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VENTURA COUNTY AIR POLLUTION CONTROL DISTRICT 

RULE 54 - SULFUR COMPOUNDS 

(Adopted 7/2/68, Revised and Renumbered 10/22/68, Revised 6/24/69, 5/23/72, 7/5/83, 06/14/94, 

01/14/14) 

A. Applicability 

 This rule is applicable to any person who discharges sulfur compounds into the 

atmosphere from any source whatsoever. 

B. Requirements 

No person shall discharge sulfur compounds which would exist as a liquid or gas at 

standard conditions, in excess of the concentrations listed below. 

1. Sulfur compounds calculated as sulfur dioxide (SO2) by volume at the point of 

discharge: 

a. Exceeding 300 ppm by volume, on a dry basis, from any combustion 

operation, corrected to exhaust gas oxygen content as follows: 

1) For sources subject to Rule 59 Electrical Power Generating 

Equipment – Oxides of Nitrogen Emissions, corrected to 3% 

oxygen; 

2) For sources subject to Rule 74.9 Stationary Internal Combustion 

Engines, corrected to 15% oxygen; 

3) For sources subject to Rule 74.11 Natural Gas-Fired Water 

Heaters, corrected to 3% oxygen; 

4) For sources subject to Rule 74.11.1 Large Water Heaters and Small 

Boilers, corrected to 3% oxygen; 

5) For sources subject to Rule 74.15 Boilers, Steam Generators and 

Process Heaters (5MMBTUs and greater), corrected to 3% oxygen; 

6) For sources subject to Rule 74.15.1 Boilers, Steam Generators and 

Process Heaters (1 to 5 MMBTUs), corrected to 3% oxygen; 

7) For sources subject to Rule 74.17.1 Municipal Solid Waste 

Landfills or 40 CFR Part 60 Subpart WWW – Standards of 

Performance for Municipal Solid Waste Landfills: 

a. Boilers corrected to 3% oxygen; 
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b. Process heaters corrected to 3% oxygen; 

c. Enclosed flares corrected to 3% oxygen; 

d. Internal combustion engines corrected to 15% oxygen; 

e. Turbines corrected to 15% oxygen; 

f. All other sources corrected to 3% oxygen; 

8) For sources subject to Rule 74.23 Stationary Gas Turbines, 

corrected to 15% oxygen; 

9) For all other flares, corrected to 15% oxygen; 

10) For all other combustion operations, corrected to 15% oxygen; or; 

b. Exceeding 500 ppm by volume from any other operation. 

2. Sulfur dioxide which results in average ground or sea level concentrations at any 

point at or beyond the property line in excess of the amounts shown below: 

 Concentration Averaging Time 

 0.25 ppm (Vol) 1 hour 

 0.04 ppm (Vol) 24 hours 

a. Sulfur dioxide which results in ground or sea level concentrations at any 

point at or beyond the property line such that the 1-hour average design 

value exceeds 0.075 ppm (Vol). 

1) For purposes of Subsection B.2.a of this Rule, the design value is 

derived from the 3-year average of annual 99th percentile daily 

maximum 1-hour values. At the District’s discretion, compliance 

with the ground or sea level concentration limit in Subsection B.2.a 

of this rule may be demonstrated using EPA-approved dispersion 

models or ambient air monitoring. If the District requires ambient 

air monitoring, the test method(s) listed in Subsection D.2 of this 

rule must be employed. 

2) To demonstrate compliance using dispersion modeling, the annual 

99th percentile daily maximum at each receptor is determined from 

model results as follows: for each year of meteorological data 

modeled, select from each day the maximum hourly modeled SO2

concentration value and sort all these daily maximum hourly 

values by descending value. The 99th percentile is the 4th highest 

value for each modeled year. Calculate the average of the 99th

percentile values for three consecutive years of modeling data for 

each receptor. Compliance is demonstrated if this average value is 
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less than or equal to the design value concentration limit in 

Subsection B.2.a of this Rule at each receptor. 

3) Compliance with the limit in subsection B.2.a may also be 

demonstrated using EPA-approved screen models. Compliance is 

demonstrated if the 1-hour SO2 ground or sea level concentration 

does not exceed 0.075 ppm (Vol) at or beyond the property line. 

4) If ambient air monitoring data is used to demonstrate compliance, 

the design value must be calculated in accordance with 40 CFR 

Part 50 Appendix T – Interpretation of the Primary National 

Ambient Air Quality Standards for Oxides of Sulfur (Sulfur 

Dioxide). 

3. Hydrogen Sulfide (H2S) exceeding 10 ppm, by volume, at the point of discharge. 

4. Hydrogen sulfide (H2S) which results in average ground or sea level 

concentrations at any point at or beyond the property line in excess of the amounts 

shown in the following table: 

 Concentration Averaging Time 

 0.06 ppm 3 minutes 

 0.03 ppm 1 hour 

For purposes of Subsections B.1 and B.2 of this Rule, all sulfur present in gaseous 

molecular compounds containing oxygen shall be calculated as SO2. For purposes of 

Subsections B.3 and B.4 of this Rule, all reduced sulfur compounds present shall be 

calculated as H2S. 

C. Exemptions 

1. Unplanned Flaring: The provisions of Subsections B.1 and B.2 shall not apply to 

the unplanned burning of gas for emergency or safety concerns provided all the 

following conditions have been met: 

a. The flaring is not the result of an intentional or negligent act or omission 

on the part of the operator or owner. 

b. The flaring is not the result of improper maintenance or improper setting 

of: 

1) High-pressure, high-temperature or high-level shut-in sensors. A 

proper setting for a high-pressure shut-in sensor is one which is 
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greater than 90 percent of the maximum allowed by applicable 

safety regulations. 

2) Low-pressure, low-temperature, or low-level shut-in sensors. A 

proper setting for a low-pressure shut-in sensor is one which is less 

than 110 percent of the minimum allowed by applicable safety 

regulations. 

c. The flaring event results from operational problems, including but not 

limited to: emergency blowdowns, process upsets, power outages, and 

equipment breakdown. 

d. Records or logs of each flaring event shall be kept which include the 

following information: 

1) Operator initials, date, time, duration, volume of gas flared. 

2) Reason for flaring including description of any equipment 

involved. 

3) If involved in flaring, setting of high-pressure, high-temperature, 

or high-level shut-in sensor or pressure relief valve, and maximum 

allowed high-pressure shut-in sensor setting by applicable safety 

regulations. 

4) If involved in flaring, setting of low-pressure, low-temperature, or 

low-level shut-in sensor, and minimum allowed low-pressure shutin sensor setting by applicable safety regulations.

5) Description of corrective measure taken to come into compliance 

with Subsections B.1 and B.2 of this Rule. 

6) For flaring events lasting one hour, or longer, description of 

actions to be taken to prevent the flaring event from recurring. 

All records shall be retained for a minimum of two years from the date of 

each entry and shall be made available to District personnel upon request. 

e. The owner or operator immediately undertakes appropriate corrective 

measures to come into compliance with Subsections B.1 and B.2 of this 

Rule. 

f. The unplanned flaring event shall not exceed 24 hours in duration. If the 

flaring event exceeds 1 hour in duration, the operator shall: 
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1) Notify the APCO as soon as reasonably possible, but no later than 

four hours after its detection by the operator. 

2) Within one week after the flaring event, submit a written report to 

the APCO which contains records from Subsection C.1.d, an 

estimate of sulfur emissions, and pictures or descriptions of the 

equipment or controls that failed. 

g. Sulfur emissions are minimized. 

2. Planned Flaring Events: The provisions of Subsections B.1 and B.2 shall not 

apply to the planned burning of gas provided all of the following conditions have 

been met: 

a. A notice to flare has been submitted in writing at least 72 hours prior to 

such work being done, which justifies that such work shall be done. This 

written notice may be submitted less than 72 hours prior to the event 

provided that it is justified in writing by the operator for at least one of the 

following reasons: imminent hazardous situation, considerable economic 

harm to the company, or excess emissions. This written notice shall 

contain the following information: 

1) Description of the safety, maintenance or production work that 

requires the proposed flaring event. 

2) Expected date and time marking the start and end of the proposed 

flaring event. 

3) Expected gas volume (MCF) and expected sulfur emissions (as 

pounds of SO2). 

4) Description of steps to be taken or equipment modifications to be 

made to minimize sulfur emissions. 

b. Each operator shall submit a planned flaring management plan to the 

APCO for approval no later than 180 days after June 14, 1994. This plan 

shall include at least the following: 

1) A description of all measures to be implemented to decrease flare 

gas volume and reduce sulfur emissions. One measure that shall 

be included in the Plan involves a method of depressurizing 

vessels, compressors and pipelines to prevent flaring. 

2) A description of all planned operational or maintenance procedures 

that may cause flaring. 
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3) A description of each flare system including design features such 

as type, dimensions, flow or pressure capacity, process flow 

diagrams, flow monitoring systems, sulfur measurement 

procedures, and pilot and purge gas features. 

4) A description of any sulfur reduction system, including process 

name, process flow diagrams, design capacity, and emission 

control efficiency. 

5) A description of all measures to be implemented to reduce the 

number of planned flaring events including changes to 

maintenance or production schedules or installation of new 

procedures or equipment. 

6) Any other information determined by the APCO that is necessary 

for evaluating the qualifications of a source for this exemption. 

c. Records of the date, time, duration, flare volume and estimated sulfur 

emissions (as pounds of SO2) are kept during the entire flaring event. 

These records shall be retained for a minimum of two years from the date 

of each entry and shall be made available to District personnel upon 

request. 

d. The District is notified in writing when work is completed. This notice 

shall include all updated information from Subsection C.2.a.1 through 

Subsection C.2.a.4. 

e. Sulfur emissions are minimized during the operation. 

f. No flaring shall occur unless an excess emission fee of $5.00 per 

pound of sulfur compounds (calculated as SO2) emitted is paid to 

the District per calendar year (Section N of Rule 42). For each 

source, an SO2 emission is excess when and after the source's 

flare gas volume allowance has been exceeded during the 

calendar year. The flare gas volume allowance is 91 percent of 

the average of the two highest, consecutive, annual flare gas 

volumes in the applicable six year period as specified below. 

 

These excess emissions shall be determined by the operator and 

the records of those measurements, including gas flows and 

calculated SO2 concentrations, shall be submitted to the District

no later than 15 days after the end of each calendar year. 

 

1) For sources operating prior to January 1, 1988, the flare gas 

volume allowance is calculated from the planned flaring conducted 
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during the period from January 1, 1988 through December 31, 

1993; or 

2) For sources constructed after January 1, 1988, the flare gas volume 

allowance is calculated from the planned flaring conducted during 

the first six whole calendar years of operation. 

D. Test Methods 

1. Sulfur compounds at the point of discharge shall be determined by EPA Test 

Methods 6, 6A, 6C, 8, 15, 16A, 16B, or South Coast AQMD Test Method 307-91 

(Determination of Sulfur in a Gaseous Matrix), as appropriate. Hydrogen sulfide 

emissions from a point of discharge may be determined using a portable monitor 

provided the instrument is operated and calibrated according to manufacturer's 

instructions. The portable monitor shall meet the following minimum 

specifications: 

a. Resolution of 1 ppm H2S. 

b. Accuracy of +/- 5 ppm at 50 ppm H2S. 

c. Drift of 1.5 percent of span over 200 days. 

d. Intrinsically safe power source. 

2. Ground or sea level concentrations of H2S and SO2 shall be determined by Bay 

Area Air Quality Management District Manual of Procedures, Volume VI, 

Section 1, Ground Level Monitoring for Hydrogen Sulfide and Sulfur Dioxide 

(July 20, 1994) with the following amendments: 

a. The wind direction shall be continuously measured and recorded to within 

5 degrees of arc, and wind speed shall be continuously measured and 

recorded to within 0.25 miles per hour (mph) at wind speeds less than 25 

mph and with a threshold no greater than 0.2 mph. 

b. The meteorological instruments and siting requirements shall comply with 

the guidelines in "Quality Assurance Handbook for Air Pollution 

Measurements Systems, Volume IV, Meteorological Measurements 

Version 2.0," EPA-454/B-08-002, March 2008. 

c. The gas standards shall be restandardized against the reference wet 

chemical method at a minimum of once every 12 months, or be 

standardized using National Institute of Standards and Technology (NIST) 

standard gases. 

E. Definitions 

1. "Flaring Event": A flaring event is any flaring that occurs for 10 minutes or 

longer. 
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2. "Planned-Flaring Event": A planned-flaring event is one which results from 

operations identified in the operator's Planned Flaring Management Plan. 

3. "Unplanned-Flaring Event": Any flaring event that occurs as a result of an 

unforeseen process upset or an equipment malfunction or breakdown.