Central ParkWeat 5001 South Miami Boulevard. Suite300 • 

### P.O. Box 12077 ResearchTriangle 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 

# A92 19 

# 11:-**B-~f** 

# I

SUBJECT: Equipment Leak

## Analysis for Amino andPhenolic 

## Resins NESHAP

The

## purpose ofthis memorandum is to presentthe 

## results ofthe MACT floor determinationand 

## regulatory alternatives analysis for amino/phenolic resin facilities with regards to 

## equipmentleaks. This 

## memorandumalso documents the procedures used to 

## estimatebaseline emissions for the

## 40 major sources included 

## in the analysis and 

## documents the estimationofemissionreductions and control costs associated with

## the selected standard for equipment leaks. The estimation ofenergy and secondary impacts is documented 

## in a separatememorandum title "EstimatedEnergy and Secondary AirImpacts for AminolPhenolic Resin Facilities," docket itemD-B-16 in 

## docketA-92-19.

MACTFIoors



## Based on data provided by the U.S. Environmental Protection Agency through surveys and follow-up telephone conversations, two amino/phenolic resinfacilities were identified 

## as having equipment leak programs subject to 

## Federal, State, or local regulations. These two facilities are: Georgia Pacific's Elk 

## Grove, Californiaplant 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 subjectto the 

## State ofMassachusetts rule 310 CMR718(19), whichessentially requires the facility to implement a leakdetection and 

## repair (LDAR) 

## program equivalent to 40 CPR·part 60, subpart W. 

## Acopy of310 CMR 

## 718(19) is found in Attachment 1.



## New Facilities

The MACT floor for new facilities is setby 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 offacilities have identified the

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

### :0) 

# I

-;

......



# . /

.. //1

.. f •



## lohnSchaefer 

# May 4, 1998 

## page2



# repairofleaks when they are seen orotherwise identified (e.g., smell or sound). However, 

# these maintenance-type LDARprograms are unlikely to be more stringentthan the LDAR programbeing implemented at Solutia's Springfield, MA, plant. Therefore, the MACT floor for equipmentleaks for new sources is representedby the LDARprogram at Solutia's Springfield, MA, facility.
Existing Sources

There are 40 major sources inthis source category. The top 12 percent is represented by the bestperforming 5 facilities. As 

## noted in 

## the previous paragraph, only one major source bas been identified as having a LDARprogramas the result ofFederal, State, orlocal regulations, while others have a maintenance-type LDARprogram. These maintenance-type

. programs are likely tobe less effective at reducing emissions than 

## the LDARprogram in place at the 

## Solutia, Springfield facility. Unfortunately, no information is 

## available to quantify the emission reduction being achieved from these maintenance-typeprograms. In 

## addition, it is 

## notpossible to estimate the costs associated with suchprograms. Therefore, the average ofthe bestperforming 5 facilities cannotbe defined atthis 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 ofaLDAR programbased on40 CFR part 63, subpart H (referred to hereafter in this memo as the HaN 

## LDARprogram). Forexisting sources, two regulatory alternatives were identified

- 40 CFR part 60, subpart VV and the HaN 

## LDAR program. Table 1 provides abriefsummary of SUbpartVV's and the HaN I

## s LDARprograms.

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

## identified to determine whether or not any ofthe regulatory alternatives are cost effective. First, component counts for each ofthe major facilities need to be determined. Second, estimates ofemissions and emission reductions need to be made. Third, the costs associated with the LDARprograms need to be estimated. The following paragraphs present the methods Used in the regulatory alternative analysis.

Estimation ofComponent Counts

Aquestionnaire was sent to companies requesting specific information oncomponent counts, the weight percentHAP contacting the components, and time the component is inJ Contact with the HAP. Facilities were also given the option ofproviding information on the number ofstorage tanks, from which the number ofcomponents would be estimated using the

# ..

John Schaefer 

# May 4,1998 page 3

informationpresented in 

## Table 2. Facilities thatuse only heavy liquids in 

## theirprocess were asked to 

## provide information on the number ofstorage tanks 

## only. Table 3 shows the number oflight liquid and heavy liquid storage tanks 

## used to estimate componentcounts for those facilities that 

## did notprovide specific componentcounts. One facility (Solutia, Springfield) provided aprintoutofcomponents. These components were added by hand to develop componentcounts and type ofservice for this facility. The actual counts used for 38 ofthe 40 facilities are shown in the emission estimation worksheets in 

## Attachment2. For the other two facilities (3M-North Cordova and Cytec-Kalamazoo) equipmentcounts were not estimated because oflack ofdata.



## Emission Estimation

Except for 3M-NorthCordova and Cytec-Kalamazoo, emissions for each facility were estimated using the equipmentcounts and the emission factors shown 

## in Table 4 for uncontrolled emissions and for each ofthe two LDARprograms identified as regulatory alternatives. In addition, the level ofemissions were adjustedbased on the 

## percentHAP and 

## time in 

## contact informationprovided in 

## the previously mentioned questionnaire responses. If 

## facilities did notprovide specific information, then default values of 

# 100% HAP (except for formaldehyde) and 8,760 hours per year were used to estimate emissions. Forestimating 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 2contains the emission estimation worksheets for each facility.

For 3M-North Cordova and Cytec-Kalamazoo, emissions were estimatedusing the average emissions from 27 ofthe 29 facilities for which costing was performed. The two largest facilities, Cytec-yvallingford and Solutia-Springfield, were notused to derive this average. In addition, the 11 facilities that are composed essentially ofheavy liquid components only were also not used to estimate emissions from 3M-NorthCordova 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 leakdefmition of5,000 ppm. (the HaN LDAR specifies a leak definition of5,000 ppm for polymerizing monomers when Phases Uand ill 

## ofthe HaN LDAR program become effective.) For this component, the emission factor was estimated as the mid-point between the emission factor for aquarterly LDAR interval with a leakdefmition of 1,000 ppmand a quarterly LDAR interval with a leak definition of 10,000 ppm. 

# .]

## John Schaefer 

# May 4, 1998 page4

The second exception 

## is for components inheavy liquid service. Forpumps, 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 

# < 10,000ppmemission factor. The 

# < 10,000 SOCMI emissionfactor for open-ended lines was assumed to

# be applicable to sampling connections inheavy liquid service.

Emission Reduction Cost Credits

Cost credits were assigned to the LDARprograms based onthe emission reductions achieved and the type ofcompound. Table 5 shows the values used to calculate this credit. The calculation ofthe cost credits for 29 ofthe facilities is shown in Attachment2. For 3MNorth Cordova and Cytec-Kalamazoo, the emission reduction cost creditwas estimated as the average achieved by 27 ofthe 29 facilities (excluding the emission reduction cost credits of Cytee-Wallingford and Solutia-Springfield).



## CostEstimatioD

Costs (1989$) were estimated for eachfacility except for those thatuse heavy liquids only or those that would not be affected by a HON-based LDARprogram. (Table 6 lists the facilities for which costing was notperformed.) Attachment 5 presents the cost algorithms used to estimate the costs. Attaclunent 6 contains the costestimates for each facility for both Subpart VV and the HON LDAR programs. Attachment7 discusses the derivation ofmany of the costelements in the costing. Specific cost items and assumptions are discussed below.

Type ofMonitoring Program. Facilities subjectto LDARmay use subcontractors or in-house personnel to conduct a LDAR program. Because ofthe 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 ofimplementation, in part, by avoiding travel to monitor pumps.
Monitoring Instrument. Facilities must decide whether 

## to purchase or rent a monitoring instrument. The cost ofa basic monitoring instrument is estimated to be $6,500 (1989$), while the cost to rent an instrument varies depending on the numbers ofdays of monitoring that is required. Because ofthe relatively low number ofcomponents, rental ofa monitoring instrument was found to be less expensive than the purchase ofthe instrument for aU ofthe amino and phenolic resin facilities. Thus, for all facilities, the number ofmonitoring days required per year was estimated and the cost ofthe 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 mustbe made as to whether to 

## tag the components initially orto enter them into 

## a log. Again, because ofthe relatively low number ofcomponents, 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 

## outsetofimplementing a

# LDAR program is whether to purchase adatabase system oruse others means (e.g., a log book) to track the components subject to the LDARand those components identified as leaking. For all except the two facilities with the greatestnumber ofcomponents, it 

## was determined that a database system would not be 

## purchased. However, it was assumed thatcosts 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 percomponentfor subsequentdata entry. For the 

## two facilities for which adatabase systemwas assumed to be purchased, itwas assumed that

## a siniple spreadsheetprogram would be purchased and 

## that in-housepersonnel would create a customized spreadsheet to 

## trackcomponents.
Reporting. Recordkeepine. Training. and Administration. These activities are required for each facility to implementan

# LDARand to maintain it once it is inplace. There are some initial costs associated with the implementation (e.g., training ofpersonnel) and there are some annual costs. For thepurposes ofthe costanalysis, a number ofassumptions were made as to the numberoftechnical hours required to implementthe 

## WAR programs. These assumptions

are 

## detailed in Table 2 

## ofAttachment 7 to 

## this memo. The following summarizes 

## the estimated'

# repo~ordkeeping, training, and 

## administration burden for a SOCMI-based LDAR program and aHON-based LDARprogram. Because the SOCMI-based programdoes notcover 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

## JohnSchaefer May 4, 1998 

## page 6



## frequencies for the HON and 

## Subpart

## VV, with one exception. Initial 

## leakand 

## fmalleak frequencies forpumps in

## light liquid servicehadto be 

## developed specifically for aquarterly LDAR interval with aleakdefmitionof5,000ppm. Forthis component, the fmalleak frequency was estimatedusing the equationfromthe Protocol document (see Attachment4) 

## for light liquidpumps with aleakdefinitionof5,000ppm. The 

## initial leakfrequency was calculatedby using theuncontrolled emissionfactor (Le., 0.0199 

## kglhr) and 

## the same equation and solving for the**aven~ge** 

## leakrate.

Cost

## Effectiveness

Table7 presents the results ofthe costeffectiveness analysis forboth new and 

## existing facilities. The informationpresented in 

## this table is 

## from uncontrolledemissionlevels to the SOCMI SubpartVV LDARprogram level andfromuncontrolledemissionlevels to 

## the 

## HON LDARprogram level. Please note that Solutia-Springtield is 

## already achieving the equivalent ofthe SOCMI SubpartVV LDARprogram. Therefore, implementationofthe 

# soeMl SubpartVV LDARprogram would not actually achieve the additional emissionreductions or costs presented inTable7. Similarly, implementationofa HON 

## LDARprograminrelationto baselineemissions would achieve anemissionreduction of20.2 

## megagrams (= 

## 45.3

- 25.1) at a"costof$12,152 (= 

## $30,356

- $18,204) <

..

### (_:.;.(.-!~.


## As seeninTable 7, the average costeffectiveness ofimplementing the SOCMI Subpart VV LDARprogram from no control ateach ofthe amino/phenolic resin facilities is approximately $3,100

## per megagram ofemissionreduction. The average incremental cost effectiveness ofimplementing the HON 

## LDARprogramfrom no control is approximately $2,300

## permegagram ofemission reduction. The average incremental costeffectiveness of going from the SOCMI Subpart VV program to the HON program is approximately $1,340 

## per megagram ofemission reduction.

## John Schaefer 

## May 4,1998 page 7

TABLE 1



## SUMMARY OF LDARREGULATIONS EVALUATED FOR AMINO AND PHENOLIC RESIN FACIUTIES I 

# j

;



## Componentand Service 40 CFRPart 

## 60, 40 CFRPart 

## 63, Subpart

## VV SubpartH
Valves, gas/vapor and light Monthly monitoring with skip Quarterly monitoring with leak liquid period option for quarterly definition of500 ppm (Phase monitoring. Leakdefinition 

# = Ill). 

## 10,000ppm. Valves, heavy liquid If

## indication ofleak,(sight, sound, smell), monitorto confirm leak Pumps, heavy liquid (leakdefinition 

# = 10,000ppm) and then repair. Pumps, lightliquid Monitormonthly with weekly Monitormonthly with weekly visual inspection. Leak visual inspections. Leak definition 

# = 10,000. defInition 

# =5,000 (Phase 01). 

## Compressors Use ofbarrier fluid system thatprevents leakage ofVOC to atmosphere. Open Ended Lines Caps, blind flanges, etc.

Pressure ReliefDevices, No detectable emissions gas/vapor

Pressure ReliefDevices, light Ifindicationofleak (sight, sound, smell), monitorto confino leak

or heavy liquid (leakdefinition 

# = 10,000ppm) and then repair. Sampling Connections Closed purge systemor closed vent system to control device Flanges and otherconnectors, Ifindication ofleak (sight, Annual monitoring with leak gas/vapor sound, smell), monitorto definition of 10,000. Flanges and otherconnectors, confirm leak (leakdefinition 

# = 10,000ppm) and then repair. light liquid Flanges and otherconnectors, Ifindicationofleak (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 STORAGETANK (numberper tank)



## COMPONENT UGHTUQUID HEAVY LIQUID STORAGETANI( 

## 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



## STORAGETANK COUNTS USED TO ESTIMATE 

## COMPONENT COUNTS

Number ofStorage Tanks Facility LightLiquid 

## Heavy Liquid

3M Hartford 4 

## 2

BTLSpecialties 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

aIndicated 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

TABLE4

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 CreditValue ($/Mg)

Aniline 1,257 

## Cresol, m-, p- 1,808 

## Cresol,o- 1,279 

## Creyslic acid 1,213 Ethylbenzene 386

## a
Ethylene glycol 882
Formalin b 

## 220 Hydrochloric acid 83


## Maleic anhydride 1,257


## Methanol 108


## Phenol 904


## Toluene 

## 232 Xylene 

## 240

SOURCE: December25, 1989, Chemical Marketing Reporter. See Attachment 8.

aUsed this value for butyl cellusolve.

b 

## 35% 

## fonnaldehyde and 7% methanol.



# I(**---~~**

## John Schaefer 

# May 4, 1998 

## page 12

TABLE 6



## FACILITIES FORwmCH LDAR COSTING 

# WAS NOTPERFORMEDa



## Company City Dynachem Georgetown GeorgiaPacific 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 LDARprogram, but notby a HON-based programbecause they are in HAP service less than 300 hours peryear. No costing for either LDARprogram 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


# -- CytecAC Molding Wallingford 0.93 $7444 4068 2341 8004 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 PortWent 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 c

### Spaulding 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 ofa HON-based IOAR program

## win result in an incremental emission reduction of20.2 megagrams atan estimated costof$12,152.

# -~ 

# -**\~.** 

# \') 

# -7),(yo

# -~ 

# l,11



# -- -v1t,v W I 

# 1_., I

## r- 

# "u- '2./. I 

# .,(

..\llf**(~.\r** -.1

# -. ATIACHMENT 2



## EMISSION ESTIMATION AND EMISSION REDUCTION CREDIT WORKSHEETS



# 113M-Cottage Grove

Components HAP Contacl llncontroUed SUbpartW HON CredIts ($\ ($/Mal

Numberof WeIght% 

## nma In EmIssions Emlsslon RedUdion Credit

SOCMI HON



## o o o o 0 

## o 0 

## o 0 Vatves,aIv 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 13M-Hartford



### Numberof Weight% 

### Time In 

### EmIssions Emission Reduction Ctedlt Components HAP 

### Conlact UnconlroUed SUbpartW 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 IItglyr) 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

# ,

Numberof 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



### Numberof Weight% 

### Time In 

### emissions EmlsslonReduction Credit Components HAP 

### Contact UncontroUed SubpartW 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 4Borden

- LouisvIlle

Numberof Weight% 

### TIme In EmIssions Emlsslon Reduction CtedIt ComPOll8llta 

### HAP Contad UnconlroUed SubpartW HON 

### CredIts ($) (SIMa) ComP«lsnl

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

### BTLSpectlalies

ComDonent 

### Numberof Weillht % TIme In EmIssions ComDonents 

### HAP Contact Uncontrolled SUbpartW HON ErnlsalonRedutllon 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 6CyIac• Mobile

Numberof 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

S8moHriQCoM, 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

Page7L Cylec>WalJlngford



### Numberof 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

NumtHlrof Walght % 

### TIme In emissions 

### ComDonenl

Va!ve8, gJv Components 

### HAP contact Uncontrolled 8uboartW 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 9Dexter-Blnnlngham

Numberof 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 10Dexter-Waukegan

ComPOnents 

### HAP Contact Uncontrolled SubpartW

Numberof 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 11Freedom-Charlotle

( Numberof 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 12GP-AIbany

Numberof 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 13GP-Lulkln

Numberof 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 tons

# vr 1.49829128 0.96927648 0.361227



### MOl

### 'vt 1.35743 0.87932 0.32770 Inaemental EmIssIon Reduction (Mglyr) 0.47810 1.02972 

# 31
Page 14GP-PortWentworth

Numberof 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 15GP·Wh/lB City


# ( Numberof 

### 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 Numberof ¥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 RedUdionlMalvrl 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 2679.305Neste

- Moncure

Numberof 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 18Neste·

### N. Winnfield

Numberof 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 tons

### Jvr 3.68221344 1.7151204 0.684988

Un

### Jvr 3.34048 1.55595 0.62142 Incremental EmIssion Reduction II .4olvr) 1.78454 2.71906 

# 310 Page**~9**

### L PO George

Numberof 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

EmIssIonReductJoo Credits (SJ SOCMI HON 

## o 

## o o 0 

## o 0 NunDerof 

### WSlllht % Tine In EmIssIons Compcmenls HAP Conlad Uncontrolled SUbpartW HON ComPDnant
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 21Ranbar-Manor

Numberof**Welaht~** 

### TIme In EmIssions EmIssionReduction 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 Incrementalemission Reduction (MgIy,) 1.65539 2.43393 

# 39
Page 22Schenectady

Numberof 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 23Simpson

### nmber

ICOrnDonenta HAP Contact Uncontlolled SubpartW

Numberof 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 24Solutla•Addyston

Numberof 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 25Solutla

- Springfield

Numberof 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

# a 4olvr) 25.08145 45.33148 

# 1-/-3

Page 26Spauldlng-DeKaIb

Numberof 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 27Dynachem

ComP01l8flt Numberof 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 15

1



### 1

30 1



### 1

1 8760

8760

8760

8760

8760 

## o o 

# o o o 

## o

. 66.4884 

## o 

# o o o o 40.5568 

## o o o o o o 

# o o 

# o o 

# o o o 

## o o o o o o o o o o 28.9D8 

## o o o o o 

## o o o 28.908 

## o o o o 

## o o o o 47.304 

## o o o 

# o o o o o 68.4884 

## o 

# o o o o 40.5568 

## 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 o o 47.304 

## o 

## o o 

# o o o o o 66.4884 

## o o o o o 40.5588 

## 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 

## o o 47.304 

## o 

## o**~,** 

## '.

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 28GP-CohJmbus

Numberof Weight % Tune In EmIuIons ComDOn8l11 Components HAP Conlad Unconb'DDed SUbPartW 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 37 

### ConnIFJanaes. 0

Mg/yr Incremental Emission Reduction (Mgfyr) 0.04020224 0.02560469 0.03647 0.02323 0.01324 0.032309 0.02931 0.00716

Page 29GP-COnway

COmponent Numberof WeIght % TIme In EmIssions COII1J)onents HAP Contact UncontroDed SubpartW 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 30GP-CrosseU

Numberof 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

Numberof !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&mberof 

### I W81aht% 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 34NaUonal-Sallsbwy



### Numberof 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 

### Mli

### ron 0.09624 0.07001 0.07001 Incremental Emlsslon Reduction (MnJvr) 0.02623 0.02623

PlIge35Neste

- Andalusia



### Numberof 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



### Ml

### tlvr 0.57743 0.42008 0.42008 lnaenumtal EmIssion Reduction (Ml1Ivr) 0.15735 0.15735 

## ....

# - 

# ,-



# _.

53 Page 36Neste· Springfield

Numberof Welghl% TImeIn 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~1**wem~~Ih1,...%~...,;TIme,::.:.;;:...::In~:-:----,--.".-,+EmI:;;.::Il6=Io~ns~I-::=..,..--I** "... COmDOnenlll HAP Contact Uncontrolled SubpartW 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 16



### 2

2

29 30 0.5

0.5

0.5

0.5

0.5

0.5 0.5 8280

4140

8760

312

8280

8280 

### 8280 

## o 0 

## o 0 

# o 0 

# o 0 

# o 0 

# o 0 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 0.5148 0 

## o 0 

## o 0 

## o 0 

## o 0 

## o 0 

## o 0 

## o 0 

## o 0 27.324 0 

## o 0 

## o 0 

## o 0 

## o 0 

## o 0 

## o 0 

## o 0 

## o 0 21.6108 21.6108



### 22.356 22.356 

# o 0 

## o o 

# o o o o 33.51744 

## o o o o 

## o 19.1682 

## o 

# o o o o o o 

## o o o o o 

# o o 30.66 

## o o o o 

## o 

# o o 

## o o o o o 

## o o o ·0



## o 

## o o 

## o o 

## o o o 

## o o 21.6108



### 22.356 

## o ..**~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

Page40

## LEAKDETECTIONANDREPAIRCOSTDERIVATIONS

The attachedtwo 

## tables 

## summarizethe

## derivationand 

## sourceofthecostelements used

## to estimatethe HaN LDAR

## program. The

## main sourceofcostelements andthecostingalgorithms

was:



# KJ. Hausleand 

## DJ. Whitt, RadianCorporation, to 

## D. Markwardt, EPA, Final 

## Cost Impacts AnalysisforHONEquipment

# Leaks. February28, 1992. (seeAttachmentA)

. A secondmemoonthe

## petroleum

## refineryMACT

## wasusedforseveralcostelements and**t~r** 

## revising certainaspects

## oCthecostingalgorithmforthe HaN

## memo. This

## memo is

## found in 

## AttacbmentB: :



## R.V. Oommen, Radian

## Corporation, to

## J. Durham, U.S. EnvironmentalProtection 

## Agency, MethodolQgyfor

## EstimatinKNational Impacts

## ofContmUinKLeakinaRefilleD' EQuipment,June

## 27, 1994.

The main

## assumptionsused 

## indeveloping thecosts

# were: (1) thefacilities woulduse in

## housepersonnel to

## conductthe

## LDAR

## program(rather

## than using

## asubcontractor); (2) the 

## facility 

## would "locateandlog" the components subjectto 

## Method21 monitoring (ratherthan 

## locatingandtaggingthecomponent); and(3) the

## facilities would rent

## (ratherthan

## purchase) a monitoringinstrument. Thislastassumption

# was based on

## therelativecostsforpurchasing and maintaining amonitoring instrumentversusthe costofrentingthe

## instrumentthroughoutthe year.

.



# lifO

# (,

TABLE 1. SUMMARYOFCOSTCOMPONENTSAND VALUES FOR ANIN-HOUSE, "LOCATEANDLOG" LDARPROGRAM (19895) .. d



# -- ;:.



# - CostComponent Values 

## Comments
MonitoringCostFees

- Initial/Subsequent(S/component)

Valves 0.7510.75 

## Thesevalues arebasedonthefollowingrequirements: 2minutesper valveand 10minutesperpump. 

## Thesetimesweretakenfromthe Pumps 

## 3.7513.75 SOCMIAID document(seeAttachmentC). Themonitoringtimefor

Connectors 

## 0.7SI0.75 connectorswasassumedtobethe sameas**fo~** 

## valves. Alaborrate

## of $22.50perhour

## wasused. Monitoring Instrument

Purchase 1 @S6,SOO 

## Reference: AttachmentA

Rental This 

### will 

## be avariablerateas follows: Basis: Rental rates 

## from IntekSouth'swebsite**forOVA~108** 

## orOVA128 (seeAttachmentD). Shippingcharges: twodaydelivery•$30; Each 1day rental: 5164.37 (includingshipping) oneovernightreturn

- $50. Total$80

## eachrentalperiodforshipping. 

## Each2dayrental: S173.50 (includingshipping) Theserateswereconvertedto 

## 1989$usingtheafinal 

## September 1997 Each 3 day

## rental: $223.72 (includingshipping) CEIndexvalueof389.2 (seeAttachmentElanda 1989CEIndex Each 6dayrental: 5369.83 (including shipping) valueof355.4. Each 15 dayrental: $757.92 (mcludingshipping)

Maintenance Rental- none Rental: assumedmaintenancecostnot

## incUl'l'Cdbecause

## the instrument Purchase

- S4J80/year 

### isrented. 

## Purchase: AttachmentA Daily calibration Rental: 

## S40.871day Rental: AttachmentB. 541.25 convertedto 

## 1989$usingtbemid-point 

### Purchase

- 

## none betweenthe 1992 and 

## 1993"CEIndex

## values0(358.2and359.2 respectively (=

## 358.7)andthe 1989 CBIndexvalue of35S.4. 

## Purchase: includedin

## maintenancecostabove(seeAttachmentA).

Calibration gases Rental: $297.24/yr Rental: 

## AttachmentB. $300peryearconvertedto 

## 1989$usingthe Purchase•none mid-pointbetweenthe 1992and 1993 CB Indexvaluesof358.2and 359.2respectively(=358.7) andthe 1989CEIndexvalue of355.4. Purchase: includedinmaintenancecost

## above(seeAuarJunentA).

# TABLE 1. SUMMARYOFLDARCOSTCOMPONENTS AND VALUES (continlJed)

CostComponent Values Comments
AdministrativeIReportingIRecordkeeping

Initial Planning

# aridTiiining-....**~.** 

# ) SeeTable2 (hours)

-

---- "- 

# --- Aiinual

# A,im**i~i~;;tive** 

# an(t--) SeeTable 2



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



### DatabaseSystem S1,200. 

### ifmore than 500components subjectto Basedonthepurchase ofaspreadsheetprogramfor$300andassumed Method21 24hours at

### S36.951hrto create aspreadsheetdatabase. Assumes that 

### SO, if

### 500 orless components subjecttoMethod forfacilities with**~SOO** 

### Method21 components,nodatabase system 21 costis incurred (I.c, willusedatalog sheetsto trackdata).



### DataAcquisition and Recordkeeping (S/component)

Initial MasterDatabase 1.88 

### Based OD

### Attaclunent

## F. which statesthatthis

## costelementincludes Acquisition determining andrecordingprocessunit. componentservice, stream namelID, andlocationinformationand includes determinationof values, field datalogging, andkeypunching into 

### thedatabase. SubsequentRecordkeeping 0.75**B~** 

### onAttachmentF. This costcomponentcoversSUbsequent routinerecordkeeping.

LaborCosts (Slbr)
Monitoring 22.50 AttachmentA. AdmiIRecordlRepon 36.95 Basedonlaborrates usedto 

### supporttho estimatedburdento the industryas follows:

technical: 

### $33.001hrx 1technical hour 

# ... 533.00 secretarial: SlS.OOlhrx0.1 technical hours = 

### S 1.50 

### management: S49.001hrx0.05 technicalhours 

# = $ 

### 2.45 weightedave: $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 

### 2people at 4 3people at 4 2 peopleat4 3 people at4 For aSOCMI-basedLDARprogram, assumes initial 3 hours each"" 8 

### hours each" 

### hours peryear hours peryear 

### hrsIperson to read rule and insUUclions and 3 hoUl'1 peryeu h" 

### 12hi"s =8 

### hcs



### - 12 

### hrs for subsl:quentreading ofrule.

Plan Activities 2 people al 

### 24 

### 3 people at 24 2 people al 1 

### 3 people at I 

### For aSOCMI·basedLDARprogram, assumes initia120 hours each "" hours each :c 

### hourper hourper hrsIperson 10

### plan and 8 hours/year less effort for 48 hrs 72hrs 

## monthfor 12 

## month for 12 subsequentplanning. 

### months c 

### 24 months;; 

## 36 hrs hrs
Trainini:; 

### 3 people at j2 

### 5people at 32 2 people at4 4 people at 4 Assumes initially a4-day training course on the rule andthe hours each

- hours each

- hours peryear hours peryear use ofmonitoring instrument Annual refresherat4 hours 96 hrs 160 hours -8 

### hcs



### - 16 hcs 

### peryear perperson. Fora SOCMI-based LDAR program,
assumes no change in 

### the training effortrequired.
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 if

### purchasing components. insttument). Componentidentification 

### is covered under 2. Calibration and Initial Master Database Acquisition on a S/eomponentbasis. maintenance ofthe monitoring instrument. 3. Component identification.

Gather Data, Monitoring, Not applicable. Initial activities Covered underAnnual InsptCI are covered elsewhere in this Monitoring costs. table.

# - 

# t TABLE2. ADMINISTRATION, RECORDKEEPING, ANDREPORTING (continued)

Initial Subsequeat(AnDuaQ

Item**~SOOMethod** 

### >SOD

### Method $500 Method >SOOMethod 

## Comments 21 21 

## 21 21 Components Components Components Components ProcesslComplleJReview SeeComments SeeComments Dataanalysis coveredbyInitialMasterDatabase This coversanalysis ofthe Acquisitionandby SubsequentR.ecordkeeping. Theseare datacollected foraccuracy routineactivities. and compliance (e.g., 

### Detenninationofreports to be

### generatedrequires

### minimal calculationof% leakers) and effortsincesameeveryyear(i.e., semiannualreport) 

## andis the determination ofthe coveredbyestimatedeffortunderCompleteReports. reports to 

### begenerated. 

### CompleteReports Assumed 32 Assumed64 Assumed4 Assumed 

### 8 

### ForaSOCMI·basedLDARprogram, assumesNotification Applies to

### Notification of hours to 

### haunto hours per hours per ofComplianceStatus wouldtake 8hours less. For ComplianceStatus and the prepare prepare reportand2 report

### and2 semiannualreports, 2hours less for**~OO** 

### component 

### semiannual repons Notification of Notificationof reports per reponsper facilities and4hours less for>500componentfacUities. Compliance Compliance year

# =8hrs 

## year= 16 

### hrs 

### Status Status

ReeordIDistlose 

### Softwaretransferand data Annual data

### management This covers softwaretransfer, managementcoveredunder coveredunderSubsequent datamanagement, and Masterdatabaseacquisition. Recordkeeping purchaseofsoftware Purchaseofsoftwarecovered underseparate lineitem.

StoreIFile Assumed 

### 16 Assumed

### 32 Assumed 

### 12 Assumed 

### 24 

### ForaSOCMI-based

### LDARprogram. assumes no changes in 

### This coversthemanagement hours to setup hours to setup 

## hours per

### year hoursperyear effortforsettingup system, 

### but2 hours 

### lessper

### yearfor oftherecorded dataforthe 2 system. system. tomaintain. to 

### maintain. maintaining

### itat

### §OO

### componentfacilities 

### and4hours less 

### years itis requiredto bekept 

### peryear

## at>500 componentfacilities.

Totals (brs): 

## 200 340 60 

## 104 ForaHON-basedLDARprogram.

183 318 46 

### 8S 

### " 'IFC]raSOCMI-basedLDARprogram. assumes slightlyless 'effort.



# L )
I