# DIXIE PIPELINE COMPANY LLC — Notice of Probable Violation

**Citation:** CPF 220085003  
**Type / status:** enforcement / historical  
**Agency:** Pipeline and Hazardous Materials Safety Administration  
**Effective:** Not stated  
**Published:** 2008-02-19

CLOSED notice of probable violation citing 195.406(a).

## Document text

Notice of Probable Violation involving DIXIE PIPELINE COMPANY LLC. PHMSA's enforcement data identifies the cited regulation as 195.406(a). The case was opened on 2008-02-19 and is reported as closed as of 2011-01-07. Open the official case record for notices, responses, orders, and the latest status.

Official case documents:

220085003_closure letter_01072011.pdf: https://primis.phmsa.dot.gov/enforcement-documents/220085003/220085003_closure%20letter_01072011.pdf

220085003_closure letter_01072011_text.pdf: https://primis.phmsa.dot.gov/enforcement-documents/220085003/220085003_closure%20letter_01072011_text.pdf

220085003_Final Order_09152010.pdf: https://primis.phmsa.dot.gov/enforcement-documents/220085003/220085003_Final%20Order_09152010.pdf

220085003_Final Order_09152010_text.pdf: https://primis.phmsa.dot.gov/enforcement-documents/220085003/220085003_Final%20Order_09152010_text.pdf

220085003_nopv letter_02192008.pdf: https://primis.phmsa.dot.gov/enforcement-documents/220085003/220085003_nopv%20letter_02192008.pdf

220085003_nopv letter_02192008_text.pdf: https://primis.phmsa.dot.gov/enforcement-documents/220085003/220085003_nopv%20letter_02192008_text.pdf

220085003_operator response_11192008.pdf: https://primis.phmsa.dot.gov/enforcement-documents/220085003/220085003_operator%20response_11192008.pdf

220085003_closure letter_01072011_text.pdf

CERTIFIED MAIL - RETURN RECEIPT REQUESTED
January 7, 2011
Mr. James M. Collingsworth
President
Dixie Pipeline Company
1100 Louisiana Street
Houston, Texas 77002-5227
CPF 2-2008-5003
Dear Mr. Collingsworth:
A failure occurred on the Dixie Pipeline Company (Dixie) propane pipeline in Carmichael,
Mississippi on November 1, 2007. The Pipeline and Hazardous Materials Safety
Administration (PHMSA) initiated an investigation of the accident and inspection of the
records involving the pipeline system pursuant to Section 60117 of Title 49, United States
Code.
As a result of the investigation and inspection, PHMSA issued a Final Order to Dixie on
September 15, 2010. The Final Order included a Compliance Order (CO), which required
Dixie to take certain actions to protect the public and the environment.
The PHMSA Southern Region has reviewed your written responses to CO and we find that
you have met the requirements specified in the CO. No further action is necessary with
regards to the Final Order and this case is now closed.
Please be advised that nothing herein state or implies that Dixie's pipeline system is in
compliance with the federal pipeline safety regulations. The pipeline system remains subject
to inspection by PHMSA.
Sincerely,
Wayne T. Lemoi
Director, Office of Pipeline Safety
PHMSA Southern Region

220085003_Final Order_09152010_text.pdf

SEP 15 2010
Mr. Jim Collingsworth
President
Dixie Pipeline Company
1100 Louisiana Street
Houston, Texas 77002-5227
RE: CPF No. 2-2008-5003
Dear Mr. Collingsworth:
Enclosed please find the Final Order issued in the above-referenced case. It makes findings of
violation and specifies actions that need to be taken by Dixie Pipeline Company to comply with
the pipeline safety regulations. When the terms of the compliance order have been completed, as
determined by the Director, Southern Region, this enforcement action will be closed. Service of
the Final Order by certified mail is deemed effective upon the date of mailing, or as otherwise
provided under 49 C.F.R. § 190.5.
Thank you for your cooperation in this matter.
Sincerely,
Jeffrey D. Wiese
Associate Administrator
for Pipeline Safety
Enclosure
cc: Mr. Wayne Lemoi, Director, Southern Region, PHMSA
CERTIFIED MAIL - RETURN RECEIPT REQUESTED[7009 1410 0000 2472 2834]



U.S. DEPARTMENT OF TRANSPORTATION
PIPELINE AND HAZARDOUS MATERIALS SAFETY ADMINISTRATION
OFFICE OF PIPELINE SAFETY
WASHINGTON, D.C. 20590
____________________________________
In the Matter of )
)
DIXIE PIPELINE COMPANY, ) CPF No. 2-2008-5003
)
Respondent. )
____________________________________)
FINAL ORDER
On November 1-7, 2007, pursuant to 49 U.S.C. § 60117, a representative of the Pipeline and
Hazardous Materials Safety Administration (PHMSA), Office of Pipeline Safety (OPS), initiated
an investigation of an accident and inspection of the records involving the pipeline system of
Dixie Pipeline Company (Respondent) in Roswell, Georgia; Carmichael, Mississippi; and
Meridian, Mississippi. Dixie Pipeline Company is a subsidiary of Enterprise Products
Operating, LLC. Dixie Pipeline Company transports propane to customers in the southeastern
United States.
As a result of the investigation, the Director, Southern Region, OPS, issued to Respondent, by
letter dated February 19, 2008, a Notice of Probable Violation and Proposed Compliance Order
(Notice). In accordance with 49 C.F.R. §190.207, the Notice proposed finding that Respondent
violated 49 C.F.R. §§195.402 (a) and 195.406(a)(2-3). The Notice also proposed ordering
Respondent to take certain measures to correct the alleged violation.
In a letter dated March 21, 2008, Respondent requested an extension of time to respond to the
Notice. Respondent was granted an extension until May 1, 2008 to respond to the Notice.
Respondent responded to the Notice by letter dated May 1, 2008 (Response). Respondent
contested the allegation of violation, submitted documentation regarding the design pressure
rating of the valves and stated that it was reviewing its maximum operating pressure.
Respondent did not request a hearing, and therefore has waived its right to one.
FINDING OF VIOLATION



Item 1: The Notice alleged that Respondent violated 49 C.F.R. §§195.402 (a) and 195.406(a)
(2-3), which state, in relevant part:
§ 195.402 Procedural manual for operations, maintenance, and
Emergencies.
(a) General. Each operator shall prepare and follow for each
pipeline system a manual of written procedures for conducting normal
operations and maintenance activities and handling abnormal operations
and emergencies. This manual shall be reviewed at intervals not exceeding
15 months, but at least once each calendar year, and appropriate changes
made as necessary to insure that the manual is effective. This manual
shall be prepared before initial operations of a pipeline system commence,
and appropriate parts shall be kept at locations where operations and
maintenance activities are conducted.
§ 195.406 Maximum operating pressure.
(a) Except for surge pressures and other variations from normal
operations, no operator may operate a pipeline at a pressure that exceeds
any of the following: . . .
(2) The design pressure of any other component of the pipeline.
(3) Eighty percent of the test pressure for any part of the pipeline
which has been pressure tested under Subpart E of this part.
The Notice alleged that Respondent did not follow its procedural manual in establishing
Maximum Operating Pressures (MOPs) for several pipeline segments. Specifically, the Notice
alleged that Respondent failed to follow Procedure IX-005,
1 which requires that the MOP not
exceed the design pressure rating of components, by establishing MOPs above the design
that Respondent failed to follow its procedures by establishing Engineering Calculated MOPs
pressure rating of installed ANSI-600 valves. The Notice and Violation Report2 further alleged
that exceeded the design pressure rating of 1,440 psi for installed ANSI-600 valves at the pump
stations shown below.
Pump Station or Pipeline
Segment
Listed Engineering
Calculated MOP
Listed Qualified
Section MOP
Component
Design Pressure
Oloh Station 1465 psi 1440 psi
Hattiesburg Station 1454 psi 1440 psi
Carmichael Station 1448 psi 1440 psi
8” and 6” Pipeline Segments -
Milner to Apex
1480 psi Between 1445 psi
and 1509 psi
1440 psi
1 Dixie Pipeline Company, Operations & Emergency Manual, Maximum Operating Pressure Procedure, Rev. No:1,
Item No: IX-005; Dated 06/02, pages 1-2. (Violation Report, Exhibit A, page 5.)
2 Violation Report, Exhibit A, page 5.



2
In response to the Notice, Respondent argued that the MOPs on its pipeline system were
developed in accordance with the MOP procedures from its previous Operations & Emergency
(O&E) Manual and complied with the regulatory requirement not to exceed the design pressure
rating of a component. Respondent explained that the portion of its “Maximum Operating
Pressure Procedure” that appeared to be in question was the language stating the MOP will not
exceed the “design pressure rating of a component.
”3 Respondent suggested that the component
design pressure noted in the Notice came from discussions between PHMSA and Respondent
and acknowledged that the manufacturer’s pressure rating for the original 1963 construction
ANSI-600 valves in its pipeline system may have been 1,440 psig. However, Respondent posed
that a regulatory interpretation of § 195.406 issued by the Research and Special Programs
Administration (RSPA),
manufacturer’s pressure rating or 80 percent of its actual or prototype factory test pressure in
determining the design pressure rating of a component.
4 dated June 17, 1981, provided operators with the flexibility to use the
First, Respondent argued that it was in compliance because it established MOPs in accordance
with its MOP procedures from its previous O&E Manual and an agency interpretation.
Respondent cited the interpretation to support its position that operators had the flexibility to
utilize the manufacturer’s pressure rating or 80 percent of its actual or prototype factory test
pressure in determining the design pressure rating of a component. Respondent cited the text
from two answers in the regulatory interpretation to assert that OPS determined that the operator
could use the manufacturer’s pressure rating or 80 percent of the test pressure as the design
pressure of the valves.
The Notice did not allege, however, that the procedure failed to comply with the regulations. The
issue is whether the Respondent followed the procedure that was in place at the time of the
inspection. The regulatory interpretation Respondent refers to does clarify the requirement that
operators not exceed the design pressures of pipeline components in order to satisfy §195.406.
The interpretation also clarifies that operators are allowed to establish the design pressure for
components using the manufacturer’s pressure rating and consensus standards or their own
independent design pressure using equally sound principles and for these individually added or
replaced valves, they may be operated at 80 percent of the actual or factory test pressure,
provided the pressure does not exceed any of the other three criteria in § 195.406, which includes
the design pressure of the component.
Second, Respondent’s Procedure IX-0055
requires that the MOP not exceed the design ppressure
rating of components. The ANSI-600 valve 1,440 psi design pressure cited in the Notice is
3 Dixie Pipeline Company, Operations & Emergency Manual, Maximum Operating Pressure Procedure, Rev. No:1,
Item No: IX-005; Dated 06/02, pages 1-2. (Violation Report, Exhibit A, page 5.)
4 The Research and Special Programs Administration is a predecessor agency. Effective February 20, 2005, the
Pipeline and Hazardous Materials Safety Administration (PHMSA) was created to further the highest degree of
safety in pipeline transportation and hazardous materials transportation. See, section 108 of the Norman Y. Mineta
Research and Special Programs Improvement Act (Public Law 108-426, 118 Stat. 2423-2429 (November 30,
2004)). See also, 70 Fed. Reg. 8299 (February 18, 2005) redelegating the pipeline safety functions to the
Administrator, PHMSA.
5Dixie Pipeline Company, Operations & Emergency Manual, Maximum Operating Pressure Procedure, Rev. No:1,



3
based on information relating to established valve design pressures6 submitted by Respondent to
PHMSA, prior to issuance of the Notice. At the time of the inspection, Respondent advised
PHMSA that the design pressure for the subject valves was 1,440 psig.
Respondent acknowledged that the manufacturer’s pressure rating for the subject valves was
1,440 psig. According to OPS, Respondent established Engineering Calculated MOPs that
exceeded the design pressure rating of 1,440 psi for installed ANSI-600 valves at three pump
stations and one pipeline segment.
7 In its Response,
After considering all the evidence, I find that Respondent violated 49 C.F.R § §195.402 (a) and
195.406(a)(2-3) by failing to follow its procedures for establishing MOPs that do not exceed the
design pressure rating of components and by establishing MOPs that exceeded the design
pressure rating of 1,440 psi for installed ANSI-600 valves at the three cited pump stations and
one pipeline segment. Pursuant to 49 C.F.R. §195.402(a), operators are required to follow for
each pipeline system a manual of written procedures for conducting normal operations and
maintenance activities and handling abnormal operations and emergencies. Improper
determination of the MOP could impact safety by pressuring the line beyond the limits
established by pipeline safety regulations.
This finding of violation will be considered a prior offense in any subsequent enforcement action
taken against Respondent.
COMPLIANCE ORDER
The Notice proposed a compliance order with respect to the violation of 49 C.F.R. §§195.402(a)
and 195.406(a)(2-3).
Under 49 U.S.C. § 60118(a), each person who engages in the transportation of hazardous liquids
or who owns or operates a pipeline facility is required to comply with the applicable safety
standards established under chapter 601. Pursuant to the authority of 49 U.S.C. § 60118(b) and
49 C.F.R. §190.217, Respondent is ordered to take the following actions to ensure compliance
with the pipeline safety regulations applicable to its operations:
1. With respect to the violation of §§195.402(a) and 195.406(a)(2-3), Respondent must
submit the design pressure rating for the ANSI-600 valves and the method used to
establish the design pressure rating.
2. Within 30 days after receipt of this Final Order, submit procedures and
documentation to demonstrate completion of Item 1, to the Director, OPS, Southern
Item No: IX-005; Dated 06/02, pages 1-2. (Violation Report, Exhibit A, page 5.)
6 See Violation Report at Exhibit C, copies of related e-mails dated December 20, 2007; January 3, 2008; January
18, 2008; January 21, 2008; and January 22, 2008.
7 Violation Report, Exhibit C, Email from Respondent to PHMSA dated January 3, 2008.



4
Region, Pipeline and Hazardous Materials Safety Administration, 233 Peachtree
Street, Suite 600, Atlanta, GA 30303.
The Director may grant an extension of time to comply with any of the required items upon a
written request timely submitted by the Respondent demonstrating good cause for an extension.
Failure to comply with this Order may result in administrative assessment of civil penalties not
to exceed $100,000 for each violation for each day the violation continues or in referral to the
Attorney General for appropriate relief in a district court of the United States.
Under 49 C.F.R. §190.215, Respondent has a right to submit a Petition for Reconsideration of
this Final Order. The petition must be sent to: Associate Administrator, Office of Pipeline
Safety, PHMSA, 1200 New Jersey Avenue, SE, East Building, 2nd Floor, Washington, DC
20590, with a copy sent to the Office of Chief Counsel, PHMSA, at the same address. PHMSA
will accept petitions received no later than 20 days after receipt of service of this Final Order by
the Respondent, provided they contain a brief statement of the issue(s) and meet all other
requirements of 49 C.F.R. § 190.215. Unless the Associate Administrator, upon request, grants a
stay, the terms and conditions of this Final Order are effective upon service in accordance with
49 C.F.R. § 190.5.
___________________________________ __________________________
Jeffrey D. Wiese Date Issued
Associate Administrator
for Pipeline Safety

## Provenance

- Official: Yes
- Source: <https://primis.phmsa.dot.gov/enforcement-data/case/220085003>
- Source ID: `phmsa-enforcement`
- SHA-256: `f37a2fa0b2310018cf2ede4230d32db5d3075557e9a7f33cf064d5bdd5958f6d`
- Retrieved: 2026-08-20T04:44:44.458Z
- Exported: 2026-08-23T06:34:35.001Z
- Document slug: `phmsa-enforcement-220085003`

### Source metadata

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  "cpf": "220085003",
  "operator": "DIXIE PIPELINE COMPANY LLC",
  "region": "Southern",
  "pipelineType": "INTERSTATE LIQUID ONSHORE",
  "caseStatus": "CLOSED",
  "citedSections": [
    "195.406(a)"
  ],
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