# Explosives Test Center, LLC — PHMSA Interpretation

**Citation:** 18-0017  
**Type / status:** guidance / guidance  
**Agency:** Pipeline and Hazardous Materials Safety Administration  
**Effective:** Not stated  
**Published:** 2018-06-15

18-0017 response to Explosives Test Center, LLC; G2 Integrated Solutions concerning 173.62, 192.903.

## Document text

<<<PAGE 1>>>

U.S . Department
ofTransportation
Pipeline and Hazardous Materials
S afety Administration
1200 New Jersey Avenue SE
Washington DC 20590
DE C 0 7 2017
Mr. John A. Jacobi
Vice President and Principal
G2 Integrated Solutions
10850 Richmond A venue, #200
Houston, TX 77042
Re: Petit~ for Finding
Dear Mj'Jacobi:
On June 28, 2017, pursuant to 49 C.F.R. § 190.9, G2 Integrated Solutions, on behalf of Olin
Pipeline Services (G2) filed a petition for a finding or approval (Petition) to use its proposed
methodology to calculate the Potential Impact Radius (PIR) of non-flammable gas anhydrous
hydrogen chloride (HCL). Specifically, G2 requested a finding allowing the use of the PIR
factor published by Pipeline and Hazardous Materials Safety Administration (PHMSA) in TT0-
13 for hydrogen, the urban setting PIR for chlorine published in TT0-14, and the TT0-14
protocol to calculate the PIR factor for the urban setting for anhydrous HCL. The resulting PIRs
would then be used to identify Part 192 High Consequence Areas using 49 CFR § 192.903,
Method2.
Section 190.9 provides that in circumstances where a rule contained in parts 192, 193 and 195 of
the pipeline safety regulations authorizes the Administrator to make a finding or approval, an
operator may petition the Administrator for such a finding or approval. The petition must refer
to the rule authorizing the action sought and contain information or arguments that justify the
action.
Having reviewed G2's request, PHMSA has determined that it does not meet the requirements
set forth in § 190.9 for a petition for finding or approval, because G2 has failed to identify a rule
authorizing the action sought. The integrity management regulation cited,§ 192.903, does not
authorize the Administrator to make a finding or approval with respect to using alternative means
to calculate PIR. Rather the regulation specifies how PIR must be calculated for the purpose of
identifying high consequence areas.

<<<PAGE 2>>>

If you have any questions or would like to discuss further, please contact Tewabe Asebe at 202-
366-5523.
Sincerely,
o . a
Director, Office of Standards
and Rulemaking

<<<PAGE 3>>>

,..2 INTEGRATED
\.:f-'s o L U TIO N S
10850 Richmond Ave .. #200 Houston, 'TX 77042
0: 713 260.4000
info@g2-is.com www.g2-is.com
June 28, 2017
Stephanie Weidman, PHMSA Program Director
Railroad Commission of Texas
P.O. Box 12967
Austin, Texas 78711-2967
Re: Request for finding or approval under 49 CFR §190.9
Olin Pipeline Services (A Division of Olin Corporation)
2301 N. Brazosport Blvd., B-101 #38
Freeport, TX 77541
PHMSA OPID 39376
T4 Permit Number #09681 (gas lines)
Dear Ms. Weidman:
Via e-Mail
G2 Integrated Solutions (G2) has been retained by Olin Pipeline Services (Olin) to request a
finding pursuant to 49 CFR §190.9(a):
(a) In circumstances where a rule contained in parts 192, 193 and 195 of this chapter
authorizes the Administrator to make a finding or approval, an operator may petition the
Administrator for such a finding or approval.
The Railroad Commission of Texas (RRC) is receiving this request because the lines affected
(see below) are intrastate Part 192 pipelines under the primary jurisdiction of the RRC and 49
CFR §190.9(b)(1) requires operators seeking a finding or approval involving intrastate pipeline
transportation to send such requests to the State agency certified to participate under 49 U.S.C.
60105 - in this case, the RRC.
Background
Olin recently acquired a number of pipelines from the Dow Chemical Company, Texas Operations
and is in the process of conducting a compliance audit under the Texas Environmental, Health
and Safety Audit Privilege Act. G2 has been and is assisting Olin in conducting the compliance
audit.
For purposes of 49 CFR Part 192, Subpart 0 - Gas Transmission Pipeline Integrity Management,
Olin has elected to use Method 2 (49 CFR §192.903) to define high consequence areas:
(2) The area within a potential impact circle containing-
(i) 20 or more buildings intended for human occupancy, unless the exception in
paragraph (4) applies; or
(ii) An identified site.

<<<PAGE 4>>>

G2 Integrated Solutions
Page 2 of 4
The following 49 CFR §192.903 definitions are relevant to this request:
Potential impact circle is a circle of radius equal to the potential impact radius (PIR).
Potential impact radius (PIR) means the radius of a circle within which the potential
failure of a pipeline could have significant impact on people or property. PIR is
determined by the formula r = 0.69* (square root of (p"d2), where 'r' is the radius of a
circular area in feet surrounding the point of failure, 'p' is the maximum allowable
operating pressure (MAOP) in the pipeline segment in pounds per square inch and 'd' is
the nominal diameter of the pipeline in inches.
Note: 0.69 is the factor for natural gas. This number will vary for other gases
depending upon their heat of combustion. An operator transporting gas other
than natural gas must use section 3.2 of ASME/ANSI B31.8S-2001 (Supplement
to ASME/ANSI 831.8; (incorporated by reference, see §192.7) to calculate the
impact radius formula.
This request arises because of PHMSA's response to Gas IMP FAQ 144:
What is the preferred method for calculating the Potential Impact Radius (PIR) of a leak
of a non-flammable gas within the context of Pipeline Integrity Management?
The regulation refers to ASME 831.85-2001 Section 3.2 for calculation of PIR for gases
other than natural gas. However, this document only deals with flammable gases. ASME
B31.8S-2001 allows alternate models to be used for calculating impact radius, but
provides no guidance as to preferred methods of modeling non-flammable or corrosive
gases. [10/25/2004)
The potential impact circle concept is only applicable for flammable gases. Operators of
pipelines carrying non-flammable gases must consider their entire pipelines as if they
were in high consequence areas, or they may apply for a waiver to use another method
that they may propose for defining HCAs. (emphasis added)
In January, 2005 (subsequent to publishing FAQ 144), PHMSA published ITO Number 14,
Derivation of Potential Impact Radius Formulae for Vapor Cloud Dispersion Subject to 49 CFR
§192 (TI0-14, available at
httos://primis.phmsa.dot.gov/qasimp/docsITT014 finalreport January2005.pdf).
Very briefly, IT0-14 developed simplified PIR formulae for non-flammable
hazardous/toxic products using the US Environmental Protection Agency's (EPA) "Risk
Management Program Guidance for Offsite Consequence Analysis." (RMP Guidance). In other
words, TI0-14 established a scientific basis for calculating CFER PIR factors (0.69 for natural
gas) for toxic but non-flammable gasses .. Note that the RMP guidance results in the calculation
of two factors for each toxic endpoint - one for rural settings and one for urban settings. The
resulting PIRs for rural settings are somewhat larger based on the theory that rural settings are

<<<PAGE 5>>>

G2 Integralcd Solutions
Page 3 of 4
flat and offer less resistance to dispersion of vapor clouds. It is Olin's position that a
refinery/chemical manufacturing facility more closely resembles EPA's urban setting.
One of the non-flammable gasses transported by Olin, chlorine, was specifically addressed by
TT0-14. Another, anhydrous HCL, was not. A third gas, hydrogen, is a flammable gas and its
CFER PIR factor was specifically calculated in TT0-13 consistent with the methodology of
section 3.2 of ASME/ANSI B31.8S-2001
(https://primis.phmsa.dot.gov/gasim p/docs/TT013 PotentiallmpactRadius Final Report June200
5.pdf}
The Specific Lines in Question
Using published data for PIR factors for hydrogen and chlorine and the TT0-14 protocol for
calculating both the rural and urban settings for anhydrous HCL yield the following PIRs for each
of the Olin Part 192 lines subject to 49 CFR Part 192:
1 28
2 130
3 246
4 261
5 331
6 406
Chlorine
Chlorine
Anhydrous HCL 24
Anhydrous HCL 12
Chlorine 12
Hydrogen 30
150
200
650
650 0.08/0.06 (6)
150 0.38/0.16
13 0.47 (5)
75/32
86/37
46/35 (6}
24/ 19 (6}
56/26
51
Notes:
1.
2.
3. 4. 5. 6. 7. Diameter of largest segment.
MAOP based on 49 CFR 192.619.
no 14 = PHMSA Final Report Derivation of Potential Impact Radius
Formulae for Vapor Cloud Dispersion Subject to 49 CFR 192.
(rural cond!t!c:1$/ urb;:m conditions}
PIR Coefficient for natural gas is 0.69 (49 CFR 192.903}.
PIR Coefficient for hydrogen is 0.47 (TTO 13 - CFER Other Gasses Report).
Calculated based on no 14 protocol.
Rounded up to nearest foot. PIR= PIR coefficient*(square root of (p* d2))
Reauest
Olin hereby requests permission to use the PIR factor published by PHMSA in TT0-13 for
hydrogen, the urban setting PIR for chlorine published in TT0-14, and the TT0-14 protocol to
calculate the PIR factor for the urban setting for anhydrous HCL. The resulting Pl Rs will be used
to identify Part 192 High Consequence Areas using 49 CFR §192.903, Method 2.

<<<PAGE 6>>>

G2 lntl'grated Solution~
Page .J of 4
Please note that, under 49 CFR §190.9, the RRC must provide the Associate Administrator for
Pipeline Safety (Alan Mayberry) a written recommendation as to the disposition of this request for
finding. If PHMSA does not reverse or modify the RRC's recommendation within 10 business
days of its receipt, the RRC's recommendation shall constitute PHMSA's decision.
Closing
Olin maintains all its lines to OSHA PSM standards. Where the pipeline safety regulations (49
CFR Parts 190 -199) impose different or additional requirements, Olin complies with those
different or additional requirements as well. The PIRs proposed above are consistent with the
best available scientific data currently available and, at least in my opinion, consistent with the
goal of providing reasonable protection of both human health and the environment and the
integrity of the lines themselves as authorized and required by the pipeline safety statutes (49
USC §60101 et.seq.), the pipeline safety regulations (49 CFR Parts 190 -199) and the Texas
Administrative Code (16 TAC Chapter 8).
Your prompt consideration of this request would be very much appreciated.
Please do not hesitate to contact the undersigned should you have any questions (cell 832-71 2-
3098, e-mail john.jacobi@g2-is.com).
CF: Terry Fassnidge (Olin)
Randal Anderson (Olin)

## Provenance

- Official: Yes
- Source: <https://www.phmsa.dot.gov/sites/phmsa.dot.gov/files/docs/standards-rulemaking/pipeline/interpretations/56666/olin-pi-17-0017-12-07-2017-part-192903.pdf>
- Source ID: `phmsa`
- SHA-256: `871fb4816a1d725e2b3e09712b9f6c801cb5ad1e37cbd55c363189122dd0bc0f`
- Retrieved: 2026-08-20T00:59:31.977Z
- Exported: 2026-08-22T05:26:19.937Z
- Document slug: `phmsa-interpretation-pi-17-0017`

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