Burden Calculation Tables

2753t01.xlsx

Risk and Technology Review of the Hazardous Organic National Emission Standards for Hazardous Air Pollutants (HON) (40 CFR Part 63, Subparts F, G, H, and I) (Proposed Rule)

Burden Calculation Tables

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Document [xlsx]
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Overview

Inputs
MemoTables
YR1
YR2
YR3
summary
EPA_YR1
EPA_YR2
EPA_YR3
EPA summary


Sheet 1: Inputs

HON All facilities 1/3 of facilities 2/3 of facilities


HON w/ EtO All facilities 1/3 of facilities 2/3 of facilities

# HON Facilities 207 69 138


# ETO Facilities w/ Flares Author: Where do we find these numbers? Send list; extra HON EtO: hex, wastewater, flare load limit, maintenance vent limit etc. Other than EtO: D/F limits w performance testing; fenceline monitoring (starts in year 1); removal of TRE process vent (instead people will have to control process vents) 9 3 6








# Facilities w/ Equip. Leaks 17 6 11








# Facilities w/ HEX 3 1 2








# Facilities w/ PV & SV 14 5 9








# Facilities w/ Wastewater 17 6 11














Flare Management Plan - One-time cost





ETO Process Vent & Storage Vessel RTO


ETO Process Vents and Tanks - Monitoring & Testing
Parameter Value
CECPI 2016 -> 2021


Parameter Capital Cost Annual Cost
Parameter Value
Avg. Cost Per Facility $17,744
541.7 1.31

Total $10,205,000 $5,276,000
Monitor Capital Cost $23,200



708


# facilities that need an RTO 7

Monitor Annual Cost $4,900







Avg. Cost Per Facility $1,457,857 $753,714
Initial Testing $38,302
Flare Monitor Costs









Testing: 5-yr Re-test $19,151
Monitoring Equipment Capital Equipment Cost ($/flare) Annualized Cost ($/yr/flare) Number of Flares Impacted Nationwide Capital Equipment Cost ($) Nationwide Total Annualized Cost ($/yr)






H2 Analyzer 46,000 29,600 64 $2,944,000 $1,894,400
HEX ETO Modified El Paso Method Monitor & Repair




Calorimeter 135,000 37,100 282 $38,070,000 $10,462,200
Parameter Capital Cost Annual Cost


Flare Gas Flow Monitor 565,600 97,700 281 $158,933,600 $27,453,700
Total $43,250 $188,792


Steam Controls/Flow Monitor 879,200 150,200 136 $119,571,200 $20,427,200
# facilities with HEX ETO 3



Air Controls/Flow Monitor 210,800 64,600 17 $3,583,600 $1,098,200
Avg. Cost Per Facility $14,417 $62,931


Avg. Cost Per Facility


$1,560,881 $296,308



















PRD Work Practice & Monitor





Equipment Leaks ETO (valves & connectors 100 ppm, pumps 500 ppm, monthly monitoring)




Parameter Capital Cost Annual Cost



Parameter Capital Cost Annual Cost


PRD Work Practice



Total $177,392 $3,533,021


Implement Prevention Measures $13,700,000 $1,360,000



# facilities with HEX ETO 17



Root Cause Analysis & Corrective Action $0 $5,700,000



Avg. Cost Per Facility $10,435 $207,825


PRD Monitor $3,140,000 $413,000









Total $16,840,000 $7,473,000









# facilities with atmospheric PRDs 207










Avg. Cost Per Facility $81,353 $36,101






















HEX El Paso Method Monitor & Repair











Parameter Capital Cost Annual Cost









Total $770,046 $228,040









# facilities with HEX 207










Avg. Cost Per Facility $3,720 $1,102






















Carbon Adsorber Monitoring and Performance Test











Parameter Capital Cost Annual Cost









Total $32,500 $3,500









# facilities with Adsorber 2










Avg. Cost Per Facility $16,250 $1,750






















Pressure Vessel Monitoring











Parameter Capital Cost Annual Cost









Total $77,665 $72,910









# facilities with Pressure Vessel 209










Avg. Cost Per Facility $372 $349






















Storage Vessel Planned Routine Maintenance











Parameter Capital Cost Annual Cost









Total $2,637,440 $456,480









# facilities with Pressure Vessel 209










Avg. Cost Per Facility $12,619 $2,184






















Dioxin/Furan Monitoring & Performance Testing











Parameter Capital Cost Annual Cost









Total $11,760,000 $6,825,000









# facilities producing chlorinated compounds 21










Avg. Cost Per Facility $560,000 $325,000






















Fenceline Monitoring











Parameter Capital Cost










Total $9,753,500 $32,055,000









# facilities impacted 126










Avg. Cost Per Facility $77,409 $254,405






















Process Vent TRE and Maintenance Vent Requirements











Parameter Capital Cost Annual Cost









Revising the standard from a TRE calculation to control of all vent streams $8,208,893 $20,571,661









Maintenance vent requirements $0 $95,095









# facilities impacted 209










Avg. Cost Per Facility $39,277 $98,884
















































Industry Wages











May 2021 National Industry-Specific Occupational Employment and Wage Estimates











NAICS 325000 - Chemical Manufacturing











Category Occupation Code Mean hourly rate ($/hr) Fringe Benefit Loading Rate Overhead and Profit Rate Loaded Rate ($/hr)






Technical 17-2112 48.21 1.5 1.4 101.24






Management 11-9041 76.83 1.5 1.4 161.34






Clerical 43-9061 21.51 1.5 1.4 45.17



















https://www.bls.gov/oes/2021/may/naics3_325000.htm
























EPA Wages












Hourly Mean Wage With Fringe & Overhead









(GS- 12, step 1) - Tech. 32.02 $51.23









(GS- 13, step 5) - Mgmt. 43.15 $69.04









(GS-6, step 3) - Cler. 17.33 $27.73









https://www.opm.gov/policy-data-oversight/pay-leave/salaries-wages/salary-tables/pdf/2016/GS_h.pdf











or https://www.opm.gov/policy-data-oversight/pay-leave/salaries-wages/

























Sheet 2: MemoTables

Capital/Startup and O&M Costs
(A) (B) (C) (D) (E) (F) (G)
Source & Monitor Type Capital/Startup Costs for One Respondent Number of Respondents with Capital/Startup Costs Total Capital/ Startup Cost
(B X C)
Annual Cost (O&M and Capital) for One Respondent Number of Respondentsa Total Annual Cost,
(E X F)
Flare Monitors $1,560,881 209 $326,224,129 $296,308 209 $61,928,372
PRD Work Practice & Monitors $81,353 209 $17,002,777 $36,101 209 $7,545,109
Heat Exchangers - El Paso Method Monitors and Repair $3,720 209 $777,480 $1,102 209 $230,318
Carbon Adsorber Monitors & Performance Test b $16,250 2 $32,500 $1,750 2 $3,500
Pressure Vessel Monitors $372 209 $77,748 $349 209 $72,941
Storage Vessel Planned Routine Maintenance $12,619 209 $2,637,371 $2,184 209 $456,456
Dioxin/Furan Monitors & Performance Test c $560,000 21 $11,760,000 $325,000 21 $6,825,000
Fenceline Monitoring d $77,409 126 $9,753,534 $254,405 126 $32,055,030
Process Vent TRE and Maintenance Vent Requirements $39,277 209 $8,208,893 $98,884 209 $20,666,756
Ethylene Oxide Heat Exchangers - El Paso Method Monitors and Repair e $14,417 3 $43,250 $62,931 3 $188,792
Ethylene Oxide Equipment Leaks Monitors $10,435 17 $177,392 $207,825 17 $3,533,021
Ethylene Oxide Process Vents & Storage Tanks - Control Device e $1,457,857 7 $10,205,000 $753,714 7 $5,276,000
Ethylene Oxide Process Vents & Storage Tanks - Control Device Monitor e $23,200 7 $162,400 $4,900 7 $34,300
Ethylene Oxide Process Vents & Storage Tanks - Control Device Testing e $38,302 7 $268,114 $0 7 NA
TOTAL

$387,330,588

$138,815,595
(a) Within a given year, there are a maximum of 209 respondents per information collection activity.





(b) We estimate 2 respondents operate carbon adsorbers.





(c) We estimate 21 respondents operate facilities that produce chlorinated compounds.





(d) We estimate 126 respondents will be required to conduct fenceline monitoring.





(e) We estimate there are a maximum of 17 respondents that operate equipment in ethylene oxide service.



















Total Annual Responses

(A) (B) (C) (D) (E)

Information Collection Activity Number of Respondents Number of Responses Number of Existing Respondents That Keep Records But Do Not Submit Reports Total Annual Responses (Over 3-Yr Period)

E=(BxC)+D

Notification of Compliance Status 

Flares 209 1 0 209

PRDs 209 1 0 209

Process Vents 209 1 0 209

Storage Vessels 209 1 0 209

Carbon Adsorbers 2 1 0 2

Ethylene Oxide Wastewater Group 1 17 1 0 17

Ethylene Oxide Process Vents & Storage Tanks 7 1 0 7

Ethylene Oxide Equipment Leaks 17 1 0 17

Periodic Reports

Flares 209 2 0 418

PRDs 209 2 0 418

Maintenance Vents 209 2 0 418

Bypass Lines 0 2 0 0

HEX El Paso Method 209 2 0 418

Storage Vessel Routine Maintenance 209 2 0 418

Carbon Adsorbers 2 2 0 4

Pressure Vessels 209 2 0 418

Ethylene Oxide Wastewater Group 1 17 2 0 34

Ethylene Oxide Process Vents & Storage Tanks 7 2 0 14

Ethylene Oxide Equipment Leaks 17 2 0 34

Fenceline Monitoring

Site-specific monitoring plan 126 1 0 126

Corrective action plan 126 1 0 126

Quarterly reports 126 4 0 504

TOTAL


4,229


Sheet 3: YR1

Table 1 - Annual Respondent Burden and Cost of Recordkeeping and Reporting Requirements for the HON RTR - Year 1
Burden Item (A)
Respondent Hours per Occurrence (Technical hours)
(B)
Non-Labor Costs Per Occurrence
(C)
Number of Occurrences Per Respondent Per Year
(D)
Technical Hours per Respondent Per Year
(A X C)
(E)
Number of Respondents Per Year a
(F)
Technical Hours per Year
(D X E)
(G)
Clerical Hours per Year
(F X 0.1)
(H)
Management Hours per Year
(F X .05)
(I)
Total Hours per Year
(F + G + H)
(J)
Total Labor Costs Per Year b
(K)
Total Non-Labor Costs Per Year
(B x C x E)
1. Applications NA









2. Surveys and Studies NA









3. Reporting Requirements










A. Read Rule c 24 $0 1 24 207.66 4,984 498 249 5,731 $567,281 $0
B. Required Activities










1. Flare Monitors d










a. Capital Cost 0 $1,560,881 1 0 0.66 0 0 0 0 $0 $1,030,181
b. Annualized Cost 0 $296,308 1 0 0.66 0 0 0 0 $0 $195,563
2. PRD Monitor










a. Capital Cost 0 $81,353 1 0 0.66 0 0 0 0 $0 $53,693
b. Annualized Cost 0 $36,101 1 0 0.66 0 0 0 0 $0 $23,827
3. HEX El Paso Method










a. Capital Cost 0 $3,720 1 0 0.66 0 0 0 0 $0 $2,455
b. Annualized Cost 0 $1,102 1 0 0.66 0 0 0 0 $0 $727
4. Carbon Adsorber Monitoring and Performance Test e










a. Capital Cost 0 $16,250 1 0 0.66 0 0 0 0 $0 $10,725
b. Annualized Cost 0 $1,750 1 0 0.66 0 0 0 0 $0 $1,155
5. Pressure Vessel Monitoring










a. Capital Cost 0 $372 1 0 0.66 0 0 0 0 $0 $246
b. Annualized Cost 0 $349 1 0 0.66 0 0 0 0 $0 $230
6. Storage Vessel Planned Routine Maintenance Control










a. Capital Cost 0 $12,619 1 0 0.66 0 0 0 0 $0 $8,329
b. Annualized Cost 0 $2,184 1 0 0.66 0 0 0 0 $0 $1,441
7. Dioxin/Furan Monitoring and Performance Test f










a. Capital Cost 0 $560,000 1 0 0.66 0 0 0 0 $0 $369,600
b. Annualized Cost 0 $325,000 1 0 0.66 0 0 0 0 $0 $214,500
8. Fenceline Monitoring g










a. Capital Cost 0 $77,409 1 0 0.66 0 0 0 0 $0 $51,090
b. Annualized Cost 0 $254,405 1 0 0.66 0 0 0 0 $0 $167,907
9. Process Vent - TRE Removal and Maintenance Vent Control










a. Capital Cost 0 $39,277 1 0 0.66 0 0 0 0 $0 $25,923
b. Annualized Cost 0 $98,884 1 0 0.66 0 0 0 0 $0 $65,263
10. Ethylene Oxide Process Vents & Storage Tanks - Control Device h










a. Capital Cost 0 $1,457,857 1 0 0 0 0 0 0 $0 $0
b. Annualized Cost 0 $753,714 1 0 0 0 0 0 0 $0 $0
11. Ethylene Oxide Process Vents & Storage Tanks - Control Device Monitor h










a. Capital Cost 0 $23,200 1 0 0 0 0 0 0 $0 $0
b. Annualized Cost 0 $4,900 1 0 0 0 0 0 0 $0 $0
12. Ethylene Oxide Process Vents & Storage Tanks - Control Device Testing h










a. Initial Testing 0 $38,302 1 0 0 0 0 0 0 $0 $0
b. Re-Testing i 0 $0 1 0 0 0 0 0 0 $0 $0
13. Ethylene Oxide HEX Modified El Paso Method h










a. Capital Cost 0 $14,417 1 0 0 0 0 0 0 $0 $0
b. Annualized Cost 0 $62,931 1 0 0 0 0 0 0 $0 $0
14. Ethylene Oxide Equipment Leaks h










a. Capital Cost 0 $10,435 1 0 0 0 0 0 0 $0 $0
b. Annualized Cost 0 $207,825 1 0 0 0 0 0 0 $0 $0
C. Create Information Inc. in 3B









D. Gather Information Inc. in 3E









E. Report Preparation










1. Notification of Compliance Status










a. Flares 5 $0 1 5 0.66 3 0 0 4 $376 $0
b. PRDs 15 $0 1 15 0.66 10 1 0 11 $1,127 $0
c. Process Vents 10 $0 1 10 0.66 7 1 0 8 $751 $0
d. Storage Vessels 10 $0 1 10 0.66 7 1 0 8 $751 $0
e. Carbon Adsorbers e 5 $0 1 5 0.66 3 0 0 4 $376 $0
f. Ethylene Oxide Wastewater Group 1 h 4 $0 1 4 0 0 0 0 0 $0 $0
g. Ethylene Oxide Process Vents & Tanks h 4 $0 1 4 0 0 0 0 0 $0 $0
h. Ethylene Oxide Eq. Leaks h 4 $0 1 4 0 0 0 0 0 $0 $0
2. Periodic Report










a. Flares 5 $0 2 10 0.66 7 1 0 8 $751 $0
b. PRDs 10 $0 2 20 0.66 13 1 1 15 $1,502 $0
c. Maintenance Vents 4 $0 2 8 0.66 5 1 0 6 $601 $0
d. Bypass Lines j 4 $0 2 8 0.00 0 0 0 0 $0 $0
e. HEX El Paso Method 3 $0 2 6 0.66 4 0 0 5 $451 $0
f. Storage Vessel Routine Maintenance 3 $0 2 6 0.66 4 0 0 5 $451 $0
g. Carbon Adsorbers e 3 $0 2 6 0.66 4 0 0 5 $451 $0
h. Pressure Vessels 4 $0 2 8 0.66 5 1 0 6 $601 $0
i. Ethylene Oxide Process Vents h 4 $0 2 8 0 0 0 0 0 $0 $0
j. Ethylene Oxide Eq. Leaks h 4 $0 2 8 0 0 0 0 0 $0 $0
k. Ethylene Oxide Wastewater Group 1 h 4 $0 2 8 0 0 0 0 0 $0 $0
3. Fenceline Monitoring g










a. Site-specific monitoring plan 10 $0 1 10 0.66 7 1 0 8 $751 $0
b. Corrective action plan 10 $0 1 10 0 0 0 0 0 $0 $0
c. Quarterly reports 4 $0 4 16 0.66 11 1 1 12 $1,202 $0
Reporting Subtotal




5,073 507 254 5,834 $577,423 $670,615
4. Recordkeeping Requirements










A. Read Instructions Inc. in 3.A









B. Implement Activities NA









C. Develop Record System NA









D. Record information










1. Ethylene Oxide Flare Load h 1 $0 12 12 0 0 0 0 0 $0 $0
2. Flares 0.4 $0 365 146 0.66 96 10 5 111 $10,968 $0
3. PRDs 10 $0 1 10 0.66 7 1 0 8 $751 $0
4. HEX El Paso Method k 0 $0 1 0 0.66 0 0 0 0 $0 $0
5. Maintenance Vents 1 $0 1 1 0.66 1 0 0 1 $75 $0
6. Bypass Lines j 0 $0 1 0 0.00 0 0 0 0 $0 $0
7. Ethylene Oxide Process Vents & Tanks h 2 $0 1 2 0 0 0 0 0 $0 $0
8. Flare Management Plan 75 $0 1 75 0.66 50 5 2 57 $5,634 $0
9. Tank Degassing 3 $0 1 3 0.66 2 0 0 2 $225 $0
10. Parameter monitoring for adsorbers, condensers, and carbon adsorbers e 1 $0 1 1 0.66 1 0 0 1 $75 $0
11. Dioxin/Furan concentration f 1 $0 1 1 0.66 1 0 0 1 $75 $0
12. Pressure Vessels 2 $0 1 2 0.66 1 0 0 2 $150 $0
13. Ethylene Oxide Equipment Leaks h 10 $0 1 10 0 0 0 0 0 $0 $0
14. Ethylene Oxide Wastewater Group 1 h 10 $0 1 10 0 0 0 0 0 $0 $0
15. Fenceline Monitoring - Meteorological data g 0.4 $0 365 146 0.66 96 10 5 111 $10,968 $0
16. Fenceline Monitoring - Sampling g 1 $0 365 365 0.66 241 24 12 277 $27,420 $0
E. Personnel Training c 16 $0 1 16 207.66 3,323 332 166 3,821 $378,187 $0
F. Time for Audits NA









Recordkeeping Subtotal




3,818 382 191 4,390 $434,528 $0
TOTAL




8,891 889 445 10,224 $1,011,951 $670,615




















Total Hours Labor Non-Labor Total





Summary of Respondent Burden

10,224 $1,011,951 $670,615 $1,682,566

















Initial Capital and Startup




$1,653,611





Annualized Capital/Start-up and O & M




$670,615












Footnotes:
(a) We have assumed that there are approximately 207 existing respondents, with 2 additional sources becoming subject to the rule over the three-year period of this ICR. We assume that one-third of the existing facilities would begin complying in year 2 and the remaining two-thirds of the existing facilities in year 3.
(b) This ICR uses the following labor rates for privately-owned sources: $161.34 for managerial, $101.24 for technical,  and $45.17 for clerical labor.  These rates are from the United States Department of Labor, Bureau of Labor Statistics, May 2021, National Industry-Specific Occupational Employment and Wage Estimates for NAICS 325000 - Chemical Manufacturing. These rates have been adjusted using a Fringe Benefit Loading Rate of 1.5 and an Overhead and Profit Rate of 1.4 (Mean Hourly Rate * Fringe Benefit Loading Rate * Overhead and Profit Rate = Loaded Rate) to account for varying industry wage rates and the additional overhead business costs of employing workers beyond their wages and benefits, including business expenses associated with hiring, training, and equipping their employees.
(c) This is a one-time cost.
(d) Includes costs for the following monitoring equipment: H2 analyzer, calorimeter, flare gas flow monitor, steam controls/flow monitor, and air controls/flow monitor.
(e) We estimate 2 respondents operate carbon adsorbers.
(f) We estimate 21 respondents operate facilities that produce chlorinated compounds.
(g) We estimate 126 respondents will be required to conduct fenceline monitoring. All 126 facilities would begin complying with requirements in year 2 and submit corrective action plans in year 3.
(h) Only applicable to facilities with ethylene oxide emissions. We assume these facilities will begin complying in year 2. Note, there are not startup/capital & O&M costs for wastewater, and no additional recordkeeping & reporting costs for HEX systems in ethylene oxide service. These are assumed to be included with all HEX systems.
(i) Retests only occur after five years from the intial performance test, and thus would not occur over the period covered by this ICR.
(j) Assumed that bypass lines were not used during the 3-year period, so costs for bypass lines would not be incurred.
(k) Assumed recordkeeping hours are comparable to previously required water methods, and assigned 0 additional hours to implement the El Paso Method.

Sheet 4: YR2

Table 2 - Annual Respondent Burden and Cost of Recordkeeping and Reporting Requirements for the HON RTR - Year 2
Burden Item (A)
Respondent Hours per Occurrence (Technical hours)
(B)
Non-Labor Costs Per Occurrence
(C)
Number of Occurrences Per Respondent Per Year
(D)
Technical Hours per Respondent Per Year
(A X C)
(E)
Number of Respondents Per Year a
(F)
Technical Hours per Year
(D X E)
(G)
Clerical Hours per Year
(F X 0.1)
(H)
Management Hours per Year
(F X .05)
(I)
Total Hours per Year
(F + G + H)
(J)
Total Labor Costs Per Year b
(K)
Total Non-Labor Costs Per Year
(B x C x E)
1. Applications NA









2. Surveys and Studies NA









3. Reporting Requirements










A. Read Rule c 24 $0 1 24 0.66 16 2 1 18 $1,803 $0
B. Required Activities










1. Flare Monitors d










a. Capital Cost 0 $1,560,881 1 0 70.33 0 0 0 0 $0 $109,776,761
b. Annualized Cost 0 $296,308 1 0 70.33 0 0 0 0 $0 $20,839,342
2. PRD Monitor










a. Capital Cost 0 $81,353 1 0 70.33 0 0 0 0 $0 $5,721,556
b. Annualized Cost 0 $36,101 1 0 70.33 0 0 0 0 $0 $2,538,983
3. HEX El Paso Method










a. Capital Cost 0 $3,720 1 0 70.33 0 0 0 0 $0 $261,628
b. Annualized Cost 0 $1,102 1 0 70.33 0 0 0 0 $0 $77,504
4. Carbon Adsorber Monitoring and Performance Test e










a. Capital Cost 0 $16,250 1 0 2 0 0 0 0 $0 $32,500
b. Annualized Cost 0 $1,750 1 0 2 0 0 0 0 $0 $3,500
5. Pressure Vessel Monitoring










a. Capital Cost 0 $372 1 0 70.33 0 0 0 0 $0 $26,163
b. Annualized Cost 0 $349 1 0 70.33 0 0 0 0 $0 $24,545
6. Storage Vessel Planned Routine Maintenance Control










a. Capital Cost 0 $12,619 1 0 70.33 0 0 0 0 $0 $887,494
b. Annualized Cost 0 $2,184 1 0 70.33 0 0 0 0 $0 $153,601
7. Dioxin/Furan Monitoring and Performance Test f










a. Capital Cost 0 $560,000 1 0 21 0 0 0 0 $0 $11,760,000
b. Annualized Cost 0 $325,000 1 0 21 0 0 0 0 $0 $6,825,000
8. Fenceline Monitoring g










a. Capital Cost 0 $77,409 1 0 126 0 0 0 0 $0 $9,753,534
b. Annualized Cost 0 $254,405 1 0 126 0 0 0 0 $0 $32,055,030
9. Process Vent - TRE Removal and Maintenance Vent Control










a. Capital Cost 0 $39,277 1 0 70.33 0 0 0 0 $0 $2,762,351
b. Annualized Cost 0 $98,884 1 0 70.33 0 0 0 0 $0 $6,954,512
10. Ethylene Oxide Process Vents & Storage Tanks - Control Device h










a. Capital Cost 0 $1,457,857 1 0 7 0 0 0 0 $0 $10,205,000
b. Annualized Cost 0 $753,714 1 0 7 0 0 0 0 $0 $5,276,000
11. Ethylene Oxide Process Vents & Storage Tanks - Control Device Monitor h










a. Capital Cost 0 $23,200 1 0 7 0 0 0 0 $0 $162,400
b. Annualized Cost 0 $4,900 1 0 7 0 0 0 0 $0 $34,300
12. Ethylene Oxide Process Vents & Storage Tanks - Control Device Testing h










a. Initial Testing 0 $38,302 1 0 7 0 0 0 0 $0 $268,114
b. Re-Testing i 0 $0 1 0 0 0 0 0 0 $0 $0
13. Ethylene Oxide HEX Modified El Paso Method h










a. Capital Cost 0 $14,417 1 0 3 0 0 0 0 $0 $43,250
b. Annualized Cost 0 $62,931 1 0 3 0 0 0 0 $0 $188,792
14. Ethylene Oxide Equipment Leaks h










a. Capital Cost 0 $10,435 1 0 17 0 0 0 0 $0 $177,392
b. Annualized Cost 0 $207,825 1 0 17 0 0 0 0 $0 $3,533,021
C. Create Information Inc. in 3B









D. Gather Information Inc. in 3E









E. Report Preparation










1. Notification of Compliance Status










a. Flares 5 $0 1 5 70.33 352 35 18 404 $40,026 $0
b. PRDs 15 $0 1 15 70.33 1,055 105 53 1,213 $120,079 $0
c. Process Vents 10 $0 1 10 70.33 703 70 35 809 $80,052 $0
d. Storage Vessels 10 $0 1 10 70.33 703 70 35 809 $80,052 $0
e. Carbon Adsorbers e 5 $0 1 5 2.00 10 1 1 12 $1,138 $0
f. Ethylene Oxide Wastewater Group 1 h 4 $0 1 4 17 68 7 3 78 $7,740 $0
g. Ethylene Oxide Process Vents & Tanks h 4 $0 1 4 7 28 3 1 32 $3,187 $0
h. Ethylene Oxide Eq. Leaks h 4 $0 1 4 17 68 7 3 78 $7,740 $0
2. Periodic Report










a. Flares 5 $0 2 10 70.33 703 70 35 809 $80,052 $0
b. PRDs 10 $0 2 20 70.33 1,407 141 70 1,618 $160,105 $0
c. Maintenance Vents 4 $0 2 8 70.33 563 56 28 647 $64,042 $0
d. Bypass Lines j 4 $0 2 8 0.00 0 0 0 0 $0 $0
e. HEX El Paso Method 3 $0 2 6 70.33 422 42 21 485 $48,031 $0
f. Storage Vessel Routine Maintenance 3 $0 2 6 70.33 422 42 21 485 $48,031 $0
g. Carbon Adsorbers e 3 $0 2 6 2 12 1 1 14 $1,366 $0
h. Pressure Vessels 4 $0 2 8 70.33 563 56 28 647 $64,042 $0
i. Ethylene Oxide Process Vents h 4 $0 2 8 7 56 6 3 64 $6,374 $0
j. Ethylene Oxide Eq. Leaks h 4 $0 2 8 17 136 14 7 156 $15,480 $0
k. Ethylene Oxide Wastewater Group 1 h 4 $0 2 8 17 136 14 7 156 $15,480 $0
3. Fenceline Monitoring g










a. Site-specific monitoring plan 10 $0 1 10 126 1,260 126 63 1,449 $143,418 $0
b. Corrective action plan 10 $0 1 10 0 0 0 0 0 $0 $0
c. Quarterly reports 4 $0 4 16 126 2,016 202 101 2,318 $229,469 $0
Reporting Subtotal




10,698 1,070 535 12,303 $1,217,707 $78,504,129
4. Recordkeeping Requirements










A. Read Instructions Inc. in 3.A









B. Implement Activities NA









C. Develop Record System NA









D. Record information










1. Ethylene Oxide Flare Load h 1 $0 12 12 9 108 11 5 124 $12,293 $0
2. Flares 0.4 $0 365 146 70.33 10,268 1,027 513 11,808 $1,168,765 $0
3. PRDs 10 $0 1 10 70.33 703 70 35 809 $80,052 $0
4. HEX El Paso Method k 0 $0 1 0 0 0 0 0 0 $0 $0
5. Maintenance Vents 1 $0 1 1 70.33 70 7 4 81 $8,005 $0
6. Bypass Lines j 0 $0 1 0 0 0 0 0 0 $0 $0
7. Ethylene Oxide Process Vents & Tanks h 2 $0 1 2 7 14 1 1 16 $1,594 $0
8. Flare Management Plan 75 $0 1 75 70.33 5,275 527 264 6,066 $600,393 $0
9. Tank Degassing 3 $0 1 3 70.33 211 21 11 243 $24,016 $0
10. Parameter monitoring for adsorbers, condensers, and carbon adsorbers e 1 $0 1 1 2 2 0 0 2 $228 $0
11. Dioxin/Furan concentration f 1 $0 1 1 21 21 2 1 24 $2,390 $0
12. Pressure Vessels 2 $0 1 2 70.33 141 14 7 162 $16,010 $0
13. Ethylene Oxide Equipment Leaks h 10 $0 1 10 17 170 17 9 196 $19,350 $0
14. Ethylene Oxide Wastewater Group 1 h 10 $0 1 10 17 170 17 9 196 $19,350 $0
15. Fenceline Monitoring - Meteorological data g 0.4 $0 365 146 126 18,396 1,840 920 21,155 $2,093,906 $0
16. Fenceline Monitoring - Sampling g 1 $0 365 365 126 45,990 4,599 2,300 52,889 $5,234,766 $0
E. Personnel Training c 16 $0 1 16 0.66 11 1 1 12 $1,202 $0
F. Time for Audits NA









Recordkeeping Subtotal




81,550 8,155 4,077 93,782 $9,282,320 $0
TOTAL




92,248 9,225 4,612 106,085 $10,500,027 $78,504,129




















Total Hours Labor Non-Labor Total





Summary of Respondent Burden

106,085 $10,500,027 $78,504,129 $89,004,156

















Initial Capital and Startup




$116,192,262





Annualized Capital/Start-up and O & M




$78,504,129












Footnotes:










(a) We have assumed that there are approximately 207 existing respondents, with 2 additional sources becoming subject to the rule over the three-year period of this ICR. We assume that one-third of the existing facilities would begin complying in year 2 and the remaining two-thirds of the existing facilities in year 3.
(b) This ICR uses the following labor rates for privately-owned sources: $161.34 for managerial, $101.24 for technical,  and $45.17 for clerical labor.  These rates are from the United States Department of Labor, Bureau of Labor Statistics, May 2021, National Industry-Specific Occupational Employment and Wage Estimates for NAICS 325000 - Chemical Manufacturing. These rates have been adjusted using a Fringe Benefit Loading Rate of 1.5 and an Overhead and Profit Rate of 1.4 (Mean Hourly Rate * Fringe Benefit Loading Rate * Overhead and Profit Rate = Loaded Rate) to account for varying industry wage rates and the additional overhead business costs of employing workers beyond their wages and benefits, including business expenses associated with hiring, training, and equipping their employees.
(c) This is a one-time cost.
(d) Includes costs for the following monitoring equipment: H2 analyzer, calorimeter, flare gas flow monitor, steam controls/flow monitor, and air controls/flow monitor.
(e) We estimate 2 respondents operate carbon adsorbers.
(f) We estimate 21 respondents operate facilities that produce chlorinated compounds.
(g) We estimate 126 respondents will be required to conduct fenceline monitoring. All 126 facilities would begin complying with requirements in year 2 and submit corrective action plans in year 3.
(h) Only applicable to facilities with ethylene oxide emissions. We assume these facilities will begin complying in year 2. Note, there are not startup/capital & O&M costs for wastewater, and no additional recordkeeping & reporting costs for HEX systems in ethylene oxide service. These are assumed to be included with all HEX systems.
(i) Retests only occur after five years from the intial performance test, and thus would not occur over the period covered by this ICR.
(j) Assumed that bypass lines were not used during the 3-year period, so costs for bypass lines would not be incurred.
(k) Assumed recordkeeping hours are comparable to previously required water methods, and assigned 0 additional hours to implement the El Paso Method.

Sheet 5: YR3

Table 3 - Annual Respondent Burden and Cost of Recordkeeping and Reporting Requirements for the HON RTR - Year 3
Burden Item (A)
Respondent Hours per Occurrence (Technical hours)
(B)
Non-Labor Costs Per Occurrence
(C)
Number of Occurrences Per Respondent Per Year
(D)
Technical Hours per Respondent Per Year
(A X C)
(E)
Number of Respondents Per Year
(F)
Technical Hours per Year
(D X E)
(G)
Clerical Hours per Year
(F X 0.1)
(H)
Management Hours per Year
(F X .05)
(I)
Total Hours per Year
(F + G + H)
(J)
Total Labor Costs Per Year
(K)
Total Non-Labor Costs Per Year
(B x C x E)
1. Applications NA









2. Surveys and Studies NA









3. Reporting Requirements










A. Read Rule c 24 $0 1 24 0.66 16 2 1 18 $1,803 $0
B. Required Activities










1. Flare Monitors d










a. Capital Cost 0 $1,560,881 1 0 140 0 0 0 0 $0 $218,523,340
b. Annualized Cost 0 $296,308 1 0 140 0 0 0 0 $0 $41,483,120
2. PRD Monitor










a. Capital Cost 0 $81,353 1 0 140 0 0 0 0 $0 $11,389,420
b. Annualized Cost 0 $36,101 1 0 140 0 0 0 0 $0 $5,054,140
3. HEX El Paso Method










a. Capital Cost 0 $3,720 1 0 140 0 0 0 0 $0 $520,800
b. Annualized Cost 0 $1,102 1 0 140 0 0 0 0 $0 $154,280
4. Carbon Adsorber Monitoring and Performance Test e










a. Capital Cost 0 $16,250 1 0 2 0 0 0 0 $0 $32,500
b. Annualized Cost 0 $1,750 1 0 2 0 0 0 0 $0 $3,500
5. Pressure Vessel Monitoring










a. Capital Cost 0 $372 1 0 140 0 0 0 0 $0 $52,080
b. Annualized Cost 0 $349 1 0 140 0 0 0 0 $0 $48,860
6. Storage Vessel Planned Routine Maintenance Control










a. Capital Cost 0 $12,619 1 0 140 0 0 0 0 $0 $1,766,660
b. Annualized Cost 0 $2,184 1 0 140 0 0 0 0 $0 $305,760
7. Dioxin/Furan Monitoring and Performance Test f










a. Capital Cost 0 $560,000 1 0 21 0 0 0 0 $0 $11,760,000
b. Annualized Cost 0 $325,000 1 0 21 0 0 0 0 $0 $6,825,000
8. Fenceline Monitoring g










a. Capital Cost 0 $77,409 1 0 126 0 0 0 0 $0 $9,753,534
b. Annualized Cost 0 $254,405 1 0 126 0 0 0 0 $0 $32,055,030
9. Process Vent - TRE Removal and Maintenance Vent Control










a. Capital Cost 0 $39,277 1 0 140 0 0 0 0 $0 $5,498,780
b. Annualized Cost 0 $98,884 1 0 140 0 0 0 0 $0 $13,843,760
10. Ethylene Oxide Process Vents & Storage Tanks - Control Device h










a. Capital Cost 0 $1,457,857 1 0 7 0 0 0 0 $0 $10,205,000
b. Annualized Cost 0 $753,714 1 0 7 0 0 0 0 $0 $5,276,000
11. Ethylene Oxide Process Vents & Storage Tanks - Control Device Monitor h










a. Capital Cost 0 $23,200 1 0 7 0 0 0 0 $0 $162,400
b. Annualized Cost 0 $4,900 1 0 7 0 0 0 0 $0 $34,300
12. Ethylene Oxide Process Vents & Storage Tanks - Control Device Testing h










a. Initial Testing 0 $38,302 1 0 7 0 0 0 0 $0 $268,114
b. Re-Testing i 0 $0 1 0 0 0 0 0 0 $0 $0
13. Ethylene Oxide HEX Modified El Paso Method h










a. Capital Cost 0 $14,417 1 0 3 0 0 0 0 $0 $43,250
b. Annualized Cost 0 $62,931 1 0 3 0 0 0 0 $0 $188,792
14. Ethylene Oxide Equipment Leaks h










a. Capital Cost 0 $10,435 1 0 17 0 0 0 0 $0 $177,392
b. Annualized Cost 0 $207,825 1 0 17 0 0 0 0 $0 $3,533,021
C. Create Information Inc. in 3B









D. Gather Information Inc. in 3E









E. Report Preparation










1. Notification of Compliance Status










a. Flares 5 $0 1 5 140 700 70 35 805 $79,677 $0
b. PRDs 15 $0 1 15 140 2,100 210 105 2,415 $239,030 $0
c. Process Vents 10 $0 1 10 140 1,400 140 70 1,610 $159,354 $0
d. Storage Vessels 10 $0 1 10 140 1,400 140 70 1,610 $159,354 $0
e. Carbon Adsorbers e 5 $0 1 5 2 10 1 1 12 $1,138 $0
f. Ethylene Oxide Wastewater Group 1 h 4 $0 1 4 17 68 7 3 78 $7,740 $0
g. Ethylene Oxide Process Vents & Tanks h 4 $0 1 4 7 28 3 1 32 $3,187 $0
h. Ethylene Oxide Eq. Leaks h 4 $0 1 4 17 68 7 3 78 $7,740 $0
2. Periodic Report










a. Flares 5 $0 2 10 140 1,400 140 70 1,610 $159,354 $0
b. PRDs 10 $0 2 20 140 2,800 280 140 3,220 $318,707 $0
c. Maintenance Vents 4 $0 2 8 140 1,120 112 56 1,288 $127,483 $0
d. Bypass Lines j 4 $0 2