Final Stm Pres. (psig)
Final Ci-ni Tomri f ° "P^
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow . (-jPrt
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
/
F&&-/
££4
/tt
3.1
M
6c/>
M.J-
3.0
/6o
/£"?
JZ4
O
//
(J
&
/6~£
/e^
&3
e.s/
&0
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit c!
Fuel
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm) *
C02 dry (%)
CO (ppm)*
up fnnTn)*
en f r\r\m ^ *
ow ipjJiii;
A
^0^ fnnm}*
TV>t-^1 "Part- (1 h/MRtu)
c;nl i rl P^rf- Mb /MR til)
SinoJcG Spot No
On a r1 "i t~ v ( %.}
Final Stm Pres. (psig)
Final Ct*Tn TfiTTin ( ° fM
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow &/*rf
Fuel Temp. (°F)
Fuel Pres. (psig)
Furnace Pres. (in.I^O)
Register (% open)
c&e-g'
A/ort~> 1.
J,r
w.a
e.q
&3
&3
13
3e
"5 -9
dS
/
&
-b
/3~&
s^J,.~^
/?
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /2 (*)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC (ppm)*
CO /r-*T-wnl*
ou I ppm;
TV-it-;*! Pa-r+* (1 "h/MR-hn^
QrO i (3 Par-+- M K /MR -l-n^
. - «££• ' /« \
Smoke Spot No .
Opacity (%)
Final Stm Pres. (psig)
FT n^l Q-f-TTi Tomn f °PM
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow . ££>rt
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
&- ^
/i£5X?
. /^
L.
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location /tf
Unit 2
Fuel #£ £?//
Test No.
Test Type
Test Load (103 Ib/hr)
Excess O2 (%)
NOX (ppm)*
NO (ppm)*
CO2 dry (%)
CO (ppm)*
HC (ppm)*
OU \±>¥111'
rprt4- -. 1 p =»>-+• / 1 "H /MR "Ml ^
c^nl i d Part ( Ih/MRtu)
T*ff • • /«. \
Boiler Eliiciency (%;
Smoke Spot No.
Opacity (%)
Final Stm Pres. (psig)
Combus. Air Temp. (°F)
Stack Temp. (°F)
Fuel Flow <£/?//
Fuel Temp. (°F)
Fuel Pres. (psig)
Furnace Pres. (in.f^O)
Register (% open)
202 -&
F&Z
J{t
/ tf
' &6
/26
/3.3
22
&
g-
g-
/57
/^
4-2£-
./
s^0&
32
ate-
66
£03-6
6£A
M.2
3.0
W
/£j£3
/ C • fa
So
7/
S3
9
-------
BOILER EMISSION MEASUREMENTS
AND CONTROL ROOM DATA
Location
Unit Pt*f
Fuel Temp. (°F)
Fuel Pres. ' (psig)
Furnace Pres. (in.H2O)
Register (% open)
eo3--7
&CA
to
|