-------
s-
3
O
CO
<£>
CM
Q. U
at
—i a.
ixi n)
a «_>
o
LU O
s^:
o: v>
o E
u_ o
CO
co r-»
ac.
LU
I—
i—i
u.
CJ
I—r
CO
CTl
CM
00
cu
(O
CO
3
• ••
as
>
^
jQ
tQ
40
O
CM
S-
d)
4J
1
•1—
u_
o
•1—
s-
Tf^
(0
u.
r—
s_
CO
•4-*
r™™
•r—
U_
O
•r~
$_
-Q
«a
'LL_
i-
O O i—
1 1 CO O r— CM O VO
1 1 r- r— CM CO r—
O)
E
•r— * — * i—
•O O O CM CO
E CT> C^^- r— O%
o vo r—
"— *
o>
<*• •* ' %
•r- O in
) O COCTk • • • • •
rjio« ir>ir>c3O LT>
S- «"•» i— CM CM
<_> r-
•^— ^
^
•^
•(/>
s:
s- •
>» 4-3
s^~ c/) oo 01 *^^ c?
u_ 2: s: s- *«» 3
C_> •* rd 2T ~O O>
4J -E OS!
4-> VI O •> i- •~ Q- •O£» T3
"O E O O i — V> CO
co -i— o •>>
i — E O>4->OS!V1O
f— ^*^. r™~ E "r"" ^*** VJ E
OCO tO -i- d T3 ««• COCO
SH E 4-^ 4^ "^ CO E S—
4-> -i- « a. s- -t- > co
O CO as CO "O i — 'r~~ 4-3
O4->OQ.COfO 4-3o
in
E
CO
V> •!"
0 O
•i- 3
4-3 O"
CO E
a. -i-
O T3
E
Ol -t-
E S-
•r- 0>
•a
E • •*
••- s-
S- 0
O> 4->
o
"O nJ
E <4-
ns
a>
Oi • E
E O -i-
•r-4-34-3
-E CO ,
-Q E \
E v»
O in s_
O CO 3
4-3 O
O O -E
4-3 E
CO O
E "O O
•r- _ O
4-> s: c\T
s_ 2:
CO =. E
Q. O
E V) -O
E -o co
3 E in
r— fO OS
O V) J3
0 3
o co •
•o .E s- s-
E 4-> rO >>
1 CO E -^
4J 4J T- in
-E O -E S-
• O> E V> 3
co .,- co 3 o
S- T3 S- -E
O U
4-> CO = O
-E s: s- o
(4— "
in E i. co
CO •!— CO in
U 4-> 4-3 E
E V) 4-> E O
CO S- CO CO
S- CO r— -r- T3
CO J3 4-3 CO
4- E CO O V)
CO 3 .E 3 rO
c£. •zz (— cr^a
"3 J3 O "O
8-b7
-------
o c
u_ o
I— o
oo tn
O «—
CM
CU
O
co
•r- O
T3 CD CO
E CM *
•r- CO>—
S- r—
CJ3
CO
col
r— O
• O 00
CO O
03
O
CO O
o -
CM
CM
in i—
CM
l— CM
1^ Cft
at
co o
• «
VOO
CM
o
CQ
CO
CO
CU
CO
o
cu
4J
CU
CO
C_5
O) -r-
CO
a>
+->
(0
•i- O
+J r— t—
•r- CO
CL S-
cO CU
O CL
o
"O
CO +->
i— O
•fa*
O)
o
CO
CJ
CU
S-TJ
o
•fa* 3
-!-> Q.
o ;
CU
tM
ca
CO
CM
CU
"4->"
(O
o
cO
-a
cu
4-) CU
l/J S-
o
CU
CO
!U
CU
O)
o
CO
o>
C 0
•I- +J
O
-a
(U >O
s-
» CU
•r- S-
CU r— >
<" 5
4J O
O -C
CU O
-n O
o
<0 s
CU =
CM
E -o cu
3 E CO CO
CO CU
.E tf) en >>
I CU E ^-.
^ s_
cn
ro
•r- CU 3 O
s- -a s- -E
o
CU = O
j=. s: s- o
CU -r- CU
O -l->
CU
s_
cu
CU
CO .
CO
in
4-> C
E O
S- CO CU
CO r— T- tJ
•»-> CU
o in
3 CO
cu
o -a
8-68
-------
S-
3
O
cn
O
CM
• •
CM
t—ta
O. U
to
_i a.
LU tO
a o
o
LU o
C£. CO
O £=
Uu O
4->
OO
I— O
oo o
O CO
CO *— *
a:
LU
co
oa
•=c
co
CO
(U
IE
03
_£
O)
3
"re
>»
a
™™
4^
O
CO
s-
o>
«v
r»
J_
u
r—
S-
a
re
J_
CM
s_
CM C7»
-E VO O O CM r~»
CO CM O LO
3 CM •>
S- CO
cn .--^
E O O r— CTl . CO
.E i— O i— O LO
CO •> * i — CM
3 i— O
S- «*
CJ
S-
s:
s- ••
- — « o — " ^^ ^^ c^
u- s: 2: s-
CJ •> fO
^C ** 4^ c~
^— ^ 4^ ) CJ
CO O
T3 E O 0 f—
CU •<— O fO
r- E 01 4->
r^ ^**x r™" E *^
o co 4-> rtJ
4J T- fO O
E •> Q. S-
O CU *O d) TIJ
o +-> o o. w
(T3 O M
E S- -0 ••-
O S r— • i— O) 3
re *+— re i— E
i. +J T- E
CU cn co Q «C
Q. re E
O • CD M
10
CO
LOO CM
r- O CO
CO i—
VO
r- VO
CM O LO
• • •
LO O CO
00
cr>
r— •
i— O CM
o o cn
i— CM
VO
CM o cn . .
VO O O
OO CM
re
3
O
'43
s-
s_-o re
>>-*-> CL
\ O
v* 3 cn
s: -o s:
"0 ^»
4-> S- &*
co Q.
O . "
o cn co
S . CO
TO ^ a>
E
N CU
•i- >
^^ »r~
re 4^
3 (JO
E CU T3
E M- CU
re ' ^— ^
cu o
•— I E
re +-> cu
4-> CO S-
o o
1— 0
*
CO
0
r—
CO
CU
o
c~
CU
S-
cu
Cj_
CU
re
id grinding operations.
>M
en
E
•r™
-E
>
_)
S-
CJ
-o
CU
E
JD
E
0
o
0
4-3
c
•p—
»TJ
4-^
S-
cu
o.
E
E
3
r—
0
u
T3
E
re
.E
1
4^
.E
cn
•r™
S-
CU
-E
-l->
E
•^
V/>
S-
cu
E
3
z:
-Q
»
o
0
E
CU
13
—
s:
2:
CO
"^3
E
re
CO
3
O
.E
4^
CO
CD
"4"^
o
E
CU
-o
—
s:
s
^.
cu
-^
4-^
CU
r—
CU
J=
1—
U
"actor; grinding quotients based on
T~
' cn
E '
•r-
re
i_
Q.
O
s-
03
0)
^
CO
S-
3
O
0
o
o
ft
CM
E
0
-a
CU
CO
re
f»
CU
S-
re
en
E
JZ
CO
3 •
S- S-
o re
cu
s- >,
o ^~~
H- CO
S-
CO 3
4-3 O
E .E
CU
•r- O
+-> 0
o «=i-
3 *
o-co
"O
8-69
-------
s_
o
en
O
in
_l O
Q. OS
Q-
_i «a
UJ C_)
3 O
a; c
o o
10 o
r-0
O—•
C£
U.
CM
CO
00
CU
(O
1—
rO
O
O
•r— S_
S- CU
tO r—
U_ T-
U_
00
o
•i- S_
S- CU
JO 4->
ret r—
U_ T-
u_
cu
R}
CM
o
•r- S-
S- CU
o 4J
U_ T-
U_
0*"
•r- S-
S- CU
U_ T-
U.
cu
+->
CU
to
to
Q_
CM CT»
1 II O ^— CT1
in in I*-
O)
•r- O O < — «— CT>
E CM CM r— i— VO
•r- « » CO CM
S- r— in
c? o"
•r- O
JE t^ O O r» i—
3 OO r— r— OO CM
S- CO CM
O - —
E O
•r- O
_E IO O CM O •=»•
3 CF»CM •— CT» CM
S- CO CM
O)
f— x- ^
•r- O
y 10 o «* ** m
3 CM «• CM 00
S— CTI
CJ
S.
•v.
<^
S
~^ w
- — . (J ' V» « «o
5. 4? "to "5
CO O
-a c: o o «—
cu T- o re
i— g CD -l->
o co nj T- c
^J £ (0 <.
E « CX S_
o cu rei cu "a
o 4-5 o o. a
i—
•i- o r- o re
4J r— r— CU =
ttj q- fO S- C
S_ 4-> •<- C
CU CO CO O «=t
Q. o en
CD *""* T*^
r— CM
)
h
s_-o
>>4->
1 O
t/3 3
s: "a 01
o s:
•fJ Q. */> ^O
co cu
O CD •> >
o s: co o
"*» co S
L ~O CU
r— -r- +J
re) 4-> ret
3 Or—
E CU 3
E 4- O
tO l»- T-
CU -M
: -— is-
: rei 4-> rei
: +-> co Q.
O O
t— 0
o
<0
s_
O)
a.
o
en
c
S-
cn
o>
£=
O
O
•a
i/i
it)
01
CU
O
cr
a>
s-
o>
S-
o
o
to
a»
• c:
o T-
-M -(->
(U
S-
>
Q.
O
•a -r- i.
cu r—
O
CU
to =
3
O
o
o
o
•k
CM
9
CO
o
r—
CO
CU
O
E
CU
s_
cu
14-
o;
cu
Q.
E
E
3
'o
O
•a
c
fO
"?
JC
cr>
si
cu
^^>
^
•r-
CO
S-
cu
S
3
sz
—
CO
^3
^
rei
CO
3
O
.E
4->
CU
o
c
cu
—
s:
S-
01
-M
-l->
CU
1—
cu
J=
1—
E
O
•a
cu
CO
ret
.a
cu
s_
re<
E
^
CO
3 •
S- S-
o rei
cu
s- >>
o --^
M- CO
S-
CO 3
•4-* O
E -C
CU
•r- O
4-> 0
O «*
3 "
o-co
8-70
-------
8,400 hours/year has been used.' For Model Plant 2, where both crushing
and grinding operations are employed, 8,400 hours/year is used as the
operating factor, solely for the purpose of computing the unit annualized
costs. ' "'','•
Each cost-effectiveness ratio appearing in the tables is simply the
quotient of the total annualized cost and the amount of particulate
collected annually by the fabric filter system. To compute the parti-
culate collected, the 2,000 and 8,400 hours/year operating factors are
applied, respectively, to the individual crushing and grinding operations.
However, for combined crushing and grinding operations, the following
expression has been used to calculate cost-effectiveness:
Cost-effectiveness =
($/Mg particulate
removed)
Where: TACr, TACr
L b
TAC
TACr
b
7.65 x 10
-7
(2000QC + 8400QG)
total annualized costs for crushing and
grinding baghouses, respectively (M$/year)
total volumetric flowrates for crushing-
and grinding baghouses, respectively (m /min)
The numerator is the sum of the annualized costs for the crushing
and grinding operations, while the denominator represents the total
amount of particulate removed by the fabric filters controlling these
operations. (Cost-effectiveness is further discussed in Section 8.2.4.)
As the tables indicate, the installed costs in the crushing (only)
model plant range from $60,000 to $336,000, as the plant capacity goes
from 9.1 Mg/hour to 540 Mg/hour. However, given the sixty-fold increase
.8-71
-------
in the plant capacity, the installed costs increase relatively little.
This is so because the fabric filter installed costs are a function of
the volumetric flowrate, not the plant capacity. Moreover, the volumetric
flowrate, while dependent on the capacity, does not increase proportionately
with the plant size.
Based on a 2000 hour operating year, the total annualized cost increases
from $14,000 to $87,000 per year, corresponding to $0.78 to $0.08/Mg
product, as the plant capacity goes from 9.1 to 540 Mg/hour. Ordinarily,
one would also expect a more substantial increase in the total annualized
cost over such a large range in plant capacities. However, as Tables
8-21 through 8-26 show, the annualized capital charges comprise the bulk
of the total annualized costs. And since the annualized capital charges
are directly proportional to the installed costs, the total annualized
cost very nearly follows the change in the capital cost.
There are several reasons why the direct operating costs are so low.
First, because the gas streams controlled are non-corrosive and low-
temperature, the fabric filter maintenance is relatively small, amounting
to less than one percent of the installed cost annually. Then, because
there is a relatively small pressure drop through the baghouse system,
the power cost is relatively low. Costs for replacement parts (i.e.,
bags) are proportional to the gas flowrate, but at the same time amount
to a small fraction of the direct operating costs.
A similar pattern appears with the costs for Model Plant 2, which
contains both crushing and grinding operations. The costs here are about
the same order of magnitude as are those for Model Plant 1. The main
difference is the additional baghouse required to control the grinder
8-72
-------
and its auxiliaries. Here the installed costs range from $93,000 to
$507,000, while the annualized costs go from $21,000 to $131,000 per
year ($0.28 to $0.03/Mg product, respectively).
The costs described above are for achieving the alternative emission
level. It is also necessary to compare these costs to the costs required
to meet a typical state emission regulation (SIP) in the model plants.
In this analysis, however, it is assumed that the SIP can be met without
controls. The SIP or baseline costs are, therefore, zero. Thus, the costs
shown in Tables 8-21 to 8-32 are solely attributable to the alternative
emission limit.
8-2-3 Modified/Reconstructed Faci1ities
As Chapter 5 points out, there appears to be no condition which
would deem an existing plant modified. Concerning reconstruction,
if replacement of components subject to high abrasion and impact,
such as crushing and screening surfaces and conveyor belts,
are exempted and considered routine for this category of sources,
there also appears to be no action which could be construed as recon-
s'truction.
Nonetheless, expansions of existing plants do occur. When they do,
only a portion of the plant would be covered under the alternative
emission limit. These expansions would more than likely involve the
grinding operation, since crushing operations are usually capable of
handling increased throughput without additional equipment. However, to
expand the plant grinding capacity, a new complete grinding line would
be added.
8-73
-------
In this document, sizes for three stationary model plants have been
developed to cover these expansions: 4.5, 9.1, and 32 Mg/hour (5,10,
and 35 tons/hour). The first two sizes apply to all industries employing
grinders (i.e"., Model Plant 2). The third size applies only to the boron
*
industry.
The option costed for controlling these expanded model plants is
fabric filtration. The gas flowrates used in the costing are listed in
Tables 8-33 and 8-34. The other technical parameters appear in Table 8-19.
Because these fabric filters would be installed at existing, as
opposed to new plants, the installed capital costs are somewhat higher,
reflecting the higher installation costs required. The difference
between the existing and new plant ins-tallation costs, or retrofit penalty,
is quite variable, depending on individual plant configuration, on-site
utility capacity, and other seemingly random variables. Nonetheless,
after polling its members, the Industrial Gas Cleaning Institute has
developed an approximate multiplier, or retrofit factor, to be used in
estimating the existing plant installation costs.5 This retrofit factor
is 2.0. Using this factor, the control system existing plant installation
cost would be twice that of the new plant installation cost.
Table 8-33 lists the costs of fabric filter systems installed in
the expanded 4.5 and 9.1 Mg/hour model plants. The 32 Mg/hour capacity
model plant costs are listed in Table 8-34.
The installed costs in Table 8-33 are $43,000 and $48,000 for the
4.5 and 9.1 Mg/hour plants, respectively. The installed cost difference
is relatively small: 10 percent. However, this is because the gas flow-
rates upon which the costs are based differ-by only 23 percent, even
8-74
-------
Table 8-33. FABRIC FILTER COSTS FOR EXPANDED MODEL PLANTS3'5
Parameter
Gas flowrate, m3/min (ACFM)
Installed capital cost, M$c
Direct operating cost, MS/yr
Annual ized capital charges, M$y
Total annualized cost, MS'yr
$/Mg product6
4.5 Mg/Hour
92.0 (3,250)
43
3.4
'yr 6.8
10.2
0.27
.9.1 Mg/Hour
113 (4,000)
48
3.8
7.5
11.3
0.15
References 1, 2, 3, and 5.
Expanded plants consist of grinding operations only.
cThe letter "M" denotes thousands; "MM" denotes millions, etc.
Since SIP control cost is zero, total and incremental annualized costs are equal
Quotients are based on an 8,400 hours/year operating factor.
8-75
-------
Parameter
Table 8-34. FABRIC FILTER COSTS FOR 32 Ma/Hour
EXPANDED MODEL PLANT3'D
Value
Gas flowrate, m3/min (ACFM)
Installed capital cost, MSC
Direct operating cost, M$/yr.
Annualized capital charges, M$/yr.
Total annualized cost
. M$/year
$/Mg product6
184 (6,500)
65
5.0
10.2
15.2
0.057
References 1, 2, 3, and 5.
bThis capacity applies to the boron industry only
GThe letter "M" denotes thousands; "MM" denotes millions, etc.
dSince SIP control cost is zero, total and incremental annualized costs are equal
Quotients are based on an 8,400 hours/year operating factor.
8-76
-------
though one plant size is twice the other. The total annualized costs
differ much less: $10,200/year for the 4.5 Mg/hour size, and $11,300/year
for the 9.1 Mg/hour case. (Because these baghouses control grinders,
neither of these costs includes a cost for dust disposal.)
Since grinding operations need not be controlled to achieve a state
regulation, the SIP costs are zero. The annualized costs shown in Table
8-33 are, therefore, both total and incremental. These incremental costs
are $0.27 and $0.15/Mg product, in turn, for the 4.5 and 9.1 Mg/hour
capacity plants. Both numbers have been based on an 8400 hours/year
operating factor. The 44 percent decrease in cost indicates a positive
economy of scale with plant capacity.
Finally, the fabric filter costs for the 32 Mg/hour expanded model
plant are listed in Table 8-34. Sized for a gas flow rate of 184 m3/min,
the installed cost is $65,000. The corresponding incremental annualized
cost is $15,200 per year, or $0.06/Mg product, based on the same 8400
hours/year operating factor.
8.2.4 Cost-Effectiveness of the Alternative Emission Limit
For each of the control options costed to achieve the alternative
emission limit,, it is informative to compare the total annualized cost
with the amount of particulate removed. A convenient yardstick for
.expressing this comparison is the cost-effectiveness ratio, which is
the quotient of the annualized cost and the quantity of particulate
removed annually. Expressed in dollars per megagram of particulate,
these ratios appear in Tables 8-21 through 8-32, for the stationary new
8-77
-------
model plant sizes costed herein. (Because an NSPS impacts most heavily
on new, rather than existing plants, the cost-effectiveness analysis will
be limited to' them.)
It is clear from these tables that the ratios vary according to the
plant capacity, design, and the model plant configuration (i.e., Model,
Plant 1 or 2). For Model Plant 1 (crushing only), the cost-effectiveness
ranges from $32.1 to $27.8/Mg, as the capacity goes from 9.1 to 540 Mg/
hour. The corresponding ratios for Model Plant 2 (crushing and grinding)
are $18.2 and $11.6/Mg particulate removed.
The ratios are plotted in Figure 8-1 against the model plant
capacity. Note, first of all, that with Model Plant 2, the cost-
effectiveness decreases from $18.2 to $14.1/Mg (23 percent) between
the 9.1 and 135 Mg/hour plant capacities. At larger sizes, however,
this rate of decrease is much less pronounced. In fact, the cost-
effectiveness ratio decreases only 18 percent between 135 and 540 Mg/hour.
Nonetheless, the fact that the ratio decreases consistently with plant
size indicates that the control costs for Model Plant 2 benefit from a
positive economy of scale.
The curve for Model Plant 1 does not exhibit this consistency,
however. Note that the cost-effectiveness decreases gradually from a
maximum of $32.1/Mg to a minimum of $26.5/Mg. This minimum occurs at a
plant capacity of about 340 Mg/hour. But for larger plant sizes, the
curve swings upward, reaching a value of $27.8/Mg at the 540 Mg/hour
capacity. This behavior indicates a negative economy of scale with
respect to plant size.
8-78
-------
s
1.
3
o
10
o
10
Q.
8
Csl
I/I
OJ
OO
o
<*-
UJ
I
o
o
I
CO
cr>
fO
(P9AOUBJ
-------
The following explanation can be offered for this anomaly. First
of all, the fabric filter costs represented by Figure 8-1 are functions
of the gas volumetric flowrate, not the plant capacity. Secondly, the
cost-effectiveness ratio is also a function of the volumetric flowrate,
as well as the annual operating hours. Now, when a model plant consists
of more than one fabric filter system, the mean cost-effectiveness ratio
for the model plant is strongly affected by the volumetric flowrates
of the individual fabric filter systems. (The equation in Section 8.2.2
bears this out.) For instance, if one fabric filter flowrate is much
smaller or larger than the others, the mean cost-effectiveness will be
weighted toward that flowrate.
Such a situation is illustrated by the data in Tables 8-25 and 8-26,
for the 270 and 540 Mg/hour model plants, respectively. In Table 8-25,
data for two fabric filters are presented, one of which is sized for five
times the flowrate as the other. Accordingly, the mean cost-effectiveness
($26.7/Mg) is heavily weighted toward the larger fabric filter. But with
the 540 Mg/hour model plant (Table 8-26), there are three fabric filters,
sized at 255, 877, and 906 m3/min. Since two of these fabric filters are
approximately equal in size, the mean cost-effectiveness for the model plant
($27.8/Mg) is weighted toward them. Note, moreover, that this ratio is
higher than that for the 270 Mg/hour plant. This, in turn, accounts for
the dip in the curve in Figure 8-1.
8.2.5 Control Cost Comparison
Before the accuracy and representativeness of model plant control
costs can be ascertained, they must be compared with costs obtained from
8-80
-------
.0
CO
o
CO
>
O
IB V
+»•»•»
OTf—
Cf-
f«U.
CXI
oo
=3
O)
e
CO
u.
u
•f—
S-
4->
-------
other data sources. In doing this, one can either compare the installed
capital costs, the annual 1 zed costs, or both. However, since the capital
costs influence the annualized costs (via the annualized capital charges),
and because there is much more variability among the several terms in the
annualized cost (utilities, for instance), it is preferable to limit the
comparison to the installed costs.
Even for a control system sized for a specific emission point, the
installed cost may vary considerably from site-to-site. Such things as
the cost of installation labor (electricians, pipefitters, etc.), the
requirement for special installation materials (e.g., extra insulation for
systems installed in colder climates), and the presence or absence of
excess utility capacity considerably influence the total installed cost.
Keeping this in mind, however, capital cost comparisons can be made,
among a range of control system sizes. This .comparison may be made
graphically; that is, installed "costs adjusted to the same reference date
(December 1976, in this case) can be plotted against some technical parameter
•*»
relevant to the control system. In this section, installed costs are
compared among various sizes of fabric filter systems, using gas volumetric
flowrate as the comparison parameter.
The model plant costs are compared with cost data obtained from
industry sources6'7 and with costs developed in-house from a compendium
of air pollution control costs (the GARD Manual).3 These costs have been
plotted against volumetric flowrate on full logarithmic paper (Figure 8-2).
For all flowrates in the domain of 42 to 1,400 actual m3/min, the costs.
developed from the GARD Manual are higher than the model plant costs. The
discrepancy ranges from 17 to 32 percent, the higher difference corresponding
3-82
-------
to 42 mVmin. The cost curve for reference 6 intersects the model plant
curve at 115 m3/min. (This is approximately the size of the grinding
operation baghouse in the 9.1 Mg/hour model plant.) Below this flowrate
the reference 6 costs are lower; above it, they are higher, but by no more
than 53 percent. The last fabric filter cost curve (reference 7) lies
consistently below the model plant curve for all flowrates between 28 and
1,050 mVmin. However, the differences between the costs-7 to 18 percent-are
not significant.
All in all, the model plant fabric filter costs compare reasonably well
with the data supplied by references 3, 6, and 7.
8-83
-------
8.3 OTHER COST CONSIDERATIONS
As discussed in Section 8.2, it is unlikely that non-metallic minerals
plants covered under the anticipated NSPS would be required to monitor the
opacity of their particulate emissions. Nonetheless, for the benefit of
those plants considering an opacity monitoring program, costs are presented
for these devices in this section.
Continuous monitoring of opacity usually involves the use of a trans-
mi ssometer installed in a fabric filter stack. This instrument relates
the transmittance of a light beam across the stack to the opacity of
the exhaust . These devices are fully automatic and usually require only
periodic maintenance. (However, manual stack testing may be required for
calibration of the instrument.)
Table 8-35 lists costs for a typical opacity monitoring system
obtained from an instrument vendor.8 The system shown consists of a
visible emission monitor, controls, data readout-converter, strip chart
recorder, and other auxiliaries. Of the $20,000 installed cost, half
is the equipment purchase cost, the other $10,000 is for installation.
It has been assumed that no scaffolding would have to be erected on the
stack being monitored. However, if scaffolding is required, the installation
cost could increase appreciably. The scaffolding cost would, as expected,
vary from site to site. For instance, the cost of scaffolding a 50-foot
"stub" stack (the kind normally used with nonmetallic minerals plant
fabric filters) would be $20,000 to $30,000.
8-84
-------
Table 8-35. MONITORING COSTS FOR NON-METALLIC MINERALS MODEL PLANTS3 'b
Parameter
Operating factor, hours/year
Installed capital cost, M$
Direct operating cost, M$/year
Annuali zed capital charges, M$/year
Total annual i zed cost, $/year
Value
2000
20
0.7
4.1
4.8
8400
20
1.0
4.1
5.1
aReference8.
These costs are for opacity monitoring of one stack. No scaffolding
costs are included.
cThe letter "M" denotes thousands; "m" denotes millions, etc.
8-85
-------
The direct operating costs have been computed at the 2000 and 8400
hours/year operating factors. Here, the only cost sensitive to a change
in the operating factor is the electric power cost. At the lower operating
factor (corresponding to the crushing model plant) the power cost.is $100/year
against $420/year at 8400 hours/year of operation. The rest of the direct
operating cost is for maintenance of the monitoring system, which amounts to
3 percent of the installed cost.
The annualized capital changes have been computed assuming a ten-year
life and a ten percent annual interest rate, plus four percent of the
installed cost for taxes, insurance, and administrative charges. Depending
on the operating factor, the total annualized cost is either $4,800 or
$5,100 per year.
For the smaller model plants, these amounts are appreciable—one-third
of the fabric filter total annualized costs at the 9.1 Mg/hour Model Plant 1.
However, with the larger plants, more than one baghouse would need to be
monitored. Thus, their monitoring costs could be two or more times the
costs in Table 8-35. In other words, there is little or no economy of
scale in the costs for monitoring multiple stacks. This is so because
each stack requires separate opacity instrumentation, scaffolding, and other
equipment. The only savings would result from some parts of the installation
cost, such as engineering. But these latter costs, when taken together,
generally comprise only a small fraction of the installed cost.
8-86
-------
References for Sections 8.2 and 8.3
1. Written communications between William M. Vatavuk (Economic Analysis
Branch, Strategies and Air Standards Division) and James A. Eddinger,
(Industrial Studies Branch, Emission Standards and Engineering Division)
Dates: August 18, 1976; June 15, June 30, July 8, 1977; and February 9,
March 17, and April 20, 1978.
2. Nonmetallie Minerals industries Control Equipment Costs. Prepared by:
Industrial Gas Cleaning Institute (Stamford, Connecticut). Prepared
for: U.S. Environmental Protection Agency, Strategies and Air Standards
Division, Economic Analysis Branch (Research Triangle Park, North
Carolina). Contract No. 68-02-1473, Task No. 19. February 1977.
3.
4.
5.
6.
7.
8.
Kinkley, M.L. and R.B. Neveril. Capital
Selected Air Pollution Control Systems.
(Niles,
and Operating Costs of
Illinois).
Strategies and Air
Triangle Park, North Carolina).
Prepared by: GARD, Inc.
Prepared for: U.S. Environmental Protection Agency
Standards Division, Economic Analysis Branch (Research
Contract No. 68-02-2072. May 1976.
McGlamery, G.G.,
Desulfurization
et al. Detailed Cost Estimates for Advanced Effluent
Processes. Prepared by: Tennessee Valley Authority,
Muscle Shoals, Alabama, under Interagency Agreement EPA IAG-134(D)
Part A. Prepared for: Office of Research and Development, U.S.
Environmental Protection Agency, Washington, D.C. January 1975.
Written communication between William M. Vatavuk (U.S. Environmental
Protection Agency, Strategies and Air Standards Division, Economic
Analysis Branch, Research Triangle Park, North Carolina) and Sidney
Orem (Industrial Gas Cleaning Institute, Stamford, Connecticut).
Date: June 15, 1977.
Written communications between F.J. Rogers (Gypsum Association, Evanston,
Illinois) and William M. Vatavuk (U.S. Environmental Protection Agency,
Strategies and Air Standards Division, Economic Analysis Branch, Research
Triangle Park, North Carolina). Dates: April 29, May 11, and July 27, 1977
Written communication between William M. Vatavuk (U.S. Environmental
Protection Agency, Strategies and Air Standards Division, Economic
Analysis Branch, Research Triangle Park, North Carolina) and Curtis
Hamilton (Englehard Minerals and Chemicals, Attapulgas, Georgia).
Date: January 18, 1978.
Written communication between William M. Vatavuk (U.S. Environmental
Protection Agency, Strategies and Air Standards Division, Research
Triangle Park, North Carolina) and Ronald Zweben (Lear Siegler, Inc.,
Raleigh, North Carolina). Date: April 26, 1978.
8-87
-------
8.4 ECONOMIC IMPACT ASSESSMENT
8.4.1 Introduction
The non-metallic mineral industries crush, size, and in some cases
grind material extracted from the ground. The resultant output is generally
used as an intermediate product in such activities as highway or building
construction.
Although the 18 non-metallic mineral industries considered in this
economic impact assessment have similar production and marketing character-
istics, there are distinct differences among them. Although these minerals
must be extracted from the ground, the particular method used for extrac-
tion depends on the hardness of the mineral and the geological deposit in
which it is found. For example, stone must generally be extracted by blasting
with dynamite, while sand can be extracted with only power shovels. The
harder minerals are first broken with drop balls and transported by truck
to the crushing plant immediately following extraction.
As described in Section 3.2, most minerals then go through a number
of crushing steps in order to produce the requisite size material for the
purposes of the customer. This stage includes primary and secondary crushing
and, in some cases, tertiary crushing. In each crushing stage the material
is further reduced to a smaller size classification. These crushing stages
are important in producing material meeting the quality specifications of
the application. For some minerals; e.g., clay, dryers are interposed between
the various crushing stages to extract the moisture found in the material.
Other minerals such as stone and pumice do not require dryers, while still
other materials, such as sand, can be extracted and processed in a wet form.
8-88
-------
For many minerals the final crushing stage produces an output which
can be sold for various purposes; e.g., stone, and sand and gravel used
as a highway or concrete aggregate. Other materials must be further
reduced in size in a grinding mill before they are acceptable in product
applications; e.g., clay which is to be expanded and gypsum used as a
retarder in cement production.
In short, non-metallic minerals are basically processed in the same
manner, but there are production distinctions which the following economic
impact analysis will address.
As Section 8.1 shows, non-metallic minerals have wide price differ-
entials. Even within a particular mineral, there are signifcant variations
in price depending on product application. The prices of non-metallic miner-
als range from $2/ton for sand gravel to $250/ton for high grade talc.
Most non-metallic minerals have regional markets. In general, the lower
the value of the mineral, the shorter is the distance that the material
travels to a customer. For example, stone, and sand and gravel, lower price
minerals, generally are not transported over 30 miles from the plant.
At this distance the f.o.b. plant price of the material is approximately
doubled by transportation costs. Therefore, transportation costs limit
the geographic area of competition for many non-metallic minerals and
competition between and among minerals is localized.
Ownership characteristics differ between the non-metallic minerals
industries. Stone quarrying and crushing is done primarily by privately
held companies which may have other business ventures requiring stone;
e.g., highway construction or concrete,manufacturing. Gypsum, on the other
hand, is generally produced by diversified, publicly held companies in the
8-89
-------
building and construction materials industry who have integrated backwards to
the mine. Publicly held companies, diversified into many other activities,
though, are in general the largest producers in the industries.
In the analysis which follows, each new non-metallic mineral plant
will be assessed as if it stands alone; i.e., the plant is not associated'
with any other business activity nor is it associated with any larger
parent company. This assumption has the effect of insulating the control
cost impact to the plant in question which must then support the control
cost without any assistance from other business activities or firms.
The impact which will be assessed is the effect of the incremental
cost of NSPS control on both:
• "Grassroots" new plants
• Expansions of existing plants.
The effect to be determined is the feasibility of these two investments,
and therefore, the potential for new and expanded plant construction.with
the superimposed NSPS costs on each investment.
Incremental NSPS control costs are costs over and above those
control costs required to meet state implementation plan (SIP) standards.
Since each state has particulate emission control standards, any new plant
or reconstructed/modified plant would have to meet SIP standards in the
absence of the NSPS. Incremental costs are the difference between the costs
associated with NSPS control and SIP control. In this analysis SIP costs
are assumed to be non-existent, and therefore incremental costs are the
total of NSPS costs. Though SIP costs are not zero in the real world, this
assumption is used in order to provide a conservative analysis for evalua-
ting economic impacts.
8-90
-------
This section is organized in three parts. Section 8.4.2 will develop
the methodological procedure utilized to estimate the economic impact. Section
8.4.3 will present the findings of this analysis and Section 8.5 will show
the total industry costs of the promulgation of NSPS.
8.4.2 Methodology
This section will describe the methodology used to measure the eco-
nomic impact on. the non-metallic mineral industries.
The economic impact is evaluated by developing model plants based on
historical characteristics in the non-metallic mineral industries. As will
be seen, these characteristics include production capabilities, asset
size and other financial characteristics. The models do not represent any
particular plant as any individual plant will differ in one or more of
these characteristics. The models are meant to provide an indication of
the degree of impact on all plants in a particular industry by incorporating
in the model the major characteristics prevailing in each segment of the
non-metallic mineral industry.
Two control cost models have been constructed for the 18 non-metallic
mineral industries, as seen in Section 6.
• Model 1 - those industries which generally only crush the
mineral
• Model 2 - those industries which generally both crush and
grind the mineral
In addition, the portable crushing plant model segments of the crushed stone,
and sand and gravel industries are discussed in Supplement A.
Each industry has been further disaggregated by typical model plant
sizes to account.for size variations within each industry. Typical plant
8-91
-------
sizes for each mineral are shown in Section 6. Although industry repre-
sentatives and equipment suppliers do not expect 9 Mg/hr (10 tons/hr), 23
Mg/hr (25 tons/hr) and 68 Mg/hr (75 tons/hr) plants in the crushed stone,
and sand and gravel industries to be constructed in the future, they were,
nevertheless, analyzed because they have historically represented the^
majority of plants in the industries.
Only minerals represented by model 2 are assumed to be in need of
expansion investment in the near future. Expansion will consist of
4.5 Mg/hr (approximately 5 tph) and 9.1 Mg/hr (10 tph) grinding mills.
Expansion of existing plants represented by model 1 is not considered
because it is expected that they will need to invest in capital expansion
to meet increased demand only on a sporadic basis. Reconstruction/modifica-
tion of existing plants is also not considered; first, because routine
replacement of worn out equipment will not subject them to the NSPS; and
second,because such replacement is expected to occur at a very slow pace
since the production life of most processing equipment is on the order of
20 to 30 years.
The first step in the analysis consisted of screening each of the
18 minerals by ranking the potential product price effects of the incremen-
tal control cost. Those minerals with the potentially highest product
price impact were then considered for further evaluation.
The next step in the analysis established the scenario under which
the plant would operate. This scenario consisted of four elements:
• the total of NSPS control costs were incremental
costs; i.e., that there are no SIP control costs
that a plant would have to incur in the absence of
NSPS control.
8-92
-------
• the production volume, is constant throughout the
life of the project except for the crushed stone
plant where it is assumed that they operate at
50% of capacity for the first year.
• NSPS control cost pass through is limited by competition of
existing plants in the same industry which do not have to meet
the NSPS.
• the new plant operates as a separate business entity and cannot
expect to finance the control from another business activity or
parent firm.
Because of technical constraints in establishing a new quarrying
operation in the crushed stone industry, which constraints are not as
severe in.the other industries, the crushed stone crushing plant is assumed
to operate at 50% of capacity during the first year.
The plant is assumed not to be dependent on any other business
venture. Therefore for new plants the NSPS control cost is not allocated
or spread over any operation except production of the affected facility
which is the new plant. Financing of the equipment can(only be made from
the expected revenues of the new plant and from no other business venture.
For expanded plants a portion of the annualized control cost was assumed to
be absorbed by the existing plant which is being expanded.
Substitutability between many of the non-metallic minerals in many
product applications prevails in the market. Because of the variations in
control cost per ton between the minerals, the potential price increase of
any mineral should be expected to equal the cost pass through portion of
the nearest available mineral substitute with the lowest control cost per
8-93
-------
ton. If a new plant of one mineral was being constructed in the same
geographical competitive area as a new plant of another mineral and both
were perfect substitutes for each other, then the cost pass through would
likely be the control cost of the less affected mineral. A more conserva-
tive analysis is where a new plant of a mineral is constructed in the
same geographically competitive area as existing plants of the same mineral.
The existing plants would not experience any NSPS standard and therefore,
cost, and the new plant would have to compete with this existing plant.
The new plant would not be a major supplier of the mineral in the area and
would not be able to control the price. Therefore, this new plant would
have to completely absorb the control cost. But as demand grew for the
mineral, additional new plants would be required and/or, in the case of gypsum
and clay, older plants would have to expand to meet the increased demand.
This condition would bring an increasingly larger segment of the mineral
supply market under NSPS control. Therefore, it is likely that new plants
will be able to pass through the control cost gradually over the years. This
is reflected in our assumption that 25 percent of the control cost is passed
through every 4 years (alternatively every 4 years 25 percent less of
the cost is absorbed). This is the premise which is used in the succeeding
discounted cash flow (DCF) analysis.
Each plant size of each of the potentially significantly affected
minerals was then analyzed by using a discounted cash flow analysis (DCF).
DCF is an investment decision technique which provides information on
tne economic feasibility of a potential capital investment. It measures
the discounted cash inflows over the life of the investment and compares
to the discounted cash outflows. If the sum of the discounted cash
8-94
-------
inflows is equal to or greater than the sum of the discounted cash outflows,
the investment is feasible from the firm's point of view. If the sum of
the discounted cash inflows is less than the sum of the discounted cash
outflows, the investment is not feasible from the firm's point of view.
In order to take into consideration the time value of money, all cash
flows must be discounted to the present by use of an appropriate discount
factor. This is necessary to bring all cash flows to a comparable present
day basis for comparison.
Four data elements are required to complete the analysis:
• Expected life of the investment
• Cash flows to be discounted
• Weighted average cost of capital
/
9 Total plant investment.
The expected life of the investment was taken to be 20 years although
the expected life of the major pieces of equipment can range from 20 to 30
years. The cash flows are discounted and summed over a 20 year period.
Any potential capital investment will generate cash flows in the
form of new earnings, and depreciation. These flows are discounted by the
weighted average cost of capital discount factors, summed, and compared to
capital outlays to determine the economic feasibility of the potential in-
vestment. In the analysis to be presented in the following section the
incremental NSPS control costs are superimposed on this model to determine
their effect on cash flow and the decision to invest in a new "grassroots"
or expanded plant for each size plant in each of the affected non-metallic
mineral industries identified for further analysis.
8-95
-------
The cash flows which are considered are:
1. Net earnings before interest and after tax.
2. Depreciation of the plant including control equipment.
3. Depletion.
4. Working capital recovery.
5. Plant and control equipment investment.
For each year cash inflows 1 through 4 are added (working capital
recovery occurs only at the end of the life of the investment, the 20th
year). This resultant annual sum is discounted and the annual discounted
sums are totalled over the 20 year period. This new sum is compared to
the discounted sum of the total investment including NSPS control invest-
ment. If the sum of the discounted cash inflows 1 through 4 is larger than
the discounted sum of cash outflow 5, the investment is economically
feasible even after the requirement of NSPS controls.
That an investment is found to be economically feasible does not
necessarily mean that the investment will be made by any individual firm.
Other forces or market concerns important to the company such as the desire
to diversify into other industries, or desire to expand through acquisitions
may preclude the new plant investment from being made.
The discount factors which are used to discount these flows are
determined by solving I/O + i)n where i is the weighted average cost of
capital and n is the year from the beginning of the project. In this case
n is from 1 to 20. For each year of the 20 year investment span a different
discount factor is generated. Each year's discounted cash flow shows the
present value of that cash flow. The cost of capital is the weighted
8-96
-------
average financing expense of an investment that is financed partly through
debt and partly through equity.
Total plant investment was determined by the equipment needed for
quarrying, crushing, and, if appropriate, drying and grinding the mineral,
and added to the required NSPS control equipment capital cost developed in
Section 8.2 and working capital requirements.
8.4.2.1 Critical Elements
The following list provides the major critical elements of the
analysis for the significantly impacted industries:
• Control cost absorption is 25 percent less every 4 years.
• Maintenance expenditures over the life of the equipment
equal salvage value of the equipment.
• The profit rate for new plants is the same as existing
plants.
• All stationary plant equipment has a 20 year life with "
the exception of rolling stock which has a 7 year life.
• 8,400 hours of operation per year is assumed for plants
with grinding capacity.
• Cost of debt capital is 3 percent above the prime rate of
7 percent in 1976.
• The total investment is financed 30 percent by debt and
70 percent by equity capital.
• Weighted average cost of capital is 11.8 percent.
• The debt financing maturity is 10 years for stationary
plants and control investment and 7 years for rolling
stock.
• Rolling stock is 77.7 percent of quarry investment.
8-97
-------
Maintenance expenditures are a cash outflow over the life of the
equipment while the salvage value of the equipment is a cash inflow at
the time of sale. No estimates of maintenance expenditures were found
during this analysis. Salvage value of equipment generally runs from 25
to 30 percent of the original cost. Since maintenance expenditures ate
a negative cash flow and salvage value a positive cash flow and since
salvage value at the time of sale should be related to the amount of
maintenance put into the equipment it is assumed that they are equal
and counterbalance each other.
The profit rate on the new plant is assumed to be equal to an
existing plant although profit rates between a new and existing plant
will differ due to unique tax consequences and differences in technolo-
gical efficiencies. It is felt that these two effects counterbalance
each other sufficiently for the purpose of this analysis.
The plant has a useful life of 20 years. Equipment life varies among
the pieces of equipment used in the non-metallic mineral industry, but, on
average, the plant has a 20 year life. In the analysis some account has
been given to this aspect by separating "rolling stock" (mineral transport
vehicles) from stationary stock equipment and^ ascribing a 7 year life to
the rolling stock.
In those industries with grinding capacity, 8,400 hours of operation
is used to generate sales volume and revenue based on information supplied
by industry.
Industry representatives have stated that generally an investment
can be financed at 2 to 3% above the prime rate. A 3% above prime rate
was utilized to reflect a conservative analysis.
8-98
-------
A weighted average cost of capital for the mining industry as a whole
of 11.8% and debt/equity financing of 30/70% is given by Dr. Gerald
Pogue (Section 8.4.2.2). To the extent that particular non-metallic mineral
industries within the mining category experience a cost of capital of more
or less than 11.8%, the discounted cash flows will be different.
8.4.2.2 Data Sources
The following list provides the data sources for various aspects
of the analysis:
• Average Selling Price - Bureau of Mines
• Profit Rates - Robert Morris Associates
- Industry Representatives
- Annual Reports
- Robert Morris Associates
- Barber-Green Co.
- Kennedy Von Saun Co.
- C. E. Raymond - Combustion Engineering
Inc.
Cost of Debt Capital - Federal Reserve Bank
- Industry Representatives
Cost of Capital, - "Estimation of the Cost of Capital for
Debt to Equity Ratio Major U.S. Industries with Application
to Pollution Control Investments", Dr.
Gerald A. Pogue, 1975.
NSPS Control Costs, - Chapter 8.2
Sizes and Operating
Hours
*
•
Working Capital
Plant Investment
8-99
-------
• Depreciation Schedules - Equipment Suppliers
• Investment Tax Credit, - Internal Revenue Code
Depletion Allowance
• Expected Life of - "Background Information
Equipment for the Non-Metallic Minerals
Industry," Vol. I, PEDCO Environ-
mental Specialists.
8.4.3 Screening Analysis
The first step in the analysis was to assess the effect on the 18
non-metallic mineral industries of NSPS control costs based on the ratio of
control cost per ton to price per ton. This ratio represents annualized cost
per ton as percent of average price. Table 8-36 presents the results of
this analysis.
Table 8-36 shows 23 entries because clay has been disaggregated into
6 distinct categories. For both those industries that fall under the Model
1 classification (crushing only) and Model 2 classification (crushing and
grinding) the impact is shown by dividing the annualized operating and
capital costs for control of the smallest size plant specified in Table
6.3 by the annual revenue of the mineral.
Because control costs per ton of mineral output are larger for the
smallest plant compared to the largest plant, this procedure inflates the
impact. Since large plants dominate the production in most industries,
average industry impact based on this ratio would be substantially lower.
Average industry impact is shown in section 8.5. Table 8-36 is not meant to
show industry impact but to be used as "worst case" screening method to
ascertain industries requiring further study.
8-100 '
-------
Table 8-36
RANK ORDER OF INDUSTRIES
Industry
Pumice
Sand and Gravel
Crushed Stone
Common Clay
Gypsum
Per lite
Fire Clay
Bentonite
Ball Clay -
Salt
Barite
Feldspar
Fuller's Earth
Mica
Kaolin
Talc
Kyanite
Vermiculite
Fluorspar
Di atomi te
Sodium Compounds
Boron
Gilsonite
WITH HIGHEST CONTROL COST IMPACT
Rank
1
2
3
4
5
6
7
9
10
11
12
13
14
14
14
17
18
18
18
18
22
23
25
Control Cost/Ton
Price/Ton u)
28.0%
15.8
13.4 Candidates
11.7 for further
5.0 evaluation.
4.1
2.0
1.4
1.3
1.2
1.1
1.1
.6
.6
.6
.4
.3
.3
•3
.3
.2
.1
-(2)
(1) Based on smallest model size in industry.
(2) No price available - only 1 company producing approximately
100,000 tpy.
8-101
-------
Any industry where the per ton control cost was larger than 2% of the average
price was considered to be potentially significantly impacted and worthy of
further evaluation. Two percent was taken to be the cut-off point because
this rate, even in the worst case situations, is considerably lower than
the 5% industry average rate which is the EPA guideline for assessing major
economic impact. The minerals considered to be potentially significantly
impacted are pumice, sand and gravel, crushed stone, common clay, gypsum,
and perlite.
Perlite, gypsum and pumice have three stationary model plant sizes:
9, 23 and 68 Mg/hr (10, 25 and 75 tph). Common clay has four; 9, 23, 68
and 136 Mg/hr (10, 25, 75 and 150 tph). Both sand and gravel, and crushed
stone have six stationary model plant sizes, 9, 23, 68, 136, 272 and 544
Mg/hr (10, 25, 75, 150, 300 and 600 tph). The portable plant segments of the
crushed stone, and sand and gravel industries are discussed in Supplement A.
Each of the six remaining potentially significantly affected miner-
als were then compared on the basis of relative prices, and the effect of
control costs on relative prices of the minerals, taking into account the
product substitutability among them. This analysis showed that the "worst
case" situation was a new plant of any mineral competing with an existing
plant of the same mineral. For each mineral, a baseline relative price was
computed. This relative price was the ratio of the price of each mineral
to the price of each of the other minerals prior to NSPS control costs.
This baseline relative price ratio was then compared to the "worst case"
situation after the imposition of control costs, assuming all control costs
were passed through. The "worst case" situation was the smallest size
plant of any mineral compared to the largest size plant of the remaining
8-102
-------
minerals since control costs per ton of output are larger for smaller
plants. A decline in this ratio, price of other minerals after control
divided by the price of this mineral after control, indicates that other
minerals are becoming less expensive relative to this mineral and that
demand should significantly shift away from this mineral if the cross-
elasticity of demand is high.1 Cross-elasticity of demand is dependent on
the minerals having acceptable substitutability potential. The substitutability
potential was evaluated by comparing the mineral of interest to the two
minerals having the largest changes in relative prices. In each case sub-
stitutability potential was rated only low to moderate because of the
product quality differences between the minerals and the geographical
separation of deposits of different minerals. For this reason the more
conservative scenario, a new plant of any mineral competing with -an existing
plant of the same mineral, was employed in the analysis.
8.4.4 Plant Investment
Grassroots Plants
Investment costs were gathered for quarrying, crushing, and where
appropriate, drying and grinding equipment from equipment suppliers.
Tables 8-37 and 8-38 show the total investment costs for each size plant
studied in each industry. For all plant sizes smaller than 136 Mg/hr (150
tph), quarrying and crushing plant costs were derived by use of the engineer-
ing 0.6 power capacity rule. For the quarrying operation, rolling stock was
1
Cross-elasticity of demand is the percentage change in the quantity of
one product divided by the percentage change in price of another
product.
8-103
-------
1
Table 8-37
PLANT INVESTMENT COSTS
(in thousands of dollars)
Size
Mg/hr (tph)
Industry
Pumice
9
(10)
$269.9 $
23
(25)
410.4 $
68
(75)
740.3
136
(150)
N.A.
272
(300)
N.A.
544
(600)
N.A.
Sand
Gravel 236.9 374.4 693.2 $1,034.6 $2,036.1 $3,986.7
Crushed Stone 251.1 399.6 742.9 1,139.0 2,188.6 4,291.4
Common Clay 817.4 1,282.3 2,160.4 3,118.1 N.A.
Gypsum
Perlite
664.9 1,058.3 1,850.2 N.A.
555.3 822.2 1,654.1 N.A.
N.A.
N.A.
N.A.
N.A.
N.A.
Includes NSPS control capital costs and working capital.
N>A'Not Applicable because plants of this size are not likely to be
constructed in the absence of a NSPS.
8-104
-------
Industry
, Table 8-38
EXPANSION INVESTMENT CQSTSl
(in thousands of dollars)
Size
Mg/hr (tph)
4.5
(5)
9
(10)
Common Clay
Gypsum
$288.1
292.9
$421.1
430.7
Includes NSPS control costs and working capital,
8-105
-------
separated from stationary stock by factoring total quarry investment cost
by 0.777.1 All plant investment costs were deflated to fourth quarter,
1976 prices in order to make investment consistent with the derivation of
sales revenue which is based on fourth quarter, 1976 average selling
tt
prices. The investment deflator was calculated from the Chemical Engineer-
ing equipment cost index.
Once total plant investment was calculated and separated into sta-
tionary plant equipment and rolling stock, NSPS control cost investment
and working capital were added to stationary stock investment. The debt
portion of the stationary stock investment was derived by using a 0.3 factor
specified by the Dr. Gerald Pogue study; i.e., 30% of investment financed
by the bank and 70% from the investor's own funds, equity. Bank financing
for stationary stock debt was taken by 10%, 10 years, giving a capital
recovery factor (CRF) of 0.16275. These industries are usually able to
receive financing at 2 to 3% above the prime rate. In T976 the prime
rate was approximately 7%. The debt portion of rolling stock investment
was also established by using a 0.3 factor. The rolling stock was assumed
to be financed at 10% over the useful life of the stock, 7 years. The CRF
is 0.20541. Subsequent purchase of new rolling stock to replace original
rolling stock was assumed to occur at the same price. For both stationary
and rolling stock, the annual principal and interest payment were calculated,
1
Derived from "The Crushed Stone Industry: Industry Characterization
and Alternative Emission Control Systems", Arthur D. Little, Inc.
where rolling stock equals 77.7% of total quarry plant costs.
8-106
-------
Expansion Plants
Investment costs for expansions consisted of 4.5 Mg/hr (5 tph) and 9 Kg/hr
(10 tph) grinding mill costs for the clay and gypsum industries only. These
investment costs are shown in Table 8-38. Debt financing was 30% of total
investment at 10% over 10 years.
8.4.5 Discounted Cash Flow Analysis
Table 8-39 which shows an analysis for construction of a new 136 Mg/hr
(150 tph) crushed stone plant is an example of the data sheets which were
developed for each of the plant sizes for each of the six potentially
significantly impacted industries. The steps in the DCF analysis will be
described below using this example and referring to row entries in Table 8-39.
• Row 1, revenue, was generated by multiplying hours of operation
by tons per hour of output and by the average P.O.B. plant sell-
ing price of the output. This revenue estimate was assumed con-
stant for each year of the life of the investment. For stationary
crushed stone plants, the plant was taken to operate at 50?- of
capacity the first year as related by industry representatives.
Control equipment was assumed to be operating; at 100 percent,
and therefore control operating costs are 100 percent.
• Row 3, interest including control, was determined by calcula-
ting the principal and interest repayment schedule for the
plant investment without control investment.
• Row 4, earnings before interest and tax, was derived by multi-
plying revenue by the before tax. profit rate of row 2 and
adding back the interest of row 3.
8-107
-------
oo
a:
OO O
>- D:
—I J—
•=C
2: 2:
«=c >-•
_
a. a.
OO C3
oou
at ow not
^ * . • •
Itelb 52*° 1 ^° „"•£ "
o > o
S 3 S SS 2
5 ~*S 3ZZ" 5 "•"• s 5 S -2
•!"6 ltC3" 3 ""• 3 5 S -2
• •«>. -*m r>. n «•
.J>
_;.
s
• •
8-108
-------
Row 5 shows the NSPS annualized control costs for each year.
Since depreciation for control equipment was taken to be
straight line over 10 years, the years from 1987 onward show
only annual operating costs.
Row 6, control cost absorbed, reflects the scenario mentioned
in Section 8.4.2, methodology. For the first 4-years all
control cost is assumed to be absorbed because the plant is
competing with existing established plants which have no NSPS
costs. Therefore, the new plant must absorb the entire cost.
In the years 1981 to 1985 the plants must absorb 75% of the
cost and can pass through 25% because other new plants are
being established. New plants must, then, meet NSPS costs.
For each succeeding 4 year period, the plant absorbs 25%
less of the original cost. Since in the year 1987 total
operating costs are less than control cost absorbed in 1986, all
operating costs are assumed to be passed through in the years
from 1987 to 1996. ...
Row 7, control interest, was derived by calculating the prin-
cipal and interest repayment schedule for the NSPS control,
investment.
1
The increased revenue from cost pass through is not shown since we
are only interested in the effect of cost absorption on net earnings,
8-109'
-------
Row 8, net earnings before interest and after control, shows
•^
the effect of NSPS absorbed control costs on the earnings
potential of the plant. Absorbed control costs are subtracted
from Row 4 and control interest of Row 7 is added back. Adding
s
back of interest is required in the model because the discount
factors taken into consideration the repayment of the loan.
Row 9, federal tax liability, is derived by multiplying net
earnings after control by the appropriate marginal tax rates.
Row 10, investment tax credit, considers the effect of the 10%
investment tax credit on the tax liability of the plant.
(The investment tax credit can be carried forward 7 years or
until 10% of the investment is credited, whichever comes first.
The tax credit cannot be greater than tax liability and for tax
liabilities over $25,000 the credit is calculated as $25,000
plus 50% of the liability over $25,000. For example, in year
1977 tax liability is $800, therefore, the credit is $800 since
the credit cannot be greater than tax liability. In year 1978
the same reasoning applies. If tax liability had been $30,000,
then the credit would have been $25,000 + (0.5) $5,000 or $27,500.
Row 11, federal tax liability after credit, is tax liability
minus the investment tax credit.
Row 12, minimum tax, shows the 15% minimum tax on tax prefer-
ence items. In this analysis the only tax preference item is
the depletion allowance.
Row 13, state tax, is assumed to be 5% of net earnings. The
5% rate is the most common rate of the majority of states.
Row 14, net earnings before interest after credit, control and
tax, shows the effect of NSPS control costs and the investment
tax credit on after tax earnings. It is derived by subtracting
8-110
-------
federal tax liability after credit, the minimum tax and state
tax, from Row 8. As can be seen, this figure varies over the
years as control cost absorbed is lowered and as the original
tax credit is exhausted and credit for new rolling stock is
taken and exhausted and as interest payments are reduced. Net
earnings before interest after credit, control and tax is the
first category of our cash flow. All succeeding categories
also affect cash flow.
Row 15 is added to Row 14 and represents depreciation of
stationary stock, depreciated straight line over 10 years.
Row 16, depreciation of rolling stock, is added to the above.
This depreciation, which is taken over 7 years, comes into
play in later years as new rolling stock is purchased in
years 1984 and 1991.
Row 17, depreciation of control equipment, is taken over 10
years and added to the other depreciable equipment.
Row 18, depletion, is added to the cash flow since all of
these industries are in the mining classification and deple-
tion allowance increases cash flow.
(Depletion can be taken in one of two ways: cost depletion or
percentage depletion. Cost depletion is dependent on the cost
basis of the land, amount of mineral mined and estimated amount
of mineral reserves. Percentage depletion is based on a
specified percentage of sales revenue, the percentage differs
by industry, to a maximum of 50% of taxable income before
depletion is counted. Cost depletion cannot be calculated here
because it is site specific; i.e., dependent on the cost of the
'property and reserves on the property. In any case, most
companies generally use percentage depletion. In the example
depletion is shown as $2,000 in 1977. The percentage depletion
allowance for stone is 5%. For 1977 this amounts to $17,600,
but the plant can only use $2,000 because of the 50% taxable
income limit.) .
8-113
-------
• Row 19, working capital recovery, shows that at the end of the
project working capital is recovered. Working capital is taken
to be 4% of revenue.
• Row 20, cash inflow, shows for each year the expected total of
the above cash flow categories, and is the amount which must be
discounted to the present by the discount factors shown in row
21. Row 22 is the result; i.e., Row 20 multiplied by Row 21.
• Row 23, cash outflow, shows the investment expenditures necessary
to establish the operation. Investment of $1.1 million is made
initially and subsequent rolling stock investment is made in
years 1984 and 1991. These cash outflows are discounted by the
appropriate discount factors of Row 21. Row 24 is the result.
The weighted average cost of capital of 11.8% generates the discount
factor for each year of the 20 year period. These factors show the present
value of a dollar of future cash flow for each future year. After the
annual cash flows are discounted, they are summed to derive the present
value of the cash inflows over the life of the project. This cash inflow
is then compared to the cash outflow, which is the present value of the
total investment. In this example the present value of net cash inflows
is greater than the present value of cash outflows, so that an investment
in a 136 Mg/hr (150 tph) crushed stone plant with NSPS controls attached is
profitable at a weighted average cost of capital of 11.8%.
8.4.6 Findings
Table 8-40 presents the results of this analysis for each size plant
of the potentially significantly affected industries. For the 9 and 23
Mg/hr (10 and 25 tph) sand and gravel, and crushed stone plants the DCF
8-112
-------
Table 8-40
SUMMARY OF DCF RESULTS
Grassroots Plants
Investment Decision
Industry
Pumice
Size - Mg/hr (tons per hour)
9 23 68~136 272" 5PT
(10) (25) (75) (150) (300) (600)
NF
N.A. N.A. N.A.
Sand & Gravel NF1 NF1 A1 F
Crushed Stone NF1 NF1 A1 F
Common Clay NF A F F N.A. N.A.
Gypsum
F N.A N.A. N.A.
Perlite
N.A. N.A. N.A.
1. Equipment suppliers and industry representatives do not expect
plants of this size to be constructed even in the absence of
NSPS.
Key: F - economically feasible to construct
NF - not economically feasible to construct
A - ambiguous
N.A. - Not Applicable because plants of this size are not
likely to be constructed in the absence of NSPS.
8-113
-------
analysis indicates that the investment is not economically feasible. The
same result holds for the 9 Mg/hr (10 tph) common clay plant.
For the 68 Mg/hr (75 tph) sand and gravel, and crushed stone plants, the
23 Mg/hr (25 tph) common clay plant and the 9 Mg/hr (10 tph) gypsum plant, the
DCF analysis showed negative discounted cash flows ranging from less than 2%
of total investment for common clay to approximately 16% for gypsum. An
internal rate of return (IRR) was calculated for each of these four model
plants. The internal rate of return is that rate which makes the discounted
cash outflow. The IRR varied from approximately 8.5% for gypsum to slightly
less than 10% for common clay. Since the net discounted cash flows were only
slightly negative; i.e., the IRR was fairly close to 11.8% cost of capital,
small changes in the parameters of the worst case analysis would produce
positive net discounted cash flows. For this reason the 68 Mg/hr (75 tph)
sand and gravel, and crushed stone plants, the 23 Mg/hr (25 tph) common clay
plant and the 9 Mg/hr (10 tph) gypsum plant are determined to be economically
feasible to construct, if the conservative assumptions used throughout this
report are relaxed.
Table 8-41 shows the results of the DCF analysis on expansions of 4.5
and 9 Mg/hr (5 and 10 tph) grinding capacity in the common clay and gypsum
industries. In the analysis the expansion was assumed to take place in the
smallest size existing plant; i.e., 9 Mg/hr (10 tph), in order to provide a
"worst case" situation, the control costs were assumed to be spread over both
new and existing output based on the ratio of new to existing output. As is
shown in Table 8-41, all expansion size plants except the 4.5 Mg/hr (5 tph)
common clay plant were determined to be economically feasible to construct.
8-114
-------
Table 8-41
SUMMARY OF DCF RESULTS
Expansions
Investment Decison
INDUSTRY
Common Clay
Gypsum
Size
Mg/hr (tph)
4.5 '
(5)
A
F
9
(10)
F
F
Key: F - economically feasible to construct
A - ambiguous
8-115
-------
It should be kept in mind that because an investment is found to be
economically feasible from a DCF analysis it does not necessarily mean
that the investment will, in fact, be made by a company.
NSPS control costs will not significantly affect those non-
metallic mineral industries for which a DCF analysis was not performed.
As seen in Table 8-36 the greatest potential NSPS control cost absorp-
tion is less than or equal to 2% of product price, since these non-metallic
minerals all have a higher product price than those non-metallic minerals
for which a DCF analysis was performed. The process economics are similar
for both industries for which a DCF analysis was performed and for which a
DCF analysis was not performed. Since the DCF analysis was favorable for
industries whose potential control cost absorption was equal to or greater
than 4% of product price, the DCF analysis will be favorable for industries
where this ratio was equal to or less than 2%. For this reason a DCF
analysis performed on each of those 17 non-metallic minerals excluded from
further consideration in Table 8-36 would show an economically feasible
investment decision for all size new plants.
. Crushing and grinding facilities are also a portion of production
operations whose final output is not a specific type of non-metallic
mineral, such as at lime and power plants; i.e, crushing and grinding are
intermediate processes in these industries.
These intermediate processing facilities are usually constructed
by firms in the above mentioned industries because the need for the
non-metallic mineral is large enough to support such a facility. Such
8-116
-------
intermediate facilities can produce the requisite size mineral at a
lower cost to the firm than can be attained from buying the mineral from an
independent producer. Consequently, some cost increase could be sustained by
intermediate processing facilities and still permit them to be competitive
with firms that purchase the requisite size material from independent
producers. Furthermore, the intermediate processor is able to spread
the incremental cost over a final product whose selling price is larger
than that of the non-metallic mineral input, and, thus can more readily
pass on these costs. Finally, because of their affiliation with larger
companies, these facilities would tend to ha.ve a lower cost of capital.
Therefore, the investment decision resulting from the DCF analysis for
various plant sizes in the non-metallic mineral industries per se would
likely hold for intermediate processing facilities (that are part, of
other facilities).
8.5 POTENTIAL SOCIO-ECONOMIC AND INFLATIONARY IMPACTS
8.5.1 Industry Cost Totals
Table 8-42 presents the upper limit to the number of typical new
plants which will be constructed in each industry in each of 5 years
based on projected industry growth and the typical plant size in each
industry. The projections of new plants required is based on growth from
1975 production statistics and assumes that 1975 production equals capacity.
To the extent that actual production was lower than capacity production,
the number of estimated typical size plants required each year will be
lower. Therefore required total industry annualized control costs will be
lower.
8-117
-------
Table 8-43 indicates the cumulative annualized industry capital and
operating costs in 1976 dollars to meet the NSPS standard. The totals are
derived by multiplying the estimated number of typical plants to be con-
structed in each year by the annualized control costs for these size plants.
As can be seen, the crushed stone industry would have the largest annualized
costs by the fifth year, $19.2 million.
Table 8-44 shows the average annualized cost per ton of output in the
fifth year after control. These figures are based on the estimated cumu-
lative annualized costs in the fifth year, Table 8-43, divided by the estimated
total industry production in the fifth year. Kyanite shows the largest
industry cost per ton of $0.137 per ton. Table 8-44 also shows that control
cost per ton as a percent of price per ton is highest for pumice, 1.7%.
New regulations shall be considered a major action if "additional
annualized cost of compliance, including capital charges (interest and
depreciation), will total $100 million (i) within any one of the first
5 years of implementation, or (ii) if applicable, within any calendar .
year up to the date by which the law requires attainment of the relevant
pollution standard," or "total additional cost of production of any major
industry product or service will exceed 5 percent of the selling price of
the product." Total industry annualized control cost in the fifth year
after promulgation of NSPS and control cost as a percent of selling price
are lower than the guidelines set for these measures of $100 million
for annualized capital and operating expense and 5 percent, respectively.
8-118
-------
TABLE 8-42 ESTIMATED NUMBER OF TYPICAL NEW PLANTS REQUIRED TO
MEET PROJECTED PRODUCTION*
Industry
Pumice
Sand and Gravel
Crushed Stone
Common Clay
Gyps in
Perl i te
Rock Salt
Sodium Compounds
Talc
Ban te
Boron
Fluorspar
Feldspar
Di atomi te
Vermiculite
Mica
Kyanite
Gilsonite
Typical
size
(Mg/hr)
9
272
272
23
23
23
68
23
9
9
272
9
9
23
68
9
9
9
Growth
rate
(%)
3.5
1.0
4.0
3.5
2.0
4.0
2.0
2.5
4.0
2.2
5.0
3.0
4.0
5.5
4.0
4.0
6.0
-
1980
2
14
72
10
1
-
2
-
-
-
-
-
- "
-
-
-
-
-
1981
2
14
75
10
1
1
2
1
1
-
-
-
'
-
-
-
-
. -
1982
2
14
78
10
1
1
3
1
1
1
-
-
1
1
-
-
-
-
1983
2
14
81
11
1
-
3
1
-
-
-
-
-
-
-
-"
-
-
1984
2
15
85
11
1
1
3
_
1
_
.'
1
'
-
1
1
1
-
n
Whenever the projected production for a given year was not
enough to justify the building of a new typical size plant, no
new plants were assumed to be built.
8-119
-------
TABLE 8-43 ANNUALIZED CAPITAL AND OPERATING CONTROL
COSTS FOR NEW PLANT CONSTRUCTION
Industry
Pumice
Sand and gravel
Crushed stone
Common clay
Gypsum
Perlite
Rock salt
Sodium compounds
Talc
Barite
Boron
Fluorspar
Feldspar
Di atomi te
Vermi cul i te
Mica
Kyanite
Gilsonite
Total
Annual i zed cost
(in thousands of dollars)
1980 1981
42.4 84.8
777 1 ,554
3,996 8,158.5
234 468
23.4 46.8
16
46.8 93.6
23,4
21.2
-
-
-
-
-
-
-
-
-
1982
127.2
2,331
12,487.5
702
70.2
32
163.8
46.8
424
21.2
-
-
21.2
23.4
-
-
-
-
1983
169.6
3,108
16,983
959.4
93.6
32
234
70.2
42.4
21.2
-
-
21.2
23.4
-
-
-
-
1984
212.0
3,940.5
21,700.5
1,216.8
117
48
304.2
70.2
63.6
21.2
-
21.2
21.2
23.4
23.4
21.2
21.2
-
27,825.6
8-120
-------
TABLE 8-44 ANNUALIZED CONTROL COST PER TON OF INDUSTRY
OUTPUT IN 5TH YEAR AND CONTROL COST AS PER-
CENT OF SELLING PRICE
Industry
Pumice
Sand and gravel
Crushed stone
Common clay
Gypsum
Perl He
Rock salt
Sodium compounds
Talc
Barite
Boron
Fluorspar
Feldspar
Diatomite
Vernriculite
Mica
Kyanite
Gilsonite
ton£?t£St An™alized cost/ton
v r§\ * price/ton
0.043
0.005
0.018
0.019
0.01
0.051
0.017
0.012
• 0.049
0.014
-
0.123
0.023
0.026
0.052
0.116
0.137
-
1.7 %
0.2
0.8
0.9
0.2
0.3
0.1
0.03
0.1
0.1
-
0.1
0.1
0.03
0.1
0.3
0.2
-
Based on 1976 average F.O.B. mine selling price
and 1978 production figures.
8-121
-------
-------
APPENDIX A
EVOLUTION OF THE BACKGROUND INFORMATION DOCUMENT
A-l
-------
TABLE A-l. EVOLUTION OF THE BACKGROUND INFORMATION DOCUMENT
Date
Company, consultant or agency
Location
Nature of action
04/30/73 Arizona Portland Cement
Ideal Ceneot
Albuquerque Gravel Products
09/13/73 Harry T. Campbell and Sons
Texas Plants
10/13/73 Nello L. Teer Company
01/16/74
02/13/74
05/28/74
to
05/31/74
05/14/74
to
05/15/74
06/03/74
Paul L1me Plant, Inc.
Arizona Portland Cement Co.
Ideal Cement Co.
Albuquerque Gravel Products, Inc.
H.G. Fenton Material Co.
RHHto, Ariz. Presurvey two sources.
Tljeras, N. Hex. Inspect haul road fugitive dust control
Albuquerque, N. Hex. technique.
Texas, Md. Measure visible emissions from the
asphalt batch plant.
Raleigh, N.C. Inspect stone processing and quarrying
operations.
Douglas, Ariz. Presurvey two quarries and stone pro-
RW1to, Ariz. cesslng plants for partlculate testing.
Tljeras, N. Mex. Inspect crushed stone plants
Albuquerque, N. Hex.
San Diego, Calif.
Essex Bituminous Concrete Corp. Dracut, Mass.
Essex Bituminous Concrete Corp.
Blue Rock Industries
Lynn Sand and Stone Co.
Massachusetts Broken Stone Co.
Kentucky Stone Co.
Caldwell Stone Co.
Arizona Portland Cement Company
Peabody, Mass.
Westbrook, Maine
Swampscott, Mass.
Weston, Mass.
Russellvnie, Ky.
Danville, Ky.
RllHto, Ariz.
Presurveys of five crushed stone plants
for testing
06/02/74 Arizona Portland Cement Company RIllUo, Ariz.
08/06/74 General Crushed Stone Co.
to Pennsy Supply Inc.
08/08/74 J. M. Brenner Stone Co.
09/16/74 Essex Bituminous Concrete Co.
10/28/74 Kentucky Stone Co.
Quakertown, Pa.
Harrlsburg, Pa.
Lancaster, Pa.
Dracut, Mass.
Russellvllle, Kv.
11/19/74 J. M. Brenner Co. Lancaster
12/27/74 Essex Bituminous Concrete Co.
Presurveys of two crushed stone plants
for testing.
Conduct emission tests for oartlculate
emission
Test report for partlculate emission
testing.
Presurveys for partlculate emission tests.
Trie report of emission tests on stone
crashing operations.
~'-ts conducted for process and fugitive
test of two baghouse operations
-isned stone plant.
iourcs testing report of stone crushing
•>ierat1on.
(continued)
A-2
-------
TABLE A-T (continued)
Date Company, consultant or agency
Location
Nature of action
12/20/74 Ferrante and Sons
06/30/75 Kentucky Stone Co.
07/08/75 Arizona Portland Cement
11/13/75 Massachusetts Broken Stone Co.
04/13/76 Blue Ridge Stone Corp.
05/06/76 Potash Company of America
05/27/76 Dravco Corp.
05/12/76 GREFCo, Inc.
05/11/76 U.S. Borax
05/27/76 Dravco Corp.
06/10/76 FUntkote Co.
06/24/76 Englehard Minerals and
Chemicals Co.
06/23/76 Georgia Kaolin Co,
07/08/76 Standard Slag Co.
07/09/76 Ozark-Mahonlng Co.
07/07/76 International Salt Co.
07/06/76 Eastern Magnesia Talc Co.
08/26/76 Massachusetts Broken Stone
09/27/76 International Minerals and
Chemicals Corp.
Bernardsville, N.O.
Russellville, Ky.
.Rillito, Ariz.
Western, Mass.
MartinsvUle, Va.
Carlsbad, N. Mex.
Newtown, Ohio
Socorro, N. Hex.
Boron, Calif.
Newtown, Ohio
Las Vegas, Nev.
Attapulgus, Ga.
Dry Branch, Ga.
Harren, Ohio
Roslclare, 111.
Retsof, N.Y.
Johnson, Vt.
Weston, Mass.
Spruce Pine, N.C.
Emission test report of stone
crushing operation.
Source tests on primary, secondary
crushers, three deck screens, and
crusher feed hopper.
Trip report of visible emissions obser-
- vations at stone crushing facility.
Report on observation of visible emis-
sion at stone processing operation.
Plant visit to study process operation
at crushed stone plant.
Plant visit to study processing of
potash ore.
Plant visit to study processing of
sand and; gravel and the resultant
particulate emissions.
Plant visit to study processing of
perlite ore and the resultant par-
ticulate emissions.
Plant visit to study processing of
borate ore and resultant particulate
emissions.
Plant visit made by PEDCo Environmental
Specialists, Inc.
Plant visit made by PEDCo and EPA to
study gypsum processing operations.
Plant visit to observe fuller's earth
processing and resultant particulate
emissions.
Plant visit to observe kaolin proces-
sing operations and resultant partlcu-
late emissions.
Plant visit to observe slag processing
and resultant particulate emissions:
Plant visit to observe fluorspar pro-
cessing and resultant particulate
emissions.
Plant visit to observe rock salt pro-
cessing and resultant particulate
emissions.
Plant visit to observe talc pro-
cessing and resultant particulate
emissions;
Visible emissions tests conducted at
stone processing operations.
Source sampling at feldspar milling
operation for particulates.
(continued)
A-3
-------
TABLE A-l (continued)
Date Company, consultant or agency Location
10/25/76 FUntkote Co.
10/21/76 Eastern Magnesia Talc Co.
Blue Diamond, Nev.
Johnson, Vt.
Nature of action
Stationary source testing of gypsum
milling operation.
Stationary source testing at several
11/10/76
05/09/77
05/10/77
06/20/77
06/20/77
07/11/78
Pfelzer Inc.
Johns-ManvWe Corp.
Pfelzer, Inc.
Pfelzer, Inc.
National Air Pollution -
Control Techniques and
Advisory Comnlttee
(NAPCTAC)
National Asphalt Pavement
Association
08/16/78
08/29/78 Kaolin Industry
09/14/78 National Slag Association
10/03/78 National Limestone Institute
12/05/78
12/06/78
12/20/78
01/09/79
01/10/79
Georgia Kaolin Company
Thlele Kaolin Company
Edward C. Levy Co.
Victorvllle, Calif.
Lompoc, Calif.
V1ctorv1lle, Calif.
Victorvllle, Calif.
Raleigh, N.C.
Durham, N.C.
Durham, N.C.
Durham, N.C.
Washington, D.C.
Dry Branch, Ga.
SandersvHle, Ga.
Detroit, HI.
Colorado Sand and Gravel Durham, N.C.
Association
North State Pyrophylllte Company Greensboro, N.C.
01/22/79 Gypsum Association
02/21/79
to
02/23/79
Colorado Sand and Gravel
Association
Durham, N.C.
Denver, Col.
plant.
Source sample analysis for physical
characteristics of particulate samples
from several plants.
Presurvey talc grinding operations for
possible source testing.
Presurvey diatomite processing oper-
ations for possible source testing.
Source test on pebble mill at talc pro-
cessing plant.
Source emission test report performed
by Pacific Environmental Services, Inc.
Meeting with non-metallic industry
spokesmen to discuss proposed NSPS.
Meeting with National Asphalt Pavement
Association to discuss proposed NSPS.
Meeting between EPA and the Kaolin
Industry to discuss the proposed NSPS
as 1t pertains to the Kaolin Industry.
Meeting between EPA and the associa-
tion to discuss the proposed NSPS as
1t pertains to the slag Industry.
Meeting between Institute and EPA to
discuss proposed NSPS as it pertains to
the limestone industry.
Source test report on Raymond Impact
Mill and Roller Mill.
Fugitive emission testing at product
loading facility at kaolin plant.
Plant visit by GCA/Technology Division
to observe slag processing and
resultant participate emission.
Source testing performed by Clayton
Associates same date.
Meeting with EPA to discuss proposed
NSPS.
Meeting with GCA/Technology Division
to discuss problems plant would havt
with proposed NSPS.
Meeting between the Association and
EPA to discuss the proposed NSPS as
It pertains to the gypsum industry.
GCA/Technology Division visited sev-
eral sand and gravel processing plants
and met with the Association to
discuss the proposed NSPS as well as
to observe process and emission
control techniques used at the sand and
gravel plants.
(continued)
A-4
-------
TABLE A-l (continued)
Date Company, consultant, or agency
Location
Nature of action
03/06/79 Refractories Institute
04/03/79 P-Stone, Incorporated
04/19/79 Iowa Manufacturing Co.
08/15/79 Johnson-March Company
08/24/79 Tillcon-Tomasso, Inc.
to Castle Concrete Co.
08/31/79 Schmidt-Tiago Construction Co.
Cooley Gravel Co.
Brannan Sand and Gravel Co.
Mobile Pre-Mix Co.
Gifford-Hill 8 Co.
Lone Start Industries
09/06/79 Vulcan Materials Co.
to Vulcan Materials Co.
09/17/79 Martin-Marietta Co.
Martin-Marietta Co.
Nello L. Teer Co.
Luck Quarries
Vulcan Materials Co.
Flintkote Stone Products Co.
Martin-Marietta Co.
Vulcan Materials Co.
10/02/79 Vulcan Materials Co.
to Castle Concrete Co.
10/30/79 Brannan Sand & Gravel Co.
Vulcan Materials Co.
FTintkote Stone Products Co.
10/15/79 Southern California Rock
Products Association
11/20/79 Georgia Kaolin, Industry
01/15/80 National Crushed Stone
Association, National Sand &
Grave.! Association
10/27/82 National Crushed Stone
Association, National Sand &
Gravel Association
Durham, N.C.
Opal, Pa.
Durham, N.C.
Philadelphia, Pa.
N. Branford, Conn.
Colorado Springs, Colo.
Eagle, Colo.
Morrison, Colo.
Denver, Colo.
Golden, Colo.
Chico, Tex.
Bridgeport, Tex.
Helena, Ala.
Newman, Ga.
Augusta, Ga.
Columbia, S.C.
Rocky Mount, N.C.
Manakin, Va.
Stafford, Va.
Frederick, Md.
Jamestown, N.C.
Stoneville, N.C.
Helena, Ala.
Colorado Springs, Colo.
Denver, Colo.
Stafford, Va.
Frederick, Md.
Durham, N.C.
Durham, N.C.
Durham, N.C.
Washington, D.C.
Meeting between Institute and EPA to
discuss the proposed NSPS as it pertains
to the Refractories Industry.
Plant visit by GCA/Technology Division to
investigate portable plant using ba'ghouse
to control dust emitted by process.
Meeting between company and EPA to
discuss the proposed NSPS as it pertains
to the crushed stone industry.
Meeting with GCA/Technology Division to
gather information on wet dust suppression
control systems.
Presurvey ten stone crushing and sand
and gravel plants by GCA/Technology
Division for visible emission testing.
(Plants controlled by wet suppression.)
Presurvey ten stone crushing and sand
and gravel plants by GCA/Technology
Division for visible emission testing.
(Plants controlled by wet suppression.)
Visible emission testing at several
crushers, screens, transfer points, etc.
controlled by wet suppression at five
crushed stone and sand and gravel
plants.
Meeting between association and EPA to
discuss ambient monitoring data performed
by the association.
Meeting between industry representatives
and EPA to discuss the proposed NSPS as it
pertains to the Kaolin Industry.
Meeting between associations and EPA to
discuss recent visible emission tests
performed by EPA and ambient monitoring
data performed by the association.
Meeting between associations and EPA to
discuss the designation of affected
facilities.
A-5
-------
-------
APPENDIX B
INDEX TO ENVIRONMENTAL IMPACT CONSIDERATIONS
This'appendix consists of a reference system, cross-indexed with the
October 21, 1974 FEDERAL REGISTER (39 FR 37419) containing the Agency guide-
lines concerning the preparation of Environmental Impact Statements. This
index can be used to identify sections of the document which contain data
and information germane to any portion of the FEDERAL REGISTER guidelines.
B-l
-------
00
«3
S_ • to I
ra C «*• -i- CM
re
-P CO -E
IO N O>
•r- 3
.c: s- o
u « s-
to i
•o cu
i- 01
(T3 rO
-o Q-
C
ra «
CM
O>
£ £
O CO r— -P- O
s- s-
ra
ra
cu
UJ
o
a>
^.
o
fO
CO
cu
CO i
cu
CO ra (O
> tO O.
•r- O
•PO."
O -P
a. u
o co
s- CM
to o •— o
S- O-i—
CU
•P S- C
r— O O
«<»-•£
>> E O
S. CU CU
O VI to
-P O
<»- s-
0)
•i- a.
to ca
J3 O
3 CO
01
co to
s- s-
co
CO -P
.E Q.
-P ra
E o
CO
I-
co -a
J3 CO
Q. 3
•r- O
.e to
c -a
o
•r- CO
•P S-
10 tO
"a) to
(O
" 4-» T3 I
•p
•P C
j= cu
O) !
i— r_) i— 3 CO CM
3 -P N
CO CO S- rO •!- .E
co .a cu -P s- co
S- -P CO re 3
i— a. go
CU r— rO CU E S-
I— 5 O h- tO -P
to 3
cn
co co CD 1-
s- c wi .c
C -I- CO 4-»
CO O S- T-
JC -r- O) i- r—
+J 4-> > 4-> I
O O to CO
>, CO O 3
to
-a to
CO
T3 "t-
CU OO •!— rd
•P ro CO Q.
U S- -P .E
CO CO CU -P «
M- -p -a
4- a.
rO
M-
CO
S- O OO
CO
J= CO C
•P S- O
•i- C S- 3
S- «r- 3 -M O
to
U_ ra O)
CO
-o +•>
C CM O 00
«r- -i- CO i— •!-
to . _ _
CO CO OO O CO
.£= S- C P
•P Q..C: o o.
co o ra
co
OJ ,
s- to
co c
a.
co to
i— O)
t/i
CO '
•p
a •
co co
fO
•P CO
CO
co in
S- I
a. co
rO
CO
CO
o
rO •
CO
U i
(O > .£=
I •!- -P
I— V) -P >
CO ra CM
-E O C r—
cn i- s- i
3 3 CO CO
O O -P
s_ to r- to
re CU
•P CO
Ol
.c >>
O ra CM
to r— •
co e: 3 oo
C7) O O)
ra •
co
Q. to S- O
3 CO
o -
to -I- O CO -P CO -r-
3 -P «r- > C
o o to T- i— «i— -a
•r- (O tO -P I tO CO
S- 3 ra CO 3 -P
ro >> o c: ja c
>o tos-to=co«
E -i— CO CO to i—
coco -o-PoicocuLn
u
u
CO
4-> O O)
, CO O -r- -P
J C O
CO
o>
i— >
CO
CO
CO
CO
•a
CO
X
CO
o
O «/)
•p -p
03 C
r— CO
Ol
CO -
o>co
ra ra i
a. Q.I—
co E
s- •-<
cu co
S-'rO Qi
O -P U-
ljj||r ^"
cu cr>
O)
c o
CO >
•a c
•r- UJ
I CO
ra
Ol
CO
ra
•a
ra to
CO
•a >
C 'T-
3 -P
O rO
s_ c
O) S-
^i CO
O -P
ra i—
CO ra
ra
ra
-p
to
CO
o>
ro
S- (0
O r—
0>
CO
cn
o to
•i- C
-P O
ra
•p c:
to s-
ra T- 3 CO
pJ: 4-> -o -P
CO CJ E r—
a: ra
i—i ra
CO
CO
co to
f- CO
to rO
CO 1=
CO S_
to co
CO -P
CJ r—
O ra
o o
•r- +J
<4- rO
O 3
CO O>
a. ai
CO S-
CO «
o»
B-2
-------
APPENDIX C
SUMMARY OF TEST DATA
A test program was undertaken by EPA to evaluate the best particulate
control techniques available for controlling particulate emissions from
non-metallic mineral plant process operations including crushers, screens
and material handling operations, especially conveyor transfer points. In
addition, a control technique for grinding operations was also evaluated.
This appendix describes the process operations tested (their operating con-
ditions, characteristics of exhaust gas streams and, where applicable, de-
viations from prescribed test procedures) and summarizes the results of the
particulate emission tests and visible emission observations.
Sixteen baghouse collectors controlling process operations at five
crushed stone installations (three limestone and two traprock), one kaolin,
and one fuller's earth plant were tested using EPA Reference Method 5 except
as noted in the facility descriptions for determination of particulate matter
from stationary sources. Baghouse collectors utilized to control particulate
emissions from grinding operations at a feldspar, gypsum, and two talc plants
were also tested, but EPA Reference Method 17 was used for determination of
particulate matter. Results of the front-half catches (probe and filter)
from the particulate emission measurements conducted are shown in Figure C-T
and the complete results are summarized in the Tables herein.
Visible emission observations were made at the exhaust of each of the
above control devices in accordance with procedures recommended in EPA
C-l
-------
Reference Method 9 for visual determination of the opacity of emissions from
stationary sources.
At the hoods and collection points for the process facilities, the visible
emission opacity observations were made in accordance with procedures recommen-
ded in EPA Reference Methods 9 and 22 and the data are presented in terms of
percent of time equal to or greater than a given opacity or in percent of total
time of visible emissions as in Table 102. Visible emission observations were
also made at four crushed stone, two sand and gravel plants and a feldspar
crushing plant where particulate emissions are controlled by dust suppression
techniques. The results of these tests are given in Table 102 (Method 22 data)
and Figures 2 through 6 (Method 9 data).
DESCRIPTION OF FACILITIES
AT. Primary crushing stage incorporating a pan feeder, vibrating grizzly,
impact breaker, T-bar belt feeder and a primary belt conveyor. The impactor
is rated at 1,000 TPH and used to reduce run-of-quarry limestone (cement rock)
to 2 1/2-inch minus. Particulate emissions generated at various points are
confined, captured and vented to a jet pulse type baghouse for collection.
Tests were conducted only during periods when the process was operating
normally. Particulate measurements were performed using EPA Method 5. Visible
emission observations were made at the baghouse exhaust and at capture points
in accordance with EPA Method 9.
A2. Primary scalping screen used for scalping the primary crusher
product of facility Al. The plus 2 1/2-inch oversize is chuted to a belt
conveyor and returned to the primary for recrushing. The screen throughs
are also discharged to a conveyor and transported to a storage facility.
Particulate emissions generated from the top of the screen, which is
totally enclosed, and from both chute-to-belt transfer points are aspirated
to a jet pulse baghouse for collection. Tests, using EPA Method 5, were
C-2
-------
conducted simultaneously with those at facility AT. Sampling during all
three tests runs reported herein was overisokinetic. Visible emission
observations were made at the baghouse exhaust using EPA Method 9.
A3. Conveyor transfer point at the tail of an overland conveyor, also
located at installation Al. The 30-inch belt conveyor has a 900 TPH
capacity at a belt speed of 700 FPM. The transfer point is enclosed and
emissions vented to a small baghouse unit for collection. Three particulate
samples were collected using EPA Method 5. Visible emission observations
were made at the baghouse outlet and at the transfer point using EPA
Method 9.
A4. The secondary crushing and screening stage at installation Al.
consisting of a vibrating screen and a cone crusher. Minus 2 1/2-inch
material is fed to the screen at about 165 TPH where it is separated in two
fractions, plus 3/4-inch and 3/4-inch minus. The oversize fraction is
discharged to the cone crusher and reduced to 3/4-inch. The crusher product
and screen throughs are then conveyed to a milling circuit. Dust control
is effected by capturing and venting emissions from the screen and crusher
to a jet pulse baghouse for collection. Both particulate measurements and
visible emission observations were made at the collector outlet using EPA
Methods 5 and 9, respectively.
Bl. Primary impact crusher used for the initial reduction of run-of-
quarry limestone rock to three inches. The normal production rate through
this primary crushing stage is 350 TPH. Particulate emissions are collected
from the impact crusher at its discharge hopper and from the discharge hopper
to primary conveyor belt transfer point and then controlled by a fabric filter
C-3
-------
collector. The fabric filter is mechanically shaken twice daily for
cleaning. EPA Method 5 was used for participate measurements and EPA
Method 9 was used for visible emission readings at the collector exhaust and at
the impact crusher.
B2. Secondary and tertiary crushing and screening facilities at the
same installation as Bl. These consist of a scalping screen, a 4-foot
cone crusher, two 3-foot cone crushers, a hammermill used to produce
agstone and two final sizing screens. The plant has a 300 TPH design
capacity, crushing to 1 1/2-inch minus, including 60 TPH of agstone. Dust
control throughout this plant is affected by enclosing or hooding dust
producing points and venting captured emissions to a fabric filter for
collection. The collector is mechanically shaken twice daily for cleaning.
Pickup points include the top of the scalping screen, both the feed and
discharge of all three cone crushers, the discharge of the hammermill, the
top of both finishing screens, five product bins and six conveyor transfer
points. Three particulate measurements were made in accordance with EPA
Method 5. In addition, visible emission observations were made at the
baghouse exhaust and at the process facilities controlled using EPA
Method 9.
B3. The same facility as B2, except that particulate emission
measurements were made using an in-stack filter. Testing was conducted
simultaneously with .that described in B2.
Cl. Limestone crushing plant consisting of a primary jaw crusher,
scalping screen and hammermill. The rated capacity of the plant is 125
TPH. End products produced range from 1 1/2-inch minus dense-graded road
base stone to minus 1/8-inch screenings. Particulate emissions are
controlled by a mechanical shaker type baghouse. Collection points include
the primary crusher discharge, the scalping screen throughs to stacking
C-4
-------
conveyor transfer point, and both the hammerrr-m feed and discharge.
Tests were conducted using EPA Methods 5 and 9.
C2. Two 3-deck vibrating screens used for final sizing at the same
installation as Cl. Both screens are totally enclosed and participate
emissions collected from the top of both screens, at the feed to both
screens, and at both the head and tail of a shuttle conveyor between the
screens are vented to a mechanical shaker type baghouse. Again, tests were
conducted in accordance with EPA Methods 5 and 9.
Dl. Secondary and tertiary crushing and screening facilities used
for processing traprock at "250 TPH. The process facilities include a"
scalping screen, a 4-foot secondary cone crusher, two sizing screens and two
4-foot tertiary cone crushers. All process facilities are enclosed and
particulate emissions are vented to one of two baghouses for collection.
The baghouses are exhausted through a common stack. Particulate measurements
were conducted using EPA Method 5. Visible emission observations using
EPA Method 9 were also made at the collector exnaust and at the process
facilities controlled.
D2. Finishing screen at the same installation as facility Dl. The
screen is totally enclosed and emissions collected from the top of the
screen enclosure, all screen discharge points, and several conveyor transfer
points are vented to a fabric filter. Tests conducted were Identical
to those at Dl and were performed simultaneously.
El. Tertiary crushing and screening facilities at a 375 TPH traprock
installation. Process facilities include two sizing screens, four 4 1/4-foot
C-5
-------
cone crushers and several conveyor transfer points. Both screens are
enclosed and emissions are collected by the enclosures and at the throughs
discharge-. The tertiary cone crushers are hooded and vented at both feed
and discharge points. Captured emissions are collected by a jet pulse type
baghouse. Tests using EPA Method 5 were conducted during periods of normal
operation. Although desirable, the pressure drop across the baghouse could
not be monitored because the pressure gauge was inoperative. Visible emission
observations were also made of the baghouse exhaust using EPA Method 9.
E2. Five screens used for final sizing and eight storage bins at the
same installation as El. All screens and bins are totally enclosed and
emissions vented to a jet pulse type baghouse for collection. Tests
conducted were identical to and performed simultaneously with those at
facility El.
Fl. Tertiary crushing and screening facilities used to reduce run-of-
quarry trap rock. Partlculate emissions are controlled by spraying
water at critical dust producing points in the process flow. Two to three
percent moisture is added to the material to suppress dust. Visible emission
observations were made in accordance with EPA Method 9 procedures.
61. Grinding system incorporating a belt feeder, ball mill, bucket
elevator, separator and a belt conveyor. The ball mill 1s used to reduce
feldspar to minus 200 mesh. Partlculate emissions generated at various
points are confined, captured and vented to a reverse air type baghouse
for collection. Partlculate measurements were performed using EPA Method 17.
Visible emission observations were made at the baghouse exhaust and all
capture points in accordance with EPA Method 9.
C-6
-------
62. Crushing facilities (primary and secondary) used to reduce feldspar
to minus 1.5 inches. Dust control is affected by the suppression techniques.
Surface moisture contents were 1.6 to 1.8 percent at the primary crusher
discharge, 1.4 to 1.5 percent at the secondary crusher feed, and 1.0 percent
at the secondary crusher discharge conveyor. Visible emission observations
were made at all process facilities in accordance with EPA Method 9
procedures.
HI. Raymond roller mill used to grind gypsum. The ground product from
the mill is air-conveyed to a cyclone collector for product recovery. The
air is returned to the mill. Excess air is vented to a baghouse. Visible
emission observations were made to determine leaks from the system in
accordance with EPA Method 9 procedures.
H2. Same facility as HI. Particulate measurements and visible emission
observations were made at the baghouse exhaust in accordance with EPA
Methods 5 and 9.
I. Bagging operation used to package ground mica. Particulate
emissions are controlled by a baghouse. Visible emission observations
were made at the capture point in accordance with EPA Method 9 procedures.
Jl. Crushing (primary and secondary), grinding "(pebble mill and vertical
mill) and bagging operations at a talc processing plant. Particulate emis-
sons are controlled by a baghouse. Visible emission observations were
made at the capture points in accordance with EPA Method 9 procedures.
J2. Same facility as Jl. Particulate measurements and visible emission
observations were made at the baghouse exhaust 1n accordance with EPA
Methods 5 and 9.
C-7
-------
K. Pebble mill used to grind talc. Captured emissions are vented to a
pulse type baghouse for collection. Particulate measurements and visible
emission observations were made at the baghouse exhaust in accordance with
EPA Methods 5 and 9.
LI. Raymond Impact Mill used to grind kaolin. Captured emissions are
exhausted to a baghouse for collection. EPA Methods 5 and 9 were used for
particulate measurement and visible emission observation at the baghouse stack,
respectively.
L2. Roller Mill used at same plant as LI. Further grinding of kaolin
is accomplished. Collection of captured emissions takes place in a baghouse
which was tested for the same parameters as LI, again by EPA Methods 5 and 9.
Ml. Roller mill used to grind fuller's earth clay. Captured
emissions are exhausted to a baghouse for collection. Particulate measure-
ments and visible emission observations were made at the baghouse exhaust
in accordance with EPA Methods 17 and 9.
M2. Fluid energy mill used to grind fuller's earth clay at same
plant as Ml. Captured emissions are exhausted to a baghouse for collection.
EPA Methods 17 and 9 were used for particulate measurement and visible
emission observation at the baghouse stack, respectively.
N. Kaolin rail car loading operation. Three complete rail car
loadings were evaluated for fugitive emissions in accordance with EPA
Method 22 test procedures. A baghouse (collection system) is used to
collect dust that is captured in the loading area.
P. Facility P produces crushed stone used primarily for road construc-
tion purposes. The processing operation is located in the bottom of an open
quarry. The quarried materials are carried by tr-jck to the upper rim of the
C-8
-------
pit where they are dumped into hoppers which feed the processing equipment.
The finished product is transported back out of the quarry by belt conveyor.
Visible emission measurements were conducted at the primary (jaw),
secondary (impact), and tertiary (cone) crushers, two process screens, and one
conveyor transfer point by means of EPA Reference Methods 9 and 22. All pro-
cess sources of emissions are directly or indirectly controlled by means of a
wet suppression system.
Q. This facility produces two grades of rock for road-base and decora-
tive stone, respectively. The ore is obtained from an open mining operation
at the top of a mountain, and the process equipment is permanently installed
in a descending arrangement from the mine site to the bottom of the mountain.
The processed rock is accumulated in bins at the lower level for subsequent
truck loading.
Visible emission measurements using the same techniques as Facility
P were conducted at the primary (jaw), and secondary (cone) crushers, three
process screens, and one conveyor transfer point all controlled by means of a
wet suppression system.
R. A fully portable crushing plant processes bank-run material for road
construction and as concrete component. Ore is removed from a gravel bank and
trucked to the bank top for dumping into the initial screens before the primary
crushers. Wet suppression techniques are used to control fugitive dust emana-
ting from the processing of the material.
EPA Reference Methods 9 and 22 were used to measure visible emissions
f
from primary (jaw), and secondary (cone) crushers, three process screens, and
two conveyor transfer points.
S. The facility produces two grades of crushed limestone. The plant is
C-9
-------
relatively new with all process equipment located at ground level. One jaw
crusher, two cone crushers, two process screens and two conveyor transfer
points are all directly or indirectly controlled by means of wet suppression
systems.
EPA Reference Methods 9 and 22 were employed to measure visible
emissions emanating from the above named process sources.
T. A large semi-portable rock crushing facility processing large-size
grades of crushed limestone was tested for visible emissions by means of EPA
Reference Methods 9 and 22.
The sources tested were the primary and secondary (cone) crushers,
one process screen, one conveyor transfer point, and one storage bin. All
sources tested are controlled by the same techniques as Facilities P, Q, R,
and S.
C-10
-------
o.o
0.015
^
o
u
•r-
CO .O
§3
Si?
*-~> to
IT T3
LU C
uj* 0.01
»- U)
f
3t
(J T3
£ S-
C£. d)
5 «
ID
i.
cn
0.005
0
Facility
Rock Type
A
KEY
H-« AVERAGE
t'
«> EPA TEST METHOD
O OTHER TEST METHOD
n
w
fl ~ -
i i
1 I
1
1
1
1
i
I
ft ^
ft M |
II 1 1 |
_jp f\ .
M ^JT 1
11 H b
« II
1 1
1 1
f * ft " ~
A !
u ^1
1 'Tl
£ kt
>J
1
1
1
Q
B
4^ t
V t)
1 1
f\
i
1
1
fl 1 ^
ii ' 1 1
^ fe ... ,-
w fl ii FI y ij
D L! ii-^ , . v NT*
j o T^ 444 «v« !
c -^ W
-4
-u-J
L L 1
Pflri
,, T. i i i
" A4 Bl §FE
- 1 L L
1 u J-L i l
ii TT i '
»• y MM
1 1 V 1 1 1 1 1 1 1 . - .
3 Cl C2 Dl D2 El E2 Gl LI L2 m • H2
L L L T T T T F K K FE FE
0.046
0.034
Ol
S
E
u
s
u
•E
o.on
0
Figure C-l.
Particulate emissions fron non-metallic minerals
processing operations.
C-ll
-------
Table 1
FACILITY Al
Summary of Results
R>;n .'lumber
Dace
Test Tiir.e-minutes
Production rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate - OSCFM
Temperature - °F
Water vapor - Vol.%
Visible Emissions at
Collector Discharge -
Percent Opacity
Particulate Emissions
Probe and Filter Catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total Catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
(1) Based on throughput through primary crusher.
(2) Back-half sample for run number 1 was lost.
C-12
Average
6/10/74
400
995
26430
22351
81.0
2.5
0.00471
0.00398
0.90
0.00091
w
-
-
_
6/11/74
320
1027
26653
22140
88.0
3.0
See Tables
0.00504
0.00419
0.96
0.00102
0.00597
0.00495
1.13
0.00121
6/12/74
240'
1010
27142
22502
88.0
3.3
2 and 3
0.00727
0.00602
1.40
0.00139
0.00839
0.00695
1.62
0.00160
-'
320
1011
i
26472
22331
85.7
'2.9
0.00567
0.00473
1.07
o.oom
0.00718
0.00595
1.38
0.00140
-------
TABLE 2
FACILITY AT
.0)
Summary of Visible Emissions
Date: 6/4/74 - 6/5/74
Type of Plant: Crushed Stone - Primary Crusher
Type of Discharge: Stack Distance from Observer to Discharge Point: 75 ft.
Location of Discharge: Baghouse Height of Observation Point: Ground-level
Height of Point of Discharge: 14ft. Direction of Observer from Discharge Point: N.E.
Description of Background: Grey building
Description of Sky: Clear
Wind Direction: East
Color of Plume: None
Wind Velocity: 0-5 mi/hr.
Detached Plume: No
Duration of Observation: 6/4/74 - 78 minutes
6/5/74 - 210 minutes
SUMMARY OF AVERAGE OPACITY^
Set Number
1 through 6
7 through 9
10 through 13
14 through 48
Time
Start
8:50
11:23
12:12
8:11
End
9:26
11:41
12:36
11:41
Opacity
Sum
0
0
0
0
Average
0
0
0
0
(1)
Readings were 0 percent opacity during all periods of observation.
Two observers made simultaneous readings.
C-13
-------
TABLE 3
FACILITY Al
SUMMARY OF VISIBLE EMISSIONS
(1)
Date: 7/8/75 - 7/9/75
Tvoe of Plant: Crushed stone (cement rock)
Tyoe of Discharge: Fugitive
Location of Discharge: Primary impact crusher discharge
Height of Point of Discharge: 6 feet
Description of Background: Grey waH
Description of Sky: N.A. (indoors)
Wind Direction: N.A.
Color of Plume: Wnite
Distance from Observer to Discharge Point: .15 feet
Height of Observation Point: Ground level
Direction of Observer from Discharge Point: SE
Wind Velocity. No wind (indoors)
/
Detached Plume: No
Duration of Observation: 7/8/75 - 2 hours
Summary of Data:
Ooacity, Total Time Equal to or
Percent Greater Than Given Onacity
Min. Sec.
5 3 30
10 0 30
15 0 15
20 0 15
25 0 0
30 -
35 -
40 -
45 -
50 -
Sketch Showing How Opacity Varied With Time:
c 20
-------
TABLE 4
FACILITY A2
Summary of Results
Run Number
1
Average
Date
6/10/74
6/11/74 6/12/74
Test Time - Minutes
Production Rate - TPH^
Stack Effluent
Flow rate - ACFM
Flow rate - DSCFM
Temperature - °F
Water vapor - Vol . %
Visible Emissions. at
Collector Discharge -
% Opacity
Particulate Emissions '^)
Probe and filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch ' '
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
400 320
965 1023
15797 15771
13368 13246
90.0 90.0
1.4 2.1
SEE TABLE 5
0.00176 0.00188
0.00149 0.00158
0.20 .0.21
0.00021 0.00024
0.00235
0.00197
0.27
0.00030
240
1056
15866
13196
94.0
2.5
0.00222
0.00184
0.25
0.00024
0.00314
0.00261
0.36
0.00034
320
1015
15811
13270
91.3
2.0
0.00195
, ,0.00164
0.22
0.00023
0.00275
0.00224
0.32
0.00032
(1) Throughput through primary crusher.
(2) All three test runs were over-isokinetic.
(3) Back-half sample for run number 1 was lost.
C-15
-------
TABLE 5
FACILITY A2
Summary of Visible Emissions
Date: 6/10/74 - 6/11/74
Type of Plant: Crushed Stone - Primary Screen
(1)
Type of Discharge: Stack
Location of Discharge: Baghouse
Height of Point of Discharge: 10 ft.
Description of Background: Sky
i
Description of Sky: Clear
Wind Direction: Southwest
Color of Plume: None
Distance from Observer to Discharge Point: 60 ft.
Height of Observation Point: Ground-level
Direction of Observer from Discharge Point: East
Wind Velocity: 0-2 mi/hr.
Detached Plume: No
Duration of Observation: 6/10/74 - 192 minutes
6/11/74 - 36 minutes
SUMMARY OF AVERAGE OPACITY
(1)
Time
Set Number
1 through 11
12 through 32
33 through 38
Start
10:35
12:30
9:40
End
11:41
2:36
10:16
Ojiacitv
Sum
0
0
0
Average
0
0
0
Readings were 0 percent opacity during all oeriods of observation.
' 'Two observers made simultaneous readings.
C-16
-------
Run Number
Date
TABLE 6
FACILITY A3
Sumnary of Results
1
6/10/74 6/11/74 6/12/74
(1) Back-half sarnie for run number 1 was lost.
Average
Test Time - Minutes
Process Weight Rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate - DSCFM
Temperature - °F
Water vapor - Vol . %
Visible Emissions at
Collector Discharge -
Fugitive (% Opacity)
Parti culate Emissions
Probe and filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch ^ '
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
360 288
910 915
2303 2313
1900 1902
98.0 101.0
2.4 2.4
SEE TABLES
0.00095 0.00162
0.00078 0.00134
0.02 0.03
0.00002 0.00003
0.00190
0.00156
0.03
0.00003
288
873
2422
2003
97.0
2.3
7
0.00207
0.00171
0.04
0.00004
0.00259
0.00214
0.04
0.00005
312
899
2346
1935
98.7
2.4
0.00155
0.00128
0.03
0.00003
0.00224
0.00185
0.035
0.00004.
C-17
-------
,(1)
TABLE 7
FACILITY A3
Summary of Visible Emissions'1
Date: 6/11/74
Type of Plant: Crushed Stone - Conveyor Transfer Point
Type of Discharge: Stack Distance from Observer to Discharge Point: 60 ft.
Location of Discharge: Baghouse Height of Observation Point: Ground-level
Height of Point of Discharge: 8 ft. m>PCt.inn nf Observer from Discharge Point: North
Description of Background: Grey apparatus
Description of Sky: Clear
Wind Direction: Westerly Wind Velocity: 0 - 10 mi/hr.
Color of Plune: None Detached Plume: No
Duration of Observation: 240 minutes
SUMMARY OF AVERAGE OPACITY
Time
(1)
Set Number
Start
End
Sum
Onaci ty
Average
1 through 30 10:40 1:40 0 0
31 through 40 1:45 2:45 0 0
Readings were 0 percent opacity during all periods of observation.
' 'Two observers made simultaneous readings.
C-18
-------
TABLE 8
FACILITY A4
Summary of Results
Run Number
Date
6/6/74 6/7/74
6/8/74
Average
Test Time - Minutes
Production Rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate - DSCFM
Temperature - °F
Water vapor - Vol . %
Visible Emissions at
Collector Discharge -
% Opacity
Parti cul ate Emissions
Probe and filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
320
170
10579
9277
81.0
2.3
0.00036
0.00031
0.03
0.00017
0.00047
0.00041
0.04
0.00022
320
162
9971
8711
77.0
2.2
SEE
0.00075
0.00065
0.06
0.00034
0.00104
0.00095
0.08
0.00050
320
152
11045
9656
80.0
2.1
TABLES 9 & 10
0.00074
0.00065
0.06
0.00041
-
'
•V
320
163
10532
9214
79.3
2.2
0.00062
0.00054
0.05
0.00031
0.00678
0.00068
0.06
0.00034
C-19
-------
TABLE 9
FACILITY A4
Summary of Visible Emissions
(1)
Date: 6/6/74
Type of Plant: Crushed Stone - Secondary Crushing and Screening
Type of Discharge: Stack
Location of Discharge: Baghouse
Height of Point of Discharge: 15 ft.
Description of Background: Sky
Description of Sky: Clear
l-find Direction: Variable
Color of Plume: None
Duration of Observation: 240 minutes
Distance from Observer to Discharge Point: 100 ft.
Height of Observation Point: Ground-level
nf Observer from Discharge Point: North
Wind Velocity: 0 to 10 nii/hr.
Detached Plume: No
(1)
Set Number
SUMMARY OF AVERAGE OPACITY
Time Opacity
Start
End
Sum
Average
1 through 30 10:40 1:40 0 0
31 through 40 1:45 2:45 0 0
Readings were 0 percent opacity during all periods of observation.
observers made simultaneous readings.
C-20
-------
TABLE 10
FACIUTY A4
SUMMARY'OF VISIBLE EMISSIONS
o:
Date: 7/9/75 - 7/10/75
Tyoe of Plant: Crushed stone (cement rock)
Tyoe of Discharge: Fugitive
Location of Discharge: Conveyor (transfer point)
Heirit of Point of Discharge: 8 feet
Description of Background: Sky
Description of Skv: Partly cloudy
Wind Direction: South
Color of Plume: White
Distance from Observer to Discharge Point: 50 feet
Heinht of Observation Point: 6 feet
Direction of Observer from Discharge Point: SE
Wind Velocity: 3 - 5 mph
Detached Plume: No
Duration of Observation: 7/9/75 - 106 minutes
7/10/75 - 60 minutes
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Tine Equal to
Greater Than Given
Min.
3
0
0
0
_
-
-
-
-
-
or
Onacity^
Sec.
0
45
30
0
_
-
-
-
-
-
Onacitv,
Percent
55
60
65
70
75
80
Q5
00
15
100
Total Tine Equal to or
Greater Than Given Opacity.
Min. Sec.
Sketch Showing How Opacity Varied '-Jith Time:
S 15
>• io
I
7/9/75
TIME, hours
0 1
7/10/75
(1) Two observers made simultaneous readings, the greater of their readings
is reported.
C-21
-------
Run Number
Date
TABLE 11
FACILITY Bl
Sunmary of Results
10/29/74 10/30/74 10/30/74
Average
Test Time - Minutes
Production Rate - TPH^1^
Stack Effluent
Flow rate - ACFH
Flow rate - DSCFH
Temperature - °F
Water vapor - Vol. X
Visible Emissions at
Collector Discharge -
X Opacity
Particulate Emissions
Probe and filter catch
gr/DSC.F
gr/ACF"
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
(1) Throughput through primary
180
324
5154
4998
70
1.80
0.009
0.012
0.402
0.0012
0.009
0.011
0.496
0.0015
crusher.
120 120
359 375
6121 6078
5896 5753
76 83
1.87 2.06
See Table 12
0.001 0.010
0.004 0.011
0.072 0.500
0.0002 0.0013
0.001 0.010
0.003 0.011
0.180 0.553
0.0005 0.0015
C-22
140
353
5784
5549
76.3
1.91
0.007
0.009
0.325
0.0007
0.007
0.008
0.408
0.0012
-------
TABLE ;;
FACILITY B1
Suimary o
ible Emissi
1 ^
.0)
Date: 10/29/74 - 10/30/74
Type of Plant: Crushed Stone - Primary Crusher
Type of Discharge: Stack
Location of Discharge: Baghouse
Height of Point of Discharge: 25 ft.
Description of Background: Grey quarry wall
Description of Sky: Clear to cloudy
Mind Direction: Northwesterly
Color of Plume: White
Distance from Ovserver to Discharge Point: 15 ft.
Height of Observation Point: Ground level
Direction of Observer from Discharge Point: West
Wind Velocity: Not available
Detached Plume: No
Duration of Observation: 10/29/74 - 180 minutes
10/30/74 - 234 minutes
SUMMARY OF AVERAGE OPACITY
SUMMARY OF AVERAGE OPACITY
Time
Set Number
10/29/74
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Zl
22
23
24
25
26
27
28
29
30
•10/30/74 ,
31
6
-------
TABLE 13
FACILITY B2
Summary of Results
Run Number
Date
Test Time - Minutes
Production Rate - TPH
Stack Effluent
Flow rate - ACFH
Flow rate - DSCFM
Temperature - °F
Water vapor - Vol. J
Visible Emissions at
Collector Discharge -
% Opacity
Particulate emissions
Probe and filter eaten
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
1 2 3
10/31/74 10/31/74 11/11/74
108 108 108
270 270 270
19684 18921 16487
18296 17638 15681
92.0 96.6 79.0
1.95 1.92 2.01
SEE TABLES 14-23
0.003 0.005 0.003
0.003 0.005 0.003
0.427 0.753 0.457
0.0016 0.0028 0.0017
0.006 0.006 0.007
0.005 0.006 0.007
0.916 0.978 0.955
0.0034 0.0036 0.0035
C-24
Average
-
108
270
18197
17205
87.0
1.96
0.0037
0.0037
0.546
0.0020
0.0063
0.0060
0.946
0.0035
-------
TABLE 14
FACILITY B2
Summary of-Visible Emissions
(Observer 1}
Date: 10/31/74 - 11/1/74
Type of Plant: Crushed Stone - Secondary and Tertiary Crushing and Screening
Type of Discharge: Stack Distance from Observer to Discharge Point: 30 ft.
.Location of Discharge: Baghouse Height of Observation Point: 5 ft.
Height of Point of Discharge: 8 ft. Direction of Observer from Discharge Point: East
Description of Background: Sky
Description of Sky: Clear to partly cloudy
Wind Direction: Southeasterly Wind Velocity: Not available
Color of Plume: White Detached Plume: No
Duration of Observation: 10/31/74 -
240 minutes
11/1/74 -
106 minutes
SUMMARY OF AVERAGE OPACITY
Date
10/31/74
11/1/74
Set Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
21 through
40
41 through
56
1
Start
9:27
9:33
9:39
9:45
9:51
9:57
10:03
10:09
10:15
10:21
10:27
10:33
10:39
10:45
10:51
10:57
11:03
11:09
11:15
11:21
1:09
8:11
Fime
End
9:33
9:39
9:45
9:51
9:57
10:03
10:09
10:15
10:21
10:27
10:33
10:39
10:45
10:51
10:57
11:03
11:09
11:15
11:21
11:27
3:09 '
9:47
Sum
5
10
5
0
5
5
10
5
20
0
0
0
5
5
10
0
5
0
0
10
0
0
Ooaci ty
Average
0.2
0.4
0.2
0
0.2
0.2
0.4
0.2
0.8
0
0
0
0.2
0.2
0.4
0
0.2
0
0
0.4
0
0
Readings ranged from 0 to 5 percent opacity.
C-25
-------
Table 15
FACILITY B2
SUMMARY OF VISIBLE EMISSIONS
Date: 6/30/75
Tyoe of Plant: Crushed stone (limestone)
Tyoe of Discharge: Fugitive
Location of Discharge: Secondary Cone Crusher.(#1)
Hsiflht of Point of Discharge: 25 ft. Distance from Observer to Discharge Point:45 ft.
Oescriotion of Background: Sky & Equipment Height of Observation Point:2 ft.
Ooscrintion of Skv: Clear Direction of Observer from Discharge Point:North
Wind Direction: East Wind Velocity: 5-10 mph
Color of Plume: White . Detached Plume: No
Duration of Observation: 231 minutes
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Min.
23
0
g
or
Opacity
Sec.
0
45
Ocacitv,
Percent
55
60
65
70
75
80
85
90
95
100
Total Time Equal to or
Greater Than Given OnacU'
Min.
Se-
C-26
-------
Tab]* ig
FACILITY B2
SUMMARY OF VISIBLE EMISSIONS
Date: 6/30/75
Tyoe of Plant: Crushed stone (limestone)
Type of Discharge: Fugitive
Location of Discharge: Secondary Cone Crusher
Height of Point of Discharged ft. Distance from Observer to Discharge Point:45 ft.
Descriotion of Background: Sky & Equipment Height of Observation Point: 2 ft.
Description of Sky: Clear Direction of Observer from Discharge Point:North
Wind Direction: East H1r)d Velocitv: 5-10 mph
Color of Plume: White Detached Plume: No
Duration of Observation: 231 minutes
Summary of Data
Ooacity,
Percent
5
10
15
• 20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Min.
0
0
or
Opacity
Sec.
15
0
Onacitv,
Percent
60
65
70
80
85
90
100
Total Time Equal to or
Greater Than Given Onacitv
Sec.
C-27
-------
Table 17
FACILITY B2
SUMMARY OF VISIBLE EMISSIONS
Date: 6/30/75
Fyoe of Plant: Crushed stone (limestone)
Type of Discharge: Fugitive
Location of Discharge: Secondary Cone Crusher
Height of Point of Discharge: 25 ft. Distance from Observer to Discharge .Point: 45 ft.
Oescriotion of Background: Sky & Equipment Height of Observation Point:. 2 ft.
Description of Sky: Clear Direction of Observer from Discharge Point:North
Wind Direction: East Wind Velocitv: 5-10 mph
Color of Plume: White Detached Plume: No
Duration of Observation: 231 minutes
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Sec.
0
0
Ooaci tv,
Percent
55
60
65
70
75
80
85
90
%
100
Total Time Equal to or
Greater Than Given Onacitv
Min. Sec.
C-28
-------
Tab!?? ]8
FACILITY B2
SUMMARY OF VISIBLE EMISSIONS
Date: 6/30/75 - 7/1/75
Tvoe of Plant: Crushed stone (limestone)
Type of Discharge: Fugitive
Location of Discharge:Surge Bin
Height of Point of Discharge: Distance from ^^ to'01scharge
Description of Background:Sky & Equipment Height of Observation Point: 15 ft.
•Description of Sky: Clear nirortfnr, nf nu
Direction of Observer from Discharge Point-SE
«1nd Direction': south Wind Velocity: 5 mph
:olor of Plume: Wh1te ' Detached plume: NQ
)uration of Observation: 6/30/74 - 234 minutes
7/1/75 - 53 minutes
iummary of Data:
Opacity, Total Time Equal to or
Percent Greater Than Given Opacity
ffin._ Sec. '
55
60
65
70
75
80
85
90
95
100
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Nin.
2
1
-
or
Opacity
Sec.
0
15
30
C-29
-------
Table 19
FACILITY B2
SUMMARY OF VISIBLE EMISSIONS
Date: 6/30/75 - 7/1/75
Tyoe of Plant: Crushed stone (limestone)
Tyoe of Discharge: Fugitive
Location of Discharge: Scalping screen
Hsinht of Point of Discharge:50 ft. • Distance from Observer to Discharge Point:150 fl
Descrintion of Background: Sky & Equipment Height of Observation Point:15 ft.
Inscription of Sky: Clear Direction of Observer from Discharge Point: SE
Wind Direction: South Wind Velocity: 5 MPH
Color of Plume: White Detached Plume: no
Duration of Observation: 6/30/75 - 234 minutes
7/1/75 - 53 minutes
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Mi n .
44
9
3
0
-
or
Opacity
Sec.
45
45
0
30
-
Ooacitv, Total Time Equal to or
Percent Greater Than Given Onacitv
Min. Sec.
55
W
65
70
75
80
85
90
%
100
C-30
-------
20
FACILITY B2
SUMMARY OF VISIBLE EMISSIONS
fate: 6/30/75 - 7/1/75
voe of Plant: Crushed stone (limestone)
Type of Discharge: Fugitive
-ocation of Discharge: Hammermi11
leight of Point of Discharge: Distance from Observer to Discharge Point:150 ft
lescriotion of Background: Sky & Equipment Height of Observation Point: 15 ft.
Inscription of Sky: Clear niv-pr-HAn «* ™, * „. '
mrection of Observer from Discharge Point: SE
find Direction: South W1nd Velocitv: 5 mph
olor of Plume: White Detached Plume: No
uration of Observation: 6/30/75 - 234 minutes
7/1/75 - 53 minutes
ummary of Data:
Ooacity,
Percent
5
10
15
'20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Mln.Sec.
0
0
Ooacitv,
Percent
55
60
65
70
75
80
85
90
«J5
100
Total Time Equal to or
Greater Than Given Onacitv
^'n. Sec.
C-31
-------
Tab!ft 21
FACILITY B2
SUMMARY OF VISIBLE EMISSIONS
Date: 7/1/75
Tyoe of Plant: Crushed stone (limestone)
Type of Discharge: Fugitive
Location of Discharge: (3-Deck) Finishing Screen (left)
Height of Point of Discharge: 40
Oescriotion of Background: Hazy Sky
Description of Sky: Clear
Wind Direction: Southeast
Color of Plume: White
Duration of Observation: 107 minutes
Distance from Observer to Discharge Point:75 ft.
Height of Observation Point: Ground level
Direction of Observer from Discharge PointrWest
Wind Velocitv: 5-15 mph
Detached Plume: No
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Mln.Sec.
4 30
Ooacitv,
Percent
55
60
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Onacitv
•Mln. Sec
C-32
-------
Tab!" 22
FACILITY 82
SUMMARY OF VISIBLE EMISSIONS
te: 7/1/75
oe of Plant: Crushed stone (limestone)
pe of Discharge: Fugitive
cation of Discharge: (3-Deck) Finishing screen (right)
ight of Point of Discharge: 40 ft.
scriotion of Background: Hazy sky
scrintion of Sky: Clear
nd Direction: Southeast
lor of Plume: White
ration of Observation: 107 minutes
Distance from Observer to Discharge Point: 75 ft.
Height of Observation Point: Ground level
Direction of Observer from Discharge Point: West
Wind Velocity: 5-15 mph
Detached Plume: No
nmary of Data;
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
-Hi-n. Sec.
0 15
Opacity,
Percent
55
60
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Opacity
11 n. Self:
C-33
-------
Table 23
FACILITY B2
SUMMARY OF VISIBLE EMISSIONS
Date: 6/30/75
Tyoe of Plant: Crushed stone (limestone)
Tyoe of Discharge: Fugitive
Location of Discharge: Two (*3-Deck) finishing screens
Height of Point of Discharge: 50 ft.
Oescriotion of Background: Hazy sky
Oescrintion of Sky: Clear
Wind Direction: Southeast
Color of Plume: White
Duration of Observation: 120 minutes
Summary of Data:
Distance from Observer to Discharge Point: 75 ft.
Height of Observation Point-.Ground level
Direction of Observer from Discharge Point:West
Wind Velocity: 10-15 mph
Detached Plume: No
Ooacity,
Percent
5
T)
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Min.
86
28
5
0
0
-
or
Opacity^
Sec.
15
15
30
15
0
_
'
Opacity,
Percent
55
60
65
70
75
80
85
90
100
Total Time Equal to or
Greater Than Given Ooacitv
Min.
Sec.
C-34
-------
TABLE 24
FACILITY B3
Summary of Results
Run Number
pate
Test Time - Minutes
Production Rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate - DSCFM
Temperature - °F
Water Vapor - Vol. %
Visible Emissions at
Collector Discharge -
* Opacity
Particulate Emissions
Probe and filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch^
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
* 'No analysis of bark-half on in-stack filter tests.
1
10/31/74
270
18674
17335
92
2.13
0.002
0.002
0.355
0.0013
2
11/1/74
270
18405
17186
90
1.73
0.004
0.004
0.614
0.0023
3
11/1/74
270
16238
15466
79
1.87
0.003
0.003
0.411
0.0015
Averac
-
270
17772
16662
87
1.91
0.003
0.003
0.460
0.0017
C-35
-------
Run Number
Date
TABLE 25
FACILITY Cl
Summary of Results
123 Average
11/19/74 11/21/74 11/22/74
Test Time - Minutes
Production Rate - TPH*1*
Stack Effluent
Flow rate - ACFH
Flow rate - DSCFM
Temperature - °F
Water vapor - Vol. I
Visible Emissions at
Collector Discharge -
X Opacity
Parti cul ate Emissions
Probe and filter catch
gr/DSQF
gr/ACF
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
120
7340
7250
66.0
1.0
0.003
0.003
0.18
0.001
0.007
0,007
0.43
0.003
Z4U
7560
7720
38.0
0.4
See table
0.0007
0.0007
0.05
0.0004
0.001
0.001
0.09
0.0008
£
-------
TABLE 25
FACILITY Cl
Summary of Visible Emissions^
Date: 11/21/74
Type of Plant: Crushed Stone - Primary and Secondary Crushing and Screening
Type of Discharge: Stack
Location of Discharge: Baghouse
Height of Point of discharge: 40 ft.
Description of Background: Dark Woods
Description of Sky: Overcast
Wind Direction: Easterly
Color of Plume: White
Duration of Observation: 240 minutes
Distance from Observer to discharge Point: 100 ft.
Height of Observation Point: 50 ft.
Direction of Observer from Discharge Point: N.W.
Wind Velocity: 10 to 30 mi/hr.
Detached Plume: No
SUMMARY OF AVERAGE OPACITY
Time
Set Number
Opacity
Start
End
jum
1 throug.1 40 12:10 4:]0 0
Readings were 0 percent opacity during the observation period.
Sketch Showing How Opacity Varied With Time:
O)
o
-------
Run Number
Date
Test Time - Minutes
TABLE 27
FACILITY C2
Sunroary of Results
123 Average
11/19/74 11/21/74 11/22/74
0)
Production Rate - TPH
Stack Effluent
Flow rate - ACFH
Flow rate - DSCFM
Temperature - °F
Water vapor - Vol. %
Visible Emissions at
Collector Discharge -
X Opacity
Particulate Emissions
Probe and filter catch
gr/DSCF
gr/ACF
Ib/hr
1b/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
(1) Throughput through primary crusher.
120
132
6220
6260
62.0
0.4
0.006
0.006
0.31
0.002
0.008
0.009
0.46
0.003
240
119
6870
6880
50.0
0.3
See Table
0.00003
0.00003
0.002
0.00002
0.0006
0.0007
0.04
0.0003
240
127
6540
6700
51.0
0.1
28
0.0004
0.004
0.02
0.0002
0.0009
0.001
0.05
0.0004
200
126
6543
6613
54.3
0.27
0.00214
0.00214
o.m
0.00074
0.0032
0.0057
0.18
0.0012
C-38
-------
TABLE
FACILITY C2
Sussary cf Visible Emissions
Date: 11/21/74
Type of Plant: Crushed Stone - Finishing Screens
Type of Discharge: Stack
Location of Discharge: Baghouse
Height of Point of Discharge: 40 ft.
Description of Background: Dark woods
Description of Sky: Overcast
o
O)
Q.
O
re
Q.
o
Time, hours
C-39
-------
Run Number
Date
Test Time - Minutes
Production Rate -
Stack Effluent
Flow rate - ACFH
Flow rate - DSCFM
Temperature - °F
Hater vapor - Vol. %
Visible Emissions at
Collector Discharge -
% Opacity
Particulate Emissions
Probe and filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
(1) Throughput through primary crusher.
TABLE 29
FACILITY 01
Summary of Results
1 2 3
9/17/74 9/18/74 9/19/74
Average
240
225
31830
31370
66.0
1.2
0.0095
0.0094
2.55
0.0113
0.0100
0.0096
2.69
G.0120
240
230
31810
30650
71.0
1.7
SEE TABLES
0.0081
0.0078
2.13
0.0093
0.0085
0.0082
2.23
0.0097
240
220
31950
31230
68.0
1.6
30-36
0.0080
0.0078
2.13
0.0097
0.0086
0.0084
2.30
0.0105
240
225
31863
31083
68.3
1.5
0.0085
0.0083
2.27
0.0101
0.0090
0.0088
2.41
0.107
C-40
-------
TABLE 30
FACILITY Ul
Summary of Visible Emissions^'
Oate: 9/17/74
Type of Plant: Crushed Stone - Secondary and Tertiary Crushing 8 Screening
Type of Discharge: Stack
Location of Discharge: Baghouse
Height of Point of Discharge: 55 ft.
Description of Background: Trees
Description of Sky: partiy Cloudy
Wind Direction: Northerly
Color of Plume: None
Duration of Observation: 240 minutes
Distance from Observer to Discharge Point: 300 ft.
Height of Observation Point: 40 ft.
Direction of Observer from Discharge Point: S.E.
Mind Velocity: 5-10 mi/hr.
Detached Plume: No
Set Number
SUMMARY OF AVERAGE OPACITY
Time
En3
Start
(2)
Opacity
Sum Average
1 through 40 9:10 1:00 0 0
Readings were 0 percent opacity during the period of observation.
Sketch Showing How Opacity Varied With Time:
c
w
&
O
•a
a.
O
3_
Time, hours
C-41
-------
Tab!-? 31
FACILITY Dl
SUMMARY OF VISIBLE EMISSIONS
Date: 7/8/75
Tyoe of Plant: Crushed stone (traprock)
Tyoe of Discharge: Fugitive
Location of Discharge: Terti'ary gyrasphere cone crusher (S)
Heiflht of Point of Discharge:
Description of Background: Machinery
Description of Sky: Overcast
Mind Direction: Southwest
Color of'Plume: white
Duration of Observation: 170 minutes
Distance from Observer to Discharge Point: 30 ft.
Height of Observation Point: ground level
Direction of Observer from Discharge Point: West
Wind Velocftv: 0-10 mph
Detached Plume: No
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Hin.Sec.
0
Ooacitv,
Percent
55
60
65
71
75
80
85
90
95
100
Total Time Equal to or
Greater Than Given Onacitv
Min.
Sec.
C-42
-------
Tablo 32
FACILITY Dl
SUMMARY OF VISIBLE EMISSIONS
ate: 7/8/75
/oe of Plant: Crushed stone (traprock)
ype of Discharge: Fugitive
>cation of Discharge: Terti'ary gyrashere cone crusher (N)
2ight of Point of Discharge:
sscriotion of Background: Machinery
sscrintion of Sky: Overcast
ind Direction: Southwest
3lor of Plume: White
uration of Observation: IJQ minutes
Distance from Observer to Discharge Point: sg ft
Height of Observation Point: ground level
Direction of Observer from Discharge Point: West
Wind Velocity: 0-10 mph
Detached Plume:
mmary of Data:
Ooacit.y,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Min.Sec.
0
Opacity,
Percent
55
60
65
70
75
80
85
90
95
100
Total Time Equal to or
Greater Than Given Opacity
Min"! '•
C-43
-------
Table 33
FACILITY Dl
SUMMARY OF VISIBLE EMISSIONS
Date: 7/8/75
Tyoe of Plant: Crushed stone (traprock)
Tyoe of Discharge: Fugitive
Location of Discharge: secondary standard cone crusher
Heiglt of Point of Discharge:
Oescriotion of Background: Machinery
Description of Sky: Overcast
Wind Direction: southwest
Color of Plume: White
Duration of Observation: 170 minutes
Distance from Observer to Discharge Point: 30 ft.
Height of Observation Point:Ground level
Direction of Observer from Discharge Point:West
Wind Velocity: 0-10 mph
Detached Plume: No
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Hin.Sec.
0
Opacity,
Percent
55
60
65
70
75
80
85
90
95
100
Total Time Equal to or
Greater Than Given Onacitv
Min.
Sec.
C-44
-------
Tabl'? 34
FACILITY Dl
SUMMARY OF VISIBLE EMISSIONS
Date: 7/9/75
Tvoe of Plant: Crushed stone (traprock)
Type of Discharge: Fugitive
Location of Discharge: Scalping screen
Height of Point of Discharge:
Oescriotion of Background: Equipment
Description of Sky: Overcast
Wind Direction: Southwest
Color of Plume: white
Duration of Observation: 210 minutes
Summary of Data:
\
Ooacity,
Percent
Distance from Observer to Discharge Point: 30 ft.
Height of Observation Point: 15 ft.
Direction of Observer from Discharge Point: North
Wind Velocitv: 0-10 mph
Detached Plume: No
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Mi n. Sec.
0
0
Ooacitv,
Percent
55
60
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Opacity
Mi n. Sec!'
C-45
-------
Tablft 35
FACILITY Dl
SUMMARY OF VISIBLE EMISSIONS
Date: 7/9/75
Tyoe of Plant: Crushed stone (traprock)
Tyoe of Discharge: Fugitive
Location of Discharge: Secondary (2-Deck) sizing screens
Height of Point of Discharge:
Descriotion of Background: Equipment
Description of Sky: Overcast
Mind Direction: Southwest
Color of Plume: White
Duration of Observation: 210 minutes
Distance from Observer to Discharge Point: 30 ft.|
Height of Observation Point: 15 ft.
Direction of Observer from Discharge Point: North
Wind Velocity: 0-10 mph
Detached Plume: No
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
MTnT Sec.
0
0
Opacity,
Percent
55
60
65
70
75
80
85
90
95
100
Total Time Equal to or
Greater Than Given Onacitv
Min. Sec.
C-46
-------
Tablr? 36
FACILITY Dl
SUMMARY OF VISIBLE EMISSIONS
)ate: 7/9/75
Fyoe of Plant: Crushed stone (traprock)
Fyoe of Discharge: Fugitive
.ocati-on of Discharge: Secondary (3-Deck) sizing screens
leig'-it of Point of Discharge:
tescriotion of Background: Equipment
)escrintion of Sky: Overcast
-------
Run Number
Date
Test Time - Minutes
Production Rate -
Stack Effluent
Flow rate - ACFM
Flow rate - DSCFH
Temperature - °F
Water vapor - Vol. %
Visible Emissions at
Collector Discharge -
X Opacity
Particulate Emissions
Probe and filter catch
gr/DSCF
gr/ACF_.
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
TABLE 37
FACILITY D2
Sunmary of Results
1 2 3
9/17/74 9/18/74 9/19/74
Average
240
225
26790
26200
69.0
1.3
0.0027
0.0027
0.61
0.0027
0.0041
0.0040
0.91
0.0040
240
230
26260
25230
74.0
1.6
See Table
0.0038
0.0036
0 82
0.0036
0.0045
0.0043
0.98
0.0043
240
220
24830
24170
72.0
1.3
38
0.0023
0.0022
0.47
0.0021
0.0031
0.0030
0.64
0.0029
240
225
25960
25200
71.7
1.4
0.0029
0.0028
0.63
0.0028
0.0039
0.0038
0.84
0.0037
(1) Throughput through primary crusher.
C-48
-------
TABLE 38
FACILITY 02
Summary of Visible Emissions^1)
i,ate: 9/18/74
Type of Plant: Crushed Stone - Finishing Screens
Type of Discharge: Stack
Location of Discharge: Baghouse
Height of Point of Discharge: 55 ft.
Inscription of Background: Trees
Description of Sky: Clear
Wind Direction: Northerly
Color of Plume: None
Duration of Observation: 240 minutes
Distance from Observer to Discharge Point: 300 ft.
Height of Observation Point: 40 ft.
Direction of Observer from Discharge Point: North
Wind Velocity: 5 to 10 mi/hr.
Detached Plume: No
Set Number
SUMMARY OF AVERAGE OPACITY
Time
(2)
Start
Opacity
Sum Average
1 through 40 8:30 12:30 0
Readings were 0 percent opacity during period of observation.
Sketch Showing How Opacity Varied with Time:
3
o
ID
Time, hours
C-49
-------
Run Number
Date
Test Time - Minutes
TABLE 39
FACILITY El
Sumnary of Results
1 2 3
11/18/74 11/18/74 11/19/74
0)
Production Rate - TPH
Stack Effluent
Flow rate - ACFH
Flow rate - DSCFH
Temperature - °F
Water vapor - Vol. %
Visible Emissions at
Collector Discharge -
% Opacity
Particulate Emissions
Probe and filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
(1) Throughput through primary crusher.
Average
120
384
15272
16297
33.1
0.5
0.0134
0.0143
1.87
0.0049
0.0170
0.0181
2.37
0.0067
120
342
13997
14796
40,4
0.0
SEE TABLE
0.0116
0.0122
1.47
0.0043
0.0137
0.0145
1,74
0.0051
120
460
14975
15642
41.0
0.5
40
0.0147
0.0154
1.97
0.0043
0.0164
0.0171
, 2.20 .
0.0048
120
395
14748
15578
38.2
0.3
0.0132
0.0140
1.77
0.0045
0.0157
0.0166
2.10
0.0055
C-50
-------
TABLE 40
FACILITY El
»v»\/ ^
Mt J w
1 * t «• I I
late: 11/W74 - 11/19/74
'ype of Plant: Crushed Stone - Tertiary Crushing and Screening
ype of Discharge: Stack
.ocation of Discharge: Baghouse
lelght of Point of Discharge: 1/2 ft.
)escription of Background: Grey Wall
Ascription of Sky: Overcast
lind Direction: Westerly
tolor of Plume: None
.Distance from Observer to Discharge Point: 60 ft.-
Height of Observation Point: Ground level
Direction of Observer from Discharge Point: South
Wind Velocity: 2 - 10 mi/hr.
Detached Plume: No
)uration of Observation: 11/18/74 •? 120 minutes
11/19/74 - 60 minutes
SUMMARY OF AVERAGE OPACITY
Time
Opaci ty
Set Number
11/18/74
1 through 10
11 through 20
11/19/74
21 through 30
Start
9:00
10:15
10:07
End
10:00
11:15
11:07
Sum
0
0
0
Average
0
0
0
Readings were 0 percent opacity during all periods of observation.
Jketch Showing How Opacity Varied With Time:
C-51
-------
TABLE 41
FACILITY E2
Sunmary of Results
Run Number
Date
Test Time - Minutes-
Production Rate - TPH*1J
Stack Effluent
Flow rate - ACFH
Flow rate - DSCFH
Temperature - °F
Water vapor - Vol. X
Visible Emissions at
Collector Discharge -
% Opacity
Parti cul ate Emissions
Probe and filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch
gr/DSCF
gr/ACF
Ib/hr
lb/ ton
(1) Throughput through primary
1
11/18/74
120
384
22169
23001
44.5
1.1
0.0132
0.0137
2.60
0.0068
0.0205
0.0213
4.05
0.0105
crusher.
C-52
2
11/18/74
120
342
19772
19930
59.2
1.1
SEE TABLE
0.0096
0.0097
1.65
0.0048
0.1378
0.0139
2.35
0.0069
3
11/19/74
120
460
21426
21779
55.0
0.6
42
0.0153
0.0155
2.85
0.0062
0.0170
0.0173
3.18
0.0069
Average
-
120
395
21122
21570
52.9
0.9
0.0127
0.0130
2.37
0.0059
0.0171
0.0175
3.19
0.0081
-------
TABLE 42
FACILITY E2
Summary of Visible'Emissions
Sate; 11/16/74 - 11/19/74
Type of Plant: Crushed Stone - Finishing Screens and Bins
(1)
Type of Discharge: Stack
.ocation of Discharge: Baghouse
leignt of Point of Discharge: 1/2 ft.
Ascription of Background: Hillside
tescription of Sky: Clear
Jind Direction: Westerly
;olor of Plume: Hone
Distance from Observer to Discharge Point: 120 ft
Height of Observation Point: Ground level
Direction of Observer from Discharge Point: South
Wind Velocity: 2-10 mi/hr.
Detached Plume: No
Juration of Observation: 11/18/74 - 120 minutes
11/19/74 - 60 minutes
SUMMARY OF AVERAGE OPACITY^
Set Number
IV 18/74
1 through 10
11 through 20
11/19/74
21 through 30
Start
12:50
1:50
9:05
Ti me
End
1:50
2:00
10:05
Opacity
Sum
0
0
0
Averaqe
"X*-
0
0
0
Readings were 0 percent opacity during all periods of observation.
ketch Showing How Opacity Varied With Time:
C-53
-------
Table 43
FACILITY F
SUMMARY OF VISIBLE EMISSIONS
Date: 8/26/76
Tyoe of Plant: Crushed stone (traprock)
Type of Discharge: Fugitive
Location of Discharge: TWO tertiary crushers (#4 and #5)
HMoht of Point of Discharge: #4-20 ft. Distance from Observer to Discharge Point: 100 ft.
J' #5-10 ft.
Descriotion of Background: Gray equipment Height of Observation Point: ground level
Structures
Description of Sky: Partly cloudy Direction of Observer from Discharge Point: West
Wind Direction: Variable
Color of Plume: No visible plume
Duration of Observation^ minutes
Wind Velocity: 0-5 mph
Peta^hed Plume:
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Min.Sec.
0
0
Opacity,
Percent
55
50
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Onacitv
Min.
Sec.
C-54
-------
Tabls 44
FACILITY p
SUMMARY OF VISIBLE EMISSIONS
Date: 8/26/76
Tvoe of Plant: Crushed stone (traprock)
Type of Discharge: Fugitive
Location of Discharge: Four processing screens
Height of Point of Discharge: 50 ft.
Descriotion of Background:gray walls
Description of Sky: Partly cloudy
Wind Direction: Variable
Color of Plume: NO visible plume
Duration of Observation: 180 minutes
Distance from Observer to Discharge Point: 100 ft
Height of Observation Point: ground level
Direction of Observer from Discharge Point: NE
Wind Velocity: 0-5 mph
Detached Plume:
ummary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Hin.Sec.
0
Ooacity,
Percent
55
60
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Opacity
Sec.
C-55
-------
Tabln 45
FACILITY F
SUMMARY OF VISIBLE EMISSIONS
late: 8/27/76
fvoe of Plant: Crushed stone (traprock)
v
fyoe of Discharge: Fugitive
Location of Discharge: Conveyor transfer points
of Point of Discharge: 75 ft. Distance from Observer to Discharge Point: 150 ft.
Oescriotion of Background: Gray equipment Height of Observation Point: 50 ft.
structures
Description of Sky: Overcast
•lind Direction: Variable, S-SE
Color of Plume: No visible plume
Duration of Observation:179 minutes
Direction of Observer from Discharge Point: SE
Wind Velocity: 0-10 mph
Detached Plume:
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Min.Sec.
0
0
Ooacitv,
Percent
55
60
65
70
75
80
85
90
%
100
Total Time Equal to or
Greater Than Given Onacitv
Min.
Sec
C-56
-------
46
FACILITY Gl
SUMMARY OF VISIBLE EMISSIONS
Date: 9/27/75
Tyoe of Plant: Feldspar
Type of Discharge: Fugitive
Location of Discharge: Priraary
Height of Point of Discharge: 10-30 ft. Distance from Observer to Discharge Point: 100 ft
Descriotion of Background: Quarry wall & . Height of Observation Point: Ground level
equipment structures level
Descrintion of Sky: Part]y cloudy Direction of Observer from nischar.- D,-n>f-S
Wind Direction: Northeast
Color of Plume:
Duration of Observation: 60 minutes
Wind Velocity: 0-10 mph
Detached Plume: NO
Summary of Data:
Ooacity,
Percent
5
n
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Hin.
0
45
nnacitv,
Percent
55
60
65
70
75
80
85
90
05
100
Total Tine Equal to or
fire a ter Than Givgn_0 -> a c i t •
Min. S/?c~~~
C-57
-------
Tab!-- 47
FACILITY Gl
SUMMARY OF VISIBLE E'JISSIQ'IS
Date: 9/27/76
Tvoe of Plant: Feldspar
Tyoe of Discharge: Fugitive
Loc.it ion of Discharge: Conveyor transfer point (#1)
Ihiq'it of Point of Discharge: 10 ft.
Oascriotion of Background: Quarry wall
Hoscrintion of Sky: Overcast
'•lind Direction: Northeast
Color of Plune: No plume
Ourvition of Observation: 80 minutes
Distance from Observer to Discharge Point:50 ft.
Height of Observation Point: ground level
Direction of Observer from Discharge Point: SE
Wind Velocitv: 0-5 mph
Detached Plun?: No
ry of Data:
Ooacity,
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Qnacjty_
Min. Sec.
0
0
Onacitv,
Percent
55
60
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Onacitv
Mi n.
Sec.
C-58
-------
Table 48
FACILITY 61
SUMMARY OF VISIBLE EMISSIONS
Date: 9/27/76
Tyoe of Plant: Feldspar
Type of Discharge: Fugitive
Location of Discharge: conveyor transfer point (#2)
Height of Point of Discharge: 40 ft. Distance fro. Observer to Discharge Point- 50 f1
Descriotion of Background: Quarry wall Height of Observation Point: ground level '
Description of s
-------
Table 49
FACILITY Gl
SUMMARY OF VISIBLE EMISSIONS
Date: 9/27/76
Tyoe of Plant: Feldspar
Tyoe of Discharge-.Fugitive
Location of Discharge: Secondary crusher
Height of Point of Discharge: 10-20 ft. Distance from Observer to Discharge Point: 75 ft|
Description of Background: Equipment Height of Observation Point: 75 ft
structure
Description of Sky: Partly cloudy -cloudy Direction of Observer from Discharge Point:$SE
Mind Direction: Northwest
Color of Plume: No visible plume
Duration of Observation: 1 hour
Wind Velocity: 0-7 mph
Detached Plums: N/A
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Min. Sec.
0
Opacity,
Percent
55
60
65
70
75
80
85
90
95
100
Total Time Equal to or
Greater Than Given Onacitv
Mi n.
Sec.
C-60
-------
TaV!.'> 50
FACILITY Gl
Sin,"ARY OF VISIRLE r.'HSS ITI
Date: 9/27/76 '
Tyoe of Plant: Feldspar
Tyoe of Discharge: Fugitive
Location of Discharge: Conveyor transfer Point (#4)
Heiqht of Point of Discharge: 10 ft. Distance from Observer to Discharge Point: 84 ft.
Description of Background: CTiff or wall Height of Observation Point: 75 ft.
Oescrintion of Sky: cloudy
Wind Direction: North-
Color of Plume: No visible plume
Duration of Observation: 84 minutes
Direction of Observer from Discharge Point: SE
Wind Velocity: 0-7 mph
Detached Plume: N/A
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
f-1in. Sec.
0
0
Onacitv,
Percent
55
60
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Onacitv
Mln. Sec.
C-61
-------
Run Number
Date
Test Time-minutes
Production rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate - DSCFM
Temperature - °F
Water vapor - Vol.%
Visible Emissions at
Collector Discharge -
Percent Opacity
Particulate Emissions
Probe and Filter Catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total Catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Table 51
FACILITY G2
Summary of Results
1
9/28/76
120
5070
4210
105
2
9/28/76
120
4830
3940
115
3
9/29/76
120 „
4470
3720
103
Average
120
4790
3960
108
See Tables 52 - 61
0.005
0.004
0.17
0.005
0.004
0.17
0.005
0.004
0.18
0.005
0.004
0.18
0.004
0.004
0.14
0.004
0.004
0.14
O.OUJ
0.004
, 0.16
0.005
0.004
0.16
C-62
-------
Summary of Visible .Emissi
Date: 9/28/76
Ty|je of Plane: Feldspar
Type of Discharge: Outlet Stack
Location of Discharge: No.2 Mill Baghouse
Height of Point of Discharge:100'
Description of Background: trees on hillside
Description of Sky: Overcast
Wind Direction: NW
u)lor of Plume: No visible plume
Duration of Observation: 2-1/4 hours
SUMMARY OF AVERAGE OPACITY
Distance from Observer to Discharq- Point-
Approx. 40'
Height of Observation Point:
Approx. 100'
Direction of Observer from Discharge,>oint: E
Wind Velocity: 0-10 mi/hr
Detached Plume: N/A
SUMMARY OF AVERAGE OPACITY
Set Number
1
2
3
4
5
6
7
8
9
10
11
12
IA
3
14
15
16
I-^
7
18
1 f\
19
20
Time
Start End
09:48 09
09:54 10
10:00 10
10:06 10
10:12 10
10:18 10
10:24 10
10:30 10
10:36 10
10:42 10
10:48 10
10:54 M
11:00 11
11:06 11
11:12 11
:54
:00
:Q6
:18
:24
:30
:36
:42
:48
:54
:00
:06
:12
:18
11:18 11:24
11:24 11:30
11:30 11:36
11:36 11:42
Dpa
Sum
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
11:42 11:48 N
Sketch Showing How Opacity
QJ
O)
a.
~;
city
Average
N
N
N
N
N
N
N
N
N
N
N
N -
N
N
N
N
N
N
N
N
lime
Set Number Start End Sum
21 11:48 11:54 N
22 11:54 12:00 N
23 12:00 12:06 N
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Opacity
Average
N
N.-.
N
Varied With Time:
C-63
-------
TABLE 53
FACILITY G2
Summary of Visible Emissions
«• •
Date: 9/29/76
Type of Plant: Feldspar
Type of Discharge: Outlet Stack
Location of Discharge: No.2 Mill Baghouse
Height of Point of Discharge: T00'
Description of Background: hillside with trees
Description of Sky: Cloudy
Wind Direction: NE Wind Velocity: 0-5 mi/hr
Color of Plume: No visible plume Detached Plume: N/A
Duration of Observation: 2 hrs.
SUMMARY OF AVERAGE OPACITY
Distance from Observer to Discharge Point:
approx. 50'
Height of Observation Point:
same level as discharge -
Direction of Observer from Discharge Point:
SUMMARY OF AVERAGE OPACITY
Time
Time
Opacity
Opacity
Set Number Start End
Sum
Average Set Number Start End Sum Average
1
2
3
4
5
6
7
8
9
10
n
12
13
14
15
16
17
18
19
20
08:35
08:41
08:47
08:53
08:59
09:05
09:11
09:17
09:23
09:29
09:35
09:41
09:47
09:53
09:59
10:05
10:11
10:17
10:23
10:29
08:40
08:46
08:52
08:58
09:04
09:10
09:16
09:22
09:28
09:34
09:40
09:46
09:52
09:58
10:04
10:10
10:16
10:22
10:28
10:34
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
.N
21 10:35 10:37 N N .
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Sketch Snowing How Opacity Varied With Time:
c
CD
u
OJ
a.
-------
TAB Li: 54
FACILITY 62
Summary of Visible Emissions
Date: 9/28/76
Type of Plant: Feldspar
Type of Discharge: Outlet Stack
Location of Discharge: No.2 Mill Baghouse
Height of Point of Discharge: 100'
Description of Background: grassy hillside
Description of Sky: partly cloudy
Wind Direction: NW
Color of Plume: No visible plume
Duration of Observation: approx. 2-1/4 hrs.
SUMMARY OF AVERAGE OPACITY
Distance from Observer to Discharge Point:
Approx. 40' SE
Height of Observation Point: Approx. 100'
Direction of Observer from Discharge Point: SE
Wind Velocity: 0-15 mi/hr
Detached Plume: N/A
SUMMARY OF AVERAGE, OPACITY
pacity
Average
N
N
Set Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Opacity
Start End
14:48 14
14:54 15
15:00 15
15:06 15
15:12 15
15:18 15
:54
:00
:06
: 12
:18
:24
15:24 15:30
15:30 15:36
15:36 15:42
15:42 15:48
15:48 15:54
15:54 16:00
16:00 16:06
16:06 16:
16:12 16:
16:18 16:
16:24 16:
16:30 16:
16:36 16:
12
18
24
30
36
42
16:42 L6:43
Sketch Showing How Opacity
•*->
0)
0
i-
OJ
Q.
^
Sum
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
N
Varied
Average
N
N
N
N
N
N
N
N
N
• • N
N
N
N
N
-. N
N
N
N
N
N
With Time:
Time
bet Number Start End Sun
2J 16:48 16:54 N
22 16:54 17:00 N
90.
25
27
28
29
•an
•31
op
0-3
oo
34
35
OC
OD
37
38
39
40
C-65
-------
Tab!" 55
FACILITY 62
SUMMARY OF VISIBLE EMISSIONS
Date: 9/28/76
Tyoe of Plant: Feldspar
Tyos of Discharge: Fugitive
Location of Discharge: Ball mill (feed end)
Heiqht of Point of Discharge: 20 ft.
Descriotion of Background: Building &
Equipment
Description of Sky: N/A
Wind Direction: N/A
Color of Plume: No visible plume
Duration of Observation: 1 hour
Distance from Observer to Discharge Point: 35 ft.
Height of Observation Point:
Direction of Observer from Discharge Point: N/A
Wind Velocity: N/A
Detached Plume: N/A
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Mi n. Sec.
0
Ooacitv,
Percent
55
60
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Ooacitv
Min.Sec.
C-66
-------
Tab!s 56
FACILITY G2
SUMMARY OF VISIBLE E'lISSIO'-IS
Date: 9/28/76
Tyoe of Plant: Feldspar
Type of Discharge: Fugitive
Location of Discharge: Ball mill (discharge end)
Height of Point of Discharge: 20 ft.
Oescriotion of Background: Building and
Oescriotion of Sky: N/A equi'Pment
Wind Direction: N/A
Color of Plume: NO visible plume
Duration of Observation: i hour
Distance from Observer to Discharge Point: «
Ob
Height of Observation Point:
Direction of Observer from Discharge Point:N/A
Wind Velocity: N/A
Detached Plume: N/A
-.
T L
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Hin.Sec.
•Ooacitv,
Percent
55
60
65
70
75
80
85
90
-------
Table 57
FACILITY G2
SUMMARY OF VISIBLE EMISSIONS
Date: 9/28/76
Tyoe of Plant: Feldspar
Tyoe of Discharge: Fugitive
Location of Discharge: Indoor transfer point (#1)
Height of Point of Discharge:
Distance from Observer to Discharge Point:
Description of Background: Building wall Height of Observation Point:
Description of Sky: N/A
'•find Direction: N/A
Color of Plume: No visible plume
luration of Observation: i hour
Direction of Observer from Discharge Point:
Wind Velocity: N/A
Detached Plume:N/A
>ummary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Min.Sec.
0
0
Onacitv,
Percent
55
60
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Onacitv
Mi n. Sec.
C-68
-------
Tnbl" 58
FACILITY G2
SUMMARY OF VISIBLE EMISSIONS
Date: 9/28/76
Tvoe of Plant: Feldspar
Type of Discharge: Fugitive
Location of Discharge: Indoor transfer point (#2)
Height of Point of Discharge:
Distance fror. Observer to Discharge Point:
Descriotion of Background: Building wall Height of Observation Point:
Description of Sky: N/A
Wind Direction: N/A
Color of Plume: No visible plume
Duration of Observation: 1 hour
Direction of Observer from Discharge Point:.N/A
Wind Velocity: N/A
Detached Plune: N/A
Summary of Data:
Ooacit.y,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Onacitv,
Percent
55
60
65
70
75
80
85
90
H5
100
Total Time Equal to or
Greater Than Given Onacitv
" '
C-69
-------
FACILITY G2
SUMMARY OF VISIBLE EMISSIONS
Date: 9/28/76
Tyoe of Plant: Feldspar
Tyoe of Discharge: Fugitive
Location of Discharge: Indoor Bucket Elevator
H2iqlit of Point of Discharge: Distance from Observer to Discharge Point:
Description of Background: Building walls Height of Observation Point:
Description of Skv: N/A Direction of Observer from Discharge Point: N/A
Wind Direction: N/A Wind Velocity: N/A
Color of Plume: NO visible plume Detached Plume: N/A
Duration of Observation: l hour
Summary of Data:
Ooacity,
Percent
5
T)
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Min.Sec.
0
0
Onacitv,
Percent
55
60
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Onacit
Min.
Sec.
C-70
-------
Tab!ft go
FACILITY G2
SUMMARY OF VISIBLE EMISSIONS
Date: 9/28/76
Tvoe of Plant: Feldspar
Type of Discharge: Fugitive
Location of Discharge: Truck loading
Height of Point of Discharge: 15 ft.
Description of Background: Building wall
Description of Sky: N/A
Wind Direction: N/A
Color of Plume: N/A
Duration of Observation: 13 minutes
Summary of Data:
Ooacity,
Percent
Distance from Observer to Discharge Point: 30 ft
Height of Observation Point: ground level
Direction of Observer from Discharge Point- c
"* . * .. £.
Wind Velocity: N/A
Detached Plume: N/A
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Min.' Sec.
0 n
-Opacity,
Percent
55
60
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given bnac'itv
Min. Sec.—
071
-------
Tab!ft 61
FACILITY 62
SUMMARY OF VISIBLE EMISSIONS
Date: 9/28/76
Tyoe of Plant: Feldspar
Type of Discharge: Fugitive
Location of Discharge: Railroad car loading
Height of Point of Discharge: 15 ft.
Descriotion of Background: Building wall
Description of Sky: Cloudy
Mind Direction: N/A
Color of Plume: N/A
Duration of Observation: 32 minutes
Distance from Observer to Discharge Point: 25 ft.
Height of Observation Point: ground level
Direction of Observer from Discharge Point: E
Wind Velocity: N/A
Detached Plume: N/A
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Min;Sec.
5
0
15
0
Opacity,
Percent
55
60
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Onacitv
Min.
Sec.
C-72
-------
Tabls 62
FACILITY HI
SUMMARY OF VISIBLE EMISSIONS
Date: 10/27 - 28/76
Tyoe of Plant: Gypsum
Type of Discharge: Fugitive (leaks)
Location of Discharge: Hammermill
Height of Point of Discharge: Leaks Distance from Observer to Discharge Point: 25 ft.
Descriotion of Background:inside plant Height of Observation Point: ground level
Description of Sky: N/A Direction of Observer from Discharge Point: $W
Wind Direction: N/A Wind Velocity: N/A
Color of Plume: White Detached Plume: N/A
Duration of Observation: 298 minutes
Summary of Data:
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Min.
1
0
0
-
or
Opacity
Sec.
45
15
0
Opacity, Total Time Equal to or
Percent Greater Than Given Onacitv
Min. Sec.
55
60
65
70
75
80
85
90
05
100
C-73
-------
Data
Test Time-minutes
Production rate - TPH
Stack Effluent
Flov/ rate - ACFM
Flow rate - DSCFM
Temperature - °F
'.•later vapor - Vol.*
Visible Emissions at
Collector Discharge -
Percent Opacity
Particulate Emissions
Proba and Filter Catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total Catch
gr/DSCF
gr/ACF
Ib/hr
l.b/ton
Table 63
FACILITY H2
Summary of :'.csi;!':s
1
10/27/76 10/27/76 10/28/76
88 88 88
4,548
3,542
145.4
4.6
0.071
0.055
2.16
0.073
0.057
2.53
4,364
3,486
147.0
1.8
See Table 64
0.063
0.050
1.87
0.064
0.051
2.40
4,306
3,423
145.3
2.6
0.066
0.053
1.94
0.068
0.054
2.65
Average
88
0.067
0.053
1.99
0.068
0.054
2.53
C-74
-------
TAB If: 64
FACILITY H2
Summary of Visible Emissions
Date: 10/27/76
Type of Plant: Gypsum board manufacturer
Type of Discharge: Stack
Location of Discharge: Above plant roof
Distance from Observer to Discharge Point: 25 ft.
Height of Observation Point: roof level .
Height of Point of Discharge: 6' above roof Direction of Observer from Discharge Pointr
225° (S.W.)
Description of Background: Sky
Description of Sky: Clear
Wind Direction: 0° (N)
Color of Plume: White
Duration of Observation: 87 Min
SUMMARY OF AVERAGE OPACITY
Wind Velocity: ~ 10 mph
Detached Plume: No
SUMMARY OF AVERAGE OPACITY
Set Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Sketch
1
Start
1312
1357
1403
1409
1415
1421
1427
1433
1439
1445
1451
1457
1503
1509
1515
Showing
-M
C
0)
J_
o>
o.
£
•f—
o
jOQ
:00
:00
:00
:00
:00
:00
:00
:00
:00
:00
:00
:00
:00
:00
How
ime
End
1316:
1402:
1408:
1414:
1420:
1426:
1432:
1438:
1444:
1450:
1456:
1502:
1508:
1514:
1519:
Opacity
45
45
45
45
45
45
45
45
45
45
45
45
45
45
05
Opacity
Sum
125
155
135
150
140
125
135
130
125
115
95
70
80
85
60
Varied
Average
6
6
5
6
5
5
5
5
5
4
3
2
3
3
3
With
.25
.46
.62
.25
.83
.21
.62
.42
.21
.79
.96
.92
.33
.54
.53
Time:
Time Opacity
Set Number Start End Sum Average
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
C-75
-------
TABLE 64 (con't)
FACILITY H2
Summary of Visible Emissions
Date: 10/27/76
Type of Plant: Gypsum board manufacturer
Type of Discharge: Stack
Location of Discharge: Above plant roof
Distance from Observer to Discharge Point:25 ft.
Height of Observation Point: roof level
Height of Point of Discharge: 6' above roof Direction of Observer from Discharge Point:
225 (S.W.J
Description of Background: Sky
Description of Sky: Clear
Wind Direction: 45° (N.E.)
Color of Plume: White
Duration of Observation: 92 min.
SUMMARY OF AVERAGE OPACITY
Wind Velocity: - io-15 mph
Detached Plume: NO
SUMMARY OF AVERAGE OPACITY
Time
Set Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Start
0830 :QO
0836:00
0842:00
0848:00
0957:00
1003:00
1009:00
1015:00
1021:00
1027:00
1033:00
1039:00
1045:00
1051:00
1057:00
1103:00
1109:00
End
0835:45
0841:45
0847:45
0849:00
1002:45
1008:45
1014:45
1020:45
1026:45
1032:45
1038:45
1044:45
1050:45
1056:45
1102:45
1108:45
1110:45
Opacity
Sum
45
65
70
5
125
60
80
85
.75
70
85
95
90
90
70
55
25
Average
1.87
2.71
2.92
1.00
5.21
2.50
3.33
3.54
3.12
2.92
3.54
3.96
3.75
3.75
2.92
2.29
3.12
Time Opacity
Set Number Start End Sum Average
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Sketch Showing How Opacity Varied With Time:
c
CJ
u
i_
o
o.
C-7fi
-------
TABLF 64 (con't)
FACILITY H2
Summary of Visible Emissions
Date: 10/28/76
type of Plant: Gypsum board manufacturer
Type of Discharge: Stack Distance from Observer to Discharge Point: 25 ft-
.ocation of Discharge: Above plant roof Height of Observation Point: roof level
teight of Point of Discharged1 above roof Direction of Observer from Discharqp Point-
225° (S.W.) ' "
description of Background: Sky
Ascription of Sky: Clear
Jind Direction: 180° (S)
)o1or of Plume: White
Jurat ion of Observation: 87 min
Wind Velocity: ~ 10 mph
Detached Plume: No
let Number
1
2
3
4
5,
6
7
8
9
10 .
11
12
13
14
15
16 ,
17
18
19
20
bUIW
1
Start
0830:00
0930:00
0936:00
0942:00
0948:00
0945:00
1000:00
1006:00
1012:00
1018:00
1024:00
1030:00
1036:00
1042:00
1048:00
„
\KY OF AV
Tine
End
0835:45
0935:45
0941 :45
0947:45
0953:45
0959:45
1005:45
1011:45
1017:45
1023:45
1029:45
1035:45
1041:45
1047:45
1050:45
ERAGE
OPACITY
Opacity
Sum
40
95
85
65
70
60
90
40
30
25
40
60
25
70
10
Average
1.67
3.96
3.54
2.71
2.92
2.50
3.75
2.50
1.25
1.04
1.67
2.50
1.04
2.92 '
0.83
Set Number
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
SUMMARY OF AVERAGE OPACITY
Time Opacity
Start End Sum Average
~
ketch Showing How Opacity Varied With Time:
OJ
u
-------
Tab!* 65
FACILITY I
SUMMARY OF VISIBLE EMISSIONS
Oate: 9/30/76
Tyoe of Plant: Mica "
Tyoe of Discharge: Fugitive
Location of Discharge: Bagging Operation
Heiflht of Point of Discharge: 3 ft.
Oescriotion of Background: Indoors
Doscrintion of Sky: N/A
Wind Direction: N/A
Color of Plume: N/A.
Duration of Observation: 1 hour
Summary of Data:
Ooacity,
Percent
Distance from Observer to Discharge Point: 7 ft.
Height of Observation Point: ground level
Direction of Observer from Discharge Point: N/A
Wind Velocity: N/A
Detached Plume: N/A
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
RTruSec.
0
0
Opacity,
Percent
55
60
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Onacitv
Mi n. Sec.
C-78
-------
Tab!ft 66
FACILITY Jl
SUMMARY OF VISIBLE EMISSIONS
Date: 10/20 - 21/76
Tyoe of Plant: Talc
Type of Discharge: Fugitive (leaks)
Location of Discharge: Vertical mill
Height of Point of Discharge: In room
Descriotion of Background: ceiling
Description of Sky: N/A
Wind Direction: N/A
Color of Plume: White
Duration of Observation: 90 minutes
Summary of Data:
„ Ooacity,
Percent
Distance from Observer to Discharge Point: 10 ft.
Height of Observation Point: Floor
Direction of Observer from Discharge Point:W
Wind Velocity: ^/A
Detached Plume: N/A ';
5
10
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Min.Sec.
Onacitv,
Percent
55
60
65
70
75
80
85
90
H5
100
Total Time Equal to or
Greater Than Given Onacitv
Min.
Sec.
C-79
-------
Table 67
FACILITY Jl
SUMMARY OF VISIBLE EMISSIONS
Date: 10/20/76
Tvoe of Plant: Talc
Type of Discharge: Fugitive
Location of Discharge: Primary crusher
Height of Point of Discharge: In room
Oescriotion of Background: wall
Description of Sky: N/A
Mind Direction: N/A
Color of Plume: White
Duration of Observation: go minutes
Summary of Data:
Distance from Observer to Discharge Point: 5 ft
Height of Observation Point: Floor
Direction of Observer from Discharge Point:w
Wind Velocity: N/A
Detached Plume: N/A
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Min.
20
8
1
0
or
Opacity^
Sec.
15
0
15
Opacity,
Percent
55
<50
65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given Onacltv
Min.
Sec.
C-80
-------
Tablr? 68
FACILITY Jl
SUMMARY OF VISIBLE EMISSIONS
Date: 10/20 - 21/76
Tyoe of Plant: Talc
Type of Discharge: Fugitive
Location of Discharge: Secondary crusher
Height of Point of Discharge: jn room
Descriotion of Background: wall
Description of Sky: N/A
Wind Direction: N/A
Color of Plume: White
Duration of Observation: 150 minutes
Summary of Data:
Distance from Observer to Discharge Point: 5 ft.
Height of Observation Point: floor
Direction of Observer from Discharge Point:s
Wind Velocity: N/A
Detached Plume: N/A
Ooacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Mi n .
3
0
0
~
or
Opacity
Sec.
45
15
0
~
•Opacity, Total Time Equal to or
Percent Greater Than Given Onacitv
Mln. Sec .
55
+j j
60
65
70
75
80
85
90
05
TOO
C-81
-------
Tab!* 69
FACILITY Jl
SUMMARY OF VISIBLE EMISSIONS
Oate: 10/19 - 21/76
Tyoe of Plant: Talc
Tyoe of Discharge: Fugitive
Location of Discharge: Bagger
Height of Point of Discharge: In room
Oescriotion of Background: wall
Description of Sky: N/A
Wind-Direction: N/A
Color of Plume: White
Duration of Observation: 150 minutes
Summary of Data:
Distance from Observer to Discharge Point: 10 ft.|
Height of Observation Point: floor
Direction of Observer from Discharge. Point: W
Wind Velocity: N/A
Detached Plume: N/A
Opacity,
Percent
5
10
15
20
25
30
35
40
45
50
Total Time Equal to
Greater Than Given
Hin.
12
5
3
2
2
2
1
1
1
1
or
Opacity
Sec.
45
15
0
15
0
0
30
30
15
15
Opacity,
Percent
55
60
-65
70
75
80
85
90
05
100
Total Time Equal to or
Greater Than Given
Min.
0
0
0
0
0
_
Opacity
Sec.
45
45
15
15
0
—
C-82
-------
Tabls 70
FACILITY Jl
SUMMARY OF VISIBLE EMISSIONS
Date: 10/19/76
Tyoe of Plant: Ta-|c
Type of Discharge: Fugitive
Location of Discharge: pebble Mill No. 2
Height of Point of Discharge: in room
Description of Background: Wall
Description of Sky: N/A
Wind Direction: N/A
Color of Plume: white
Duration of Observation: 90 minutes
Summary of Data:
Opacity,
Percent
Distance from Observer to Discharge Point: lo ft.
Height of Observation Point: floor
Direction of Observer from Discharge Point:w
Wind Velocity: N//\
Detached Plume: N/A
5
n
15
20
25
30
35
40
45
50
Total Time Equal to or
Greater Than Given Opacity
Mi n. Sec.
5
0
0
0
45
0
•Opacity,
Percent
55
SO
65
70
75
80
85
90
95
100
Total Time Equal to or
Greater Than Given Opacity
sec.
C-83
-------
Run Jtober
Date
Test Tirce-fflinutes
Production rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate - OSCFH
Temperature - °F
Hater vapor - Vol.%
Visible Emissions at
Collector Discharge -
Percent Opacity
Particulate Emissions
Probe and Filter Catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total Catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Table 71
FACILITY J2
iry of Results
1 2
10/20/76 10/20/76
120 120
21 ,100 21 ,300
20,200 20,200
80 83
0.3 . 0.3
See Table 72
0.047 0.068
0.045 0.065
8.17 11.8
0.065 0.071
0.062 0.067
11.2 12.2
3
10/21/76
120
21 ,300
19,500
82
1.0
0.067
0.061
11.2
0.068
0.062
11.3
- Average
120
21,200
20,000
82
'0.5
0.061
0.057
10.4
0.068
0.064
11.6
C-84
-------
TABLF: 72
FACILITY J2
Summary of Visible Emissions
Date: 10/21/76
Type of Plant: Talc
Type of Discharge: Stack
Location of Discharge: Baghouse Outlet
Height of Point of Discharge:30'
Description of Background: Hills and trees
Description of Sky: Overcast - rain
Wind Direction: 60° NE
Color of Plume: White
Duration of Observation: Approx. 2 hrs.
SUMMARY OF AVERAGE OPACITY
Distance from Observer to Discharge Point:
approx. 100'
Height of Observation Point:
approx. 36'
Direction of Observer from Discharge Point:
160° SE
Wind-Velocity: 8_12 mi/hr - Gust up to 20
Detached Plume: N/A
SUMMARY OF AVERAGE OPACITY
Set Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20 *
T
Start
08:00
08:06
08:12
08:18
08:24
08:30
08:36
08:42
08:48
08:54
09:00
09:06
09:12
09:18
09:24
09:30
09:36
09:42
09:48
09:-54
ime
End
08:06
08:12
08:18
08:24
08:30
08:36
08:42
08:48
08:54
09:00
09:06
09:12
09:18
09:24
09:30
09:36
09:42
09:48
09:54
10:00
Opacity
Sum
10
0
0
5
0
5
5
0
0
0
5
10
15
5
5
5
5
0
5
5
Average
0.4
0
0
0.2
0
0.2
0.2
0
0
0
0.2
0.4
0.6
0.2
0.2
0.2
0.2
0
0.2
0.2
Time Opacity
Set Number Start End Sum
21 10:00 10:05 0
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Average
0
Sketch Showing How Opacity Varied With Time:
GJ
O
-------
TABLE 72 (con't)
FACILITY J2
Summary of Visible Emissions
Date: 10/20/76
Type of Plant: Talc
Type of Discharge: Stack
Location of Discharge: Baghouse Outlet
Height of Point of Discharge: 30'
Description of Background: Hills and trees
Description of Sky: Overcast - Rain
Wind Direction: 290° NW
Color of Plume: White
Duration of Observation: 2:05 min.
.: SUMMARY OF AVERAGE OPACITY
Distance from Observer to Discharge Point: 100'
Height, of Observation Point:approx. 36'
Direction of Observer from Discharge Point:
160° SE
Wind Velocity: 4-7 mi/hr
Detached Plume: N/A
SUMMARY OF AVERAGE OPACITY
Opacity
Time
Opacity
ime
Set Number Start End. Sum Average Set Number Start End Sum Average
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20 •
12:54
13:00
13:06
13:12
13:18
13:24
13:30
13:36
13:42
13:48
13:54
14:00
14:06
14:12
14:18
14:24
14:30
14:36
14:42
14:48
13:00
13:06
13:12
13:18
13:24
13:30
13:36
13:42
13:48
13:54
14:00
14:06
14:12
14:18
14:24
14:30
14:36
14:42
14:48
14:54
0
0
0
5
5
10
5
5
15
15
5
0
5
0
5
0
5
5
0 '
0
0
0
0
0.2
0.2
0.4
0.2
0.2
0.6
0.6
0.2
0
0.2
0
0.2
0
0.2
0.2
0
0
21 14:54 14:59 0 0
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Sketch Showing How Opacity Varied With Time:
O)
o
O)
C-86
-------
TABLC 72 (con't)
FACILITY J2
Summary of Visible Emissions
Date: 10/20/76
Type of Plant: Talc
Type of Discharge: Stack
Location of Discharge: Baghouse Outlet
Height of Point of Discharge: 30'
Description of Background: Hills and trees
Description of Sky: Overcast
Wind Direction: 290° NW
Color of Plume: White
Duration of Observation: 2:22 min.
SUMMARY OF AVERAGE OPACITY
Distance from Observer to Discharge Point:
approx. 100'
Height of Observation Point:
approx. 36'
Direction of Observer from Discharge Point:
160 SE
Wind Velocity: 4-7 mi/hr
Detached Plume: N/A
SUMMARY OF AVERAGE OPACITY
Time
Set Number
1
2
3
4
5
6
7
8
9
10
n
12
13
14
15
16
17
18
19
20
Start
08:35
08:41
08:47
08:53
08:49
09:05
09:11
09:17
09:23
09:29
09:35
09:41
09:47
. 09:53
09:59
10:05
10:11
10:17
10:23
10J29
End
08:41
08:47
08:53
08:59
09:05
09:11
09:17
09:23
09:29
09:35
09:41
09:47
09:53
09:59
10:05
10:11
10:17
10:23
10:29
10:35
Opacity
Sum
0
5
5
5
5
5
10
5
5
5
0
10
0
0
5
5
10
5
0
10
Average
0
0.2
0.2
0.2
0.2
0.2
0.4
0.2
.0.2
0.2
0
0.4
0
0
0.2
0.2
0.4
0.2
0
0.4
Set Number
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Time Opacity
Start End Sum Average
10:35 10:41 5 0.2
10:41 10:47 5 0.2 .
10:47 10:53 10 0.4
10:53 10:58 5 0.25
Sketch Showing How Opacity Varied With Time:
c
o
a.
•*
>,
C-87
-------
Test Tiria-firinutes
Production rate - TPH
Stack Effluent
Fle'i rate - ACFM
Flow rate - G5CFM
Temperature - °F
Hater vapor T Vol.%
Visible Emissions at
.;Col lector Discharge -
Percent Opacity
% * t V
Particiilate -Enilsslons
Table 73
FACILITY K
jry of Insults
1 2
6/21/77 6/21/77
120 120
4,567 4,113
3,637 3,196
135.3 152.3
1.69 1.36
See Table 74
0.024 0.027
0.020 0.022
0.75 0.75
3
6/22/77
120
4,579
3,646
136.8
1.63
0.041
0.034
1.29
Average
120
4,420
3,493
141.5
1.56
Prohs and Filter Catch
' gr/DSCF • ' •
gr/ACF*
Ib/hr
Tb/ton
Total Catch
gr/DSCF
gr/ACF
Ib/hr '
Ib/ton
0.024 0.027 0.041 0.031
0.020 0.022 0.034 0.025
0.75 0.75 1.29 0.93
- - -
C-88
-------
TABLE 74
FACILITY K
Summary of Visible Emissions
Date: 6/20 - 6/21/71
Type of Plant: Talc
Type of Discharge: Stack
Location of Discharge: Pebble mill
Height of Point of Discharge: 40 ft.
Description of Background: Equipment and Mountain
Description of Sky: Clear
Distance from Observer to Discharge Point: 125 ft,
Height of Observation Point:25 ft.
Direction of Observer from Discharge Puint: W
Wind Direction: North
Color of Plume: White
Duration of Observation:
Wind Velocity: 5 mph
Detached Plume: N/A
SUMMARY OF AVERAGE OPACITY
Opacity
Time
SUMMARY OF AVERAGE OPACITY
Opacity
lime
Set Number Start End Sum Average Set Number Start
End
Sum Average
1
2
3
4
5
6
7
8
9
10
n
12
1 O
13
1 C
15
16
17
18
19
20
1314
1320 '
1326
1332
1338
1344
1350
1356
1402
1408
1417
1423
1429
1435
1441
1447
1453
1459
1505
1511
1320
1326
1332
1338
1344
1350
1356
1402
1408
1414
1423
1429
1435
1441
1447
1453
1459
1505
1511
1517
80
10
5
10
10
0
5
0
5
5
5
5
5
10
5
0
0
5
0
10
3.33
0.42
0.21
0.42
0.42
0.0
0.21
0.0
0.21
0.21
0.21
0.21
0.21
0.42
0.21
0.0
0.0
0.21
0.0
0.42
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
802
808
814
820
826
832
838
844
850
856
903
909
915
921
927
933
939
945
951
957
808
814
820
826
832
838
844
850
856
902
909
915
921
927
933
939
945
951
957
1003
10
5
5
30
0
0
40
75
50
65
35
20
55
25
55
55
30
55
70
40
0.42
0.21
0.21
1.25
0.0
0.0
1.67
3.13
2.;08
2.32
1.46
0.83
2.29
1.04
2.29
2.29
1.24
2.29
2.92
1.67
Sketch Showing How Opacity Varied With Time:
O)
u
Ol
O-
C-89
-------
TABLE 74 (con't)
FACILITY K
Summary of Visible Emissions
Date: 6/20 - 6/21/71
Type of Plant: Talc
Type of Discharge: Stack
Location of Discharge: Pebble Mill
Height of Point of Discharge: 40 ft.
Description of Background: Equipment and Mountain
Description of Sky: Clear
Wind Direction: North Wind Velocity: 5 mph
Color of Plume: White Detached Plume: N/A
Duration of Observation:
Distance from Observer to Discharge Point:125 ft]
Height of Observation Point: 25 ft.
^
Direction of Observer from Discharge Point: W
SUMMARY OF AVERAGE
Time
Set Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Start
1004
1208
1214
1220
1226
1232
1238
1244
1250
1256
1302
1313
1319
1325
1331
1337
1343
1349
1355
HOI
End
1009
1214
1220
1226
1232
1238
1244
1250
1256
1302
1308
1319
1325
1331
1337
1343
1349
1355
1401
1407
OPACITY
Opacity
Sum
30
105
no
85
90
125
85
105
95
25
65
95
105
40
30
60
55
35
5
75
Average
1.25
4.38
4.58
3.54
3.75
5.21
3.54
4.38
3.96
1.32
2.95
3.96
4.38
1.67
1.30
2.61
2.29
1.94
0.36
3.13
SUMMARY OF AVERAGE OPACITY
Time Opacity
Set Number Start End Sum
21 1407 1413 125
22
23
24
25
26
27
28
29
30 .
31
32
33
34
35
36
37
38
39
40
Average
5.21
Sketch Sftowing How Opacity Varied With Time:
o
o
o.
C-90
-------
Run Number
Date
Test Time - Minutes
Production Rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate- DSCFM
Temperature - °F
Water vapor - Vol . %
Visible Emissions at
Collector Discharge -
% Opacity
Parti cul ate Emissions
Probe and Filter catch
gr/DSCF
9r/ACF
Ib/hr
Ib/ton
TABLE 75
FACILITY LI
Summary of Results
1*
12/6/78
60
17180
14040
136
7.4
4.53
545
Total catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
* Test conducted concurrently with Run 2, Table 76.
(1) No analysis of back-half on in-stack filter tests,
C-91
-------
Run Number
Date
Test. Time - Minutes
Production Rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate- DSCFM
Temperature - °F
Water vapor - Vol . %
Visible Emissions at
Collector Discharge -
% Opacity
Parti oil ate Emissions
Probe and Filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total
TABLE 76
FACILITY LI
Summary of Results
1
12/6/78
96
2* 3 Average
12/6/78 12/6/68
96 96 " 96
17690
14790
131.
7.0
see
Table
77
17960
14650
141.
7.8
-
18060
15080
141.
5.4
-
17903
14840
138
6.7
-
0.020
0.017
2.49
0.012
0.010
1.54
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
*Test conducted concurrently with Run 1, Table 75.
(1) No analysis of back-half on in-stack filter tests,
0.016 0.016
0.013 0.013
2.01 2.01
C-92
-------
TABLE 77
FACILITY LI
Summary of Visible Emissions
Date: 12/6/78
Type of Plant: Clay Processing
Type of Discharge: Stack Distance from Observer to Discharge Point: 7 ft.
Location of Discharge: Baghouse Height of Observation Point: 80 ft.
Height of Point of Discharge: 80 ft. Direction of Observer from Discharge Point: South
Description of Background: Green Pine Forest
Description of Sky: Blue
Wind Direction: Northwest Wind Velocity: 5 mi/hr.
Color of Plume: White Detached Plume: No
Duration of Observation: 90 minutes
SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
Start
1400
1406
1412
1418
1424
1430
1436
1442
1448
1454
1500
1506
1512
1518
1524
Time
End
1406
1412
1418
1424
1430
1436
1442
1448
1454
1500
1506
1512
1518
1524
1530
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Opacity
Average
0
0
o
0
0
0
0
0
n
\j
0
n
w
o
\J
o
o
0
C-93
-------
Run Number
Date
Test Time - Minutes
Production Rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate- DSCFM
Temperature - °F
Water vapor - Vol . %
Visible Emissions at
Collector Discharge -
% Opacity
Parti cul ate Emissions
Probe and Filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total
TABLE 78
FACILITY 12
Summary of Results
1
12/6/78
56
• 8550
6960
134
7.9
see
Table
82
1.76
1.43
105.
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
(1) No analysis of back-half on in-stack filter tests.
C-94
-------
Run Number
Date
Test Time - Minutes
Production; Rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate- DSCFM
Temperature - °F
Water vapor - Vol. %
Visible Emissions at
Collector Discharge -
% Opacity
Particulate Emissions
Probe and Filter catch
gr/DSCF
gr/ACF
Ib/hr
lb/ton
TABLE 79
FACILITY L2
Summary of Results
1 2
12/5/78 12/5/78
120 120
Total catch
(1)
0.010
0.008
0.73
0.005
0.004
0.38
gr/DSCF
gr/ACF
?b/hr
Ib/ton
(1) No analysis of back-half on in-stack filter tests.
3 Average
12/6/78 - ,
120 120
9780
8120
129
8.4
see
Table
80
9830
8150
123
9.4
see
Table
81
10340
8560
136
6.7
see
Table
82
9983
8277
129
8.2
—
0.007 0.007
0.006 0.006
0.48 0.53
C-95
-------
TABLE 80
FACILITY 12
Summary of Visible Emissions
Date: 12/5/78
ff
Type of Plant: Clay
Type of Discharge: Stack Distance from Observer to Discharge Point: 25 ft.
Location of Discharge: Baghouse Height of Observation Point: 100 ft.
Height of Point of Discharge: 100 Ft. Direction of Observers from Discharge Point: Southeast
Description of Background: Clear Blue
Description of Sky: Clear Blue
Wind Direction: East Wind Velocity: 5-10 mi/hr.
Color of Plume: White Detached Plume: Yes
Duration of Observation: approx. 120 minutes
SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Start
0953:00
0959:15
1005:45
1011:45
1018:15
1024:15
1030:15
1037:00
1044:00
1048:00
1054:15
1100:15
1106:15
1112:15
1118:30
1124:30
1131:00
1137:00
1143:15
1149:30
1156:30
Opacity Set Time Opacity
End
0959:15
1005:45
1011:45
1018:15
1024:15
1030:45
1037:00
1039:00
1048:00
1054:15
1100:15
1106:15
1112:15
1118:30
1124:30
1131:00
1137:00
1143:15
1149:30
1156:30
1202:30
Sum Average Number Start End bum Average
120
120
120
120
120
120
100
80
120
120
120
120
120
120
120
120
120
120
115
no
5 21 1202:30 1203:00 10 5
5
5
5
5
5
4.2
3.3
5
5
5
5
5
5
5
5
5
5
4.8
4.6
C-96
-------
TABLE 81
FACILITY 12
Summary of Visible Emissions
Date: 12/78
Type of Plant: Clay
Type of Discharge: Stack
Location of Discharge: Baghouse
Distance from Observer to Discharge Point: 25 ft.
Height of Observation Point: 100 ft.
Height of Point of Discharge: 100 ft.Direction of Observer from Discharge Point: South
east
Description of Background: Clear Blue
Description of Sky: Clear Blue :
Wind Direction: East Wind Velocity: 5-10 mi/hr.
Color of Plume: White Detached Plume: Yes
Duration of Observation: 128 minutes
SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Start
1357
1403
1409
1415
1421
1427
1433
1439
1445
1451
1457
1503
1509
1515 '
1521
1527
1533
1539
1545
1551
Opacity Set Time Opacity
End
1403
1409
1415
1421
14?7
1433
1439
1445
1451
1457
1503
1509
1515
1521
1527
1533
1539
1545
1551
1557
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average Number Start End Sum Average'
0 21 1557 1603 0 0
0 22 1603 1605 '. • 0 0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
C-97
-------
TABLE 82
FACILITY L2
Summary of Visible Emissions
Date: 12/5/78
Type of Plant: Clay
Type of Discharge: Stack
Location of Discharge: Baghouse
Distance from Observer to Discharge Point: 25 ft.
Height of Observation Point: 100 ft.
Height of Point of Discharge: 100 ft.Direction of Observer from Discharge Point: South)
east
Description of Background: Clear Blue
Description of Sky: Clear Blue
Wind Direction: East Wind Velocity: 5-10 mi/hr.
Color of Plume: White Detached Plume: Yes
Duration of Observation: approx. 120 minutes
SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
18
20
Time
Start
1050
1056
1102
1108
1114
1120
1126
1132
1138
1144
1152
1158
1204
1210
1216
1222
1228
1234
1240
1246
End
1056
1102
1108
1114
1120
1126
1132
1138
1144
1150
1158
1204
1210
1216
1222
1228
1234
1240
1246
1251
Opacity
Set Time
Sum Average Number Start End
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0 •
0
0
0
0
0
0
0
0
0
0
0
0
0
Opacity
Sum Average
C-98
-------
Run Number
Date
Test Time - Minutes
Production Rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate- DSCFM
Temperature - °F
Water vapor - Vol. %
Visible Emissions at
Collector Discharge -
% Opacity
Particulate Emissions
Probe and Filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total
TABLE 83
FACILITY Ml
Summary of Results
1 2
6/14/78 6/15/78
120 120
0.001
0.001
0.01
0.001
0.001
0.02
gr/DSCF
.gr/ACF
Ib/hr
Ib/ton
(1) No analysis of back-half on in-stack filter tests,
3 Average
6/15/78
120 120
1840
1620
124
2.8
see
Table
84
1490
1300
121
4.1
see
Table
85
1560
1360
124
4.2
see
Table
86
1630
1427
123
3.7
-
0.007 0.003
0.006 0.003
0.09 0.04
C-99
-------
TABLE 84
FACILITY Ml
Summary of Visible Emissions
Date: 6/14/78
Type of Plant: Clay
Type of Discharge: Stack
Location of Discharge: Baghouse
Height of Point of Discharge:
Description of Background: Sky
Description of Sky: Partly cloudy
Wind Direction: NNE
Color of Plume:
Duration of Observation: 151 minutes
Distance from Observer to Discharge Point: 90 ft.
Height of Observation Point: 35 ft.
Direction of Observer from Discharge Point: East
Wind Velocity: 10 mi/hr.
Detached Plume:
SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Start
1538
1544
1550
1556
1602
1608
1614
1620
1626
1632
1638
1644
1650
1656
1702
1708
1714
1720
1726
1732
End
1544
1550
1556
1602
1608
1614
1620
1626
1632
1638
1644
1650
1656
1702
1708
1714
1720
1726
1732
1738
Opacity
Sum Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set
Number
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Time
Start
1738
1744
1750
1756
1802
1808
End
1744
1750
1756
1802
1808
1809
Opacity I
Sum Average 1
0
0
0
0
0
0
o
o
o
o
o
0
C-100
-------
• TABLE 85
FACILITY Ml
Summary of Visible Emissions
Date: 6/15/78
Type of Plant: Clay
Type of Discharge: Stack
Location of Discharge: Baghouse
Height of Point of Discharge:
Description of Background: Sky
Description of Sky: cloudy
Wind Direction: NNE
Color of Plume:
Duration of Observation: 134 minutes
Distance from Observer to Discharge Point: 90 ft.
Height of Observation Point: 35 ft.
Direction of Observer from Discharge Point: East
Wind Velocity: 10 mi/hr.
Detached Plume:
SUMMARY OF AVERAGE OPACITY
Set
Numbc
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
jr Start
913
919
925
931
937
943
949
955
TOO!
1007
1013
1019
1025
1031 -
1037
1043
1049
1055
1101
1107
End
919
925
931
937
943
949
955
1001
1007
1013
1019
1025
1031
1037
1043
1049
1055
1101
1107
1113
Opacity
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0 '
Set Time Opacity
Number Start
21 1113
22 1119
23 1125
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
End Sum Average
1119 0 0
1125 0 0
1127 0 0
C-101
-------
TABLE 86
FACILITY HI
Summary of Visible Emissions
Date: 6/15/78
Type of Plant: Clay
Type of Discharge: Stack
Location of Discharge: Baghouse
Height of Point of Discharge:
Description of Background: Sky
Description of Sky: cloudy
Wind Direction: NNE
Color of Plume:
Duration of Observation: 183 minutes
Distance from Observer to Discharge Point: 90 ft.
Height of Observation Point: 35 ft.
Direction of Observers from Discharge Point: East
Wind Velocity: 10 mi/hr.
Detached Plume:
SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Start
1332
1338
1344
1350
1356
1402
1442
1448
1454
1500
1506
1512
1518
1524
1530
1536
1542
1548
1554
1600
Opacity
End
1338
1344
1350
1356
1402
1408
1448
1454
1500
1506
1512
1518
1524
1530
1536
1542
1548
1554
1660
1606
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Q
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set Time
Number Start End
' 21 1605 1608 '
1625 1629
22 1629 1634
24
25
26
27
28
29
30
31 .
32
33
34
35
36
37
38
39
40
Opacity
Sum Average
0 0
0 0
C-102
-------
TABLE 87
FACILITY M2
Summary of Results
Run Number
Date
Test Time - Minutes
Production Rate - TPH
Stack Effluent
Flow rate - ACFM
Flow rate- DSCFM
Temperature - °F
Water vapor - Vol. %
Visible Emissions at
Collector Discharge -
% Opacity
Parti culate Emi ss ions
Probe and Filter catch
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
Total catch
(1)
1
6/14/78
120
2580
2100
183
1.1
see
Table
88
0.002
0.002
0.03
2
6/15/78
120
2460
2090
151
1.7
see
Table
89
0.002
0.002
0.04
3
6/15/78
120
2450
2100
150
1.6
see
Table
90
0.001
0.001
0.02
Average
-
120
2497
2097
161
1.5
*•
0.002
0.002
0.03
gr/DSCF
gr/ACF
Ib/hr
Ib/ton
(1) No analysis of back-half on in-stack filter tests,
C-103
-------
TABLE 88
FACILITY M2
Summary of Visible Emissions
Date: 6/14/78
Type of Plant: Clay
Type of Discharge: Stack
Location of Discharge: Bag'house
Height of Point of Discharge:
Description of Background: Sky
Description of Sky: Partly cloudy
Wind Direction: NNE
Color of Plume:
Duration of Observation: 30 minutes
Distance from Observer to Discharge Point: 90 ft.
Height of Observation Point: 85 ft.
Direction of Observer from Discharge Point: East
Wind Velocity: 10 mi/hr.
Detached Plume:
SUMMARY OF AVERAGE OPACITY |
Set Time
Number Start End
1 1528 1534
2 1534 1540
3 1540 1546
4 1546 1552
5 1552 1558
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Opacity
Sum Average
0 0
0 0
0 0
0 0
0 0
Set Time
Number Start End
21
22
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
Opacity
Sum "Average!
"I
C-104
-------
TABLE 89
FACILITY M2
Summary of Visible Emissions
Date: 6/15/78
Type of Plant: Clay
Type of Discharge: Stack
Location of Discharge: Baghouse
Height of Point of Discharge:
Description of Background: Sky
Description of Sky: cloudy
Wind Direction: NNE
Color of Plume:
Duration of Observation: 128 minutes
Distance from Observer to Discharge Point: 90 "ft.
Height of Observation Point: 85 ft.
Direction of Observer from Discharge Point: East
Wind Velocity: 10 mi/hr.
Detached Plume:
SUMMARY OF AVERAGE OPACITY
Set
Numbi
,
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
?r Start
850
856
902
908
914
920
926
932
938
944
950
956
1002
1008 „
1014
1020
1026
1032
1038
1044
End
856
902
908
914
920
926
932
938
944
950
956
1002
1008
1014
1020
1026
1032
1038
1044
1050
Opacity
Sum
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set Time Ooacitv
Number Start
21 1050
22 1056
23
24
25
26
27
28
29
30
31
32
33
34
35
36
37
38
39
40
End Sum Average
1056 0 0
1058 - 0 0
C-105
-------
TABLE 90
FACILITY M2
Summary of Visible Emissions
Date: 6/15/78
Type of Plant: Clay
Type of Discharge: Stack
Location of Discharge: Baghouse
Height of Point of Discharge:
Description of Background: Sky
Description of .Sky: Partly cloudy
Wind Direction: : NNE
Color of Plume:
Duration of Observation: 139 minutes
Distance from Observer to Discharge Point: 90 ft.
Height of Observation Point: 85 ft.
Direction of Observers from Discharge Point: East
Wind Velocity: 10 mi/nr.
Detached Plume:
SUMMARY OF AVERAGE OPACITY
Set
Number
1
2
3
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Time
Start
1359
1405
1411
1417
1423
1429
1435
1441
1447
1453
1459
1505
1511
1517
1523
1529
1535
1541
1547
1553
End
1405
1411
1417
1423
1429
1435
1441
1447
1453
1459
1505
1511
1517
1523
1529
1535
1541
1547
1553
1559
Opacity
Sum Average
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
0
Set Time Opacity
Number Start End Sum Average
21 1559 1605 0 0
22 1605 1611 0 0
23 ' 1611 1617 0 0
24 1617 1618 0 0
25
26
27
28
29
30
31
32 '
33
34
35
36
37
38
39
40
C-106
-------
TABLE 91
FACILITY N
Summary of Results of Fugitive. Emission Tests performed
on three separate rail car loadings
Accumulated Accumulated
Observation observation emission % Emission
area period time (AET/AOP x 100)
(mi n: sec) (mi n: sec)
1.
A.
B.
C.
A
B
C
A
B
C
A
B
C
Designation
144:32
144:32
144:32
99:45
99:45
99:45
154:20
154:20
154:20
Test #1
22:42 •
17:30
0:00
Test #2
18:50
2:06
0.00
Test #3
63:42
0:20
9:21
15.7
12.1
0
18.9
2.1
0
41.3
0.2
6.1
— _
of observation positions
Loading hose
West end of
East end of
shed
shed
C-107
-------
TABLE 92
SUMMARY OF METHOD 22 RESULTS - FACILITY P
Time
peri od
Observed time
(minutes)
Percent of time
with visible emissions
Observer
Test point 5, Final screens, 10/3/79
1035-1055 20
1105-1125 20
1130-1150 20
Test point 7, Transfer point, 10/3/79
1324-1424 . 60
0
0
C-108
-------
TABLE 93
METHOD 9 - 6-MINUTE AVERAGES*
FACILITY P
Run
TP-1
Primary
Crusher
Observer
3 4
1
2
3
4
5
6
7
8
9
10
n
12
13
14
15
16
17
18
19
20
9
7
14
14
13
11
12b
7C
-
9
11
10
13
8
10
10
8
13
11
15
17
11
11
11
10
13
10
15
18
10
8
10
11
5
TP-4 TP-6
Impact Cone
Crusher Crusher
Observer Observer
34 34
15 10 4
11 7 5
11 7 9
n 10 n
n 10 9
10 8 10
10 13 9
n 13 7
13 10 10
n 9 8
8
13
7
8
8
1
0
0
0
1
n
18
22
25
23
17
16
15
15
16
15
21
13
13
15
4
2
1
1
4
Values reported in percent opacity.
34-minute average
"5-minute average
C-109
-------
TABLE 94
SUMMARY OF METHOD 22 RESULTS - FACILITY Q
Time Obse
period - (m
Test point 2, Initial screens
1010-10409
0820-0856
Test point 3, Transfer point,
0851-0921a
0931-1001a
wi
iv*\/^H "f"im*s
> I V Cvl U I MIC
linutes)
, 10/10/79 - 10/11/79
30 '
30
10/10/79
30
30
Percent of time
th visible emissions
Observer "
1
34
4
27
64
2
65
7
31
67
Test point 5, Secondary screens, 10/8/79
0848-0918
0940-1010
1015-1045
1057-1127
Test point 7, Final screens,
1250-1320
1330-1400
1407-1437
1451-1521
30
30
30
30
10/8/79
30
30
30
30
0
0
0
<1
0
0
0
0
0
0
0
0
0
0
0
0
a"Red Rock" material. Not processed under representative conditions. Data
omitted.
c-no
-------
TABLE 95
METHOD 9 - 6-MINUTE AVERAGES9
FACILITY Q
Run
1
2
3
4
5
6
7
8
9
10
n
12
13
14
15
16
17
18
19
20
21
TP-1 TP-6
Primary crusher Cone crusher
Observer
3
11
11
6
12
12
3
2
1
2
1
1
1
2
3
3
3
2
2
1
1
4
11
14
8
18
17
5
9
4
8
6
6
7
8
12
TO
6
6
5
2
3
Observer
3
15
18
18
17
10
. 15
19
20
23
24
28
26
28b
25
28
29
27C
27
29
26
25C
4
12
17
19
19
12'
18
19
21
23
23
24
26
28b
23
28
26
26^
29
34
38
39C
Values reported in percent opacity.
4-minute average.
c5-minute average.
c-m
-------
TABLE 96
SUMMARY OF METHOD 22 RESULTS - FACILITY R
Time Observi
period (min
Test point 1, Initial screens
0720-0750
0800-0830
0840-0910
0920-0941 )
0722-0732 |
Test point 3, Transfer point,
0731-0801
Percent of time
with visible emissions
cU U 11116
utes)
10/12/79, 10/15/79
30
30
30
30
10/16/79
30
Observer
-*
1
2
1
2
2
6
2
1
<1
T
4
12
Test point 4, Secondary screens, 10/16/79
0907-0937
0945-1015
1035-1105
1310-1340
Test point 6, Final screens,
1020-1050
1055-1125
1130-1200
1303-1333
Test point 7A, Transfer point
1610-1640
1646-1716
Test point 7B, Transfer point
1415-1445
1455-1525
30
30
30
30
10/15/79
30
30
30
30
, 10/15/79
30
30
, 10/16/79
30
30
5
1
42a
5
0
0
0
0
0
0
0
4
15
1
4a
10
0
0
0
0
6
0
0
4
Data omitted - wind interference.
C-112
-------
TABLE 97
METHOD 9 - 6-MINUTE AVERAGES3
FACILITY R
Run •
1
2
3
4
5
6
7
8
9
10
11
12 .
13
14
15
16
17
18
19
20
TP-2 TP-5
Primary crusher Cone crusher
Observer
3
14
16
16
16
12
9
13
9
13
12
17
9
14
13
15
8
6
7
10
9
4
13
14
14
9
13
15
14
14
15
13
16
13
11
12
13
9
6
9
11
12
Observer
3
8
9
9
12
13
11
13
12
13
12
12
10
9
7
8
12
13
11
11
12
4
12
14
17
15
15
15
16
14
16
14
17
17
17
10
15
10
11
11
11
11
Data reported in percent opacity.
C-113
-------
TABLE 98
SUMMARY OF METHOD 22 RESULTS - FACILITY S
Time Obs
period (
Test point 2, Initial Screens
1516-1546
1558-1628
1100-1130
1302-1332 v
Percent of time
with visible emissions
ci VcU U Mile
minutes)
, 10/24/79
30
30
30
30
Observer
1
0
0
0
0
2
0
0
0
0
Test point 4, Secondary screens, 10/22/79, 10/23/79
1108-1138
1143-1158
0745-0805
0810-1840
0845-0915
Test point 6, Transfer point,
1257-1327
1335-1350
1338-1353
1355-1425
1433-1503
Test point 7, Transfer point,
0750-0820
0826-0856
0915-0945
0955-1025
30
15
15
30
30
10/23/79, 10/24/79
30
15
15
30
30
10/25/79
30
30
30
30
1-
1
1
1
1
0
0
0
0
0
0
0
0
0
10
13
5
6
7
0
1
0
0
0
0
0
0
0
C-114
-------
TABLE 99
METHOD 9 - 6-MINUTE AVERAGES*1
FACILITY S
TP-3
TP-1
Run
Primary
crusher
Observer
1
2
3
4
5
6
7
8
9
10
n
12
13
14
15
16
17
18
19
20
3
2
1
1
1
1
1
1
<1
0
1
1
0
0
0
2
1
3
3
2
0
4
1
2
1
0
1
3
2
1
2
1
1
0
0
1
2
0
2
3
1
1
4-1/2
in.
Cone crusher
Observer
3
3
4
4
2
4
6
6
3
2
5
4
5
3
5
5
4
3
3
3
1
4
3
4
5
3
3
4
4
2
2
3
3
5
2
4
3
2
0
2
1
2
TP-5
5-1/2
in.
Cone crusher
Observer
3
0
0
3
5
4
10
11
14
11
13
n
n
12
8
10
12
9
6
7
5~
4
0
2
5
5
4
9
9
10
10
10
n
10
15
9
12
12
TO,
9
11
9
Data reported in percent opacity.
C-115
-------
TABLE 100
SUMMARY OF METHOD 22 RESULTS - FACILITY T
Time
period
Test point 2, Transfer
1353-1427
1428-1458
1533-1603
1125-1155
Test point 3, Initial
1300-1330
1336-1406
1412-1542
1450-1520
Test point 5, Storage
0755-0825
1023-1053
0908-0938
0947-1017
Observed time
(minutes)
point, 10/26/79, 10/29/79
30
30
30
30
screens, 10/29/79, 10/30/79
30
30
30
30
bin, 10/29/79, 10/30/79
30
30
30
30
Percent of time
with visible emissions
Observer
1 2
0 1
4 2
3 1
2 0
0 0
0 0
0 0
0 0
0 0
0 0
0 0
0 0
C-116
-------
TABLE 101
METHOD 9 - 6-MINUTE AVERAGES9
FACILITY T
TP-1 TP-4
Primary crusher Cone crusher
Run,
T
2
3._
4
5
6
7
8
9
10
11
12
13
14
15
16
17
18
19
20
Observer
3
4
6
9
3
5
10
4
9
8
7
8
8
8
13
10
13
10
9
10
6
4
8
7
8
3
5
8
3
5
7
7
8
8
6
8
6
8
5
4
6
5
Observer
3
18
21
22
23
19
17
20
15
15
15
16
6
10
17
19
18
15
16
18
13
4
15
14
14
15
13
n
13
8
8
9
6
7
11
16
16
15
15
13
16
14
*Data reported in percent opacity.
C-117
-------
Table 102 and Figures 2 through 6 represent visible emission data given in
this Appendix, on a basis of percent of total time of recorded visible emissions
(e.g., in a Method 22 format) and on a basis of how opacity varied with time
(e.g., in a Method 9 format). These observations were executed for fugitive
emissions. The use of Method 22, as it applies to the proposed standard for
non-metallic mineral processing plants would be applicable to all fugitive non-
crushing sources of dust. This test would also be employed to check the effec-
tiveness of a capture system, if used, at any process facility. Method 9
would be used for measurement of all crusher-related sources of dust. A des-
cription of each of the process facilities listed in Table. 102 is given at the
beginning of this Appendix.
Data-for 64 observation periods of visible emissions readings covering
54 process facilities at 14 non-metallic processing plants is given in Table
102. All facilities observed were fugitive emission discharges from uncontrol-
led, hooded or wet suppression controlled facilities.
C-118
-------
i —
co
1 1 1
I-LJ
O
cc.
o
co
UJ
5 *
!_.
1
u_
•z.
o
u_
co
j—
UJ
s:
VISIBLE EMISSIONS MEASURE!
1C MINERALS PLANTS
U 1
«^
^ r^
• v>
V J= E
a.
•0 i
J +31/7
a ai
i ° 3
U !n E
O -i •
0)
i
•o •?
5 ** ^-»
3
3 IB C
••-
in
2*"
T3
in
)
01
U
e
o.
s.
U
*J
c
o.
0 fl CM
O •* CO
O O IO
<• «r vo
CM CM —1
Baghouse discharge to conveyor
Primary impact crusher discharge
Conveyor transfer point
in
r^
§
0)
c
0
c Ja is
'a. o> c
•5 ? 8
O 3 QJ
(/> t/> t/)
in
!**•
«— 1
0)
c
2
(A
i
r—
^
in
0
CO
0 O O
o o o
CO CO OO
CM CM CM
Secondary cone crusher No. 2
Secondary cone crusher No. 3
Hanmer mill
«• O CM
r*x
«*• 0 U>
OO
O O CM
i-4 r-4 i— 1
3-deck finishing screen (L)
3-deck finishing screen (R)
Two 3-deck finishing screens
in
^!>
S
o
o
£;
No. 1 tertiary gyrasphere
cone crusher
in
^^
0?
%
S
in
01
^
in
o
0
O 0
0 0
1
_ o
1—1 1— 1
No. 2 tertiary gyrasphere
cone crusher
Secondary standard cone crusher
o o o
o o o
o o o
t-4 rH f— *
CM CM CM
Scalping screen
Secondary (2-deck) sizing screen
Secondary (3-deck) sizing screen
;
i
0 0
O O
in Q
m CO'
Two tertiary crushers
Four processing screens
,0
^*
IO
CO"
y
-2
0.
1
U.
o
o
O\
5
Conveyor transfer points
'
•o
-------
r — _^
O)
G
•r—
+2
O
O
*•»-•
CVJ
O
LU
_J
CQ
f3-
i
1- Ol
**SS
**-*!- O
O tA *t—
•i- V)
+J > t/>
111
0) X
0.
-oi
Q) .,-._*.
-M -M U)
fO 0)
i— C 4->
ill
3 ut'i
u ••-—
«£ E
Ol
1
tj +J
•S c"in
(O O Ol
1— 1- 4J
§4-> 3
ro c
o t« E
U 0)^_-
*C in
•8
•Jj
•r-
U
tn
0)
u
s
O-
o^
01 in
*->
^^
u
o
ce
c
IO
Q.
oocMoooooooom 1-1 o ocMcoo>r-» CM CM 10
i-l CM i-4
ooi-«oooooooom CM o oo^-coio i^cMcn
CM •— 1 i-4
S^^ ^D CO ^f C3 <"^ C3 ^^ C3 f) CM CO ^3 **" ^ ^3 C3 CO CO ^" Crt *^
coioiocoioioioiovoi-^co en 10 cncnmmcn ^cniD
CM !—!•—* i— 1 i-4
^.
•-« CM "51-
• • • i-l CM
O O O
z z z ^o o e>
•M •*-> 4J C Z Z
c c cat s-
o o o ^- QJ c: c 4->
O.O. O. *O Ot *r- f- IO
c s- o o >
i-t- u 4- ai in *^
cc.caca)'r-u-<<-+->o>-o 10 •— jc 3 t3
ro4->k +J (OlOOTJt— ^- CL E t- r— r—
O >> r~ r^* k !• 3 « >r-
t-S. Ct-i— 1— 4J4->J3O1-E r— C E t- i-HCMrO
ooxraoir-'r* r-io a>4>«(a 10
>,5,C-T3>,EE!-I-'- 0 t- C uC-Ol-IU 04J-M4J
OJOinscoi ooo.^ qj'r-'r-foccijr— i/tinin
>>Eo>i—r-oooui— £ en -»J E o 01 ja i— ai ai a>
CCi-OCf— i— -OTJTJ3-1- E 0) J-.f-UOt.O ••-(— 1— 1—
ooi^aiOflSioccczL-ra o.cocoo. ce
vo 10
10 I^N 10 r^ co
p*. ^«» r^« "^» i*^
r% CM o CM r~
51 o- ^ 0* Si
Ot I— 1 Cf» 1-1 i-H
<_
10
°" .^
•a in to u F—
r— Q. O r- O
ai >s *r> IO (O
iZ c? £ f- x:
C3 Z •-. 0 Z
*
^_,
•o
O)
3
•r—
4_>
O
O
C-120
-------
, —
0)
Z3
••«
j %
o
o
rf"S
Car
^^»
Ul
J
^i
t—
0. -(->
TJ
-
IB 4->
l?l
3 O> •*->
O U)
U -O
<£ O
Crtf-
0^
2 Jo
Q» *t-
*£
Hi in
4->
o
Q) TJ
O. Ol
•iS1!/)
Q)
-tt U
o o
o E"
(X 0.
^
IB
Q.
in
O
in
in
•r—
Q)
IB
^•^
in
O)
-M
c
1
^, ^
IA
.at
4->
3
.c
c
^M*
*
0
0
0
<£>
c
at
C
U
in
£
IB
^O
C
o
i/>
en
CM
O
0
jQ
c
2
J—
—
V
CM
O
CM
l/>
c
at
t.
o
i/i
VI
v>
at
i-
Q-
at
at
j_
JZ
H-
S
O
^^
O
00
at
^
•^
_i
TJ
at
SL
>
i.
oc.
*-
V
-
o
CM
in
c
•I™1
o
a.
at
in
c
IB
^
^J
§
1—
"S-
o
o
CM
I/I
O)
at
S-
u
tn
in
in
at
o
O
s_
a.
o
i—
S
co
CM
O
'~
f1 >^
10
at
•r»
c
IB
S-
to
TJ
at
C"
in
i
1/5
O
—
v
O
CM
in
c
o
a.
<2?
in
c
IB
S-
§
j—
O CM O
O CO O
*
o o o
CM CM CM
C 4->
S -^
t. 0 C
O Q. -i-
in JD
S_
1/1 at at
in <^- o
Lt C L.
O IB O
S_ S- -U
Q- t— CO
ff
CM
O
*~
a.
«^_^
at
c
o
+j
i/i
at
F
•^
_i
TJ
a>
JC
in
s-
t-
.
in
Ql
C
(0
at
s-
j *
in
at
en
-C
JZ
•r- ^
5 »B -*J
r— C
fc. Q. (B
at i —
> >i Q-
at IB at
-Q O S
O T- (B
E IB L.
2-4J 0
OO O.
II II
+J ^~* ^~.
-------
in
CO
ffl
(M
UI
UJ
V)
(D
:;
^x
*;
C\J
UJ
w
CM
CM
O
tu
ui
w
m
CM
00
CM
CD
CO
O
01 -•-»
> en
.
CO CL
CU =5
J3 (/)
E •*-*
£1
"-v-
in O
4->
£= CO
0) E
co >>
tO J2
o>
E <->
tl
u_
(LI I
O
CVJ
(U
en
C-122
-------
O
2
o
u
(M
K
U
in
o>
o
CT>
c
LU
(O
CM
CM
111
UJ
o
o -4->
•4-> CD
3 T3
<*- i-
O
t3 O
Q) (J
r- (O
*> O
C •<-
'O W
o in
>
Ol jQ
cS"
-------
u
2
o
**
c
u
U
2
o
CM
J-
UJ
O
CJ
CD
'AllOVdO
CM
in "O
3 O
i- .£=
O 4->
OJ
to
O)
CO i-
3 O
4- O
o
"O to
"o o
S- •!-
o cu
o s-
Q.
•)-> Q.
CO 3
tU CO
E (U
g 3
4- <4-
O
(/)
•(-> in
c s=
QJ (O
E O)
E
co ja
ns
QJ —
E on
c >>
o -M
•f— •!—
CO i —
CO T-
•i- O
E co
O) U_
XI ra
•r- c:
) O
4_ +J
O CO
u
3 O
I/O CO
«3-
CJ
-------
O
o.
o
o
I.
Q.
£L
O
0
a.
x'V I-
^S. Ill
'X I W -
**
(O
10
a
c
UJ
LU
CO
<0
CM
CM
O CO
'AilDVdO
CM
i- O
u ^r
>> a)
s- 5:
to
T3 <
C 0.
C UJ
O
O) O
C
•£> -5
CD O
3 CJ
M- O
re
-o —-
U1
O)
S-
*
S-
1/1 _Q
OJ -—
E 00
!.$
U1 i—
tO -r-
•r— O
E re
Q} ''
I
OJ >,
(/> O
'> '-13
fD
M- 4->
O (/)
00
ID
I
3
CD
C-125
-------
<6
®
U>
10
UJ
CD"CJ
c o
o <
>)LU
(O O
•
O CD
„ o
CD •
a> o
> u
CD
3 C
*»- o
T3 (/)
0) CO
i— a;
r— S-
o a.
S- Q-
O -P
O)
-Q O
E co
o c
S- ro
M- QJ
CD
E — • -
cu co
C (O
o u_
•r- I
CO >,
CO S-
•r- to
E -a
a> c
o
CO
O r-
ra u
CO CO
VO
O)
CD
C-126
-------
APPENDIX D
EMISSION MEASUREMENT AND CONTINUOUS MONITORING
D.I EMISSION MEASUREMENT METHODS
For participate matter and visible emissions measurements from stacks,
EPA relies primarily upon Methods 5 and 9, which have been established as
reference methods. The emission data from the non-metallic industry may
be obtained using these reference methods as prescribed in the Federal
Register. In addition, as the particulate concentrations are expected to
be independent of temperature for this industry, Method 17 (in-stack
filtration) is an acceptable particulate sampling method.
The one serious problem encountered during the testing of stacks in
the non-metallic minerals industry was the low concentration levels of
particulate. Some emissions tests resulted in particulate catches of less
than 10 mg corresponding to 0.0005 gr/dscf. An EPA laboratory study showed
that because of positive biases from the "clean-up" blank, results from
tests where low concentration levels are encountered are biased toward the
high side. This bias was no more than a factor of two for particulate
catches down to 8 mg.
Data from an EPA report, "Additional Studies on Obtaining Replicate
Particulate Samples From Stationary Sources," by William J. Mitchell,
indicate that particulate catches of about 50 mg are adequate to insure an
error of no more than 10 percent. Lower levels were not studied. Based on
theoretical calculations, particulate weights as small as 12 mg were
estimated to be sufficient to insure an error no greater than 10 percent.
D-l
-------
D.2 MONITORING SYSTEMS AND DEVICES
The effluent streams from the non-metallic industry sources are at
essentially ambient conditions. The visible emissions monitoring
instruments found adequate for power plants would be applicable for this
industry. These systems are covered by EPA performance standards contained
in Appendix B of 40 CFR Part 60.
Equipment and installation costs are estimated to be $18,000 to
$20,000 and annual operating costs, including data recording and reduction,
are estimated at $8,000 to $9,000.
D.3 PERFORMANCE TEST METHODS
Either Method 5 or 17 for particulate matter is recommended as the
performance test method. Due to low concentrations sometimes encountered,
a minimum sample volume must be established to insure adequate amounts of
particulate matter are collected to minimize recovery errors. This
particulate catch amount is preferably 50 mg, but should be at least 25 mg.
It is also recommended that sampling trains with higher sampling rates, which
are allowed by Method 5 and are commercially available, be used to reduce
•sampling time and costs.
Sampling costs for a test consisting of three particulate runs,
the number normally specified by performance test regulations, is estimated
to be about $5,000 to $7,000. This estimate is based on sampling site
modifications and testing being conducted by contractors. If in-plant
personnel are used to conduct the test, the costs will be somewhat less.
Since the outlet gas streams from control devices used in this
industry are generally well contained, no special sampling probelms are
anticipated.
D-2
-------
SUPPLEMENT A
ECONOMIC IMPACT ANALYSIS FOR PORTABLE PLANTS.
A.O Introduction and Summary
After the preparation of Section 8, Economic Impact, of the background
information document9 comments were received from the crushed stone and
sand and gravel industries concerning the impact analysis conducted for
portable plants. Specifically, they commented that the costs of controlling
portable processing plants with baghouses are substantially higher than
those for fixed processing plants. The reasons given for the higher costs
are the regular movement of the plants and the changes made in the operating
configuration of the plants. Since these issues were not addressed in the
original analysis, this analysis was prepared.
Because portable plants are used primarily in the crushed stone and
sand and gravel industries, the impacts on these plants were evaluated by
developing a Discounted Cash Flow (DCF) analysis for each model new plant
size in these industries. DCF is an investment decision analysis which
shows the economic feasibility of a planned capital investment project over
the life of the project.
The DCF analysis was conducted by using conservative assumptions.
Assumptions used include:
• the total of NSPS control costs were incremental costs; i.e.,
that there are no SIP control costs that the plant would have to
incur in the absence of NSPS control.
9 the plants operate at 1250 hours per year through the life of the
project.
0 NSPS control cost pass through is limited by competition of
existing plants in the same industry which do not have to meet
the NSPS.
• the new plant operates as a separate business entity and cannot
- expect to finance the control from another business activity or
parent firm.
S-l
-------
For new plants, the DCF analysis indicated that the 68 and 135 Mg/hr
(75 and 150 ton/hr) portable plants in both industries are likely to be
precluced by an NSPS. The DCF model was unable to determine a clear positive
or negative investment decision for the 270 Mq/hr (300 ton/hr) portable
plants in both industries. However, in view of the conservative assumptions
used, they were judged to be economically feasible. All of the ottier plant
sizes in the two industries are likely to be economically feasible after the
promulgation of the NSPS.
S-2
-------
A.I INDUSTRY CHARACTERIZATION
A.1.1 General Profile
Portable mineral processing plants (portable plants) are used primarily
by sand and gravel processors and crushed stone processors. The United
States Geological Survey estimates that there were 3,285 portable plants in
the sand and gravel industry-and 1,232 portable plants in the crushed stone
industry in 1978. Portable plants account for 53 percent of total existing
plants in the sand and gravel industry and 42 percent of total existing
plants in the crushed stone industry.
Based on industry data, portable plants account for 40 to 50 percent of
total annual mine output for the sand and gravel industry2'3 and 30 to 40
percent of total annual mine output for the crushed stone industry.4'5 .In
1978, this amounted to 340-425 million megagrams (375-469 million tons) of
sand and gravel and 260-347 million megagrams (287-382 million tons) of
crushed stone.
The clay, gypsum, and pumice industries also use portable plants. How-
ever, these plants are used for specialized small output crushing operations
which amount to an insignificant portion of total mine output for these
industries.6'7'8
The major manufacturers of portable plant equipment are Iowa Manufac-
turing, Telsmith Division of Barber-Green, Portec, Universal Engineering,
and Allis-Chalmers. These companies manufacture a variety of interchangeable
portable crushers, screens, conveyor belt units, and combination systems
which can be combined into an integrated portable plant that meets the
requirements of the individual mineral processor.
The output capacity of manufactured portable plant equipment ranges
from 45 megagrams per hour (50 tons per hour) to 998 megagrams per hour
(1,100 tons per hour). A large majority of new and,existing portable plants
are in the 227 megagrams per hour (250 tons per'hour) to 635 megagram per
hour (700 tons per hour) output capacity range.
S-3
-------
Portable plants are owned and operated by a variety of mineral processing
firms. These firms range from the small, independent mineral processor with
one portable plant to large construction materials companies (e.g. Moline
Consumers Company, Flintkote) which may own and operate 12 or more portable
plants.
Construction companies .also purchase portable plant equipment for large
and/or remote site construction projects. The portable plant equipment is
used to supply material for a specific construction project and is usually
sold or scrapped after completion of the project. ' '
The contract processor owns portable plant equipment and contracts min-
eral processing services to a community or another firm. These services may
be contracted for during periods of high product demand when a mineral
processor's output capacity is limited or when a community or firm requires
a supply of construction material. A contract processor may cover a geogra-
phical area which encompasses several states. '
A.1.2 Geographic Distribution
Portable plants are used throughout the nation. However, over 70
percent of existing portable plants are located west of the Mississippi
14
River. The popularity of portable plants in the western and mid-western
states is due mostly'to the demand for crushed stone and sand and gravel in
sparsely populated areas. Such areas can not be economically served
by fixed plants due to high transportation cost for crushed stone and sand
and gravel.
The crushed stone and sand and gravel industries can be divided into
three basic national regions based on portable pi ant/fixed plant usage
(see Figure 1). These regions are:
Region I - In this region, which encompasses the states in the
Northeast and Southeast and most of California, over
80 percent of mine output for the sand and gravel and
crushed stone industries is from fixed plants. The
region has a relatively high population density and well
established product markets for construction materials.
Portable plants are used at large construction projects
(i.e. dams, highways) and to supplement mine output at
fixed operations, particularly during periods of high
S-4
-------
T5
O)
Ifl
3
O
O)
I
to
4-J
o >
re
•r— C/)
Q
-a
re re
o a>
cr> o
a> 4->
a: oo
S- 5
-------
product demand.
Region II - In this region, which encompasses most of the Midwest
section of the country, portable plants account for 20
to 40 percent of mine output for the crushed stone indus-
try and 30 to 50 percent of mine output for the sand and
gravel industry. The region has many large metropolitan
areas with well established product markets for construction
materials. However, some of the areas are sparsely popu-
lated and portable plants are used to meet the fluctuating
product demand in these areas. Product transportation costs
for sand and gravel and crushed stone, which range from
$0.08 to $0.15 per megagram kilometer ($0.12 to $0.22 per
ton mile) nationally, make the establishment of a fixed
plant economically unattractive in parts of this region and
most of Region III.
Region III - In this region, which encompasses the Western states and
northern California, portable plants account for over 50
percent of mine output for the sand and gravel and crushed
stone industries. In New Mexico, Utah, Wyoming, Colorado,
and Nebraska, over 80 percent of mine output for both indus-
tries is from portable plants. The region is sparsely popu-
lated and product demand for construction materials is usually
not high enough to warrant the establishment of a fixed plant.
The portable plant/stationary plant usage distribution, as described above, is
14
not expected to change in the near future.
A.1.3 Industry Trends
The projected growth rate-for the sand and gravel industry through 1985
is 1.0 percent per year, while the growth in crushed stone over the same period
is 4.0 percent per year.15 These growth projections are for the entire industry;
separate projections for the portable plant segments of each industry are
unavailable.
Based on mineral processing equipment sales, more portable plant
equipment is sold per year than fixed plant equipment. However, the total
S-6
-------
output capacity of the portable plant equipment is less than the total
output capacity of the fixed plant equipment.10'14 This equipment sales
trend, which is expected to continue for the near future, indicates that the
average new portable plant would have a lower output capacity than the
average new fixed plant.
A.1.4 Methods of Operation
The mobility of portable crushed stone plants allows portable plant
operators to move their plants according to either of two major methods:
among various quarry sites, or both among, as well as within, quarries.
With regard to the former, the operator may choose to move a single plant
to a number of quarries over the year; however, once set at a site, several
haul trucks are used to transport blasted rock to the primary crusher.
However, other operators may elect to move not only to different quarries
but also within an individual quarry as well. Movement within quarries
allows the plant to follow blasting activities as they take place at various
locations around larger quarries. In effect, the movement of portable
plants within individual quarries reduces the need for haul trucks to trans-
port newly blasted rock to the primary crusher. While the decision to move
about or remain stationary within a quarry may depend upon the physical
condition of the quarry and/or the individual preferences of operators, the
economic analysis has recognized both methods of operation.
S-7
-------
A.2 COST ANALYSIS
A.2.1 Model Portable Plants
Model portable plants have been developed which describe the types
of equipment and size ranges for portable plants in the sand and gravel
and crushed stone processing industries. The equipment selected for
these model portable plants are:
I. Portable sand and gravel plant
1. Primary crusher
2. Secondary crusher and associated screen
3. Final screen
4. Conveyor belts
II. Portable crushed stone plant
1. Primary crusher
2. Secondary crusher and associated screen
3. Tertiary crusher and associated screen
4. Final screen
5. 'Conveyor belts
Five output capacities were chosen for both the sand and gravel and
crushed stone model portable plants. The five output capacities used are
68, 135, 270, 540, and 817 megagrams per hour (75, 150, 300, 600, and
900 tons per hour). Specific sizes of portable crushing and screening
equipment have been combined to meet the output capacities of the model
portable plants. Tables 1 through 5 list the equipment requirements for
the model portable plants along with energy usage and air volume requirements.
The equipment size ranges listed in Tables 1 through 5 represent minimum
and maximum product outputs for each piece of processing equipment.
Processing equipment for a portable plant can be arranged in a
variety of operating configurations at the mine site. Two basic operating
configurations are used for the model portable plants. One configuration
is a straight line setup in which the portable plant equipment lies in a
basic straight line. The second configuration is an "L" shaped setup.
In this configuration the final screen is situated at a right angle from
the secondary screen at the portable sand and gravel plant, and the
tertiary crusher/screen unit and final screen are situated at a right
angle from the secondary screen at the portable crushed stone plant.
S-8
-------
TABLE 1
MODEL PORTABLE PLANT EQUIPMENT REQUIREMENTS
68 megagrams per hour
(75 tons per hour)
1. Primary crusher
2. Secondary crusher
3. Secondary screen
4. Tertiary crusher
5. Tertiary screen
6. Final screen
Given in megagrams per hour with tons per hour in parenthesis
Given in kilowatts with horsepower in parenthesis
c
Given in cubic meters per minute with actual cubic feet per minute in
parenthesis
References: Portable processing equipment brochures from Iowa Manufacturing
Company, Tel smith Division of Barber-Green, and All is Chalmers.
a
Size"
54
(60
68
(75
45
(50
109
(120
45
(50
45
(50
- 227
- 250)
- 104
- 115)
- 181
- 200)
- 136
- 150)
- 181
--200)
- 181
- 200)
Energy
Usageb
56.0
(75)
74.6
(100)
14.9
(20)
m.9
(150)
14.9
(20)
14.9
(20)
Air
Vol ume
43
(1500)
43
(1500)
127
(4500)
43
(1500)
99
(3500)
127
(4500)
S-9
-------
TABLE 2
MODEL PORTABLE PLANT EQUIPMENT REQUIREMENTS
135 megagrams per hour
(150 tons per hour)
1. Primary crusher
2. Secondary crusher
3. Secondary screen
4. Tertiary crusher
j* .
5. Tertiary screen
6. Final screen
aGiven in megagrams per hour with tons per hour in parenthesis
Given in kilowatts with horsepower in parenthesis
°Given in cubic meters per minute with actual cubic feet per minute in
parenthesis
References: Portable processing equipment brochures from Iowa Manufacturing
Company, Telsmith Division of Barber-Green, and Allis Chalmers.
Size9
91
(100
181
(200
45
(50
136
(150
45
(50
45
(50
- 363
- 400)
- 272
- 300)
- 181
- 200)
- 227
- 250)
- 181
- 200)
- 181
- 200)
Energy
Usage"
74.6
(100)
93.3
(125)
14.9
(20)
167.9
(225)
14.9
(20)
14.9
(20)
Air
' Volume
99
(3500)
99
(3500)
142
(5000)
57
(2000)
113
(4000)
142
(5000)
S-10
-------
TABLE 3
MODEL PORTABLE PLANT EQUIPMENT REQUIREMENTS
270 megagrams per hour
(300 tons per hour)
Sizea
136
(150
227
(250
181
(200
272
(300
181
(200
1ST
(200
- 363
- 400)
- 454
- 500)
- 363
- 400)
-363
- 400)
- 363
- 400)
- 363
- 400)
Energy
Usageb
93.3
(125)
111.9
(150)
22.4
(30)
186.5
(250)
22.4
. (30)
14.9
(20)
Air
Vol umec
113
(4000)
113
(4000)
198
(7000)
142
(5000)
198
(7000)
198
(7000)
Primary crusher
Secondary crusher
Secondary screen
Tertiary crusher
Tertiary screen
Final screen
Given in megagrams per hour with tons per hour in parenthesis
Given in kilowatts with horsepower in parenthesis
cGiven in cubic meters per minute with actual cubic feet per minute in
parenthesis
References: Portable processing equipment brochures from Iowa Manufacturing
Company, Tel smith Division of Barber-Green, and All is Chalmers.
S-ll
-------
TABLE 4
MODEL PORTABLE PLANT EQUIPMENT REQUIREMENTS
540 megagrams per hour
(600 tons per hour)
Size
408 -
(450 -
408 -
(450 -
363 -
(400 -
408 -
(450 -
363 -
(400 -
363 -
(400 -
a
635
700)
635
700)
680
750)
635
700)
680
750)
680
750)
Energy
Usage"
186.5
(250)
223.8
(300)
29.8
(40)
261.1
(350)
29.8
(40)
29.8
(40)
Air
- Vol ume
142
(5000)
142
(5000)
227
(8000)
170
(6000)
227
(8000)
227
(8000)
1. Primary crusher
2. Secondary crusher
3. Secondary screen
4. Tertiary crusher
5. Tertiary screen
6. Final screen
aGiven in megagrams per hour with tons per hour in parenthesis
bGiven in kilowatts with horsepower in parenthesis
cGiven in cubic meters per minute with actual cubic feet per minute in
parenthesis
References: Portable processing equipment brochures from Iowa Manufacturing
Company, Telsmith Division of Barber-Green, and All is Chalmers.
S-12
-------
TABLE 5
MODEL PORTABLE PLANT EQUIPMENT REQUIREMENTS
1. Primary crusher
2. Secondary crusher
3. Secondary screen
4. Tertiary crusher
5. Tertiary screen
6. Final screen
817 mega grams per hour
(900 tons per hour)
Size8
726 - 907
(800 - 1000)
635 - 907
(700 - 1000)
816 - 998
(900 - 1100)
816 - 998
(900 - 1100)
816 - 998
(900 - 1100)
816 - 998
(900 - 1100)
Energy
Usage"
298.4
(400)
298.4
(400)
37.3
(50)
298.4
(400)
37.3
(50)
37.3
(50)
Air
Volume
170
(6000)
170
(6000)
283
(10,000)
170
(6000)
283
(10,000)
283
(10,000)
a
Given in megagrams per hour with tons per hour in parenthesis
Given in kilowatts with horsepower in parenthesis
Given in cubic meters per minute with actual cubic feet per minute in
parenthesis
References: Portable processing equipment brochures from Iowa Manufacturing
Company, Tel smith Division of Barber-Green, and All is Chalmers.
$-13
-------
The average output capacity for new and existing portable sand and
gravel plants in the eastern U.S. is between 227 and 270 megagrams per hour
(250 and 300 tons per hour). The installed capital cost for these plants
would be between approximately $0.45 minion and $1 million. ' ' ' '
The average output capacity for new and existing portable sand and gravel
plants in the western U.S. is between 540 and 635 megagrams per hour (600
and 700 tons per hour). The installed capital cost for these plants would
be at least $1 million.9'10'15'17'18
The average output capacity for new and existing portable crushed
stone plants is between 227 and 270 megagrams per hour (250 and 300 tons
per hour). The installed capital cost for these plants is between $0.6
million and $1.3 million.9'10'16'17'18
The,cost per ton of material processed by a portable plant is higher
than the cost per ton of material processed by a similar output capacity
fixed plant. This higher cost is primarily due to higher maintenance
costs and a lower annual operating schedule for portable plants. Portable
plants are designed for mobile transport and lack some of the structural
strength of fixed plants. Thus, portable plants have shorter operating
lives than fixed plants and require more (nan-hours to maintain. On the
average, portable plants operate fewer hours per year (1250 to 1600
hours)16'17'18'19 than fixed plants (2000 hours). This difference is due
primarily to the downtime associated with the movement of portable plants.
Due to this, total annual costs for a portable plant must be recovered on
a lower total product output compared to similar output capacity fixed
plants.
A.2.2 Movement
There are two basic types of portable plant movements. One type
involves transporting the entire portable plant from one quarry to another.
On the average, this type of move occurs four times per year. '
i n in
' The second type of portable plant move is an in-quarry operation in
which the primary crusher is moved near the mined material along the
highwall. In this mode, the mineral processor establishes a core operating
configuration in the quarry and transports the product from the primary
S-14
-------
crusher to the core operating configuration by a conveyor belt. This
eliminates the need for haul trucks for the transporting of mined material
from the highwall to the portable plant. In-quarry moves of the primary
crusher may occur up to 24 times per year. This type of move is characteris-
tic of the small, independent processor. The larger firms in the sand and
gravel and crushed stone industries usually employ haul trucks to transport
mined material from the highwall to the portable plant, instead of moving
the primary crusher to the mined material.21'22 Table 6 lists average
movement parameters and associated costs for a typical portable plant.
These parameters and costs were obtained from mineral processors who use
portable plants. Also listed in this table are estimated movement para-
meters and associated costs for the baghouse systems considered in this
analysis. The baghouse movement costs are based on rental charges for
equipment necessary for an offsite move. A mineral processor may decide
to purchase 'a crane for moving the baghouse systems and/or haul trucks to
minimize the amount of in-quarry moves necessary. The cost of a crane is
$80,000 and the cost of a 20 megagram (22 ton) capacity haul truck is
$50,000.
A.2.3 Control Options
Two control options are used for the model portable plants. The
options are:
Option I - In this option, one baghouse would be used to control
the entire portable plant for the 68, 135, and 270 megagrams per
hour (75, 150, and 300 tons per hour) model plants. For the 540
and 817 megagrams per hour (600 and 900 tons per hour) model
plants, the primary crusher would be ducted to one baghouse and
all other pieces of equipment would be ducted to a second
baghouse.
Option II - In this option, the following pieces of equipment or
_ groupings of equipment would have their own baghouse for all
output sizes of model plants:
S-15
-------
o
o
CO
CM
•feO-
000
o o o
CO O CM
r» *> **
«d- 01 r--.
i i i
000
o o o
CO
ft
ID
CM
CO 00
o o o
O O CO
IO CO CO
CO
CM
CM CO CM
to
•to-
vo
r-«
Lf)
CO
CM
CO
• CM
III
O O O
O O
CTi
CM i—
CM
r—
in
n
00
bO-
cu
03
o
03
O)
CU
cu
CU
CO
-a
CU
ai
O $- =J
.c re s-
OJ O
s- >>
cu $-
o. s- o
a;
ta
cu
10
LU
i- s- re
o> 3 s-
CU oB
£ CD
in *o
O CM C
t~^ •> 03
CM r— 00
cu
a.
O)
cu
en
03
o
a>
cu
en
C XI
O «r- r-
CU
•t-i
••- -a 4^
CU -r-
m
0) CU T-
s- in -o
O +J
03 to
C -M O
O to O
•»->
+-> O i
03
03
03
cu
03
CU E
cu a.
NO 03
'(/5 CU •»-> C
01 O O
•P 03 =S
C i- t3 03
03 CU O +*
i— > S- 03
O- «=C D. Q
CT QO £=03 S- CU O
O>+J
S- E <" E ^ Q-'<-
Q. o
o 01
CU -i— O *r- O
CU
_ •«->
•r- cr cr i- *o
03
LU
CO
CU
o
03
CU
o.
cu
cu
4->
in
03
cu
CU T3
cu
03
03
03
a>
cu
03
cu
E -r-
o o
03 r—
E •»-> 03
O tO 4->
-(-> I—
i— 4-> i— •)-> O
o 10 o in
s- o S- o r—
-M O +-> O r—
c: c 03
O O E
CJ O (/)
_ I—O -r- O O
4J 4J +J 4J 4-> U +1
in e: in 10
O. O 03 O •»-> $- -D
3 O E O S- CU CU
cu
00
to
o >
•r- CL-i- 03
to s-
c
03
i— CM
4-)
in
CM O
r— O
O M-
O
CU
cu
tO 03
O $-
O •)->
i— -a
4J +-> 03 CU
fO 00 +-> JD
5. C3 C
CU 4-5
CU
03
Cn i— r—
03 03 CU M-
CU
en
03
S- ^4 i—
cu
03
O i—
03
O3 O3 O3
03
O •
3 t3
S- CU
O3 3
CT
C CU
O J-
CU CU CU CU 4->
(/) t/> tO ) 'I—
03 03 O3 03 C
co ca co co 3
03
O T3
CQ C_3 Q
LU
S-16
LU
-------
1. Primary crusher
2. Secondary crusher and associated screen
3. Tertiary crusher and associated screen
4. Final screen
For both options, emissions from conveyor belt transfer points are hooded
and ducted to the baghouse systems.
Costs are presented for the two baghouse control options used for
controlling particulate emissions from the five output capacities of the
two model portable plants. The control costs have been based on technical
parameters associated with the control system used. These parameters are
listed in Table 7.
These costs cannot be assumed to reflect control costs for any given
installation. Estimating control costs for an actual installation requires
performing detailed engineering studies. Nonetheless for purposes of this
analysis, control costs are considered to be sufficiently accurate.
The control costs have been obtained from a variety of sources. These
sources include vendors of air pollution control equipment, industrial
contractors, metal work contractors, and published reports on air pollution
control system costs.23'24'25'26'27'28
Two cost parameters have been developed: installed capital and total
annualized cost. The installed capital costs for each emission control
system include the purchased cost of the major and auxiliary equipment,
costs for site preparation and equipment installation, and design engineering
costs. The capital costs in this section reflect third quarter 1979
prices for equipment, installation materials, and installation labor and
are based on pulse-jet baghouses with a pressure differential of 1.5 kPa
(6 in. W.G.) and an air to cloth ratio of seven to one. The filter bags
for the baghouses are polypropylene.
The total annualized costs consist of direct operating costs and
annualized capital charges. Direct operating costs include fixed and
variable -annual costs, such as:
• Labor and materials required for operation of the control equipment
t Maintenance labor and materials
S-17
-------
TABLE 7
TECHNICAL PARAMETERS USED IN
DEVELOPING CONTROL SYSTEM COSTS
Parameter
1. Temperature
2. Volumetric flowrate
3. Moisture content
4. Particulate loadings:
A. Inlet
B. Outlet
5. Plant capacities
6. Operating schedule
Value
Ambient
See tables 1 through 5, 9, and 10.
2 percent (by volume)
12.8 g/Nm3 (5.6 grains/scf)
0.050 g/Nm3 (0.02 grains/scf)
68, 135, 270, 540, and 817 megagrams per hour
(75, 150, 300, 600, and 900 tons per hour)
1,250 hours per year
S-18
-------
9 Dust disposal
» Replacement parts
Dust disposal costs apply to the baghouse control systems A unit cost of
$4.40 per megagram ($4.00 per ton) of particulate collected is used to
cover the costs of trucking the collected particulate to an on-site
disposal point.
The snnualized capital charges account for depreciation, interest,
administrative Overhead, property taxes, and insurance. The depreciation
and interest havsr been computed by use of a capital recovery factor. The
capital recovery-factor depends on the depreciable life of the control
system and the interest rate. For the portable plant analysis, a seven
year depreciable life for the control system and a 10 percent interest
rate are used. This gives a capital recovery factor of 20.54 percent.
Administrative overhead, taxes, and insurance have been fixed at an
additional four percent of the installed capital cost per year. Table 8
lists the annualized capital cost factors used. .
A.2.4. New Portable Plants
Two model portable plants have been developed for costing purposes.
One is a portable sand and gravel plant and the other is a portable
crushed stone plant. The control option used to achieve the emission
level of 0.05 grams "per dry standard cubic meter (0.02 grains per dry
standard cubic foot) is a baghouse system. For an uncontrolled emission
rate of 12.8 grams per dry standard cubic meter (5.6 grains per dry
standard cubic foot) this control option is 99.6 percent efficient in
removing particulate at the model portable plants. The size and number
of baghouses required to achieve the emission limit vary according to the
output capacity of the portable plant. The air flowrates for the baghouse
systems are listed in Tables 9 and 10.
Tables 11 through 15 list installed capital, direct operating,
annualfzed capital, and total annualized costs for each of the baghouse
systems installed in the two model portable plants. The five portable
plant output capacities for which costs have been developed represent the
output capacities applicable to portable plants in the sand and gravel
S-19
-------
TABLE 8
ANNUALIZED CAPITAL COSTS
1. Operating labor
2. Annual maintenance
3. Utilities:
Electric power
4. Replacement parts:
Polypropylene bags
5. Capital recovery factor
6. Taxes, insurance, and
administration charges
7. Estimated life of baghouse
control system
$12.00/hour
5 percent of the total installed cap-
ital cost for each control system
$0.04/kWh
$8.00/m2 ($0.75/ft2)
14.60 percent of total cost for
each control system
4 percent of total installed capital
cost for each control system
7 years
*Three quarters of total filter bag area is replaced every year
S-20
-------
JC
g
i-- co
CM ---
o CD
CO O •
Csl O 3
^D *•
CM =
CM (£>
O CD
CO O «
t£> O 3
CO ID
ta
CO
o.
o
•^ Q-
cr>-4->
LO un
CO i —
O tD
r— O •
CO O 3
o o
O •
o 3
*»
CO =
CM VO
O
O.
CT>
CO
O CD
O O •
CM =
O CD
I— O •
CO O 3
LU
CO
O
C£
I
CD
«c
CO
oj
3
E
I
^
co O
a.
o
o s- s: re
•I— O) C_ •!—
• ^ 1 % *S 1^
re O) e£ E
o3 S"*~" S!
O. C1J
O •• «f-
O) re T3
re s Q)
s- o s-
CD r— 3
«4- to
TO t/)
to (1)
re s-
CD O.
-a
E
re • •
co «t co
(O
o
2
0)
o.
o
O
+J
CO
•o
O)
(/I
3
CJ
CM
»-
S- S 03
O> CE -r-
+-> CJ 4J
d) eC C
s-
3
| ^
re
S-
Q)
Q.
0)
I—
0
C\J
1
1
^_J
c
(U
E
O
0
O)
s-
3
•P
to
•I—
O
E
(1)
re
s-
cu
>
a*T
-Q
,0)
3
E
S-
0)
Q.
O)
CD
U-
0
• ^
JD
3
0
|—
re
3
.$_>
O
1
1
£
o
•a:
0
O)
C7)
3
re
CD
s-
Q}
4-^
re
3
" i
CD
•
3
•o
S-21
-------
CO
O CD
O O •
r-- o 3
O CD
VO O •
CO O 3
r-- «
vo =
O CD
O O
O 3
•*
10 =
CT> o •
CO O 3
jp.jn-1 V\
"CM =
I— «* IO
O)
CU
CD
CU
•r- CU
XI CT>
(O
CO
LU
_J
CO
O
oo
tn
VO
O CD
O CD
O CD
OJ O
O 3
Lf) =
- -- VO
ID O
cn o:
CM O
O 3
*»
LO =
O CD
i— O •
CTi O 3
CTv •*
in =
co vo
CD
cu
to
CD
o -a
LJ
O
cn
UJ
ca
LU
CO
oo
to S-
QJ
cu
O) S-
O)
_
•»-> O 4->
•i- tO
CD
eC
CO
to
a>
CU
to
CD 4—
•O CU
to cu <
o
>»
a)
QJ
CD
0)
to
OJ
O-
ca
a>
>- i*. to
.. _ cu G--I-
3 CU 4-> O 4->
a>
O)
S- CU CU '
O S- ~
o
(C i —
•r- -a
CU O) I
c- 4J i
to CU '
cn
to
03
o •«-
,8"- cS
l/l -O l—
{" *,!
S- (C
O 01
1- S- (C
CU CD
CU E
to CU
3 CU «
O S- «=C
(O
ca
4-> -r-
n3 X3
CU
CU E
a_ T-
a>
a>
CO
CU
CM
tO
O
CU
CU
CU
4J
tO
CD
O «=C
cn
(O
CU
to
to
CU
ca
CU •> S- in *~*r—
j= s. cu s- s: O -t->
s- to cu cu «a: E
031. s:—• cu
S- 0
O tO
•i- -a s-
cu
_ re E 4- 3
CU S- O
10 CU t> r—
•(J E <4-
S- (O
O « to
«4- S- S~ fO
CU CU CD
CU E E
to cu •
O S- S- et
JC <-> O
cn t/i to
ro
CO
CU
CU
CU
ca
CM
CU
CU E
•r- O
.a o
to cu
CU •!-
to cu
S- cn
a> ro
Q. i-
E cu
cu >
I—
-------
03
I
LU
o
LU
si
to
t/)
8
CD
r-. o
r— CTi
00---
C3 CD
o
oo
•3- VD
o o
I^» CO
CVJ<>
•^ o.
O14J
COi—
O CD
CM CD •
•a- o 3
r— «
to =
«—vo
O CD
CO O •
•—03
co
O CD
in o •
CO O 3
*
CO =
O CD
r~- o •
in o 3
*t
CVJ =
O CD
COO •
in o 3
«* -
vo =
r— VO
O CD
00 O •
VO O 3
CO •>
CO =
f— VO
O CD
CO O •
CO O 3
CM "
O =
i— vo
O CD
r-. o •
CM O3
CVJ •>
CO =
«—VO
O CD
CM O •
«* O 3
I— ••
in =
v—-VD
o o
co o •
in o 3
«3- «
vo =
t— VD
O CD
VO O •
<7»0 3
CO •>
O CD
CO O •
00 O 3
CM "
o =
F— VO
O CD
r«» o •
C\J O 3
CM •>
co =
O C5
o o •
«* o 3:
CO •>
CM =
i— VO
O CD
o o •
r-. o 3
fimm ft
vo =
v-^ VO
o CD
CM O •
«d- O 3
O CD
!•-. o •
CM O 3-
CM «-
00 =
O CD
o o •
r-. o 3
fHHU. ft
vo =
O CD
CM O •
vf O 3
^"* **
in =
I
en O
10
JCU U_ •!-
•P O -P
£
re re
•^ S
s- o
Q. r-
>
Q.
O
0)
CO
cn
re
CD
O)
I
)
CO
cu
0.
O)
CO
CO*—M—
s. s: re
CU UU «r-
•PO -P
s:*— cu
cu
cu
•P
£
O
O
CU
M-
O 10
<•- re
CD
cu
to
3 '
O «C
cn
re
CQ
s-
cu
cu
cu
o
CO _
1 I
re ,— •
CO
S- co^-^i—
cu s- s: re
^. CU U_ -r-
fcO +J O -P
3 CU E v-
+•* o -P
cuS c
cu
re
co
cu
cu
«*-
•r-
•o
3
2
o.
cu
JD
re
i
• i
cu
3
re
cu
Q.
cu
CM
cu
o
o
cu
3
cu
O-
cu
cu
U-
3
CJ
re
cu
3
re
CD
S-*
cu
re
co
• o
O^ T f
S-23
-------
a.
o
CD
I
TD
ns
03
•a
to
"O
re
CO
o
i— CO
CO O
«*• "
o
en
C\J
A
CO
CO
O CO
en cr>
co en
co i—
CO
5-i
co
LO
O
O O
«3- O
CO •>
CM
LO
CO
en
en
LO CD
r^ CM
«* <£>
«* co
CM i—
ID
en
CO
CO
LO «*
l— O
•LO CO-
to
O
UJ
u.g
CO
t— as
CO UJI—
SO. 2*
5 l~l
S CO 0. C
tuz: o
1— O UJ '<-
>- CD Q.
CO tf)
co
i— CO
oS
«sf O
CO •>
CM
O
cn
LO
r- CO
CU
+i
CO
I
cu
10
LO
LO LO
CTi O
CM
CM
en
«*
co
CO
o o
r- O
«d- LO
o en
CD
•r- c:
O-'i-
o re
•a cu
cu a.
M O
•p-
r— -)->
SciJ're
^^ t» *^™'
E *r- O
i=r i— i t—
'
(/)
CU
c
cu
•r-
O
cu
t^_
cu
;icu1ate remcv
late removed)
1- 3
re o
Q.T-
n- s-
o re
a.
£ 0
en
re c
CT O
a> 4->
^* *^*^
*^^'CO
CO "*-^
c
•r—
S
S-
CD
a.
40
cu
£
illl—
u
•r-
•§
<_5
r~"
re
•P
o
1
re
re
o
CQ
I
-------
«=c
C£.
00
LL. 3:
co a:
l-LU
CO a. f—
z:^ a!
2 £5^
^ CO _l
,,, >- CD CQ
Jjj COLO fit
0:1 _lC-o;
' a: co Q-
|__ y
^y ^C '
CD a: LU
o CD o
-< S-
o
o
r— O
LO O
CO
CM
E
0
•1—
Q. i—
O O)
>
re
s-
CD
-o
E
re
-a
E
re
CO
CO
^"*S
5-
i — i C_5
o
r— O
CO O
f-«x»
|—
*^-^
+~ *»
O
r- O
LO O
VD ^
CO
CM
^~~s
E
O
•i—
-M i—
O.
s_
CD
•a
c:
re
-o
re
CO
o
i— CD
CO CD
p*^
I —
-
O)
^j
E
1 -i—
E
(13
re w ^*~^
s- s- s:
S CJ)
i — OJ =t
<4- 2:^-
co
re •
O LO CM
«=j- cn CM
«3- CO -^d-
LD CO CM
LO CO CM
•feO^
LO LO •c}-
CTl CM O
LO i — l£i
n * r*
«3- CO CT
O •!- E
1 CL-i-
i — re 4->
re co o re
4-5 4-> S-
•i— CO T3 CD
Q. O O) Q
re UNO
O -r-
T3 i— 4-J
-o cu re u
cu NI 2 a;
r— -i- E S-
i^ r— E T-
re re «a: Q
CO E
E E • •
K-,
i— O-i CO
CO -bq--i=^-
o
*°
CT> t^- CO
CM cr> co
P^- CO -fr
»1 *. — ^
«tf-
fe^
LO OsJx-^
^~ o** "cd"
UO -feO- OD
^ * '
f^*.
LO
t^>
LO r*^-
0
a> E
4-5 <1)
re s-
i—
3 CU
0 4J
•i— re
4-5 r—
S- 3
> i re o
0-T-
t/> 4-J
co 4- S-
O) O re
E Q-
OJ E
> re <4-
•r- S- O
4-5 Ol
o re E
r— Ol CTi O
re *+— cu 4-5 •
4-5 H— E *"^
O O) *<=>•
H~ co ^— ^
CO
O • •
CJ) CJ «=C CQ
^)
1 ^
•T"7
e
•r-
S
S-
QJ
Q.
4-J
QJ
OJ
LL.
O
•i —
o
^
f i
r—
re
3
4-5
0
"^
1
ro
co
S-25
-------
cu
+J
CO
cu
co CD
ID O
cn "
*±
CO
CM
CO
o tn
•vf I—
r— CO
oo
cn cn
*a- CM
00
cu
>
to
CO O
CM O
OJ
en
oo
o o
cn r-
CM «*•
•5t- CD
co
CM CO
en oo
•oo to
in
CO
CO
oi
CO Q- |
co
cu
CO O
IO CD
en •>
«3-
CO
co
o
CM
to in
cn 10
cn cn
«=i- CM
«3 00
oo r--
cn
co ,
co
LU
CO
CO
UJ
>-O CO
co o «=C
CO I—
_
O Qi UJ
cu
ro
CD
-a
co o
CM o
CM
CM
OO
CO
in
r— CO
cn co
co o
co CM
CM
LO
CM
r- CO
cn oo
•co oo
UD
CO UJ
CO
CD r-»
•a: CM
CQ
01
cu
cu
cu "I
CU
ea
CO
u
cu
o
cu
cu
CD
s-
ta
s: +J
u 10
o
t— O
(O
+J O>
•r- C
D.T-
fC +J
O fO
•o cu
CU Q.
N O
(O Or
•»-> O r—
cu «a;
cu to
s- •»-»
r- r— C-r- O
fO fO es: Q h~
cu
cu
o
cu
cu
0) CU
S- >
o
cu E
•M CU
(O 5-
r—
3 O)
O -4->
•r- CO
•4-» r—
S- 3
ro o
Q-'i-
o to
s- o
CD
(O C
cn o
CU 4J
cu
cu
cu
CJ
o
fO
CD
«=C CQ
•a: CQ
; CQ
CO
S-26
-------
Q.
O
cu
c:
O
+J
00
-o
cu
.E
to
3
S-
o
CU
•a
E
to
•o
E
ro
to
co o
co o
i— O
O
«*
vo
CO
CM
o Ln
co f-
m in
in co
co r~-
•oo -co
CM
en
• o
VO O
CO O
r-- «
vo
CM
o
CTi
vo
in
m o
co vo
co o
t\ *
CO CO
CO CM
co
vo
co r>-
OO (/I
a:
LUO
LjJ COO CQ
_J VO «=C
CQ —I t
CD o; — i
O CD LU
cC O
UJ CD O
a.
o
•a
QJ
O)
. >
ro
CD
ro
to
CO
co o
CO O
i— O
** n
r— O
O
r-.
vo
f\
r^-
co
o co
CO t^~
CO CO
rt A
CO •*
in co
co
o
CM
CO
01
VO CO
co r».
o
VO CD
CM O
VO •*
VO
CM
O
in
vo
in vo
cr> co
o t—
9* •>
«* CM
CO
un
vo
CM «d-
CTi CO
CO LT>
t!3
O
CQ
t/)
O
a
ro
a.
ro
O
•a
QJ
ro
IO
O
o
T3
CU
N
•i- E
Du'r-
ro 4^
O ro
-o a>
cu a.
N O
(B O r—
3 CU «0
C S- -M
E -r- O
•a: o I—
CQ CO
"O
CU
o •*—•*
cu cu
i- >
o
CU £ •
-(-* CU
ro i-
*3 CO
O -M
•r- tO
S- "3
I ro O
Q.T-
v> M- S-
CU O ro
E O.
ro v»-
•i- 1-0
o
cu
M-
**-
CU
-u
to
o
o
ro E
CT> O
CU 4->
=S CQ
CU
•1-5
S-
cu
Q.
O)
CU
O
•r-
3
CJ
ro
4->
o
-------
CO
TD
CU
LO O
CO O
«\ «*>
i— 00
CO
cr>
f>
CO
LT>
CM
LO CO
LO V£>
LO O
ft f
CO O
IQ ^J-
•09-
CO
CM
10
CO
O CM
CO r-.
•fa^-faO-
cu
to
CD
ro
ro
CO
O O
en "
CM
CO
CM
CO
•bO-
LO O
CM CO
LO O
LO
ID
Lf)
CM LO
co r^
•CO bO-
CU
CO
O)
cr> c>
LO o
co o
rt ft
T— CO
LO
«=f
CO
•*
CM
VO
CM
co o
co «*
CO
o co
CO 1^-
• o
UJ
_i
CO
cu
>
(0
ro
CM
CO
LO
CM
LO
CO
00
LO
CM
CO
co r-~
CO CO
co
ro
CO
:co
cu
01
O)
cn
ro
J=
O
O
cu
ro
to
CU
+J
OJ
O
O
CU
O
(O
O.-t-
(O -P
O ro
•O 0)
CO Q-
M O
-o t—
cu
O r—
CU ro
i— £= T- O
ro
«=C O J—
(J
CU
M-
CU
cu cu
s- >
o
o> E
4J CU
ro i-
3 CU
O •)->
t- 3
ro O
Q.T-
O ro
O-
cu
£=
CU
•i- S- O
CD
ro C
O) O
CU 4J
O)
cu
cu
o
ro
o
ro
(O
CD
CQ
-------
and crushed stone industries. The cost-effectiveness ratios appearing in
Tables 11 through 15 are simply the total annualized costs divided by the
estimated amount of particulate collected per year.
S-29
-------
A.3 ECONOMIC IMPACTS
A.3.1 Introduction and Summary
In order to further analyze the potential economic impacts of NSPS
controls upon the portable plant segments of the crushed stone and sand
and gravel industries, a Discounted Cash Flow (DCF) model was developed.
This model has been used to estimate the financial status or profitability
of portable plant operations, both before and after the aodition of NSPS
controls.
The model has recognized several major variations in the methods of
operation chosen by various firms within the industry. For this reason
separate analyses have been completed under different assumptions regarding:
• • Portable plant capacity
• [Average hours of operation per year
• Level of portable plant mobility, i.e., mobility among quarries
alone, or both mobility among and within various quarry sites.
In the discussion which follows, those plants which typically move
within the quarry (in order to minimize the distance between the primary
crusher and newly blasted rock) are said to "follow the highwall", while
those which remain stationary within each quarry are denoted as "no highwall".
Sand and gravel plants were not examined under the "follow the highwall"
option since this mode of operation is not used by such plants.
The results of the DCF analysis are summarized in Table 16. For
those cases where the potential new investment is Tabled F (feasible), the
economic feasibility of the investment will be unaffected by NSPS controls.
Where NF (not feasible) is noted, the investment may not be made if the plant
is to operate under the parameters specified. Where A (ambiguous) is noted,
the DCF analysis has yielded '"borderline" potential impacts for reasons
discussed below. All assumptions made and steps taken in arriving at these
conclusions are detailed in the sections which follow.
A.3.2 Methodology
The findings noted above have been derived through the application of
a Discounted Cash Flow (DCF) model, constructed to reflect the financial
situation of a given portable crushed stone or sand and gravel plant which
S-30
-------
may be purchased and operated in the future. The basic distinctions between
fixed and portable operations have been considered in the development of
this model. These distinctions include variations in equipment life, annual
hours of operation, investment requirements, markets served, and the costs
associated with the NSPS controls.
TABLE 16
SUMMARY .OF DCF RESULTS FOR PORTABLE PLANTS
Crushed Stone
Sand and Gravel
Plant
Capacity
Mg/hr tph
68
135
270
540
75
150
300
600
Operating
Hours
(hours/year)
1250
1600
1250
1600
1250
1600
1250
1600
Uncon-
trolled
NF
NF
NF
A
A
F
F
F
With NSPS
No
Highwall
NF
NF
NF
NF
NF
A
F
F
Controls
Follow
Highwall
NF
NF
NF
NF
NF
NF
F
F
Uncon-
trolled
NF
NF
NF
A
A
F
F .
F
With NSPS Controls
No-
High wall
NF
NF
NF
NF
NF
A
F
F
Key: F - economically feasible
NF - not economically feasible
A - ambiguous (investment not necessarily precluded)
All plants for which the DCF analysis has been applied have been assumed
to function within a scenario defined by the following conditions:
s The plant will operate as a separate business entity or "profit
center",
S-31
-------
• The pass through of control costs to the consumers of the products
of new portable plants'is, to some extent, limited by competition
of existing portable plants which will not be affected by the NSPS
to the same degree,
• Individual plants may choose to operate either 1250 hours/year or
"1600 hours/year,
• Individual plants may choose to remain stationary within each
quarry (i.e., not follow the highwall) or move about within the
quarry (i.e., follow the highwall),
•' The planning horizon for potential investors in portable plants
is 10 years.
The assumption that the new portable plant will operate as a separate
business entity implies that the plant will not at any time be dependent
upon, or supported by revenues generated by other business activities of the
investing firm. It is implied therefore, that debt incurred through the
initial investment, and all other expenses associated with the plant's
operation will be paid only through those revenues generated by the new plant
itself. This assumption may reflect a conservative point-of-view for vertically
integrated or multi-plant firms; however, the assumption is plausible for
horizontally integrated firms having a single processing plant.
The condition that the pass through of control costs to the consumers
of portable plant products, will be limited by competition from existing
portable plants (which will not be affected by NSPS), reflects the reality
that portable plants typically compete with other portable plants, since
the ability of a plant to locate near the site of an impending job, is the
key to lowering customer transport costs and thus securing orders for crushed
stone and sand and gravel. For stationary plants it has been projected that,
due to the replacement of old plants by new (NSPS) plants, 25 percent of the
cost of pollution control will be passed through every four years (see
Section 8.4.2). Recognizing that the competition among portable plants is
potentially greater, and thus the cost pass through ability lower, it has
been assumed that portable plant operators will require twice as much time
(i.e., eight years) to pass through 25 percent of pollution control costs.
In the DCF analysis this level is reached by way of pass through increments
of 6.25 percent every two years. This assumption is conservative in that for
those sections of the country where competition is less intense, product
prices may be increased sooner to reflect additional costs.
S-32
-------
The DCF analysis detailed in Section A.3.3 has been constructed in such
a way that the operational peculiarities of individual portable plant opera-
tors are considered. For example, it has been noted that the preferences of
individual operators vary, especially with regard to the hours of operation
per year and the movement of plants within individual quarries. -Therefore,
in an attempt to differentiate impacts for each of these modes of operation,
each model plant has been individually examined assuming 1250 and 1600
operating hours per year, as well as preference for moving within individual
quarries (i.e., following the highwall) or remaining stationary within each
quarry (i.e., no highwall). It should be noted that the preference for
within quarry mobility will entail higher pollution control costs due to the
need to dismantle and set up control equipment more often.
The investment planning horizon of 10 years has been selected based upon
the 10 year normal useful life of portable plants. The 10 year life has been
supported by representatives of the industry.30
The cash flows considered by the DCF model are:
• Earnings after tax,
• Depreciation of plant and rolling stock,
• Depreciation of pollution control equipment,
• Working capital recovery,
e The salvage value of plant and rolling stock, and
• Payback of debt.
Earnings after tax have been determined after consideration of all oper-
ating costs, depreciation expenses, interest expenses, overhead, and pollution
control costs. In the determination of earnings after tax the availability
of depletion allowances and investment tax credits, have been recognized.
Regarding depreciation, plant and rolling stock have been depreciated (straight-
line) over their respective useful lives. Pollution control equipment has
been depreciated over five years to a zero salvage value. It has also been
assumed that working capital requirements are funded out of equity and that
all plant and rolling stock is sold at salvage value after 10 years. Each of
these items is discussed in greater detail in the following section.
S-33
-------
A.3.2.1 Critical Elements. In the estimation of the potential impacts
of NSPS controls, numerous data elements have been assembled and evaluated to
allow their incorporation into the DCF model. In the descriptions listed
below each of the critical elements is identified and discussed in terms of
its use in the model. Sources of data pertinent to each critical element are
listed in Section A.3.2.2.
With regard to operating hours per year, individual firms contactedSO
indicated a variety of preferences, however most tended toward two levels,
1250 and 1600 hours per year. Although the actual hours per year is heavily
dependent upon the weather, these two figures have been identified as target
levels. The number of operating hours per year is perhaps the most critical
data element since it is the prime determinant of net revenues generated by
each plant, in this high fixed cost, low profit margin industry. In the DCF
model all production is assumed to be sold and thus there is no net change in
the inventories of the model plant.
Concerning product prices, distinctions between crushed stone and sand
and gravel have been made. The values employed in the DCF model are $3.25/ton
for crushed stone and $2.86/ton for sand and gravel. The price of crushed stone
was noted by two industry representatives and the price of sand and gravel
was derived from the crushed stone price, based upon Bureau of Mines31*32
data indicating that for recent years the price of sand and gravel has
approached 88 percent of that for crushed stone.
Based upon the $3.25/ton price of crushed stone, operating costs (exclu-
ding depletion, depreciation, interest and overhead) have been identified
based on discussion with industry representatives, as $2.10/ton. Operating
costs for sand and gravel plants have been estimated by applying the ratio of
operating cost/price for crushed stone ($2.10/$3.25), to the price of sand
and gravel, to estimate sand and gravel operating costs of $1.85/ton.
The validity of the $2.10 and $1.85/ton operating cost levels for
i
crushed stone and sand and gravel portable plants, respectively, has been
supported through the determination of the pre-control Internal Rates of
Return (IRR) for those plants faced by these costs. Such rates have been
calculated and are summarized in Table 17.
S-34
-------
TABLE 17
INTERNAL RATES OF RETURN FOR PORTABLE CRUSHED STONE
AND SAND AND GRAVEL PLANTS
(Pre-Pollution Control)
Plant Capacity
(Mg./hr) (tph)
68
135
270
540
75
150
300
600
Operating Hours
(hours/year)
1250
1600
1250
1600
1250
1600
1250
1600
Crushed
Stone
io.°o%
10.1%
14.0%
14.2%
18.2%
20.9%
25.6%
Sand and
Gravel
<9.9%
9.9%
10.2%
14.3%
14.5%
18.4%
21.4%
The IRR percentages in Tabie 17 appear to be reasonable. In light of
current returns on other forms of long-term investment. Had the pre-control
rates been higher than those actually calculated, the understatement of
operating costs could be a suspected cause. On the other hand, if the
pre-control rates were estimated to be lower than those of Table 17, the
overstatement of operating costs/ton might have been suspected.
Depreciation of plant equipment has been taken as straight-line over
its 10 year life. Depreciation of rolling stock has been taken as straight-
line over a seven year life in order to take full advantage of the investment
tax credit. Depreciation of pollution control equipment has been taken as
straight-line over five years to a zero salvage value. Investment tax credit
is also available, and is taken on pollution control equipment using a 5-year
rapid amortization writeoff.
Debt terms for plant, rolling stock, and pollution control equipment
have been assumed to be five years at a 15 percent interest rate. Industry
contacts have noted that the availability of debt financing at terms better
than those noted, would be uncommon. It should be noted that the results of
the DCF model are not sensitive to variation of the interest rate.
The financing of portable equipment in terms of debt/equity has been
observed to range from 0 percent to 100 percent, dependent upon the prefer-
ences and abilities of individual firms. For purpose of the DCF model a
S-35
-------
ratio of 50/50 is employed. The use of this ratio has been judged realistic
by industry representatives. It should be noted that the results of the
DCF model are not sensitive to variation in the debt/equity ratio over the
0 to 100 percent range.
With regard to overhead expenses of portable plant operations, industry
sources have indicated that for a 270 Mg/hr (300 tph) portable plant'such
costs would be about $.25/ton for each ton of crushed stone produced. For
the 540 Mg/hr (600 tph) plants this figure has been reduced to $.22/ton due,
for the most part, to economies of scale. These figures have been employed
for both crushed stone and sand and gravel plants.
Pollution control costs for purposes of the DCF analysis, have been
grouped into four basic classes:
t Excess moving costs,
• Annual Cost of operation and maintenance,
t Depreciation, and
• Interest on borrowed capital used to purchase and install pollution
control equipment.
The inclusion of excess moving costs account for those added costs incurred
due to the need to dismantle, move and set up the pollution control system
each time the portable'plant is moved, regardless of whether the move is
within the quarry or to another quarry. The costs associated with these
activities are summarized in Table 6, while their inclusion into the DCF
model is described in Section A.3.3. Regarding the number of moves made by
the typical portable plant, industry sources have indicated that the typical
portable plant moves to a different quarry, on average, four times each
year.30 For those plants which prefer to follow the highwall, an average
of 24 such within-quarry moves might be made. Sand and gravel plants, on
the other hand, do not often move within the gravel pit, since very little
blasting is done.
The annual cost category represents the annual total of pollution control
costs incurred by each mo-del plant. .The costs summarized under this heading
include annual maintenance and operating costs, utilities, filter replacement,
dust disposal costs, property taxes, insurance, and administrative expenses.
Depreciation of pollution control equipment is taken over a 5 year useful
life, with a zero salvage value. For those plants which choose to follow the
S-36
-------
highwall, the cost of a small crane (needed to facilitate dismantling and
reconnecting of pollutions-control equipment) has been added to the plant
costs, and is thus depreciated over ten years. (Plant investment costs are
summarized in Section A.3.2.3.)
Interest on the pollution control equipment for each plant has been
determined by calculating the annual interest-principal repayment schedule
according to the debt terms described above.
Depletion expenses have been determined for each model plant, under the
assumption that the quarry site is leased rather than owned by the portable
plant operator. Under these circumstances the operator is entitled to a
depletion allowance according to a depletion base defined as:
Depletion base = price/ton - royalty/ton.
Industry representatives have noted that royalties paid by portable plant
operators are typically 5 percent of the sale price per ton. In the DCF
model the annual depletion allowance is calculated as:
Depletion = depletion base x annual output x % depletion.
The Internal Revenue Code allows percentage depletion for both crushed stone
and sand and gravel minerals of five percent. Two limitations to the use of
percent depletion are:
• The maximum depletion claimed in any year cannot exceed one-half of
that year's earnings before tax, and
• Depletion is subject to minimum tax as a tax preference item.
These limitations have been included, where appropriate, in the year-by-
year calculations of the DCF model. The assumption that the owner must pay
royalties represents a conservative point of view, since this slightly
reduces the available depletion base.
Regarding the Federal tax rate, the marginal tax rate can "vary up to a
maximum of 46 percent of earnings before tax and after depletion. In the DCF
model it is assumed that taxable income of the firm, resulting from other
activities, is sufficiently greater than $100,000 annually, and thus the tax
rate employed is 46 percent. State taxes are assumed to be 5 percent of
earnings before tax since this is the most common state tax rate.
S-37
-------
Working capital or capital required to finance accounts receivable and
inventories have been considered in the DCF models. Industry contacts30
have noted that both accounts receivable and inventories each require -
capital financing on the level of 15 percent of sales, giving total working
capital requirements of 30 percent of sales. In the DCF models it has been
assumed that working capital is financed from equity and that all working
capital is recovered after the tenth year.
Salvage values of plant and rolling stock have been considered in the
DCF model as cash inflows resulting from their sale in the tenth year. The
salvage values have been determined through industry contacts as well as
inspection of the used equipment markets as defined by industry trade jour-
nals. 33 The'salvage value factors used in the DCF model are 36 percent for
plant and equipment and 16 percent for rolling stock.
The model assumes that firms will take maximum advantage of the invest-
ment tax credit. It is recognized that the credit cannot exceed 10 percent
of the investment and may not be carried forward more than seven years.
A.3.2.2 Sources of Data. Sources of data used in the DCF analysis are
noted in Table 18.
A.3.2.3. Plant Investment. Estimates of the costs of new portable
crushed stone and sand and gravel plants were assembled after discussion with
both the manufacturers of portable plants34 and firms who use portable
equipment in their quarrying activities. On the basis of these discussions
the investment levels noted in Table 19 were developed and used in the DCF
model. In those instances where a small crane is purchased, in order to
maintain within-quarry mobility, the cost of such a crane is assumed to be
$80,000.
Plant and equipment investment for the 270 Mg/hr (300 tph) sand and
gravel plant was determined by noting the difference in equipment require-
ments (and thus costs) between the 270 Mg/hr (300 tph) crushed stone model
plant and the sand and gravel model plant of the same capacity. Plant and
equipment investments for the 68, 135 and 540 Mg/hr (75, 150 and 600 tph)
plants were estimated through the .6 power capacity rule.
S-38
-------
TABLE 18
SOURCES OF DATA
Source
Data Element
Operating Hours/Year
Product Prices
Operating Costs
Depreciation
Debt Terms
Debt/Equity
Overhead
Pollution Control Costs
Moves/Year
Depletion
Tax Rates
Investment Tax Credit
Working Capital
Salvage Values
Plant Investment
CO
GJ
c
•r—
21
Cj—
O
3
TO
O)
i.
co
X
j^
c
TO
CD
O)
>
i-
0)
CO
CD
C£
r_
TO
^
(U
-o
0)
u.
X
O)
"o
•»—
3
f ^
X
TO
t—
^_
OJ
•M
CO
TO
s:
•
OO
^3
CTl
Ol
T-H
X
X
X
X
CO
O)
4~)
TO
•r~
U
o
CO
CO
CO
•^
s_
^.
0
s:
^_j
s_
o
X
o
o
s_
4_>
CO
2^
0
^_5
^>
>
TO
~a
c
TO
>>
§
c~
en
X
C\J
•
^<
'
o
, ^
u
01
C/1
X
^_^
c
TO
Q.
E
O
O
CO
.__
*
-^
-M
U
4^
3
JjT
(T5
O
X
X.
X
CO
0}
•r-
TO
C
Q)
CO
S_
Q.
O)
Q;
>,
^
CO
-o
c
X
X
X
X
X-
X
X
X
X
X
X
X
X
X
S-39
-------
TABLE 19
REQUIRED INVESTMENT FOR NEW PORTABLE CRUSHED STONE
AND SAND AND GRAVEL PLANTS
($l,000's 1979)
Plant Capacity
Mg/hr) (tph)
Crushed Stone
PI ant .and Rolling
Equipment Stock
Total
Invest-
ment
Sand and Gravel
Plant and
Equipment
Rolling Total
Stock Invest-
ment
68
135
270
540
75
150
300
600
305
462
700
1061
217
330
500
758
522
792
1200
1819
213
323
490
743
218
330
500
758
431
653
990
1501
A.3.3 Discounted Cash Flow (DCF) Analysis. Table .20 presents an
example of the data sheets which were developed for each model plant under
the previously discussed scenarios regarding operating hours and plant
movements. The example presented in Table 20 is that for the 270 Mg/hr
(300 tph) crushed stone plant which operates at 1,600 hours per year and
prefers to maintain its mobility within the quarry (i.e., follow the highwall),
In this case the total investment required (excluding pollution control) is
$1,748,000 represented by:
Plant
Small Crane
Rolling Stock
Working Capital
Total Investment
Cost
$700,000
80,000
500,000
468,000
$1,748,000
Source of Funds
50% debt, 50% equity
-do-
-do-
100% equity
S-40
-------
o> co
°i ° °!
col *~ "!
2! ? ..Z\
C i—
T3 O .0
CJ -•— JD O>
O I'JD f"^ ^"
-'"1°.
Lt_
0
O
2w~
i CD u~i «— i cG i i o^ LO cn t-H ro CO i**- i
*— ' CM CO CM •— t
§ f:
0 —
UJ
r-- 1 1 1 r-^ CM O"i CM CT* t
f*** f*** •— « cO uo ^"
o u
>> II 11
0?
i£ CD 1
i cn co co t » i
r^ J
O CM CM|
CNJ
-* •-' -<
to o — « ro ~H
^.4" ^
jj
.
ovoo.ogo^-aj.oog
,H"«
-— »
"o to".— T
o + o «
4-* • S-
oo ' •£ *
Cn -t- O CO
C _a£ CNJ CJ r— -—
._ u v _ o
•— 0 COL.—
r— 4-J CT O t- 4J C
O -iCOO O •»— 4-> C r— 1^
Ct: U ••- 4J C O O 4-J
o cn 4-J 3 o o i- c
«O -MC U^— (_? -UC
oo -^- ra i — c c t_>
•4-J t— T3 O C C O
C Oil— O O_ O -i- J_) C
ro CO l_ •— +J C
r-4-J-t-Ct: Q- *J 3 C •«-
O. C •— * • Z3 f— O 4J
fU( — oO 4J4-ir^> — -1—3
»— O C tfl •— O -M i—
"Q-OC+J TOOOQ-3*—
VI C t— O Q_ •— O
•*-> TO CL t— ex.
OCCCu C"CQ_
t_J O O •• "- -*-> O
•r- -F- *J > W •— *J
Ol-*-'-^" ulOO-4->"W
C fO f04->t> OSIt-3 <«•»-> O
LjJ -t- -r- ••— C/) fD O ••— CO (_>
ZD4JCJOQJOJ W »— O OJ
21^O) QJ *J U C C-J-) 4->
LLjcxaiarc >OXCCO
CCOCDO—tO^ UJcCO*— '(—
i — CMro^rLOUDr^cocno — CM
t— 4
CTl
J"
oo
-
JC
C71
3
£
_C
4->
I/I I 1
fu ro
cx— *
>*- —
XCM
CM •-<
— *r^.
I i
_c:
CT! -.
3 t—
0 00
1- O
-C LJ
J—
_l
w <
Irt H-
13 O
Cu 1—
ro -tf-
CC vf
LO CM
^r
—
X
>_ OJ
Z ^
o: o-
<: o
UJ O
uo UD
TJ- ^O i^D
LO CM CM
uo
— ••
o
4->
OJ
CL
o
Q
L.
CU
4->
**-
«£
-o
C
T3 >,-*->
4-> -r-
X -r- X3
ro i — aj
i— -^ i_
JD CJ>
OJ (D
t- -r- X
o __j rc
4- 1—
ai x
co ^ 4-j
(— C
i/l
/O O) C
UJ U. •— •
r-- CO CTi
o cu *s-
^-^ CM
O CD UO
X CM
(13 1
t— *JO
oT eO
i £
CO •— ••
^H c a;
" -•!— (/)
z: 'D
^
X •• X
tl 4-J fO
(— C J—
OJ
r— E e
TO 4-> 3
I- LO E
OJ 3 ••-
t3 *'-5 C
OJ -O ••-
U. <£ E
O *— CM
CM CM CM
CM CM CO
ro
CM
-*-
CD
CM
X
—
cz>
h-
ro «s- LO yo
CM CNJ CM CM
I-H cr> o
"•O *3" MP
LO cn CD
- — * .^
(JO U
CM O
1 4-»
LO CO
» — cn
C
4-> ••-
x ro " —
«< r- 0
H- Q_ C£
cr;
L— C C
LL. O O
<: .^- «^-
^ .,_ .p_
z: u u
^- a> QJ
z: i- i-
CE: CL Q.
O CM
+
C CO
O CM
4-J
3
O O
o_ ••-
4J
ro
C U
O OJ
••- L.
4-J CL
ro QJ
•— o
u
QJ —
CX*J
QJ O
01—
o^
ro ro
O ro ty
t 1 LO CD LO
cn ro CM
U
0
'o
CTl U
C 4-)
f— O LO
^ t_> ro
O -4-
a: c «=r
o ro
4->
4-J 3
C •— ••
ro — 4->
>•> — 0 C
t- CL. Cv. cu
QJ E
> >->
o -- •• ro
4-> d.
QJ C C QJ
ce o GJ CE:
f— >,>,'—
4-J GJ Cw Cu CL
•*- 3 QJ CJ ••-
cx— ce c£ u
ro ro C
C.J > f— r— -r-
ro ro i-
o> ai CL CLQ.
c cn-— ••- -
••- ro u u i—
^: > c c ro
i_ ^_ ._ .^ ^j
O TO t- t- o
S oo a. Q_ H-
CM ro -a- uo o
ro ro ro ro ro
i*O LO O
"O LO ^n
r-.
o-> o o
CO
^£>
ro
i i
ro ^
ro CO;
+ roj
CM X
ro i —
-t- ro
— » — -J
ro j
+
f^
CM 3
•— ' 0
U.
3 1- ZI
O C 00
U. U LJ
zr ro
— U_ C3
i_U
— -4-J t^
00 C ^
53 0
0 O
U 0
h- l/l VO
UJ -f- i— •
z: Q o
r»- co cn
ro ro ro
j
S-41
-------
Since the plant, crane and rolling stock are financed 50/50 debt/equity,
and working capital from equity alone, the total investment from equity
is 51,108,000.
The steps summarized below detail how the discounted cash flows for the
ten year life of this plant were determined. The derivation of individual
values are explained in Section A.3.2.1.
• Row 1, Revenue, was determined by multiplying operating hours per
year (1,600) by the capacity per hour (300 tph) and the price per
ton for crushed stone ($3.25).
• Row 2, Operating Costs: Plant and Rolling Stock, has been esti-
mated by multiplying operating hours per year (1,600) by the
'. capacity per hour (300 tph) and the operating costs per ton
($2.10). In addition $8,000/ year was included as the operating
costs for the small crane.
t Row 3, Depreciation: Plant, was derived by subtracting from the
total investment in plant ($700,000 + $80,000), the estimated
salvage value at 36 percent ($281,000) and calculating the annual
depreciation charge for each of the 10 years.
• Row 4, Depreciation: Rolling Stock, was determined by subtracting
from the investment ($500,000) its salvage value of 16 percent
(580,000) and calculating the annual depreciation charge for each
of seven years. For years 8, 9 and 10, the model assumes the fully
depreciated rolling stock requires increased maintenance and so
operating costs have been increased by $60,000 (i.e. the value of
annual depreciation) for those years (Row 2).
• Row 5, Interest: Plant and Rolling Stock for each year has been
determined by calculating the annual interest-principal repayment
schedule based on the terms of a five year loan of $640,000 at 15
percent.
t Row 6, Overhead, has been determined by multiplying the operating
hours per year (1,600) by the capacity per hour (300 tph) and the
estimated overhead costs per ton ($.25).
. Row 8, Excess Moving Costs: Pollution Control have been estimated
based upon the data summarized in Table 6 regarding the cost of
S-42
-------
moving the control system. Based upon an estimated 24 mcves/yesr
within the quarry, 4 moves/year among quarries, labor costs for
control system dismantling and set up of $1,440/move and average
transportation costs of $5,120 for moves to different quarries, the
annual excess moving costs have been determined to be $61,000-.
Row 9, Annual Cost: Pollution Control was obtained by summing the
following annual direct cost components (Table 13); annual 0 &M costs
utilities, filter replacement, dust disposal, and taxes, insurance
and administration. , ~
Row 10, Depreciation: Pollution Control, was determined by assuming
the total installed capital costs ($203,6£0) of Table 13 will be
depreciated to zero salvage value over five years.
Row 11, Interest: Pollution Control, was. determined through the
interest-principal repayment schedule for a loan of ($203,600) for
five years at 15 percent.
Row 13, Pass-through, was determined based on the assumptions
regarding the gradual pass-through of pollution control costs to
the consumers of crushed stone and sand and gravel (see Section
A.3.2). More specifically, the DCF model assumes that the follow-
ing percentages ,.of the total costs of pollution control will be
passed to consumers in the form of higher prices:
- Years 1 and 2 = 0 percent
- Years 3 and 4 =6.25 percent
- Years 5 and 6 = 12.50 percent
- Years 7 and 8 = 18.75 percent
- Years 9 and 10 = 25.00 percent
While in reality the pass through of control costs will increase
the yearly revenues, the arithmetic of Table 20 is based upon
the deduction of the pass through amounts from total costs.
Row 16, Depletion, has been estimated for each year by multiplying
the depletion base ($3.08), the calculation of which is described
in Section A.3.2.1, by the capacity per hour, operating hours per
year, and the five percent depletion allowance. Following this
procedure has yielded a maximum annual depletion of $73,000.
However, Federal tax laws prohibit the claiming of depletion allow-
S-43
-------
ances in excess of one-half of earnings before tax. In the case
presented in Table 20 the plant cannot claim full depletion
until the fifth year of operation.
Row-18, Federal Tax Liability, has been calculated on the basis of
a marginal tax rate of 46 percent.
Row 19, Investment Tax Credit, has been calculated or, the assump-
tion that the firm will attempt to apply the full credit available,
.which in this case is $148,000 (i.e., 10 percent of the total
investment of $1,483,600 including pollution control). Current tax
laws dictate that credit may be taken on the first $25,000 of
earnings before tax and after depletion, plus a percentage of
earnings above this amount. Presently the tax laws allow credit
for 60 percent of earnings above the $25,000 level in 1979, and 70
and 80 percent for 1980 and 1981, respectively. For 1982 and all
following years the percentage is 90 percent.
Row 21, Adjustment: Minimum Tax. Since the previously discussed
depletion allowance is a "tax preference item" the tax law calls
for the payment of a minimum tax if the amount of the firm's
Federal tax (row 20) is less than the depletion claimed (row 16).
For those years which this is so, an adjustment of the year's
depletion must be made in order to define a "minimum tax base" (• ow
22). This adjustment is taken as the years Federal tax (row 20)
unless that tax is less than $10,000 in which case the adjustment
is $10,000 according to the Internal Revenue Code.
Row 22, Minimum Tax Base, was determined by subtracting the adjust-
ment (row 21) from the year's depletion (row 16).
Row 23, Minimum Tax, was determined by applying the minimum tax
rate of 15 percent, to each year's minimum tax base (row 22).
Row 24, Total Federal Tax, was derived through the addition of each
year's minimum tax (row 23) and Federal tax (row 20).
Row 25, State Tax, was determined through the application of the
most common state tax rate (5 percent) to each year's earnings
before income tax (row 15).
Row 26, Total Tax, shows the amount of Federal and state taxes
payable for a particular year.
S-44
-------
Row 27, Earnings After Tax, forms the first item in the cash flow
calculations (Rows 27 through 37).
Rows 28, 29, and 30, entail the "adding back" of various deprecia-
tion amounts into the annual cash flows of the portable plant.
Row 32, Working Capital Recovery, was added to the final year's
cash flow to reflect the recovery of equity capital previously
sunk in accounts receivable and inventories.
Row 33, Salvage Value, was added to the tenth year's cash flow to
reflect cash gene -ated from the sale of the ten year old portable
plant. The calculation of this salvage value was noted previously
in Section A.3.2.1.
Row 34, Principal Repayment: Plant and Rolling Stock, was deducted
from each of the first five year's cash flows since one-half of the
investment in pi ant and rolling stock has been financed through
debt over five years at 15 percent.
Row 35, Principal Repayment: Pollution Control, was also deducted
from the cash flows of years one through five since the investment
in pollution control equipment has been financed completely, through
debt over five years at 15 percent.
Row 38, Discount Factor. In order to account for the fact that
cash flows to be received during the near future are "more valuable"
to the firm than those to be generated in the later years, all cash
flows have been discounted to their present value. The discount
factors have been determined on the basis of a cost of equity of 15
percent. The cost of equity has been used since the DCF'analysis
detailed above has accounted for the repayment of all loans (i.e.,
debt) used to support the portable plant's operation.
Row 39, Discounted Cash Flow. When the cash flows of each year are
discounted to their present value and summarized a value of $828,000
is derived. It is this value which is compared to the original
investment from equity ($1,108,000) to allow the further calcula-
tion of the Internal Rate of Return (IRR) as described below.
A.3.4 Conclusions
A.3.4.1 Internal Rates of Return* IP an effort to gain greater insight
into the specific economic impacts upon those plants examined, the Internal
S-45
-------
Rate of Return (IRR) for each plant was determined. Such a rate is defined,
in each instance, as that rate of return which equates the present value of
future cash flows with the value of the initial required investment from
equity. Therefore, according to this definition, the feasibility of indivi-
dual investments is judged by whether or not the IRR is greater than the
cost of equity (and thus economically attractive) or less than the cost of
equity (and thus not attractive). Based on discussions with industry repre-
sentatives, the cost of equity was assigned a value of 15 percent per year.
A.3.4.2 Feasibility Definitions. Once each IRR was identified it
became necessary to establish boundaries or "cut-off" points so that eco-
nomically feasible and non-feasible investments might be more clearly dis-
tinguished. While in the strictest sense, such a cut-off point should be
the cost of equity, a middle range of "ambiguous" results has been selected.
The need for such a range is based upon the reality that the economic envi-
ronment of all portable plants is not, and will not be identical. Recognizing
this reality, the values for a number of parameters chosen in the above DCF
analysis have reflected conditions which would be faced by a small number of
plants in the extreme. Recognition of the use of such conservative assumptions
is crucial in the interpretation of the DCF results (Table 16) since, in
reality, many plants will not face conditions of such an unfavorable nature.
Specific examples of the use of conservative assumptions made in this
analysis include:
• Operating hours per year - it is quite possible that the plants in
question can or will operate for a number of years during the 10-year
span at rates higher than 1,250 hours per year,
• Prices - control costs may be passed to the consumer at a rate much
higher than that assumed, especially in those areas of less strict
competition,
• Debt terms - some firms, especially those with well established
credit lines, may be able to obtain bank financing at less than 15
percent, or over periods longer than 5 years.
For these reasons a range of ambiguity of 12 to 15 percent IRR has been
selected, and for the purpose of Table 16, NSPS controls for those plants
S-46
-------
whose post-control IRR is greater than 15 percent are identified as "econo-
mically feasible", while those below 12 percent are said to be "not economi-
cally feasible". For a specific plant whose internal rate of return, as
calculated by the method employed here, .falls within the 12 to 15 percent
range (termed "ambiguous"), an investment decision will have to be made
after careful revaluation of prevailing process, market and economic condi-
tions.
A.3.4.3 Adaptation of Portable Plants to NSPS Control. In general, the
implications of the results of the DCF analysis summarized by Table 16 are
that the profitability of those new plants who desire to operate at relatively
low hours per year and/or maintain within quarry mobility will be adversely
affected. With specific regard to crushed stone, it appears that the new 270
Mg/hr (300tph) portable plants may be forced to operate at a greater number
of hours each year and limit the number of within quarry moves made.
However, it should be noted that for those new plants which can operate at
levels above 1,250 hours per year and also pass a greater portion of
control costs to consumers of crushed stone, profitability will be main-
tained. Since sand and gravel plants ordinarily do not move within gravel
pits, the new 270 Mg/hr (300 tph) portable plants which will maintain
profitability will be those which either operate at a higher level of hours
each year, or can increase the price of their products enough to cover the
increased costs of pollution control.
S-47
-------
REFERENCES
1. Letter and attachments from Brown, Howard, _Iowa Manufacturing Company,
to Viconovic, George, GCA/Technology Division. June 18, 1979. Data
on portable and stationary plants in the crushed stone and sand and
gravel industries.
2. Telecon. Hart, Michael, Colorado Sand and Gravel Association with
Viconovic, George, GCA/Technology Division. June 13, 1979.
Portable plants in the sand and gravel industry.
3. Telecon. Davidson, Edward, National Sand and Gravel Association with
Viconovic, George, GCA/Technology Division. June 13, 1979.
Portable plants in the sand and gravel industry.
4 Telecon. Hoover, Earl, United States Bureau of Mines with Viconovic,
4. Telecon. noo^, GCA/f echnol Qgy Division. june 8, 1979. Portable
plants in the crushed stone industry.
5. Telecon. Renninger, Frederick, National Crushed Stone Association
with Viconovic, George, GCA/Technology Division. June 13,
1979. Portable plants in the crushed stone industry.
6. Telecon. Pressler, J., United States Bureau of Mines with Viconovic,
George, GCA/Technology Division. June 8, 1979. Portable
plants in the gypsum industry.
7. Telecon. Messinger, Arthur, United States Bureau of o
Viconovic, George, GCA/Technology Division. June 8, 1979.
Portable plants in the pumice industry.
8 Telecon. Ampian, S., United States Bureau of Mines with Viconovic,
8. Telecon. gjjjj; GC^Technol0gy D1v1s1on. June 11, 1979. Portable
plants in the clays industry.
9. Telecon. Brown, Howard, Iowa Manufacturing Company with Viconovic,
George, GCA/Technology Division. June 11, 1979. Portable
plant industry data.
10. Telecon. Brown, Howard, Iowa Manufacturing Company with Viconovic,
George, GCA/Technology Division. June 15, 1979. Industry
data.
11. Telecon. Hart, Michael , Colorado Sand .and Gravel Association with
Viconovic, George, GCA/Technology Division. June 18, 1979.
Industry data.
S-48
-------
15,
22,
23,
24,
Telecon. Olson-, DeTv Gifford-Hill Company with Viconovic, George,
GCA/Technology Division. June 28, 1979. Industry data.
Cole, Richard, Flintkote Company with Harnett, William,
Gu,A/ Technology Division. November 8, 1979. Portable
plant operating and movement data.
12,
13. Telecon,
14. Telecon.
Brown, Howard, Iowa Manufacturing Company with Viconovic
George, GCA/Technology Division. June 21, 1979. Portable
and stationary plant sales data.
U.S. Bureau of Mines Mineral Commodity Summaries 1979. Washington
B.C., U.S. Department of the Interior, 1979. 190 p.
16. Telecon,
17. Telecon,
Cole, Richard, Flintkote Company with Viconovic, George,
GCA/Technology Division. June 13, 1979 and June 14,
1979. Portable plant cost and movement data.
Olson, Del, Giffor-Hill company with Viconovic. George,
GCA/Technology Division, June 15, -1979. Portable plant
cost and movement data.
19. Telecon,
20. Telecon,
18. Telecon. Hart, Michael, Colorado Sand and Gravel Association with
Viconovic, George, GCA/Technology Division. June 17,
1979. Portable plant movement data.
Lahu, Peter, Speer Construction with Viconovic, George,
GCA/Technology Division. July 17, 1979. Portable plant
operating and movement data.
Ellis, Oscar, Moline Consumers Company with Viconovic,
George, GCA/Technology Division. July 18, 1979. Portable
plant operating and movement data.
21. Telecon. Hart, Michael, Colorado Sand and Gravel Association, with
Viconovic,'George, GCA/Technology Division. July 19,
1979. Portable plant operating and movement data.
Telecon. Ellis, Oscar, Moline Consumers Company with Harnett,
William, GCA/Technology Division. November 8, 1979.
Portable plant operating and movement data.
Letter and attachments from Schroeder, Philip N., M.C. Schroeder
Company to Viconovic, George, GCA/Technology Division. July 27, 1979
Baghouse cost data.
Letter and attachments from Meyer, Robert J., Joy Industrial
Equipment Company-Western Precipitation Division to Viconovic, George,
GCA/Technology Division. July 27, 1979. Baghouse cost data'.
S-49
-------
25. Telecon. Schroeder, Philip N., M.C._Schroeder Company with Viconovlc,
George, GCA/Technclogy Division. August 6, 1979. UuctworK
cost data.
26. Telecon. Hamlin, Robert, Hamlin Sheet Metal Company with Vlconovlc,
George, GCA/Technology Division. August 8, 1979. Ductwork
cost data.
27. PEDCo. Environmental Inc. Cost Analysis Manual for Standards
Support Document. Cincinnati, PEDCo. Environmental Inc., April 1979.
82 p.
28. Perry, Robert H. and Cecil H. Chilton. Chemical Engineers' Handbook.
New York, McGraw-Hill Book Company, 1973.
29. Memo from Brown, Howard, Iowa Manufacturing Company, to Goodwin,
Don EPA/OAQPS. March 1,1979. Data on portable plants and
stationary Plants in the crushed stone and sand and gravel industries.
30. Included among industry contacts are;
': Douglas E. Anderson, B.L. Anderson, Inc., Jedar Rapids, Iowa
Larry Hinton, Azrelli Construction, Inc., Kankakee, Illinois
Flovd Lillig, Iowa Manufacturing Company, Cedar Rapids, Iowa
William J. Paxson, Chief Engineer, Iowa Manufacturing Co.,
AlbertRRichardson! Gordon Quarries, Inc., Forrest City, Missouri-
Howard L. Slife, V.P., Cedar Rapids Aggregate Equipment Sales,
Iowa Manufacturing Co., Cedar Rapids, Iowa
• Robert Treager, Farmers Stone and Treager Quarries, Inc.,
lafi, Missouri
31 U.S. Bureau of Mines Mineral Commodity Profiles Stone. MCP-17. U.S.
Department of the Interior, Washington, D.C. July 19/8. p.10
32. Lr.S. Bureau of Mines. Mineral Commoidity Profiles. Sand and Gravel.
MCP-23. U.S. Department of the Interior. Washington, u.t.
September 1978. p.12
33. Highway and Heavy Construction. September 1979. p. 150-158.
24. Iowa Manufacturing Company. Cedar Rapids. Iowa
ig-
S-50
-------
TECHNICAL REPORT DATA
(nease read Instructions on the reverse before completing)
EPA-450/3-83-QQla
3. RECIPIENT'S ACCESSION MO.
I. TITLE AND SUBTITLE
Nonmetallic Mineral Processing Plants _
Background Information for Proposed Standards
5. REPORT DATE
April 1983
-ftp.
n%
6. PERFORMING ORGANIZATION CODE
)OR(S)
8. PERFORMING ORGANIZATION REPORT N'O.
IZATION NAME AND ADDRESS
Office of Air Quality Planning and Standards
U.S. Environmental Protection Agency
Research Triangle Park, North Carolina- 27711
10. PROGRAM ELEMENT NO.
11. CONTRACT/GRANT NO.
68-02-3057
12. SPONSORING AGENCY NAME AND ADDRESS
DAA for Air Quality Planning and Standards
Office of Air, Noise, and Radiation
U.S. Environmental Protection Agency
Research Triangle Park, North Carolina 27711
13. TYPE OF REPORT AND PERIOD COVERE-1
14. SPONSORING AGENCY CODE
EPA/200/04
Standards of performance for the control of emissions from nonmetallic mineral
processing plants are being proposed under the authority of Section 111 of the Clean
Air Act. These standards would apply to new, modified, or reconstructed facilities
at any nonmetallic mineral processing plant including crushers, grinding mills,
screens, bucket elevators, conveyor belt transfer points, bagging operations, storage
bins, and enclosed truck and railcar loading stations. This document contains
background information and environmental and economic impact assessments, as proposed
under 40 CFR Part 60, Subpart 000.
7.
KEY WORDS AND DOCUMENT ANALYSIS
DESCRIPTORS
b.lDENTIFIERS/OPEN ENDED TERMS
c. cos AT I ! ield/Group
Air pollution
Pollution control
Standards of performance
Nonmetallic mineral processing plants
Particulate emissions
Air Pollution Control
13B
8. DISTRIBUTION STATEMENT
Unlimited
19. SECURITY CLASS (This Report/
Unclassified
21. NO. OF PAGES
469
20. SECURITY CLASS (Thispage!
Unclassified
22. PRICE
EPA Form 2220-1 (Rev. 4-77)
PREVIOUS EDITION IS OBSOLETE
-------
-------