Central Park Weat

5001 South Miami Boulevard. Suite 300 •

P.O. Box 12077

Research Triangle Park, NC 27709-2077

(919) 94100333

FAX (919) 94100234

MEMORANDUM

TO: John Schaefer, EPA/OCO

FROM: Kenneth R. Meardon

Pacific Environmental Services, Inc.

DATE: May 4, 1998

A 92 19

11:- B-~f I

SUBJECT: Equipment Leak Analysis for Amino and Phenolic Resins NESHAP

The purpose of this memorandum is to present the results ofthe MACT floor

determination and regulatory alternatives analysis for amino/phenolic resin facilities with

regards to equipment leaks. This memorandum also documents the procedures used to

estimate baseline emissions for the 40 major sources included in the analysis and documents

the estimation of emission reductions and control costs associated with the selected standard

for equipment leaks. The estimation of energy and secondary impacts is documented in a

separate memorandum title "Estimated Energy and Secondary Air Impacts for AminolPhenolic

Resin Facilities," docket item D-B-16 in docket A-92-19.

MACTFIoors

Based on data provided by the U.S. Environmental Protection Agency through surveys

and follow-up telephone conversations, two amino/phenolic resin facilities were identified as

having equipment leak programs subject to Federal, State, or local regulations. These two

facilities are: Georgia Pacific's Elk Grove, California plant and Solutia's Springfield,

Massachusetts plant. However, only one facility - Salutia's Springfield, MA, plant - was

identified as a likely major source. This facility is subject to the State of Massachusetts rule

310 CMR 718(19), which essentially requires the facility to implement a leak detection and

repair (LDAR) program equivalent to 40 CPR·part 60, subpart W. A copy of310 CMR

718(19) is found in Attachment 1.

New Facilities

The MACT floor for new facilities is set by the amino/phenolic resin facility with the

most stringent LDAR program. The only likely major facility identified as having a fonnal

LDAR program is Solutia's Springfield, MA, plant. A number of facilities have identified the

WASHINGTON. D.C' RESEARCH TRIANGLE PAIIl<. HC • LOS ANGELES. CA • CINCltlNATL OH

:0) I -
; ......

.

..///1.. f

•

lohn Schaefer

May 4, 1998

page 2

repair of leaks when they are seen or otherwise identified (e.g., smell or sound). However,

these maintenance-type LDAR programs are unlikely to be more stringent than the LDAR

program being implemented at Solutia's Springfield, MA, plant. Therefore, the MACT floor

for equipment leaks for new sources is represented by the LDAR program at Solutia's

Springfield, MA, facility.

Existing Sources

There are 40 major sources in this source category. The top 12 percent is represented

by the best performing 5 facilities. As noted in the previous paragraph, only one major source

bas been identified as having a LDAR program as the result of Federal, State, or local

regulations, while others have a maintenance-type LDAR program. These maintenance-type .

programs are likely to be less effective at reducing emissions than the LDAR program in place

at the Solutia, Springfield facility. Unfortunately, no information is available to quantify the

emission reduction being achieved from these maintenance-type programs. In addition, it is

not possible to estimate the costs associated with such programs. Therefore, the average of the

best performing 5 facilities cannot be defined at this time, and the MACT floor for equipment

leaks for existing sources is considered to be no control.

Regulatory Alternatives

For new sources, one regulatory alternative was identified - the application of a LDAR

program based on 40 CFR part 63, subpart H (referred to hereafter in this memo as the HaN

LDAR program). For existing sources, two regulatory alternatives were identified - 40 CFR

part 60, subpart VV and the HaN LDAR program. Table 1 provides a briefsummary of

SUbpart VV's and the HaNIs LDAR programs.

In conducting the regulatory alternatives analysis, there are several items that need to

be identified to determine whether or not any of the regulatory alternatives are cost effective.

First, component counts for each of the major facilities need to be determined. Second,

estimates of emissions and emission reductions need to be made. Third, the costs associated

with the LDAR programs need to be estimated. The following paragraphs present the methods

Used in the regulatory alternative analysis.

Estimation of Component Counts

A questionnaire was sent to companies requesting specific information on component

counts, the weight percent HAP contacting the components, and time the component is inJ

Contact with the HAP. Facilities were also given the option of providing information on the

number of storage tanks, from which the number of components would be estimated using the
..

John Schaefer

May 4,1998

page 3

information presented in Table 2. Facilities that use only heavy liquids in their process were

asked to provide information on the number ofstorage tanks only. Table 3 shows the number

of light liquid and heavy liquid storage tanks used to estimate component counts for those

facilities that did not provide specific component counts. One facility (Solutia, Springfield)

provided a printout of components. These components were added by hand to develop

component counts and type ofservice for this facility. The actual counts used for 38 ofthe 40

facilities are shown in the emission estimation worksheets in Attachment 2. For the other two

facilities (3M-North Cordova and Cytec-Kalamazoo) equipment counts were not estimated

because of lack of data.

Emission Estimation

Except for 3M-North Cordova and Cytec-Kalamazoo, emissions for each facility were

estimated using the equipment counts and the emission factors shown in Table 4 for

uncontrolled emissions and for each of the two LDAR programs identified as regulatory

alternatives. In addition, the level of emissions were adjusted based on the percent HAP and

time in contact information provided in the previously mentioned questionnaire responses. If

facilities did not provide specific information, then default values of 100% HAP (except for

formaldehyde) and 8,760 hours per year were used to estimate emissions. For estimating

formaldehyde, the assumption was used that the formalin used was 37% formaldehyde with a

7% methanol component. This is a common fonnulation for formalin. Attachment 2 contains

the emission estimation worksheets for each facility.

For 3M-North Cordova and Cytec-Kalamazoo, emissions were estimated using the

average emissions from 27 of the 29 facilities for which costing was performed. The two

largest facilities, Cytec-yvallingford and Solutia-Springfield, were not used to derive this

average. In addition, the 11 facilities that are composed essentially of heavy liquid

components only were also not used to estimate emissions from 3M-North Cordova and CytecKalamazoo.

The basic emission factors used were taken from a memorandum prepared for the

Group IV resin NESHAP project (see Attaclunent3), with two exceptions. The first exception

is for pumps in light liquid service that are monitored quarterly with a leak defmition of 5,000

ppm. (the HaN LDAR specifies a leak definition of 5,000 ppm for polymerizing monomers

when Phases U and ill of the HaN LDAR program become effective.) For this component,

the emission factor was estimated as the mid-point between the emission factor for a quarterly

LDAR interval with a leak defmition of 1,000 ppm and a quarterly LDAR interval with a leak

definition of 10,000 ppm.

.]
John Schaefer

May 4, 1998

page 4

The second exception is for components in heavy liquid service. For pumps, openended lines, and connectors in heavy liquid service, the SOCMI <10,000 ppm emission

factors were used (see Attachment 4). For sampling connections in heavy liquid service, there

is no <10,000 ppm emission factor. The <10,000 SOCMI emission factor for open-ended

lines was assumed to be applicable to sampling connections in heavy liquid service.

Emission Reduction Cost Credits

Cost credits were assigned to the LDAR programs based on the emission reductions

achieved and the type of compound. Table 5 shows the values used to calculate this credit.

The calculation of the cost credits for 29 of the facilities is shown in Attachment 2. For 3MNorth Cordova and Cytec-Kalamazoo, the emission reduction cost credit was estimated as the

average achieved by 27 of the 29 facilities (excluding the emission reduction cost credits of

Cytee-Wallingford and Solutia-Springfield).

Cost EstimatioD

Costs (1989$) were estimated for each facility except for those that use heavy liquids

only or those that would not be affected by a HON-based LDAR program. (Table 6 lists the

facilities for which costing was not performed.) Attachment 5 presents the cost algorithms

used to estimate the costs. Attaclunent 6 contains the cost estimates for each facility for both

Subpart VV and the HON LDAR programs. Attachment 7 discusses the derivation of many of

the cost elements in the costing. Specific cost items and assumptions are discussed below.

Type of Monitoring Program. Facilities subject to LDAR may use subcontractors or

in-house personnel to conduct a LDAR program. Because of the relatively low number of

components at most amino and phenolic resins facilities, it was assumed that each facility

would elect to conduct the LDAR programs using in-house personnel. Using in-house

personnel should reduce the cost of implementation, in part, by avoiding travel to monitor

pumps.

Monitoring Instrument. Facilities must decide whether to purchase or rent a

monitoring instrument. The cost of a basic monitoring instrument is estimated to be $6,500

(1989$), while the cost to rent an instrument varies depending on the numbers of days of

monitoring that is required. Because of the relatively low number of components, rental of a

monitoring instrument was found to be less expensive than the purchase of the instrument for

aU of the amino and phenolic resin facilities. Thus, for all facilities, the number of monitoring

days required per year was estimated and the cost of the monitoring instrument was then

calculated based on renting the instrument. In addition, costs were included for calibrating the

rental instrument and for calibration gases.

If
-;---_.....

10hn'Schaefer

May 4, 1998

pageS

Lolgiol ys Tageing. In implementing a WAR program, a decision must be made as

to whether to tag the components initially or to enter them into a log. Again, because of the

relatively low number of components, it was assUined'thii aii fucilities would log their

~~p_onents rather than tag th~m. .-'

Database System. Another decision to be made at the outset of implementing a LDAR

program is whether to purchase a database system or use others means (e.g., a log book) to

track the components subject to the LDAR and those components identified as leaking. For all

except the two facilities with the greatest number of components, it was determined that a

database system would not be purchased. However, it was assumed that costs would be

incurred for entering the data in a central location. These costs were estimated to be $1.88 per

component for the initial data eritry and $0.88 per component for subsequent data entry. For

the two facilities for which a database system was assumed to be purchased, it was assumed

that a siniple spreadsheet program would be purchased and that in-house personnel would

create a customized spreadsheet to track components.

Reporting. Recordkeepine. Training. and Administration. These activities are required

for each facility to implement an LDAR and to maintain it once it is in place. There are some

initial costs associated with the implementation (e.g., training of personnel) and there are some

annual costs. For the purposes of the cost analysis, a number of assumptions were made as to

the number of technical hours required to implement the WAR programs. These assumptions

are detailed in Table 2 of Attachment 7 to this memo. The following summarizes the

estimated'repo~ordkeeping, training, and administration burden for a SOCMI-based

LDAR program and a HON-based LDAR program. Because the SOCMI-based program does

not cover connectors, a slightly reduced level of effort was assumed for that WAR program.

\

500 Method 21

Components

>500 Method 21

ComponentS

Initial Hours Annual Hours Initial Hours Annual Hours

SOCMI-based

LDAR: 46 183· . \ '

HON-based

LDAR: 60 200

. 318 85 .

340 . 104

Leak Frequencies. In developing these cost estimates, initial leak and fmalleak

frequencies have (0 be identified. Attachment 3 also presents data used to detennine the leak

s
John Schaefer

May 4, 1998

page 6

frequencies for the HON and Subpart VV, with one exception. Initial leak and fmalleak

frequencies for pumps in light liquid service had to be developed specifically for a quarterly

LDAR interval with a leak defmition of 5,000 ppm. For this component, the fmalleak

frequency was estimated using the equation from the Protocol document (see Attachment 4) for

light liquid pumps with a leak definition of 5,000 ppm. The initial leak frequency was

calculated by using the uncontrolled emission factor (Le., 0.0199 kglhr) and the same equation

and solving for the aven~ge leak rate.

Cost Effectiveness

Table 7 presents the results of the cost effectiveness analysis for both new and existing

facilities. The information presented in this table is from uncontrolled emission levels to the

SOCMI Subpart VV LDAR program level and from uncontrolled emission levels to the HON

LDAR program level. Please note that Solutia-Springtield is already achieving the equivalent

of the SOCMI Subpart VV LDAR program. Therefore, implementation of the soeMl

Subpart VV LDAR program would not actually achieve the additional emission reductions or

costs presented in Table 7. Similarly, implementation of a HON LDAR program in relation to

baseline emissions would achieve an emission reduction of 20.2 megagrams (= 45.3 - 25.1) at

a"cost of $12,152 (= $30,356 - $18,204) < .. (_:.;.(.-!~.

As seen in Table 7, the average cost effectiveness of implementing the SOCMI Subpart

VV LDAR program from no control at each ofthe amino/phenolic resin facilities is

approximately $3,100 per megagram of emission reduction. The average incremental cost

effectiveness of implementing the HON LDAR program from no control is approximately

$2,300 per megagram of emission reduction. The average incremental cost effectiveness of

going from the SOCMI Subpart VV program to the HON program is approximately $1,340

per megagram of emission reduction.
John Schaefer

May 4,1998

page 7

TABLE 1

SUMMARY OF LDAR REGULATIONS EVALUATED FOR

AMINO AND PHENOLIC RESIN FACIUTIES

I

j

;

Component and Service 40 CFR Part 60, 40 CFR Part 63,

Subpart VV SubpartH

Valves, gas/vapor and light Monthly monitoring with skip Quarterly monitoring with leak

liquid period option for quarterly definition of 500 ppm (Phase

monitoring. Leak definition = Ill).

10,000 ppm.

Valves, heavy liquid If indication of leak,(sight, sound, smell), monitor to confirm leak

Pumps, heavy liquid (leak definition =10,000 ppm) and then repair.

Pumps, light liquid Monitor monthly with weekly Monitor monthly with weekly

visual inspection. Leak visual inspections. Leak

definition = 10,000. defInition = 5,000 (Phase 01).

Compressors Use of barrier fluid system that prevents leakage of VOC to

atmosphere.

Open Ended Lines Caps, blind flanges, etc.

Pressure Relief Devices, No detectable emissions

gas/vapor

Pressure Relief Devices, light If indication of leak (sight, sound, smell), monitor to confino leak

or heavy liquid (leak definition = 10,000 ppm) and then repair.

Sampling Connections Closed purge system or closed vent system to control device

Flanges and other connectors, If indication of leak (sight, Annual monitoring with leak

gas/vapor sound, smell), monitor to definition of 10,000.

Flanges and other connectors,

confirm leak (leak definition = 10,000 ppm) and then repair. light liquid

Flanges and other connectors, If indication of leak (sight, sound, smell), monitor to confirm leak

heavy liquid (leak definition = 10,000 ppm) and then repair.
John Schaefer

May 4, 1998

page 8

TABLE 2

ESTIMATED COUNTS BY TYPE OF STORAGE TANK

(number per tank)

COMPONENT UGHTUQUID HEAVY LIQUID

STORAGE TANI( STORAGE TANK

Valves 15 15

Pumps 2 1

Open-Ended Lines 2 1

Sampling Connections 2 1

Flanges 30 30
John Schaefer

May 4. 1998

page 9

TABLE 3

STORAGE TANK COUNTS USED TO ESTIMATE

COMPONENT COUNTS

Number of Storage Tanks

Facility

Light Liquid Heavy Liquid

3M Hartford 4 2

BTL Specialties 1 0

Borden - Fayetteville 4 5

j:ytec - Mobile , 2 1

"Dexter - Birmingham 1 1

Dexter - Waukegan 2 1

Freedom - Charlottea 0 1

Solutia - Addyston 2 1

[,Neste - Moncure 1 3

["Neste - North Winnfield 2 8

Schenectady 1 3

Simpson Timber 2 3

a Indicated that two pumps were used in light liquid service. even

though there were no storage tanks in light liquid service.
John Schaefer

May 4,1998

page 10

TABLE 4

SUMMARY OF EMISSION FACTORS

(lbslhr/component)

COMPONENT UNCONTROLLED SUBPARTVV HON

Valves, gas 0.0131 0.00165 0.001

Valves, light liquid 0.00887 0.00141 0.0011

Valves, heavy liquid 0.000506 0.000506 0.000506

Pumps, light liquid 0.0438 0.0135 0.01225

Pumps, heavy liquid 0.00463 0.00463 0.00463

PROs, gas/vapor 0.2~88 0.007 0.007

PRDs, liquid 0.2288 0.2288 0.2288

OELs, gas/vapor and light . 0.00374 0 0

liquid

OELs, heavy liquid 0.0033 0 0

Compressors 0.5016 0 0

Sampling Connections, 0.033 0 0

gas/vapor and light liquid

Sampling Connections, 0.0033 0 0

heavy liquid

Flanges and Other 0.00403 0.00403 0.000286

Connectors, gas/vapor and

light liquid

Flanges and Other 0.00018 0.00018 0.00018

Connectors. heavy liquid

/0
l-. John Schaefer

May 4, 1998

page 11

TABLES

COMPOUND VALUES USED IN ESTIMATING

EMISSION REDUCTION CREDITS

Compound Credit Value ($/Mg)

Aniline 1,257

Cresol, m-, p- 1,808

Cresol,o- 1,279

Creyslic acid 1,213

Ethylbenzene 386a

Ethylene glycol 882

Formalinb 220

Hydrochloric acid 83

Maleic anhydride 1,257

Methanol 108

Phenol 904

Toluene 232

Xylene 240

SOURCE: December 25, 1989, Chemical Marketing Reporter. See Attachment 8.

a Used this value for butyl cellusolve.

b 35% fonnaldehyde and 7% methanol.

I (

---~~
John Schaefer

May 4, 1998

page 12

TABLE 6

FACILITIES FOR wmCH LDAR COSTING

WAS NOT PERFORMEDa

Company City

Dynachem Georgetown

Georgia Pacific Columbus

Conway

Crossett

Louisville

Russellville

Taylorsville

National Starch Salisbury

Neste Andalusia

Neste Springfield

Perstorp Florence

a Except for Georgia Pacific-Columbus and -Conway,

all these facilities have components only in heavy liquid

service. GP-Columbus and -Conway have a few components

in light liquid service that would be affected by a SOCMI-based

LDAR program, but not by a HON-based program because

they are in HAP service less than 300 hours per year. No

costing for either LDAR program was performed for these two

facilities.

•
(

TABLE 7. COST EFFECTIVENESS SUMMARY

-7

SeCMI SeCMI seeMI HON HON Incremental

Facility Location Emission Annual Cost Emission Cost Cost

Reduction Costs Effectiveness Reduction Effectiveness Effectiveness

(Mg/yr) ($/yr) ($lMg) (Mglyr) ($lMg) ($JMg)

3M Col Grove 0.96 $6,177 6434 1.51 4615 1438

3M North Cordova ctltJ 2.13 4174 2479

3M Hartford 1707 1119--

Akzo Louisville 3.12 3712 2647

Borden Fayetteville · 8 cgp 42859 28378-

Borden Louisville 0.4 ,34 56 1 49990 34400

BTL Specialties Toledo 0.24 $6.121 25504 0.36 20111 9325-

Cytec Kalamazoo 4174 2479

Cytec Mobile 199 2830 1573--

Cytec Wallingford .10 $36,162 41.20 1415 918

-- Cytec AC Molding Wallingford 0.93 $7444 8004 4068 2341

Dexter Birmingam 5, 4761 1515-

Dexter Waukegan 1.32' $6,167 3529 1373--

Freedom Chartotte 0.27' $5 2184~ 24664 100900 -

GP Albany · B $5,964 1.27 5203 1092

GP Lufkin 0.48 S6,098 12704 1.03 6657 1380

GP Port Went 0.53 $6,138 11581 0.74 11877 12624

GP White City 1.96 $5.825 2972 2.73 3430 4596

'otero Paper Hampton Qib 7.65 2508 4288

Solutia Addyston .98 ,n6 (W:) 2818 1560 ,.,-

Solutia Springfield 25.10 $1 , 04 45.30 670 602

Neste Moncure ,69 <mD 4994 2223 .--

Neste North Winnfield 1.78,. $7,657 302 3138 934--

PO George St. Louis · 3 , 1 6636 2.83 2155 289

Pioneer Florence 1.53 $7,180 4693 2.62 3423 1640

Ranbar Manor $8,848 d!> c!J 4823 3731

Schenectady Rotterdam JuncUo 1. .2 4741 2077 ,.,-

Simpson Timber Portland 1.04' 63 61 1.5 4863 2175 cSpaulding DeKalb .6 $6,180 11036 0.88 7973 2613

Totals 77.67 $239,516 3084 144.12 $328,669 2281 1342

NOTE: Solutia, Springfield Is already achieving the SOeMI emission reduction and incurring the SOCMI costs. Implementation of a HON-based IOAR

program win result in an incremental emission reduction of 20.2 megagrams at an estimated cost of $12,152.

- \~. \') -7),( yo -~ -~ l,11 -- -v1t,vW I

1_., I r- "u- '2./. I .,(..\llf (~.\r -.1
-.

ATIACHMENT 2

EMISSION ESTIMATION AND

EMISSION REDUCTION CREDIT WORKSHEETS

11
3M-Cottage Grove

Components HAP Contacl llncontroUed SUbpart W HON CredIts ($\ ($/Mal

Number of WeIght % nma In EmIssions Emlsslon RedUdion Credit

SOCMI HON

o

o

o

o 0

o 0

Vatves,aIv o 0

IComponent

Valves, D 20 1 8760 1554.024 247.032

o 0

192.72

o

130.4265 135.8464 220

o 0 o

Valves, hl 14

7

0.37

1

8760

8760

22.9605608 22.9606608

31.02792 31.02792

o 0

22.96066

31.02792

o

-0 0

o 0

220

904

Pumps, D 1 1 8760 383.688 118.26

o 0

107.31

o

26.48742 27.58013 220

IPumPs, hi 2

2

0.37

1

8760

8760

o 0

30.013512 30.013512

81.1176 81.1176

o 0

o

30.01351

81.1176

o

o 0

o 0

220

904

Compressors, D o 0

o 0

o

o

o 0 o

Compressors, hi o 0

o 0

o

o

PRVs,gJv

o 0

o 0

o 0

o

o

o

o 0 o

PRVs.n o 0

o 0

o

o

o 0 o

PRVs,hl o 0

o 0

o

o

o 0 o

OELs,gJv o 0

o 0

o

o

o 0 o

OELs,l1 2 8160 65.5248 0

o 0

o

o

o 0 o

OELs. hI 3

3

0.37 8760

8760

32.08788 0

86.724 0

o 0

o

o

o

Sampling Conn, oN

Samo\lnQ Conn, D 1 8760

o 0

o 0

o 0

289.08 0

o 0

o

o

o

o

o

28.84768 28.84768 220

Samp\lnQ Conn, hi

es,aN

2

2

0.37 8760

8760

o 0

21.39192 0

57.816 0

o 0

o 0

o 0

o

o

o

o

o

o

2.134728 2.134728

23.70755 23.70755

220

904

Conn/Ranges, U 35 8760

o 0

1235.598 1235.598

o 0

o

87.6876

o

o 114.5515 220

Totsls Ibslyr 136

ConnlFlanlles. hl 22

20

0.37

1

8760

8760

o 0

12.835152 12.835152

31.536 31.536

o 0

3935.42544 1810.380845

o

12.83515

31.536

o

597.2084

o 0

o 0

211.6039 332.668

220

904

1.96171272 0.905190422 0.298604

Incremental emission Redudlon (Mg/yr)

1.78510 0.82118

0.96391

0.27089

1.51421

IS

Page 1
3M-Hartford

Number of Weight % Time In EmIssions Emission Reduction Ctedlt

Components HAP Conlact UnconlroUed SUbpart W HON Credlta 1$\ ($/Mil)

SOCMI HON

\- Component

VaJves,aIV

Valves, n

Valves,hI

PumPs, 0

Pumps, hi

Compressors, n

Compressors, hi

PRVs,g/v

PRVs,U

PRVs, hi

OELs,aJv

OELs.D

OELs,hI

Sampling CoM, oJv

3D

3D

30

4

4

4

4

4

4

1

1

0.44

1

1

0.44

1

1

0.44

8760

8760

8760

8760

8760

8760

8760

8760

8760

o

o

o

2331.038

2331.038 .

o

58.509792

o

o

1534.752

1534.752

o

71.383488

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

131.0495

131.0496

o

50.87808

o

o

o

o

o

o 0

o 0

o 0

370.548 289.08

370.548 289.08

o 0

58.509792 58.50979

o 0

o 0

473.04 429.24

473.04 429.24

o 0

71.383488 71.38349

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

206.311 214.8842

213.4252 222.294

o 0

111.7287 116.338

115.5815 120.3497

o 0

o 0

o 0

13.79094 13.79094

14.26649 14.26649

5.077192 5.077192

232

240

220

232

240

220

220

220

232

240

220

samPling CoM, II "

4

Sampling COM, hi 4

ConnIFlanges, oJv

1

0.44

8760

8760

8760

1156.32

1156.32

o

50.87808

o

o

o

o

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

121.6848 121.6848

125.8808 125.8808

5.077192 5.077192

232

240

220

ConnIFlanges, U

ConnIFlanges, hi

60

60

60 0.44

8760

8760

8760

o

2118.168

2118.168

o

41.62752

o

o

o 0

2118.168 150.3216

2118.168 150.3216

o 0

41.62752 41.62752

o 0

o 0

o 207.0854

o 214.2262

o 0

232

240

220

Tolals Ibstyr 306

lonstvr

Incremenlal EmIsskm RedUdion II tglyr)

14815.9282

7.40796408

6.72~6

6095.0328 1908.804

3.0475164 0.954402

2.76469 0.86583

3.95577 5.85463

932.8237 1380.955

Page 2
,

Number of Welaht% Time In Emissions EmIssion Reduction Credit

Component Components HAP Contact Uncontrolled SubpartW HON Credits IS) . ISIMa)

SOCMI HON

Valves, aIV 0 0 0

0 0 0

0 0 0

Valves, U 15 0.1957 8760 228.091873 36.2581218 28.28648 33.58787 34.98362 386

15 0.81 8760 944.06958 150.07194 117.0774 86.43719 90.02909 240

15 0.522 8760 608.400396 98.713028 75.44988 51.06197 53.18385 220

Valves, hi 0 0 0 0 0 220

0 0 0 0 0 220

0 0 0

Pumps, a 2 0.1957 8760 150.175483 46.286964 42.00113 18.18968 18.94008 386

1 0.81 8760 310.78728 95.7906 88.9211 23.40525 24.37081 240

1 0.522 8760 200.285136 61.73172 56.01582 13.82643 14.39683 220

PumpS,hI 0 0 0 0 0 220

0 0 0 0 0 220

0 0 0

CompressOl'8, a 0 0 0

0 0 0

0 0 0

Compressors, hi 0 0 0

0 ·0 0

0 0 0

PRVs,aIV 0 0 0

0 0 0

0 0 0

PRVS,D 2 0.1957 8760 784.478323 784.4783232 24.00065 0 133.1509 386

1 0.81 8760 1823.47328 1623.47328 49.6692 0 171.3295 240

1 0.522 8760 1046.23834 1046.238338 32.00904 0 101.2113 220

PRVs, hi 0 0 0

0 0 0

0 0 0

OELs, aIV 0 0 0

0 0 0

0 0 0

OELs,II 2 0.1957 8760 12.8232034 0 0 2.245195 2.245195 386

2 0.81 8760 53.075088 0 0 5.777928 5.777928 240

2 0.522 8760 34.2039456 0 0 3.413258 3.413258 220

OELs, hi 0 0 0 0 0 220

0 0 0

0 0 0

sampUng COM, glY 0 0 0

0 0 0

0 0 0

Sampllna Conn, a 2 0.1957 8760 113.145912 0 0 19.81054 19.81054 386

2 0.81 8760 468.3096 0 0 50.98172 50.98172 240

2 0.522 8760 301.79952 0 0 30.11698 30.11698 220

Sampling COM, hi 0 0 0 0 0 220

0 0 0 0 0 220

0 0 0

Conn1Flanaes, gIv 0 0 0

0 0 0

0 0 0

Conn1FIanaes, II 30 0.522 8760 552.841848 552.841848 39.23394 0 51.25362 220

0 0 0

0 0 0

ConnlFlanaes, hi 0 0 0 0 0 220

0 0 0 0 0 220

0 0 0

Totats Ibs/vl 95 7432.1988 4493.884161 550.6646 338.854 805.1952

tona/yr 3.7160994 2.246942081 0.275332

Uglyr 3.37122 2.03841 0.24978

Incremental emission Reduction fI ~1Vr) 1.33281 3.12144

;(0

Page 3
,

Borden - FayellevlDe

Number of Weight % Time In emissions Emlsslon Reduction Credit

Components HAP Contact UncontroUed Subpart W HON Credits (S) ($/Mg)

SOCMI HON

Compenent

Valves. gIv

Valves, n

Valves. hi

PumpS,U

Pumps. hi

Compressors. D

Compressors. hi

PRVs,glv

PRVs.D

PRVs, hi

OELs.gIv

OELs.n

OELs.hl

Sampling CoM, g/v

Sampling Conn. U

SampUna COM. hi

Conn1Flanges. glv

60

75

15

8

5

1

8

5

1

8

5

1

1

0.44

1

0.44

1

0.44

1

0.44

1

400

400

400

400

400

400

400

400

400

400

400

400

o

o

o

212.88

o

o

6.6792

3.036

o

140.16

o

o

4.0744

1.852

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

11.968

o

o

2.904

1.32

o

o

o

o

105.6

o

o

2.904

1.32

o

o

o

o

o

o

33.84

o

o

6.6792

3.036

o

43.2

o

o

4.0744

1.852

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

26.4

o

o

6.6792

3.036

o

39.2

o

o

4.0744

1.852

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

8.770897

o

o

o

o

4.749923

o

o

o

o

o

o

o

0.586294

o

o

0.289794

0.541268

5.173183

o

o

0.289794

0.541268

9.135371

o

o

o

o

4.945877

o

o

o

o

o

o

o

0.586294

o

o

0.289794

0.541268

5.173183

o

o

0.289794

0.541268

108

220

108

220

904

108

220

904

108

220

904

ConntFlanaes, II

ConntFlanges. hi

120

150

3D

0.44

1

400

400

400

o

193.44

o

o

4.752

2.16

o

o

193.44

o

o

4.752

2.16

o

o

13.728

o

o

4.752

2.16

o

o 8.803817

o 0

o 0

108

220

904

Totals Ibs/yr 492

lonslvr

Incremental EmIssion Reduction (MaJyr)

~I

695.0496

0.3475248

0.31527

293.0336

0.1465168

0.13292

0.18235

101.8616

0.050941

0.04821

0.26906

20.94242 30.30667

Page 4
Borden - LouisvIlle

Number of Weight % TIme In EmIssions Emlsslon Reduction CtedIt

ComP«lsnl ComPOll8llta HAP Contad UnconlroUed Subpart W HON CredIts ($) (SIMa)

Valve8.aJv o

o

o

o

SOCMI HON

o

o

o o o

Valves. U 45 1 400 159.66

o

o

25.38

o

o

19.8

o

o

9.075442

o

o

9.452572

o

o

149

Valves, hi 45 1 400 9.108

o

o

9.108

o

o

9.108

o

o

o

o

o

o

669

Pumps,U

PumPS, hi

Compressors, II

6

3

1 400

400

105.12

o

o

5.556

o

o

o

o

o

32.4

o

o

5.556

o

o

o

o

o

29.4 4.914851

o 0

o 0

5.556 0

o 0

o

o

o

o

5.117609

o

o

o

o

149

669

Compressors, hi o

o

o

o

o

o

o o o

PRVs,gtv o

o

o

o

o

o

PRVs,n

PRVs,hI

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o \ '.-J

o o o

OELs,gJv o

o

o

o

o

o

o

o

o

OELs,n

OELs,hl

6

3

1

1

400

400

8.976

o

o

3.98

o

o

o

o

o

o

o 0.606652

o 0

o 0

o 1.201687

o

0.606652

o

o

1.201687

149

669

o o o

Totals Ibslyr 297 80.64 22.35313 32.04252

o

o

149

149

669

669

o

o

o

o

o

5.352808

1.201687

o

o

o

o

o

o 9.109506

5.352808

1.201687

o

o

o

o

o

o

o

o

o

o

o

o

o

6.48

o

10.296

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

6.48

o

145.08

224.004

o

o

o

o

o

o

o

o

o

o

o

o

o

3.96

79.2

6.48

o

145.08

527.1

400

400

1

1

1

3

6

90

90

OS,a

5amDlina Conn, hi

ConnlFlanges, hi

Sampling Conn, U

SampHng Conn, gJv

ConnlFlanges, gJv

tonslVr

Mg/yr

0.26355

0.23909

0.11200

0.10161

0.04032

0.03658

Inctemental Emission Reduction (Mglyr) 0.13748 0.20251

Page 5
BTL Spectlalies

ComDonent

Number of Weillht % TIme In EmIssions

ComDonents HAP Contact Uncontrolled SUbpart W HON

Ernlsalon Redutllon Credit

Credlts ($) ($'Mg)

Valves, a/V o 0

o 0

o

o

SOCMI HON

o 0 o

Valves, U

Valves, hi

15 1 2190 291.3795 46.3185

o 0

o 0

o 0

o 0

o 0

38.135

o

o

o

o

o

12.00517

o

o

o

o

12.50404

o

o

o

o

108

Pumps, U

PtJmI)lI,hI

Compressors, I

2 1 2190 191.844 59.13

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

53.655 6.501457

o 0

o 0

o 0

o 0

o

o

o

o

6.769669

o

o

o

o

108

Compressors, hi o 0

o 0

o

o

PRVs,aIv

PRVs,U

PRVs, hi

oas,oJv

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o

o

o

o

o

o

o

o

o

o

o

o

o

O·

o

o

o

o

o 0

o 0

o 0

o 12.05023

108

108

108

o

o

o

o

o

o

7.080795

o

o

o

o

o

o

0.80249 0.80249

7.080795

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

18.7902

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

2190 264.771 264.771

2190 144.54 0

2190 16.3812 0

1

1

2

2

30

SamDIing Conn, oJv

Sampling Conn, U

ConnlFlanaes. hi

OELs,hl

ConnIFlanges, U

oas,n

Samprmg Conn, hi

ConnIFIal\lles, oIv

Totals Ibslvr 51

tonsIVr

Mgtyr

InaementaJ emission Reduction (Mglvr)

908.9157 370.2195

0.45445785 0.18510975

0.41228 0.16793

0.24435

108.5802 26.38991 39.20722

0.05429

0.04925

0.36303

Page 6
CyIac • Mobile

Number of Welaht % Time In emissions emission Reductlon Credll

Comoonent Components HAP Contad UncontroUed SUbpartW HON Credits ($) l!IMal

Valves, aN o

o

o

o

o

o

SOCMI HON

o

o

o

o 0

o 0

429.24 46.23258

Valves,lI

Valves, hi

Pumns, U

30

15

4

1

0.44

1

8760

8760

8760

2331.036

o

o

29.254896

o

o

1534.752

o

o

370.548

o

o

29.254896

o

o

473.04

o

o

289.08

o

o

29.2549

o

o

85.37007

o

o

o

o

88.91762

o

o

o

o

48.13987

o

o

96

220

96

Pumps, hi

ComDressors, U

Comoressors, hi

2 0.44 8760 35.691744

o

o

o

p

o

o

o

o

35.691744

o

o

o

o

o

o

o

o

35.69174 0

o 0

o

o

o

o

o

o

o

o

o

220

o

o

o 85.69049

Tolals Ibslvr 153

Incremental emission Reduction (Mntvr)

954.402 192.7388 283.8841

PRVs,aN

PRVs, II

PRVs, hi

OELs,II

OELs, hi

S8moHriQ CoM, gJv

S8mDllna Conn, II

samDllno Conn, hi

ConnIFJanaes. oJv

ConnIFlanges, II

Conn/Flanges, hi

tonslvr

Molvr

4

2

4

2

60

30

1

0.44

0.44

1

0.44

8760

8760

8760

8760

8760

8760

o

o

o

o

o

o

o

o

o

o

o

o

131.0496

o

o

25.43904

o

o

o

o

o

1156.32

o

o

25.43904

o

o

o

o

o

2118.168

o

o

20.81376

o

o

7407.96408

3.70398204

3.36023

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

2118.168

o

o

20.81376

o

o

3047.5164

1.5237582

1.38234

1.97789

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

150.3216

o

o

20.81376

o

o

0.4n201

0.43291

2.92732

o

o

o

5.706596

o

o

2.538596

50.35232

o

o

2.538596

o

o

o

o

o

o

5.706596

o

o

2.538596

50.35232

o

o

2.538596

o

o

o

95

220

96

220

96

220

Page 7
L

Cylec>WalJlngford

Number of Welaht .. Timaln Emlalliona emission Reduction Credit

COmponent Components HAP Contact UnconlrODad SubpartW HON Credlla ($) (WD)

SOCMI HON

Valves, gIv 0 0 0

0 0 0

0 0 0

Valves, U 355 1 4490 14138.3385 2247.4695 1753.345 1188.606 1235.915 220

0 0 0 0 0

427 0.35 5427 7194.14788 1143.601862 892.1717 603.7921 628.8827 220

~aIves, hi 27 1 18 0.245916 0.245916 0.245916 0 0 882

0 0 0 0 0

0 0 0

Pumps, U 33 1 4490 6489.846 2000.295 1815.083 448.0183 466.5009 220

0 0 0 0 0

39 0.35 5427 3244.64049 1000.060425 907.4622 223.9897 233.2302 220

Pumps, hl 2 1 18 0.16668 0.1666B 0.16668 0 0 BB2

0 0 0 0 0

0 0 0

ssors,U 0 0 0

0 0 0

0 0 0

Compressors, hl 0 0 0

0 0 0

0 0 0

PRVs,glv 0 0 0

0 0 0

0 0 0

PRVs,U 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

PRVs, hl 0 0 0

0 0 0

0 0 0

OELs,g/v 0 0 0

0 0 0

0 0 0

OELs,U 155 0.35 5427 1101.11117 0 0 109.8814 109.8814 220

0 0 0 0 0

0 0 0 0 0

OELs,hl 0 0 0 0 0 882

0 0 0

0 0 0

Sampling Conn, g/v 0 0 0

0 0 0

0 0 0

samnllna Conn, U 74 1 4490 10964.58 0 0 1094.17 1094.17 220

16 0.35 5427 1002.9096 0 0 100.0817 100.0817 220

0 0 0 0 0

sampling Conn, hi 6 1 18 0.3564 0 0 0.142586 0.142586 882

0 0 0 0 0

0 0 0

Conn/Flanges, gIv 0 0 0

0 0 0

0 0 0

COnnlFlanges, U "" 2303 1 4490 41672.0941 41672.0941 2957.374 0 3863.394 220

1865 0.35 5427 14276.1712 14276.17123 1013.148 220

0 0 0

ConnlAanges, hl 173 1 18 0.56052 0.56052 0.56052 0 0 882

0 0 0 0 0

0 0 0

Totals Ibslvr 5475 100085.166 62340.66523 9339.557 3766.682 7732.199

tOniiJvr 50.0425832 31.17033262 4.669778

M,Ilyr 45.39833 28.27754 4.23640

Incremental EmIssion Reduction (MaIvr) 17.12079 41.16194

Page 8
C~AC Molding

NumtHlr of Walght % TIme In emissions

ComDonenl

Va!ve8, gJv

Components HAP contact Uncontrolled 8uboart W HON

o 0

o 0

o 0

o

o

o

EmIssion Reduction Credit

Credlta ($) ($/Mg)

800M! HON

Valves. D 43 0.455 8760 1520.22398 241.659054

o 0

18B.5283

o

127.58971

o

132.8917

o

220

Valves, hi

14 0.06 1188 8.8515504 1.4070672

o 0

o 0

o 0

1.09n12

o

o

o

0.742895

o

o

0.773766

o

o

220

B82

PumPS,U 3 0.455 8760 523.73412 161.4249

o 0

146.4782

o

36.155325

o

37.646881

o

220

Pumps,hI '

Compressors, D

Compressors, hi

PRVs,g/v

5 0.06 1188 15.61032 4.8114

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

4.3659

o

o

o

o

o

o

o

o

o

o

o

1.0n6388

o

o

1.1220958

o

o

220

882

PRVs,U

PRVs,hi

OEls. g/v

3 0.455 8760

o 0

2735.85312 2735.85312

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o

83.7018

o

o

o

o

o

o

o

o 264.66175

o 0

o 0

220

OELs,II

OELs, hi

5alnllllna Conn, aJv

Sampling Conn, II

Sampling Conn, hi

ConnlFJanges. gIv

3 0.455 8760

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

394.5942 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

39.377086

o

o

o

o

o

o

o

o

39.3n086

o

o

o

o

220

882

220

220

882

Totals IbslVr 254

tonstvr

ConnlFlanges. U

ConnIFIana8s, hi

129

54

0.455

0.05

8760

1188

o 0

2072.09785 2072.097846

15.5119536 15.5119536

o 0

o 0

o 0

o 0

7286.4n09 5232.765341

3.64323854 2.61638267

o

147.0521

1.100848

o

o

o

o

572.3249

0.286162

o 192.1029

o 1.4381036

o 0

o 0

204.94266 670.01428

220

220

882

Incremental Emission Reduction (Mnll/r)

3.30512 2.37357

0.93156

0.25960

3.04552

;)Jo Page 9
Dexter-Blnnlngham

Number of Welahl% Tune In Emlaalons EmIssIon Reducllon Credit

Compemenl COntSJonenta HAP Contact UnconlroDed SUbpartW HON Credits ($I (SIMa)

SOCMI HON

Valves, aN 0 0 0

0 0 0

0 0 0

Valves, II 15 1 8760 1165.518 185.274 144.54 171.6294 178.76148 386

0 0 0 0 0

0 0 0 0 0

Valves. hi 15 1 8760 66.4884 68.4884 66.4884 0 0 386

0 0 0 0 0

0 0 0

Pumps,lI 1 1 8760 383.688 118.26 107.31 46.473377 48.390596 386

0 0 0 0 0

0 0 0 0 0

PumPS, hi 1 1 8760 40.55B8 40.5568 40.5588 0 0 386

0 0 0 0 0

0 0 0

Compressors, II 0 0 0

0 0 0

0 0 0

COntSJressors, hi 0 0 0

0 0 0

0 0 0

PRVs,OIv 0 0 0

0 0 0

0 0 0

PRVs,U 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

PRVs,hI 0 0 0

0 0 0

0 0 0

OELs,aN 0 0 0

0 0 0

0 0 0

OELs,U 2 1 8760 65.5248 0 0 11.472636 11.472636 386

0 0 0 0 0

0 0 0 0 0

OELs,hI 1 1 8760 28.908 0 0 5.061457 5.061457 386

0 0 0

0 0 0

Ssmpllnll Conn, "'" 0 0 0

0 0 0

.0 0 0

SamDlirnI CoM, II 2 1 8760 578.16 0 0 101.22914 101.22914 386

0 0 0 0 0

0 0 0 0 0

Ssmpllna Conn, hi 1 1 8760 28.908 0 0 5.061457 5.061457 386

0 0 0 0 0

0 0 0

ConnIFlanlles, aN 0 0 0

0 0 0

0 0 0

ConnIFIanges, n 30 1 8760 1059.084 1059.084 75.1608 0 172.27359 386

0 0 0 0 0

0 0 0

ConnIFlanges, hi 30 1 8760 47.304 47.304 47.304 0 0 386

0 0 0 0 0

0 0 0

Totals IbsI1 r 98 3464.142 1516.9592 481.362 340.92747 522.25033

tons Yr 1.732071 0.7584846 0.240681

Mg yr 1.57132 0.68609 0.21834

Incremental Emission Reduction (Malvn 0.88323 1.35298

Page 10
Dexter-Waukegan

ComPOnents HAP Contact Uncontrolled SubpartW

Number of Weight % Tlma In EmIssions

Comoonent

Valves, g/lI o

o

o

o

o

o

HON

o

o

o

EmIssion Reduction

Credits ($)

seeMI HON

Credit

(SIMa)

Valves, U

Valves, hi

,Pumps,n

PumPS, hi

Compressors, U

Compressors, hi

PRVs,a/V

PRVs, U

PRVs, hi

OELs,gJv

oas.n

OELs, hi

Sampling Conn, oIv

SampDng Conn, U

Sampling Conn, hi

ConnIFlanges, Olv

30

15

2

1

..

1

4

1

1

1

1

1

1

1

6750

4380

6570

4380

6570

4380

6570

4360

1796.175

o

o

33.2442

o

o

575.532

o

o

20.2794

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

98.2872

o

o

14.454

o

o

o

o

o

867.24

o

o

14.454

o

o

o

o

285.525

o

o

33.2442

o

o

1n.39

o

o

20.2794

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

222.75

o

o

33.2442

o

o

160.965

o

o

20.2794

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

213.10539

o

o

o

o

56.165364

o

o

o

o

o

o

o

13.865245

o

o

1.4423841

122.3404

o

o

1.4423841

o

221.96098

o

o

o

o

58.482417

o

o

o

o

o

o

o

13.865245

o

o

1.4423841

122.3404

o

o

1.4423841

o

311

220

311

220

311

220

311

220

ConnIFlanaes, U

ConnIFlanges, hi

60

30

6570

4380

o

1588.626

o

o

23.652

o

o

o

1588.626

o

o

23.652

o

o

o

112.7412

o

o

23.652

o

o

o 208.20111

o 0

o 0

o 0

311

220

Totals IbslVr 148

tonslVr

Incremental EmIssion Reduction (MlIlvr)

5031.9438

2.5159719

2.28247

2128.7166

1.0643583

0.96558

1.31690

573.6318

0.286816

0.26020

2.02228

408.36117 627.73492

Page 11
Freedom-Charlotle

( Number of WelAht % TIme in EmIssions EmIssion Reducllon Credit I-:---...,..--f-~~~~~~~~~~~w~~~~~~~-+-::;~ Component Components HAP Contact UnconlroDed ISUbpart HON Credils ($) ($lM'l)

Valves.a/V

Valves.U

Valves. hi 15 1 8760

o

o

o

o

o

o

66.4884

o

o

o

o

o

o

o

o

66.4884

o

o

o

o

o

o

o

o

68.4884

o

o

SOCMI HON

o

o

o

o

o

o

o

o

o

o

220

Pumps,"

Pumps. hi

Compressors, U

Com0res50rs. hi

PRVa.alv

PRVa.U

PRVs.hl

OELs. nlv

2

2 1

8760

8760

767.376

o

o

81.1176

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

238.52

o

o

81.1176

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

214.62

o

o

81.1176

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

52.974834

o

o

o

o

o

o

o

55.160265

o

o

o

o

o

o

o

220

220

OELs,"

OELs.hI

Sampling Conn. gIv

1 8760

o

o

o

o

28.908

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o 0

o 0

o 0

2.8847682 2.8847682 220

Sampling Conn. II

Sampling Conn. hi

Conn/Flanges. gIv

ConnIFlanges, U

ConnIFlannea. hi 30 1

8760

8760

o

o

o

o

28.908

o

o

o

o

o

o

o

o

47.304

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

47.304

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

47.304

o

o

o

o

o

2.8847682

o

o

o

o

o

o

o

o

2.8847682

o

o

o

o

o

220

220

Totals Ibs/yr 51

MgJyr

Incremental EmIssion Redudlon (Mglyr)

1020.102

0.510051

0.46272

431.43

0.215715

0.19570

0.26702

409.53

0.204765

0.18576

0.27695

58.744371 60.929801

Page 12
GP-AIbany

Number of IWeight % Tlmaln EmlSslDns Emlsslon Reduction Credit

ComDOJUmt Compomm1s HAP Contad UncontroUed SubparlW HON Credits (S) CSlMg)

SOCMI HON

Valves, a/V 0 0 0

0 0 0

0 0 0

Velves, D 14 1 8760 1087.8168 172.9224 134.904 44.819285 46.681748 108

0 0 0 0 0

0 0 0 0 0

Valves, hi 45 0.5 8760 99.7326 99.7326 99.7326 0 0 220

32 1 8760 141.84192 141.84192 141.8419 0 0 904

0 0 0

!PurnDs, II 0 0 0 0 0 108

0 0 0 0 0

0 0 0 0 0

Pumps, hi 3 0.5 8760 60.8382 60.8382 60.8382 0 0 220

4 1 8760 162.2352 162.2352 162.2352 0 0 904

0 0 0

Compressors, D 0 0 0

0 0 0

0 0 0

Compressors, hi 0 0 0

0 0 0

0 0 0

PRVs,aJv 0 0 0

0 0 0

0 0 0

PRVs, II 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

PRVs, hi 0 0 0

0 0 0

0 0 0

OEls,gIv 0 0 0

0 0 0

0 0 0

OEls,D 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

OELs,hI 1 0.5 8760 14.454 0 0 1.4423841 1.4423841 220

2 1 8760 57.816 0 0 23.70755 23.70755 904

0 0 0

Sampling Conn, g/II 0 0 0

0 0 0

0 0 0

Sampling Conn, II 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

Sampling Conn. hi 12 0.5 8760 173.448 0 0 17.308609 17.308609 220

12 1 8760 346.896 0 0 142.2453 142.2453 904

0 0 0

ConnIFlanges, glv 0 0 0

0 0 0

0 0 0

ConnIFlanaes. II 38 1 8760 1341.5064 1341.5064 95.20368 0 61.054474 108

0 0 0 0 0

0 0 0

ConnIFlanges, hi 128 0.5 8760 100.9152 100.9152 100.9152 0 0 220

112 1 8760 176.6016 176.6016 176.6016 . 0 0 904

0 0 0

Totals IbsJvr 403 3764.10192 2256.59352 972.2724 229.52313 292.44006

tonfllyr 1.88205096 1.12829676 0.486135

Mglyr 1.70739 1.02358 0.44102

Incremental Emlsslon Reduction (I 4gJyr) 0.68380 1.26637

30 Page 13
GP-Lulkln

Number of Weltlht% TIme In Emlsslons EmIssion Reduction Credit

ComPOJl8f\t IS HAP Contact Uncontrolled SUbpartW HON Credits ($) ($lMg)

SooMI HON

Valves.gJv 0 0 0

0 0 0

0 0 0

Valves,U 9 1 8760 699.3108 111.1844 86.724 28.812397 30.009695 108

0 0 0 0 0

0 0 0 0 0

Valves, hi 18 1 8760 79.78608 79.78608 79.78608 0 0 904

20 1 8760 88.6512 88.6512 88.6512 0 0 220

8 1 8760 35.46048 35.46048 35.46048 1213

Pumps,D 1 1 8760 383.688 118.26 107.31 0 0

0 0 0 0 0

0 0 0 0 0

[PumPs, hi 1 1 8760 40.5588 40.5588 40.5588 0 0 220

1 1 8760 40.5588 40.5588 40.5588 0 0 1213

3 1 8760 121.6764 121.6764 121.6764 0 0 904

ra,D 0 0 0

0 0 0

0 0 0

Comnressors, hi 0 0 0

0 0 0

0 0 0

PRVs,gJv 0 0 0

0 0 0

0 0 0

PRVs,1I 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

PRVs,hI 0 0 0

0 0 0

0 0 0

OELs,aJv 0 0 0

0 0 0

0 0 0

OELs,II 3 1 8760 98.2872 0 0 4.8149404 4.8149404 108

0 0 0 0 0

0 0 0 0 0

08..s,hl 1 1 8760 28.908 0 0 11.853775 11.853775 904

2 1 8760 57.816 0 0 31.811126 31.811126 1213

0 0 0 0 0

5amPtiIlQ CoM, QJv 0 0 0

0 0 0

0 0 0

Sampling Conn. D 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

SampUIlQ Conn, hi 1 1 3600 11.88 0 0 1.1855212 1.1855212 220

1 0.5 1080 1.782 0 0 0.1778282 0.1778282 220

1 0.5 1080 1.782 0 0 0.7307121 0.7307121 904

ConniFlallQes, aJv 0 0 0

0 0 0

0 0 0

ConnIFlanaes. 0 36 1 8760 1270.9008 1270.9008 90.19296 0 57.841081 108

0 0 0 0 0 . 0 0 0

ConnlFlanaes. hi 20 1 8760 31.536 31.536 31.536 0 0 1213

0 0 0 0 0 220

0 0 0 220

Totals Ibsll'" 126 2992.58256 1938.55296 722.4547 79.3863 138.42468

tonsvr 1.49829128 0.96927648 0.361227

MOl'vt 1.35743 0.87932 0.32770

Inaemental EmIssIon Reduction (Mglyr) 0.47810 1.02972

31 Page 14
GP-Port Wentworth

Number of Welahl% Time In EmIssJons EmJssIon Reduction credit

Component Components HAP Contact UncontroDed SubpsrtW HON credits ($) ($lMO)

SOCMI HON

VaIveIl, g/tI 0 0 0

0 0 0

0 0 0

Valves, U 7 1 8760 543.9084 86.4612 67.452 22.409842 23.340874 108

0 0 0 0 0

0 0 0 0 0

Valves, hi 15 0.5 8760 33.2442 33.2442 33.2442 0 0 220

15 1 8760 66.4884 66.4884 66.4884 0 0 904

0 0 0

Pumps.U 1 1 8760 383.688 118.26 107.31 13.002914 13.539338 108

0 0 0 0 0

0 0 0 0 0

PumPS, hi 1 0.5 8760 20.2794 20.2794 20.2794 0 0 220

1 1 8760 40.5588 40.5588 40.5588 0 0 904

0 0 0 0 0

Compressors, D 0 0 0

0 0 0

0 0 0

Compressors, hi 0 0 0

0 0 0

0 0 0

PRVs,QIv 0 0 0

0 0 0

0 0 0

PRVs,U 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

PRVs, hi 0 0 0

0 0 0

0 0 0

OELs, a/lI 0 0 0

0 0 0

0 0 0

OELs,U 2 1 8760 65.5248 0 0 3.2099603 3.2099603 108

0 0 0 0 0

0 0 0 0 0

OELs. hi 1 0.5 8760 14.454 0 0 1.4423841 1.4423841 220

0 0 0 0 0

0 0 0 0 0

Sampllna Conn, a/v 0 0 0

0 0 0

0 0 0

Sampling Conn, U 1 1 8760 289.08 0 0 14.161589 14.161589 108

0 0 0 0 0

0 0 0 0 0

Sampling Conn, hi 3 0.5 8760 43.362 0 0 4.3271523 4.3271523 220

1 1 8760 28.908 0 0 11.853775 11.853775 904

0 0 0 0 0

ConnIFlanges. gJv 0 0 0

0 0 0

0 0 0

ConnlFlanges, I 13 1 8760 458.9364 458.9364 32.56968 0 20.887057 108

0 0 0 0 0

0 0 0

ConntFlanges, hi 35 0.5 8760 27.594 27.594 27.594 0 0 220

37 1 8760 58.3416 58.3416 58.3416 0 0 904

0 0 0

Totals Ibsl\ 133 2074.368 910.164 453.8381 70.407417 92.76213

tonsJ'It 1.037184 0.455082 0.226919

MOl." 0.94093 0.41285 0.20586

Incremental Emission Reduction (Ma/vr) 0.52808 0.73507

Page 15
GP·Wh/lB City

( Number of WalDht% TJmeIn Em1aslona emission Reduction Credit

- Component Components HAP Contact UnconIrolled SubDartW HON Credits (Sl ($/Mg)

SOCMI HON

Valvea,gIv 0 0 0

0 0 0

0 0 0

Valves. D 61 1 8760 4739.7732 753.4476 587.796 195.28403 203.39905 108

0 0 0 0 0

0 0 0 0 0

Valves. hi 8 0.5 8760 17.73024 17.73024 17.73024 0 0 220

11 0.6 8760 29.254898 29.254896 29.2549 0 0 220

0 0 0

Pumps. n 1 1 8760 383.688 118.26 107.31 13.002914 13.539338 108

0 0 0 0 0

0 0 0 0 0

PumPS. hi 1 0.5 8760 20.2794 20.2794 20.2794 0 0 220

1 0.6 8760 24.33528 24.33528 24.33528 0 0 220

0 0 0 0 0

Drs. D 0 0 0

0 0 0

0 0 0

COm..- ........ hI 0 0 0

0 0 0

0 0 0

PRVa,g!V 0 0 0

- 0 0 0

0 0 0

PRVs.n 1 0.05 564 6.45216 6.45216 0.1974 0 0.3084112 108

0 0 o· 0 0

0 0 0 0 0

PRVs. hi 1 0.5 4380 501.072 501.072 15.33 0 48.472848 220

1 0.6 4380 601.2864 601.2864 18.396 0 58.167417 220

0 0 0

OELs.gJv 0 0 0

0 0 0

0 0 0

OELs,n 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

OELs.hI 3 0.5 8760 43.362 0 0 4.3271523 4.3271523 220

2 0.6 8760 34.6896 0 0 3.4617219 3.4617219 220

0 0 0 0 0

Sampling Conn, gJv 0 0 0

0 0 0

0 0 0

S8IIIP1inQ Conn. n 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

SnmpliI\IJ Com. hi 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

ConnIFlanges, gJv 0 0 0

0 0 0

0 0 0

ConnIFlanges. U 13 1 8760 458.9364 458.9364 32.56958 0 20.887057 108

- 0 0 0 0 0 . 0 0 0

ConnIFlanges. hi 45 0.5 8760 35.478 35.478 35.478 0 0 220

12 0.6 8760 11.35296 11.35296 11.35296 0 0 220

0 0 0

Totals IbSil 161 6907.69054 25n.885336 900.0299 216.07581 352.56099

tonSi 'If 3.45384527 1.288942668 0.450015

MlIJ 'If 3.13331 1.16932 0.40825

Irn:remental emission Reduction (M!J/vr) 1.96399 2.72506

33

Page 16
IP-Hampton

COrrloononl

lVaIves, aIV

Number of ¥YUIYIIl % TIme In EmIssIona

.ComDonents HAP Conted Uncontrolled Subpart W HON

000

000

000

emission Reduction

Credits ($)

seCMI HON

Credit

($/Mal

Vulves. D

Valves, hi

PumDS, D

PumDS,h1

Comnressors, •

Co ,hi

PRVs,Q1v

52

69

185

37

27

2

3

12

3

0.44

1

0.3

1

0.998

0.44

1

0.3

1

0.998

8760 1m.80346 282.604608 220.4717

8760 5361.3828 852.2604 664.884

8760 4312.4166 685.5138 534.798

8760 164.00472 164.00472 164.0047

8760 119.439762 119.4397618 119.4398

000

8760 337.64544 104.0688 94.4328

8760 1151.064 354.78 321.93

8760 1361.2768 425.736 386.316

8760 121.6764 121.6764 121.6764

8760 40.4776824 40.4776824 40.47768

000

o 0 0

DOD

000

000

o 0 0

o 0 0

o 0 0

000

149.2079

347.70517

832.44707

o

o

23.308927

39.008742

219.31581

o

o

o

155.40823

362.15404

887.03938

o

o

24.270517

40.618013

228.3635

o

o

o

220

170

506

1213

904

220

108

506

1213

904

PRVs,D

PRVs, hi

OELs,oJv

6 0.3

o 0 0

8760 3607.7184 3607.7184 110.376

o 0 0

000

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 802.71038

o 0

o 0

o 0

o 0

506

OELs.1I

OELs. hi

Samplinll Conn, gJv

Sal1\1)lina Conn, n

Conn, hi

ConnlFlanoes, gJv

8

13

16

2

8

6

1

0.3

0.999

0.07

0.44

0.999

5255 157.2296 0 0

8760 127.77336 0 0

2190 130.91855 0 0

2190 1.146684 0 0

5255 69.181024 0 0

1750 34.61535 0 0

000

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

16.54598

29.326554

6.4135006

0.1144291

8.9036675

16.627604

o

o

o

o

o

o

16.54598

29.326554

6.4135006

0.1144291

6.9036675

16.627804

o

o

o

o

o

o

232

506

108

220

220

1059

ConnlFtanaes. D

ConnlFlanaes. hi

13

11

24

14

5

0.37

1

0.3

1

0.998

o 0 0

8760 169.BD6468 169.806468 12.05078

8760 388.3308 388.3308 27.55896

8760 254.18016 254.18016 18.03859

8760 22.0752 22.0752 22.0752

8760 7.868232 7.868232 7.868232

o 0 0

o 36.2081

o 32.401717

o 54.199235

o 0

o 0

506

198

506

1213

904

Totals IbsIvr 517

tonsIYr

MaIVr

Incremental EmIaaIon RedUdion lMalvrl

19738.0315 7600.541432 2866.399

9.86901574 3.800270716 1.433199

8.95311 3.44758 1.30019

5.50553 7.65292

3LJPage 17

1686.9256 2679.305
Neste - Moncure

Number of welaht % Time In Emlll!llons

Components HAP Contact UncontroDed SubpartW HON

Valves. g/V o

o

o

o 0

o 0

o 0

emission Reduction Crectll

Credits ($) ($/Mg)

SOCMI HON

o 0

o 48.200901

Valves. II

Valves. hi

Pumas.D

Pumps. hi

CoITIDf8Ssors. II

Compressors, hi

PRVs.Wv

PRVs. II

PRVs. hi

CELs. g/V

CELs.1I

CELs. hi

Sampling Conn. D1v

Sampling Conn, II

Sampling Conn, hi

ConnIflanaes. gIv

Conn/Flanges. II

15

30

15

2

2

1

2

4

2

2

4

2

30

1

0.44

1

1

0.44

1

1

0.44

1

0.44

1

8760

8760

8760

8760

8760

8760

8760

8760

8760

6760

8760

8760

8760

1165.518

o

o

58.509792

66.4884

o

767.376

o

o

35.691744

40.5588

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

65.5248

o

o

50.87808

57.816

o

o

o

o

578.16

o

o

50.87808

57.816

o

o

o

o

1059.084

o

185.274 144.54

o 0

o 0

58.509792 .58.50979

66.4884 66.4884

o 0

236.52 214.62

o 0

o 0

35.691744 35.69174

40.5588 40.5588

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

1059.084 75.1608

o 0

48.020662

o

o

o

o

26.005828

o

o

o

o

o

o

o

o

o

o

3.2099503

o

o

5.0771921

23.70755

o

28.323179

o

o

5.0771921

23.70755

o

50.016159

o

o

o

o

27.078675

o

o

o

o

o

o

o

o

o

o

3.2099603

o

o

5.0771921

23.70755

o

28.323179

o

o

5.0771921

23.70755

o

108

220

904

108

220

904

108

220

108

220

904

108

ConnIFIanne&. hi 60

3D

0.44 8760

8760

o

41.62752

47.304

o

o 0

41.62752 41.62752

47.304 47.304

o 0

o 0

o 0

o 0

220

Totals IbsIyr 201

tonslvr

Inemmental EmIssion Reduction fMglyr)

4143.23122

2.07161561

1.87936

35

1771.0583 724.5011

0.8855291 0.362251

0.80335 0.32863

1.07601 1.55073

163.12911 214.39836

Page 18
Neste· N. Winnfield

Number of Weight % Time In Eml&SIDnB emission Reduclion Credit

ComDonent CompOnents HAP . Contact UncontroUad SubpartW HON Credits ($) ($lMg)

SOCMI HON

Valves, aJv 0 0 0

0 0 0

0 0 0

Valves,D 30 1 8760 2331.038 370.548 289.08 96.041325 100.03232 108

0 0 o , 0 0

0 0 0 0 0

Valves, hi 30 1 8760 132.9768 132.9768 132.9768 0 0 904

90 0.44 8760 175.529376 175.52938 175.5294 0 0 220

0 0 0

Pumps,D 1 1 8760 383.688 118.26 107.31 13.002914 13.539338 108

0 0 0 0 0

0 0 0 0 0

Pumj)S, hi 2 1 8760 81.1176 81.1176 81.1176 0 0 904

12 0.44 8760 214.150464 214.15046 214.1505 0 0 220

0 0 0 0 0

Co ,0 0 0 0

0 0 0

0 0 0

Compressors,hI 0 0 0

0 0 0

0 0 0

PRVa, gJv 0 0 0

0 0 0

0 0 0

PRVs,U 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

PRVs,hI 0 0 0 0 0

0 0 0 0 0

0 0 0

OELs,gJv 0 0 0

0 0 0

0 0 0

OELa,D 4 1 8760 131.0496 0 0 6.4199205 6.4199205 108

0 0 0 0 0

0 0 0 0 0

OELs, hi 2 1 8760 57.816 0 0 23.70755 23.70755 904

12 0.44 8760 152.63424 0 0 15.231576 15.231576 220

·0 0 0 0 0

Samplil\ll Conn, gJv 0 0 0

0 0 0

0 0 0

Sampling Conn. II 4 1 8760 1156.32 0 0 56.646358 56.646358 108

0 0 0 0 0

0 0 0 0 0

Sampling Conn, hi 2 1 8760 57.816 0 0 23.70755 23.70755 904

12 0.44 8760 152.63424 0 0 15.231576 15.231576 220

0 0 0 0 0

Conn/Flanges, gJv 0 0 0

0 0 0

0 0 0

Conn/Aanges, U 60 1 8760 2118.168 2118.168 150.3216 0 96.401801 lOB

0 0 0 0 0

0 0 0 0 0

ConnlAanges, hi 60 1 8760 94.608 94.608 94.608 0 0 904

180 0.44 8760 124.88256 124.88256 124.8826 0 0 220

0 0 0

Totals Ibsi''If 501 7364.42688 3430.2408 1369.976 249.98877 350.91799

tonsJvr 3.68221344 1.7151204 0.684988

UnJvr 3.34048 1.55595 0.62142

Incremental EmIssion Reduction II .4olvr) 1.78454 2.71906

310

Page ~9
L

PO George

Number of Welaht% Tlmaln EmIssions EmIssion Reduction Credit

Component Components HAP Contact Uncontrolled SubDarlW HON Cf'ed118 IS) ($IMg)

SOCMI HON

Valve8,gIv 0 0 0

0 0 0

0 0 0

Valves. 0 24 1 8760 1864.8288 296.4384 231.284 191.37123 199.32366 269

0 0 0 0 0

0 0 0 0 0

Valves, hi 21 0.91 8760 84.7052216 84.7062216 84.70622 0 0 1808

0 0 0 0 0

0 0 0

PumPS, 0 1 1 8760 383.688 118.26 107.31 32.386887 33.72298 269

0 0 0 0 0

0 0 0 0 0

Pumps,hI 1 0.91 8760 36.908508 36.908508 36.90851 0 0 1808

0 0 0 0 0

0 0 0 0 0

Compressors, 0 0 0 0

0 0 0

0 0 0

COtnnressors. hi 0 0 0

0 0 0

0 0 0

PRVs.gIv 0 0 0

0 0 0

0 0 0

PRVs,O 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

PRVs,hI 0 0 0 0 0

0 0 0 0 0

0 0 0

OELs.gIv 0 0 0

0 0 0

0 0 0

OELs.O 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

OELs.hI 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

sampling Conn. gIv 0 0 0

0 0 0

0 0 0

Sampling Conn. II 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

Sampling COM. hi 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

ConnIFlanges, aN 0 0 0

0 0 0

0 0 0

ConnIFlangas. U 132 1 8760 4659.9696 4659.9696 330.7075 0 528.24617 269

0 0 0 0 0

0 0 0 0 0

ConnlFlanges, hi 131 0.91 8760 187.970328 187.970328 187.9703 0 0 1808

0 0 0 0 0

0 0 0

Totals Ibs 'If 310 7218.07146 5384.253058 978.8666 223.75812 761.2928

tOni ;Jyr 3.60903573 2.692126529 0.489433

M I/Vr 3.27410 2.....228 0.44401

Incremental emission Reduction (Mg/yr) 0.83181 2.83008

31-

Page 20
Pioneer

EmIssIon ReductJoo

Credits (SJ

SOCMI HON

o

o

o 0

o 0

NunDerof WSlllht % Tine In EmIssIons

ComPDnant Compcmenls HAP Conlad Uncontrolled SUbpart W HON

Valves,aIV

o 0 o

VaIves,U

Valves, hi

15

10

8

0.5

0.33

1

8760

8760

8760

582.759 92.637

256.41396 40.76028

621.6096 98.8128

o 0

o 0

o 0

72.27

31.7988

n.088

o

o

o

48.909934

8.119049

25.61102

o

o

50.942384

8.4564358

26.675285

o

o

220

83

108

IPumps,U

Pumps, hi

ColllJ)J'eSsora, D

Compressors, hi

PRVs.Wv

2

2

0.5

0.33

1

8760

8760

8760

383.688 118.26

126.61704 39.0258

767.378 238.52

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

107.31

35.4123

214.62

o

o

o

o

o

o

o

o

o

o

o

26.487417

3.2976834

26.005828

o

o

o

27.580132

3.4337265

27.078675

o

o

o

220

83

108

PRVs, U

PRVs, hi

OELs,Wv

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

OEls,II

OELs, hi

sampling Conn, gIv

Sampling Conn. U

sampling Conn, hi

Co es,aIV

4

3

2

3

2

0.5

0.33

1

0.5

0.33

1

8760

8760

8760

8760

8760

8760

o 0

65.5248 0

32.434776 0

65.5248 0

o 0

o 0

o 0

o 0

o 0

o 0

433.62 0

95.3964 0

578.16 0

o 0

o 0

o 0

o 0

o 0

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

6.5388079

1.2211224

3.2099603

o

o

o

43.271523

3.5915364

28.323179

o

o

o

6.5388079

1.2211224

3.2099803

o

o

o

43.271523

3.5915364

28.323179

o

o

o

220

83

108

220

83

108

ConnIFlanlles, U

Conn/Flanges, hi

46

58

28

0.5

0.33

8760

8760

8760

o 0

811.9644 811.9644

675.695592 675.695592

988.4784 988.4784

o 0

o 0

o 0

o

57.62328

47.95259

70.15008

o

o

o

o 75.276715

o 23.633616

o 44.987507

o 0

o 0

220

83

108

Totals Ibslyr 185 6485.26277 3102.154272 714.2251 224.58706 374.22061

tonslYr 3.24263138 1.551077136 0.357113

2.94170 1.40713 0.32397

Incremental emission Redudlon (Mnlvr) 1.53457 2.61773

39

Page 21
Ranbar-Manor

Numberof Welaht~ TIme In EmIssions EmIssion Reduction Credit

ComDOnent Comporumta HAP Contacl Uncontrolled SUbpartW HON CredIts(Sl (SIMa)

SOCMI HON·

Valves, a/V 0 0 0

0 0 0

0 0 0

Valves, U 60 0.3 8760 1398.6216 222.3288 173.448 125.92085 131.15348 236

15 0.44 8760 512.82792 81.52056 63.5976 43.040742 44.829298 22D

0 0 0 0 0

Valves, hi 15 1 8760 66.4884 66.4884 66.4884 0 0 904

15 1 6760 66.4884 68.4884 66.4884 0 0 180B

0 0 0

Pumps, n 8 0.3 8760 920.8512 . 283.824 257.544 68.19306 71.006305 238

2 0.44 8760 337.64544 104.0688 94.4328 23.308927 24.270517 220

0 0 0 0 0

PumPS, hi 1 1 8760 40.5588 40.5588 40.5588 0 0 9D4

1 1 8760 40.5588 40.5588 40.5588 0 0 1808

0 0 0 0 0

BSOl'S, U 0 0 0

0 0 0

0 0 0

Compressors, hi 0 0 0

0 0 0

0 0 0

PRVs,a/V 0 0 0

0 0 0

0 0 0

PRVs,n 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

PRVs,hI 0 0 0 0 0

0 0 0 0 0

0 0 0

OEl..s, a/V 0 0 0

0 0 0

0 0 0

OEl..s,U 8 0.3 8760 78.62976 0 0 8.4172291 8.4172291 236

2 0.44 8760 28.830912 0 0 2.8770755 2.8770755 220

0 0 0 0 0

OELs, hi 1 1 8760 28.908 0 0 11.853775 11.853775 904

1 1 8760 28.908 0 0 23.70755 23.70755 1808

0 0 0 0 0

sampling Conn, gJv 0 0 0

0 0 0

0 0 0

Sampling Conn, U 8 0.3 8760 693.792 0 0 74.269669 74.269669 236

2 0.44 8760 254.3904 0 0 25.38596 25.38596 220

0 0 0 0 0

SamDl1nR Conn. hi 1 1 8760 28.908 0 0 11.853775 11.853775 904

1 1 8760 28.908 0 0 23.70755 23.70755 1808

O· 0 0 0 0

ConnIFla",~es. g/v 0 0 0

0 0 0

0 0 0

Conn1F1anges, n 120 0.3 8760 1270.9008 1270.9008 90.19296 0 126.39347 236

30 0.44 8760 465.99696 465.99696 33.07075 0 43.202289 220

0 0 0 0 0

ConnlAanges, hi 30 1 8760 47.304 47.304 47.304 0 0 904

30 1 8760 47.304 47.304 47.304 0 0 1808

0 0 0

Totals IbsIl , 351 6386.82139 2737.34232 1020.989 442.53616 622.92795

tons.'Vr 3.1934107 1.38867116 0.510494

Mg.V' 2.89704 1.24165 0.46312

Incremental emission Reduction (MgIy,) 1.65539 2.43393

39

Page 22
Schenectady

Number of Weight % TIme In Emlsslons EmIssion Reduction Credit

nt Components HAP Contact Uncontrolled SubD8ltW HON Credits ($) (SIMa)

SOCMI HON

Valves, g/V 0 0 0

0 0 0

0 0 0

Velves, n 15 1 8760 1165.518 185.274 144.54 106.71258 111.14702 240

0 0 0 0 0

0 0 0 0 0

Valves, hi 15 0.44 8760 29.254896 29.254896 29.2549 0 0 220

15 1 8760 66.4884 68.4884 66.4884 0 0 904

15 1 8760 68.4884 66.4884 66.4884 0 0 1279

IPwnps,n 2 1 8760 767.376 236.52 214.62 57.790728 60.174834 240

0 0 0 0 0

0 0 0 0 0

Pumps,hI 1 0.44 8760 17.845872 17.845872 17.84587 0 0 220

1 1 B760 40.5588 40.5588 40.5588 0 0 904

1 1 8760 40.558B 40.5588 40.5588 0 0 1279

Compressors, D 0 0 0

0 0 0

0 0 0

ComPressors, hi 0 0 0

0 0 0

0 0 0

PRVs,oIv 0 0 0

0 0 0

0 0 0

PRVs,U 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

PRVs,hI 0 0 0 0 0

0 0 0 0 0

0 0 0

OELs,gJv 0 0 0

0 0 0

0 0 0

OELs,II 2 1 8760 65.5248 0 0 7.133245 7.133245 240

0 0 0 0 0

0 0 0 0 0

OELs,hI 1 0.44 8760 12.71952 0 0 1.269298 1.269298 220

1 1 8760 28.908 0 0 11.853775 11.853775 904

1 1 8760 28.90B 0 0 16.770993 16.770993 1279

Samplina COM, g/v 0 0 0

0 0 0

0 0 0

Sampllna COM. II 2 1 8760 578.16 0 0 62.940397 62.940397 240

0 0 0 0 0

0 0 0 0 0

Sampling Conn. hi 1 0.44 8760 12.71952 0 0 1.269298 1.269298 220

1 1 8760 28.908 0 0 11.853775 11.853775 904

1 1 8760 28.90B 0 0 16.170993 16.770993 1279

Co es,gJv 0 0 0

0 0 0

0 0 0

ConnlFlanges.1I 30 1 8760 1059.084 1059.084 75.1608 0 91.046146 204

0 0 0 0 0

0 0 0 0 0

Conn/FIanQes. hi 30 0.44 8760 20.81376 20.81376 20.81376 0 0 220

30 1 8760 47.304 47.304 47.304 0 0 904

30 1 8760 47.304 47.304 47.304 0 0 1279

Totals Ib~ 195 4153.35077 1857.4949 810.9377 294.36509 392.22977

tons 'It 2.07667538 0.9287475 0.405469

Mg 'It 1.88395 0.84255 0.36784

Inaemental Emission Redudion (Mglyr) 1.04139 1.51611

'fo

Page 23
Simpson nmber

ICOrnDonenta HAP Contact Uncontlolled SubpartW

Number of weight % TIme In EmIssions

Component

Valves, aN o

o

o

o

o

o

HON

o

o

o

EmJssIon Reduction

Cnldlts (S)

SOCMI HON

Credit

(SIMg)

Valves, U

Valves, hi

Pumps, D

Pumps, hi

Compressors, U

rs,hI

PRVa,Wv

PRVa,U

PRVs, hi

OELs,gIv

OELs,n

OELs, hi

sampling Conn, gIv

Sampling COM, II

Sampling Conn, hi

Conn/Flanges, aN

15

15

30

2

1

2

2

1

2

2

1

2

0.44

1

1

0.44

1

1

0.44

1

0.44

1

8760

8760

8760

8760

8160

8160

8160

8760

8760

8760

8760

8760

1185.518

o

o

29.254896

132.9768

o

767.316

o

o

17.845812

81.1176

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

65.5248

o

o

12.71952

51.816

o

o

o

o

578.16

o

o

12.71952

57.816

o

o

o

185.274

o

o

29.254898

132.9768

o

236.52

o

o

17.845872

81.1116

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

144.54

o

o

29.2549

132.9768

o

214.62

o

o

17.84587

81.1176

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

48.020562

o

o

o

o

26.005828

o

o

o

o

o

o

o

o

o

o

3.2099603

o

o

1.269298

23.70755

o

28.323179

o

o

1.269298

23.70755

o

50.016159

o

o

o

o

27.078675

o

o

o

o

o

o

o

o

o

o

3.2099603

o

o

1.269298

23.70755

o

28.323179

o

o

1.269298

23.70755

o

108

220

904

108

220

904

108

220

904

108

220

904

ConnfFIanges,U

ConnIFlanges. hi

30

30

60

0.44

1

8760

8760

8760

o

1059.084

o

o

20.81376

94.608

o

o

1059.084

o

o

20.81376

94.608

o

o

75.1608

o

o

20.81376

94.608

o

o 48.200901

o 0

o 0

o 0

o 0

108

220

904

Totals Ibslvr 195

tonslvr

Mglyr

Incremental Emission Redudion (14g1yr)

4153.35077

2.07667538

1.88395

1857.4949

0.9287475

0.84255

1.04139

810.9377

0.405469

0.36784

1.51611

155.51332 206.78257

Ifl

Page 24
Solutla • Addyston

Number of Weight % TJmeIn Emlsslons emission Reduction Credil

, Components HAP Contact UncontroDed SubparlW HON Credits ($) ($lMa)

SOCMI HON

Valves, g/V 0 0 0

0 0 0

0 0 0

Valves,U 30 1 8760 2331.036 370.548 289.08 96.041325 100.03232 108

0 0 0 0 0

0 0 0 0 0

Valves. hi 15 0.44 8760 29.254898 29.254896 29.2549 0 0 220

0 0 0 0 0

0 0 0

PumpS, U 4 1 8760 1534.752 473.04 429.24 52.011658 54.157351 108

0 0 0 0 0

0 0 0 0 0

Pumps, hi 2 0.44 8760 35.691744 35.691744 35.69174 0 0 220

0 0 0 0 0

0 0 0 0 0

Compressors, U 0 0 0

0 0 0

0 0 0

Comr>ressora, hi 0 0 0

0 0 0

0 0 0

PRVs, gJv 0 0 0

0 0 0

0 0 0

PRVs, n 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

PRVs.hI 0 0 0 0 0

0 0 0 0 0

0 0 0

OELs. gJv 0 0 0

0 0 0

0 0 0

oas,a 4 1 8760 131.0495 0 0 6.4199205 6.4199205 108

0 0 0 0 0

0 0 0 0 0

0ELs.h1 2 0.44 8760 25.43904 0 0 2.536598 2.538596 220

0 0 0 0 0

0 0 0 0 0

SamprJng Conn. gJv 0 0 0

0 0 0

0 0 0

SaI1lJ)Iino Conn. II 4 1 8760 1156.32 0 0 56.646358 56.646358 108

0 0 0 0 0

0 0 0 0 0

Sampling Conn, hi 2 0.44 8760 25.43904 0 0 2.538596 2.538596 220

0 0 0 0 0

0 0 0 0 0

ConnIFlanges. gJv 0 0 0

0 0 0

0 0 0

Conn/Flanges. U 60 1 8760 2118.168 2118.168 150.3216 0 96.401801 108

0 0 0 0 0

0 0 0 0 0

ConnIFlanaes. hi 30 0.44 8760 20.81376 20.81376 20.81376 0 0 220

0 0 0 0 0

0 0 0

Totals IbsJ: r 153 7407.96408 3047.5164 954.402 216.19645 318.73494

tons 'yr 3.70398204 1.5237582 0.4n201

Mg 'yr 3.36023 1.38234 0.43291

Incremental Emlsslon Reduction (Uglyr) 1.9n09 2.92732

Page 25
Solutla - Springfield

Number of YVelght% TIme In EmIssions EmIssion Reducllon Credit

COmponent ComP0n8nla HAP Contact Unconlrolled SubpartW HON Credits ($) ($/Ma)

seeMI HON

Valves, gill 0 0 0

0 0 0

0 0 0

Valves,U 646 1 8160 50194.9752 7979.1336 6224.856 2068.0899 2154.0292 108

0 0 0 0 0

0 0 0 0 0

Valves, hi 646 0.44 8760 1259.91085 1259.910854 1259.911 0 0 220

0 0 0 0 0

0 0 0

Pumps,lI 41 1 8160 18033.336 5558.22 5043.57 611.13695 836.34887 108

0 0 0 0 0

0 0 0 0 0

Pumps,hI 23 0.44 8760 410.455056 410.455058 410.4551 0 0 220

0 0 0 0 0

0 0 0 0 0

Compressors, U 0 0 0

0 0 0

0 0 0

CoI11Dr8SSOI1l, hI 0 0 0

0 0 0

0 0 0

PRVs,glv 0 0 0

0 0 0

0 0 0

PRVs,U 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

PRVs,hl 0 0 0 0 0

0 0 0 0 0

0 0 0

OELs.aJv 0 0 0

0 0 0

0 0 0

oas,n 1 8760 0 0 0 0 0 108

0 0 0 0 0

0 0 0 0 0

Oas,hI 0.44 8760 0 0 0 0 0 220

0 0 0 0 0

0 0 0 0 0

sampllng Conn, olv 0 0 0

0 0 0

0 0 0

SampUng COM. U 2 1 87£0 518.16 0 0 28.323179 28.323179 108

0 0 0 0 0

0 0 0 0 0

sampling Conn. hi 2 0.44 8760 25.43904 0 0 2.538596 2.538596 220

0 0 0 0 0

0 0 0 0 0

ConnIFlanges, glv 0 0 0

0 0 0

0 0 0

ConnIFIanaes, U 1292 1 8760 45611.2176 45611.2176 3236.925 0 2075.8521 108

0 0 0 0 0

0 0 0 0 0

ConnIFlanlles, hi 1292 0.44 8760 896.379254 896.379254 896.3793 0 0 220

0 0 0 0 0

0 0 0

Totals Ibs/yr 3950 117009.873 81715.31637 17072.1 2710.0886 4897.092

tonslvr 58.5049365 30.85765819 8.536048

MgIyr 53.07533 27.99388 7.74385

Incremental Emission Reduction a4olvr) 25.08145 45.33148

1-/-3

Page 26
Spauldlng-DeKaIb

Number of Welaht DAt Tbneln EmlsslDns emission Reduttlon Credit

CollUlOnent Components HAP Contect Uncontrolled SubDertW HON Credits (Sl ($IMg)

SOCMt HON

Valves, aN 0 0 0

0 0 0

0 0 0

Valves, D 10 1 8760 777.012 123.516 96.36 32.013775 33.344106 108

0 0 0 0 0

0 0 0 0 0

Valves, ht 19 1 8760 84.21864 84.21864 84.21884 0 0 712

8 1 24 0.097152 0.097152 0.097152 0 0 1257

3 1 192 0.291456 0.291456 0.291456 0 0 1213

4 1 48 0.097152 0.097152 0.097152 0 0 1279

6 1 240 0.72864 0.72864 0.72864 0 0 904

0 0 0 0 0

PumPS, D 1 1 8760 383.688 118.26 107.31 13.002914 13.539338 108

0 0 0 0 0

0 0 0 0 0

PumPS,ht 1 1 24 0.11112 0.11112 0.11112 0 0 1257

1 1 192 0.88898 0.88896 0.88896 0 0 1213

1 1 48 0.22224 0.22224 0.22224 0 0 1279

1 1 8760 40.5588 40.5588 40.5588 0 0 220

1 1 240 1.1112 1.1112 1.1112 0 0 904

0 0 0

Coll1J)reBSOrs, \I 0 0 0

0 0 0

0 0 0

Compressors, hi 0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

0 0 0 0 0

PRVs, g/V 0 0 0 0 0

0 0 0

0 0 0

PRVs, U 0 0 0

0 0 0

0 0 0 0 0

PRVs, hi 0 0 0 0 0

0 0 0 0 0

OEls, atv 0 0 0 0 0

0 0 0 0 0

OELs,U 0 0 0 0 0

0 0 0

OELs, hi 0 0 0

sampling Conn, glv 0 0 0

sampling Conn. U 1 1 8760 289.08 0 0 14.161589 14.161589 108

sampling Conn. hi 1 1 24 0.792 0 0.792 0.4515758 0 1257

1 1 192 6.338 0 6.338 3.4861508 0 1213

1 1 4B 0.1584 0 0.1584 0.0918959 0 1279

1 1 8760 28.908 0 0 2.8847682 2.8847682 220

1 1 240 0.792 0 0.792 0.324761 0 904

CoMIFIanges, glv 0 0 0

ConnlFlanges, U 20 1 8760 706.056 706.056 50.1072 0 32.133934 108

ConnIFIanoes. hi 20 1 8760 31.536 31.536 31.536 0 0 589

10 1 24 0.0432 0.0432 0.0432 0 0 1257

17 1 192 0.58752 0.58752 0.58752 0 0 1213

5 1 48 0.0432 0.0432 0.0432 0 0 1279

17 1 240 0.7344 0.7344 0.7344 0 0 904

Tolals Iball r 151 2354.09208 1109.10168 423.1253 '66.41743 96.063735

tons yr 1.17704604 0.55455084 0.211563

Ug vr 1.06781 0.50309 0.19193

Incremental Emission Reduction (Mglyr) 0,56472 0.87588

Page 27
Dynachem

ComP01l8flt

Number of WelQhl% TIme In EmIssions

Components HAP Conted UnconlroDed SUbpartW HON

Valves. gIv

Valves.D

Valves. hi

Pumps,D

Pumps, hi

Compressors,D

Compressors. hl

PRVs,gIv

PRVs,O

PRVs. hi

OELs.gIv

OELs.n

OELs, hi

Sampling Conn. gIv

Sampling Conn.U

sampling Conn. hi

ConnfAanges, glv

Co es.O '-

Conn/Flanges. hi

1511

30

1118760

8760

8760

8760

8760

oooooo

. 66.4884ooooo

40.5568ooooooooooooooooooooooo

28.9D8oooooooo

28.908oooooooo

47.304oo

oooooo

68.4884ooooo

40.5568ooooooooooooooooooooooooooooooooooooooooo

47.304oo

oooooo

66.4884ooooo

40.5588ooooooooooooooooooooooooooooooooooooooooo

47.304oo

~, '.

Tolals IbsJyr 48

tonslyr

Incremental Emlsslon Reduction (MgIvr)

212.1672

0.1060836

0.09624

1/-S

154.3512

0.on1756

0.07001

0.02623

154.3512

0.077176

0.07001

0.02623

Page 28
GP-CohJmbus

Number of Weight % Tune In EmIuIons

ComDOn8l11 Components HAP Conlad Unconb'DDed SUbPart W HON

Valves, gIv o 0

o 0

o

o

Valves, U o 1 71

o 0

o 0

o 0

o

o

o

o 0 o

Valves; hi

Pumps,D

22

22

78

o

1

0.5

0.25

1

420

568

738

71

4.67544 4.67544

3.161488 3.161488

7.262112 7.262112

o 0

o 0

4.67544

3.161488

7.262112

o

o

o 0 o

Pumps, hi

ComDressors, U

10

1

0.5

0.25

420

568

736

1.9446 1.9446

1.31492 1.31492

8.5192 8.5192

o 0

o 0

1.9446

1.31492

8.5192

o

o

o 0 o

ComDressors, hi o 0

o 0

o

o

o 0 o

PRVs, gIv o 0

o 0

o

o

o 0 o

PRVa,U o 0

o 0

o

o

o 0 o

PRVs, hi o 0

o 0

o

o

OELs,gJv

o 0

o 0

o 0

o

o

o

o 0 o

OELs,O o 0

o 0

o

o

o 0 o

OELs,hI 7

7

0.15

0.08

70

70

0.24255 0

0.12936 0

0.24255

0.12938

Sampling Conn, g/v

7 0.02 70 0.03234 0

o 0

o 0

0.03234

o

o

o 0 o

Samo6na COM, 0 o 0

o 0

o

o

Conn,hI 37

37

1

0.5

71

71

o 0

8.6691 0

4.33455 0

o

8.6691

4.33455

26

ConnIFlanges, gIv

0.25 736 15.7872 0

o 0

o 0

o

o

o

o 0 o

415

415

Conn/Flanges, hi 415

Totala Ibslyr 1537

o

o

8.24688

4.398336

1.099584

10.58681

64.61727

o 0

o 0

8.24688 8.24688

4.398336 4.398336

10.58681 10.58681

1.099584 1.099584

80.40447 51.20937

71

736

736

738

0.15

0.02

0.08

ConnIFJanaes. 0 37

Mg/yr

Incremental Emission Reduction (Mgfyr)

0.04020224 0.02560469

0.03647 0.02323

0.01324

0.032309

0.02931

0.00716

Page 29
GP-COnway

COmponent

Number of WeIght % TIme In EmIssions

COII1J)onents HAP Contact UncontroDed Subpart W HON

Valves, aJv

Valves, U

Valves, hi

PumpS,"

PumpS, hi

COmpressors, D

COmpressors, hi

PRVs,aJv

PRVs, n

PRVs, hl

OELs, glv

OELs,n

OELs, hi

Sampling CoM, alv

Sampling COM, D

Conn, hi

ConnlFJanges. alv

ConnIFlanges. n

Conn/Flanges. hi

32

32

32

8

8

8

80

80

1

0.5

1

1

0.5

1

0.5

1

77.3

595

498

78

595

498

595

498

o 0 0

o 0 0

o 0 0

21.940832 3.48m6 21.94083

o .0 0

o 0 0

4.81712 4.81712 4.81712

8.063616 8.063616 8.063816

o 0 0

27.3312 8.424 27.3312

o 0 0

o 0 0

11.0194 11.0194 11.0194

18.44592 18.44592 18.44592

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

o 0 0

4.284 4.284 4.284

7.1712 7.1712 7.1712

o 0 0

. '.

Totals Ibslyr 280

tonsIYr

Malvr

Incremenlal Emission Reduction (Mn/vr)

103.073288 65.713032 103.0733

0.05153664 0.032856516 0.051537

0.04675 0.02981 0.04675

0.01695 0.00000

Page 30
GP-CrosseU

Number of Welllht% TIme In EmIaslons

CompOnent Components HAP Contad UnconlroUed SubparlW HON

Valves. aJv 0 0 0

0 0 0

0 0 0

Valves. 0 0 0 0

0 0 0

0 0 0

Valves. hi 30 1 8760 132.9768 132.9768 132.9768

0 0 0

0 0 0

PtJmI)S.D 0 0 0

0 0 0

0 0 0

PumPS. hi 2 1 8760 81.1176 81.1176 81.1176

0 0 0

0 0 0

Compressors. 0 0 0 0

0 0 0

0 0 0

.hl 0 0 0

0 0 0

0 0 0

PRVs,gIv 0 0 0

0 0 0

0 0 0

PRVs. U 0 0 0

0 0 0

0 0 0

PRVs. hi 0 0 0

0 0 0

0 0 0

OELs.gJv 0 0 0

0 0 0

0 0 0

OELs.1I 0 0 0

0 0 0

0 0 0

OELs, hi 2 1 8760 57.816 0 0

0 0 0

0 0 0

Sampling Conn, gJv 0 0 0

0 0 0

0 0 0

sampling Conn. U 0 0 0

0 0 0

0 0 0

sampling COM. hi 2 1 8760 57.816 0 0

0 0 0

0 0 0

ConnIFIalKl8S. gJv 0 0 0

0 0 0

0 0 0

ConnIFlanges. U 0 0 0

0 0 0

0 0 0

Co es, hi 60 1 8760 94.608 94.608 94.608

0 0 0

0 0 0

Totals IbsIvr 96 424.33441 308.7024 308.7024

tonslyr 0.2121672 0.1543512 0.154351

Mgtyr 0.19248 0.14003 0.14003

Incremental emission Redudion (Mglyr) 0.05245 0.05245

Page 31

.\

...."
GP-LoulsviDe

Numberof Welaht% Time In lJ;iN....iftns

Component Components HAP Contact Urn:ontrolled SUbparlW HON

VaIves,aJv 0 0 0

0 0 0

0 0 0

Valves,U 0 0 0

0 0 0

0 0 0

Valves. hl 105 1 8760 485.4188 465.4188 465.4188

0 0 0

0 0 0

Pumps,U 0 0 0

0 0 0

0 0 0

PumDS, hi 7 1 8760 283.9116 283.9116 283.9116

0 0 0

0 0 0

Compressors, n 0 0 0

0 0 0

0 0 0

sors, hi 0 0 0

0 0 0

0 0 0

PRVs,aJv 0 0 0

0 0 0

0 0 0

PRVs,n 0 0 0

0 0 0

0 0 0

PRVs.hI 0 0 0

0 0 0

0 0 0

OELs,aJv 0 0 0

0 0 0

0 0 0

OELs,U 0 0 0

0 0 0

0 0 0

OELs,hI 7 1 8760 202.356 0 0

0 0 0

0 0 0

Sampling COM. oJv 0 0 0

0 0 0

0 0 0

Sampling COM. U 0 0 0

0 0 0

0 0 0

Sampling Conn. hi 7 1 8760 202.356 0 0

0 0 0

0 0 0

ConnIFlanges. glv 0 0 0

0 0 0

0 0 0

ConnIFlanges. II 0 0 0

0 0 0

- 0 0 0

ConnJFlanges. hi 210 1 8760 331.128 331.128 331.128

0 0 0

0 0 0

Totals Ibslyr 336 1485.1704 1080.4584 1080.458

lllnslyr 0.7425852 0.5402292 0.540229

MolYr 0.67367 0.49009 0.49009

Incremental Emission Redudion (Mglyr) 0.18358 0.18358

Page 32

•

.....---

.-:-

... ,

.<
GP-RusaeDvDle

Number of !Welaht% TIme In EmIssIons

Component Components HAP Contact Uncontrolled SubparlW HON

ValveS. aN 0 0 0

0 0 0

0 0 0

~aJves. U 0 0 0

o· 0 0

0 0 0

Valves. hi 75 1 8760 332.442 332.442 332.442

0 0 0

0 0 0

Pumps. 0 0 0 0

0 0 0

0 0 0

IPumpS. hi 5 1 8760 202.794 202.794 202.794

0 0 0

0 0 0

Compmssors. 0 0 0 0

0 0 0

0 0 0

IComPressors. hi 0 0 0

0 0 0

0 0 0

PRVs, alii 0 0 0

0 0 0

• 0 0 0

PRVs, D 0 0 0

0 0 0

0 0 0

PRVs,hI 0 0 0

0 0 0

0 0 0

oas,gJv 0 0 0

0 0 0

0 0 0

oas,o 0 0 0

0 0 0

0 0 0

OELs, hi 5 1 6760 144.54 0 0

0 0 0

0 0 0

Sampling Conn, otv 0 0 0

0 0 0

0 0 0

Sampling Conn, U 0 0 0

0 0 0

0 0 0

Sampllng Conn. hi 5 1 6760 144.54 0 0

0 0 0

0 0 0

ConnIFlanges. alv 0 0 0

0 0 0

0 0 0

ConnlFlanaes, D 0 0 0

0 0 0

0 0 0

ConnIFlanaes. hi 150 1 6760 236.52 236.52 236.52

0 0 0

0 0 0

Totals Ibs/yr 240 1060.838 771.756 771.756

tonsl'Yr 0.530418 0.385878 0.385878

Mol'yr 0.48119 0.35007 0.35007

lru:remental EmIssion Reduction (Mglyr) 0.13113 0.13113

60 Page 33
ComDOnent

GP-Taylorsville

N&mber of IW81aht % Time In Em1ss1ona

Components HAP Contact UncontroRed SUbpartW HON

Vatves,gJv

~alves,n

Valves, ht

PumPll,D

PumPS, ht

nI,n

Comoressors, hi

PRVs,oJv

PRVs, D

PRVs, ht

OELs, gJv

OELs,II

OEls. hi

Sampling Conn, o/v

sampling CoM. U

sampling COM, hi

Conn/Flanges, gJv

ConnlFlanaes,D

60

4

1

1

1

8760

8760

8760

8760

o

o

o

o

o

o

265.9536

o

o

o

o

o

162.2352

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

o

115.632

o

o

o

o

o

o

o

o

115.632

o

o

o

o

o

o

o

o

o 0

o 0

o 0

o 0

o 0

o 0

265.9536 265.9536

o 0

o 0

o 0

o 0

o 0

162.2352 162.2352

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o • 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

o 0

....

_.

-.. ....

Conn/F~nges.ht 120

Totals IbsIyr 192

tonslyr

Inaemental emission Reduction (Mglyr)

8760 189.216

o

o

848.6688

0.4243344

0.38495

189.216 189.216

o 0

o 0

617.4048 617.4048

0.3087024 0.308702

0.28005 0.28005

0.10490 0.10490

51 Page 34
NaUonal-Sallsbwy

Number of Wa1Qht% TIme In emissions

COmoonent ComDOnents HAP Contact Unconttolled SUbpaltW HON

ValveS, oJv 0 0 0

0 0 0

0 0 0

Valvea, n 0 0 0

0 0 0

0 0 0

Valves, hi 15 1 8760 66.4884 66.4884 66.4884

0 0 0

0 0 0

PumPS, n 0 0 0

0 0 0

0 0 0

Pumps, hi 1 1 8760 40.5588 40.5588 40.5588

0 0 0

0 0 0

Commessora, a 0 0 0

0 0 0

0 0 0

sora,hI 0 0 0

0 0 0

0 0 0

PRVs,Q/V 0 0 0

0 0 0

0 0 0

PRVs,n 0 0 0

0 0 0

0 0 0

PRVs, hi 0 0 0

0 0 0

0 0 0

OELs,fiJv 0 0 0

0 0 0

0 0 0

OELs,U 0 0 0

0 0 0

0 0 0

OELs,hl 1 1 8760 28.908 0 0

0 0 0

0 0 0

SamD6no Conn, olv 0 0 0

0 0 0

0 0 0

SanlDUna Conn,lI 0 0 0

0 0 0

0 0 0

SamDIlna Conn, hi 1 1 8760 28.908 0 0

0 0 0

0 0 0

ConnlFlana8S, oJv 0 0 0

0 0 0

0 0 0

ConnIFlanaes, U 0 0 0

0 0 0

0 0 0

ConnIFlanaes. hi 30 1 8760 47.304 47.304 47.304

0 0 0

0 0 0

Totals Ibsl1" 48 212.1672 154.3512 154.3512

tonsflit 0.1060836 0.0771756 0.077176

Mliron 0.09624 0.07001 0.07001

Incremental Emlsslon Reduction (MnJvr) 0.02623 0.02623

PlIge35
Neste - Andalusia

Number of Wetght% Time In emissions

ComDonent Componenla HAP Contact Uncontroned SubpartW HON

Valves,aJv 0 0 0

0 0 0

0 0 0

Valves, n 0 0 0

0 0 0

0 0 0

Valves, hi 90 1 8760 398.9304 398.9304 398.9304

0 0 0

0 0 0

Pumps,D 0 0 0

0 0 0

0 0 0

PwnP5, hi 6 1 8760 243.3528 243.3528 243.3528

0 0 0

0 0 0

asors, a 0 0 0

0 0 0

0 0 0

Compressors. hi 0 0 0

0 0 0

0 0 '0

PRVs.gJv 0 0 0

0 0 0

0 0 0

PRVs,n 0 0 0

0 0 0

0 0 0

PRVs,hI 0 0 0

0 0 0

0 0 0

OELs.aJv 0 0 0

0 0 0

0 0 0

OELs.O 0 0 0 .. 0 0 0

0 0 0

• OELs,hl 6 1 8760 173.448 0 0

0 0 0

0 0 0

Sampfing Conn. gJv 0 0 0

0 0 0

0 0 0

Sampling Conn, U 0 0 0

0 0 0

0 0 0

Sampling Conn, hi 6 1 8760 173.448 0 0

0 0 0

0 0 0

ConnlFJanges, gJv 0 0 0

0 0 0

0 0 0

ConnIFlalllJes. II 0 0 0

0 0 0

- 0 0 0

ConnIFlanges, hi 180 1 8760 283.824 283.824 283.824

0 0 0

0 0 0

Totals IbSl'yr 288 1273.0032 926.1072 928.1072

mn >lvr 0.6365016 0.4830536 0.463054

Mltlvr 0.57743 0.42008 0.42008

lnaenumtal EmIssion Reduction (Ml1Ivr) 0.15735 0.15735

....-

,-

_.

53 Page 36
Neste· Springfield

Number of Welghl% TIme In Emlaslons

Comoonant ComDonents HAP Contad Uncontrolled SubparlW HON

Valves, afri 0 0 0

0 0 0

0 0 0

Valves. U 0 0 0

0 0 0

0 0 0

Valves, hi ·30 1 8760 132.9768 132.9768 132.9768

105 0.5 8760 232.7094 232.7094 232.7094

0 0 0

Pumps, II 0 0 0

0 0 0

0 0 0

PumDS,hI 2 1 8760 81.1176 81.1176 81.1176

14 0.5 8760 283.9116 283.9116 283.9116

0 0 0

COIJ\pressors. U 0 0 0

0 0 0

0 0 0

Com ,hi 0 0 0

0 0 0

0 0 0

PRVs,aJv 0 0 0

0 0 0

0 0 0

PRVs,U 0 0 0

0 0 0

0 0 0

PRVs, hi 0 0 0

0 0 0

0 0 0

OEls.gJv 0 0 0

0 0 0

0 0 0

OEls.n 0 0 0

0 0 0

0 0 0

OEls. hi 2 1 8760 57.816 0 0

14 0.5 8760 202.356 0 0

0 0 0

Sampling Conn. g/v 0 0 0

0 0 0

0 0 0

Sampling Conn, D 0 0 0

0 0 0

0 0 0

Samp\ing Conn. hi 2 1 8760 57.816 0 0

14 0.5 8760 202.356 0 0

0 0 0

ConnIFlanaes. ofv 0 0 0

0 0 0

0 0 0

ConnIFlana8s. II 0 0 0

0 0 0

0 0 0

ConnIFJanaes. hi 60 1 8760 94.608 94.608 94.608

210 0.5 8760 165.564 165.564 165.564

0 0 0

To/als IbsJyr 453 1511.2314 990.8874 990.8874

tonslvt 0.7556157 0.4954437 0.4954+'

Mafvr 0.68549 0.44946 0.44946

Incremental emission Reduction (I AaIYr) 0.23603 0.23603

Page 37
Perstorp

L .'-::Com=.~""o:-:n-en"":t---+:,,:.;N;.;;umber=~Of~1wem~~Ih1,...%~...,;TIme,::.:.;;:...::In~:-:----,--.".-,+EmI:;;.::Il6=Io~ns~I-::=..,..--I "... COmDOnenlll HAP Contact Uncontrolled Subpart W HON

Valves, g/v

Valves,U

Valves. hi

Pumps.D

PumPS, hi

Compressors,U

Compressors, hi

PRVs,gJv

PRVs,U

PRVs, hi

OELs,g/v

OELs,n

OELs, hi

Sampling Conn, gJv

SamIlIiOQ Conn.n

Sampling Conn, hi

ConnIFIanges, olv

ConnIFlanges,U

ConnlFlanaes. hi

1622

29

30

0.5

0.5

0.5

0.5

0.5

0.5

0.5

8280

4140

8760

312

8280

8280

8280

o0

o0

o0

o0

o0

o0

33.51744 33.51744 o 0 o 0 o 0 o 0 o 0

19.1682 19.1682 o 0 o 0 o 0 o 0 o 0 o 0 o 0 o 0 o 0 o 0 o 0 o 0 o 0 o 0

1002.144 1002.144 o 0 o 0 o 0 o 0 o 0 o 0 o 0 o 0

0.51480

o0

o0

o0

o0

o0

o0

o0

o0

27.3240

o0

o0

o0

o0

o0

o0

o0

o0

21.6108 21.6108

22.356 22.356 o 0

oooooo

33.51744ooooo

19.1682oooooooooooooo

30.66ooooooooooooooo

·0oooooooooo

21.6108

22.356o

.. ~t.•

.........

Totals Ibalyr 81

lonslVr

Mglyr

lnaemental emission Reduction (Mg/yr)

1126.63524 1098.79644

0.56331762 0.54939822

0.51104 0.49841

0.01263

127.3124

0.063656

0.05775

0.45329

55 Poge 38
Emission Factors

Emission Factors (Ibslhr)

Component Uncontrolled SubparlW HON

Valves, g/V 0.0131 0.00165 0.001

Valves, II 0.00887 0.00141 0.0011

Valves, hi 0.000506 0.000506 0.000506

Pumps,lI 0.0438 0.0135 0.01225

Pumps. hi 0.00463 0.00463 0.00463

Compressors, II 0.5016 0 0

Compressors, hi 0.5016 0 0

PRVs, g/V 0.2288 0.007 0.007

PRVs, II 0.2288 0.2288 0.007

PRVs, hi 0.2288 0.2288 0.007

OELs, gJv 0.00374 0 0

OEls,1I 0.00374 0 0

OELs, hi 0.0033 0 0

Sampling Conn, g/v 0.033 0 0

Sampling Conn, II 0.033 0 0

Sampling Conn. hi 0.0033 0 0

Conn/Aanges. gJv 0.00403 0.00403 0.000286

Conn/Flanges. II 0.00403 0.00403 0.000286

Conn/Flanges, hi 0.00018 0.00018 0.00018

Page 40
LEAK DETECTION AND REPAIR COST DERIVATIONS

The attached two tables summarize the derivation and source ofthe cost elements used to

estimate the HaN LDAR program. The main source ofcost elements and the costing algorithms

was:

KJ. Hausle and DJ. Whitt, Radian Corporation, to D. Markwardt, EPA, Final Cost

Impacts Analysisfor HON EquipmentLeaks. February 28, 1992. (see Attachment A)

. A second memo on the petroleum refinery MACT was used for several cost elements and

t~r revising certain aspects oCthe costing algorithm for the HaN memo. This memo is found in

Attacbment B: :

R.V. Oommen, Radian Corporation, to J. Durham, U.S. Environmental Protection

Agency, MethodolQgy for EstimatinK National Impacts ofContmUinK Leakina RefilleD'

EQuipment,June 27, 1994.

The main assumptions used in developing the costs were: (1) the facilities would use inhouse personnel to conduct the LDARprogram (ratherthan using a subcontractor); (2) the

facility would "locate and log" the components subject to Method 21 monitoring (rather than

locating and tagging the component); and (3) the facilities would rent (ratherthan purchase) a

monitoring instrument. This last assumption was based on the relative costsfor purchasing and

maintaining a monitoring instrument versus the cost ofrenting the instrument throughout the

year. .

lifO
(,

TABLE 1. SUMMARY OF COST COMPONENTS AND VALUES FOR

AN IN-HOUSE, "LOCATE AND LOG" LDARPROGRAM

(19895)

..

d

;:. --

-

Cost Component Values Comments

Monitoring Cost Fees - Initial/Subsequent (S/component)

Valves 0.7510.75 These values are based on the following requirements: 2 minutes per

valve and 10 minutes per pump. These times were taken from the

Pumps 3.7513.75 SOCMI AID document (see Attachment C). The monitoring time for

Connectors 0.7SI0.75

connectors was assumed to be the same as fo~ valves. A laborrate of

$22.50 per hourwas used.

Monitoring Instrument

Purchase 1 @S6,SOO Reference: Attachment A

Rental This will be a variable rate as follows: Basis: Rental rates from IntekSouth's website forOVA~108 or OVA128 (see Attachment D). Shipping charges: two day delivery • $30;

Each 1day rental: 5164.37 (including shipping) one overnight return - $50. Total $80 each rental period for shipping.

Each 2 day rental: S173.50 (including shipping) These rates were converted to 1989$ using the a final September 1997

Each 3 day rental: $223.72 (including shipping) CE Index value of389.2 (see AttachmentEland a 1989 CE Index

Each 6 day rental: 5369.83 (including shipping) value of355.4.

Each 15 day rental: $757.92 (mcluding shipping)

Maintenance Rental- none Rental: assumed maintenance cost not incUl'l'Cd because the instrument

Purchase - S4J80/year is rented.

Purchase: Attachment A

Daily calibration Rental: S40.871day Rental: AttachmentB. 541.25 converted to 1989$ using tbe mid-point

Purchase - none between the 1992 and 1993"CE Index values 0(358.2 and 359.2

respectively (= 358.7) and the 1989 CB Index value of35S.4.

Purchase: included in maintenance cost above (see Attachment A).

Calibration gases Rental: $297.24/yr Rental: Attachment B. $300 per year converted to 1989$ using the

Purchase • none mid-point between the 1992 and 1993 CB Index values of358.2 and

359.2 respectively (=358.7) and the 1989 CE Index value of355.4.

Purchase: included in maintenance cost above (see AuarJunent A).
TABLE 1. SUMMARY OF LDAR COST COMPONENTS AND VALUES

(continlJed)

Cost Component Values Comments

AdministrativeIReportingIRecordkeeping

Initial Planning aridTiiining-.... ~.

)

See Table 2

(hours) - ---- "-

---Aiinual A,imi~i~;;tive an(t-- ) See Table 2

- '-_ " Reporting (ho~~l- ,~.- -.

Database System S1,200. ifmore than 500 components subject to Based on the purchase ofa spreadsheet program for $300 and assumed

Method 21 24 hours at S36.951hrto create a spreadsheet data base. Assumes that

SO, if 500 or less components subject to Method for facilities with ~SOO Method 21 components, no database system

21 cost is incurred (I.c, will use data log sheetsto track data).

Data Acquisition and Recordkeeping (S/component)

Initial Master Database 1.88 Based OD Attaclunent F. which states that this cost element includes

Acquisition determining and recording process unit. componentservice, stream

namelID, and location information and includes determination of

values, field data logging, and keypunching into the database.

Subsequent Recordkeeping 0.75 B~ on Attachment F. This cost component covers SUbsequent

routine recordkeeping.

Labor Costs (Slbr)

Monitoring 22.50 Attachment A.

AdmiIRecordlRepon 36.95 Based on laborrates used to support tho estimated burden to the

industry as follows:

technical: $33.001hr x 1technical hour ... 533.00

secretarial: SlS.OOlhrx 0.1 technical hours = S 1.50

management: S49.001hr x 0.05 technical hours = $ 2.45

weighted ave: $36.95

l"
TABLE 2. ADMINISTRATION, RECORDKEEPING, AND REPORTING

•

Initial Subsequent (Annual)

Item ~500 Method > 500 Method 5500 Method > 500 Method Comments

21 21 21 21

Components Components Components Components

Read rule and instructions 2 people at 4 3 people at 4 2 people at 4 3 people at 4 For a SOCMI-based LDAR program, assumes initial 3

hours each"" 8 hours each" hours per year hours per year hrsIperson to read rule and insUUclions and 3 hoUl'1 per yeu

h" 12 hi"s =8 hcs - 12 hrs for subsl:quent reading ofrule.

Plan Activities 2 people al 24 3 people at 24 2 people al 1 3 people at I For a SOCMI·based LDAR program, assumes initia120

hours each "" hours each :c hour per hour per hrsIperson 10 plan and 8 hours/year less effort for

48 hrs 72hrs month for 12 month for 12 subsequent planning.

months c 24 months;; 36

hrs hrs

Trainini:; 3 people at j2 5 people at 32 2 people at 4 4 people at 4 Assumes initially a 4-day training course on the rule and the

hours each - hours each - hours per year hours per year use ofmonitoring instrument Annual refresher at 4 hours

96 hrs 160 hours -8 hcs - 16 hcs per year per person. For a SOCMI-based LDAR program,

assumes no change in the training effort required.

Crute, Test, and R&D 5.. 5.. 5.. 5.. Each ofthree elements ofthis item are already accounted for

This tovers the following Comments Comments Comments Comments in the costing. Initial testing and remonitoring is covered

items: under the monitoring and remonitoring costs. Calibration

1. Initial monitoring and and maintenance are covered (S40.87/day for calibration if

remonitoring oflhe renting, or included in the S4.280/year ifpurchasing

components. insttument). Component identification is covered under

2. Calibration and Initial Master Database Acquisition on a S/eomponent basis.

maintenance ofthe

monitoring instrument.

3. Component identification.

Gather Data, Monitoring, Not applicable. Initial activities Covered under Annual

InsptCI are covered elsewhere in this Monitoring costs.

table.
-

t

TABLE 2. ADMINISTRATION, RECORDKEEPING, AND REPORTING

(continued)

Initial Subsequeat(AnDuaQ

Item ~SOOMethod >SOD Method $500 Method >SOOMethod Comments

21 21 21 21

Components Components Components Components

ProcesslComplleJReview See Comments See Comments Data analysis covered by Initial Master Database

This covers analysis ofthe Acquisition and by SubsequentR.ecordkeeping. These are

data collected for accuracy routine activities.

and compliance (e.g., Detennination ofreports to be generated requires minimal

calculation of% leakers) and effortsince same every year (i.e., semiannual report) and is

the determination ofthe covered by estimated effort under Complete Reports.

reports to be generated.

Complete Reports Assumed 32 Assumed 64 Assumed 4 Assumed 8 For a SOCMI·based LDAR program, assumes Notification

Applies to Notification of hours to haunto hours per hours per ofCompliance Status would take 8 hours less. For

Compliance Status and the prepare prepare report and 2 report and 2 semiannual reports, 2 hours less for ~OO component

semiannual repons Notification of Notification of reports per reponsper facilities and 4 hours less for >500 component facUities.

Compliance Compliance year=8 hrs year= 16 hrs

Status Status

ReeordIDistlose Software transfer and data Annual data management

This covers software transfer, management covered under covered under Subsequent

data management, and Master database acquisition. Recordkeeping

purchase ofsoftware Purchase ofsoftware covered

underseparate line item.

StoreIFile Assumed 16 Assumed 32 Assumed 12 Assumed 24 For a SOCMI-based LDARprogram. assumes no changes in

This covers the management hours to set up hours to set up hours per year hours per year effort forsetting up system, but 2 hours less per year for

ofthe recorded data for the 2 system. system. to maintain. to maintain. maintaining it at §OO componentfacilities and 4 hours less

years it is required to be kept per year at >500 component facilities.

Totals (brs): 200 340 60 104 For a HON-based LDARprogram.

183 318 46 8S " 'IFC]r a SOCMI-based LDARprogram. assumes slightly less

'effort.

L

)

I