Magellan Pipeline
Product Specifications
Version 94
January 06, 2015
QUALITY CONTROL CONTACTS
Rod Lawrence, Manager, Quality Control
Office:
(918) 574-7286
Cell:
(816) 805-3334
Jerry Higgins, Product Quality Program Consultant
Office:
(918) 574-7485
Cell:
(918) 760-4130
Brian Topping, Manager, Quality Assurance and Analytical Services
Office:
(918) 574-7381
Cell:
(918) 724-0342
Jim Boos, Supervisor, Quality Control
Office:
(918) 574-7539
Cell:
(918) 671-3142
Marcia Eckhoff, Quality Control Program Coordinator
Office:
(515) 276-0169
Cell:
(515) 710-5146
Bryan Middendorf, Quality Control Specialist Sr.
Office:
(913) 827-7489
Cell:
(913) 827-7489
Jimmy Gillman, Quality Control Specialist Sr.
Office:
(918) 884-8514
Cell:
(918) 884-8514
Caleb Guse, Quality Control Specialist Sr.
Office:
(918) 260-6712
Cell:
(918) 260-6712
Katie Stubbs, Quality Control Specialist Sr.
Office:
(918) 310-7735
Cell:
(913) 620-4114
Revision Date: August 13, 2014
PRODUCT ACCEPTANCE TERMS
The most current version of the methods referenced in these
specifications will prevail at all times. Alternate test methods
listed in ASTM, MPL product specification standards may be
used. In instances of dispute, tests will be conducted using the
referee methods identified in the applicable standard.
Sampling
LPG products must be sampled in accordance with D1265. All
other products must be sampled according to D4057, D4177,
and/or D5842.
Compliance with Magellan Pipeline Specifications will be
determined by the shipper’s analysis of a composite sample
produced in accordance with D5854. Top, middle, and bottom
samples may not deviate more than 1.0° API from the gravity
of the composite, nor contain product below the flash point
minimum for oils, or above the seasonal RVP maximum for
gasolines.
Reporting
It is the responsibility of the shipper to enter a certificate of
analysis representative of each shipment into Magellan’s
Prospector database for approval.
Tests performed by the carrier are for carrier's information and
do not relieve the shipper of the responsibility to comply with
the specifications.
The carrier reserves the right to sample the product and/or tank
water below any product proffered for shipment.
Workmanship
Products must be clear and bright, and free of sediment. Any
undissolved water received with incoming product may be
deducted from the shipment volume ticketed. Additionally,
Magellan may request for the shipper to remove the water
received, and/or invoice the shipper for water disposal and
other costs incurred.
Revision Date: June 29, 2009
PRODUCT ACCEPTANCE TERMS
Delivery test results may deviate by the amount of the
reproducibility of the test method.
Shipments of proprietary grades must comply with corrosion
inhibitor requirements for the applicable product grade.
Revision Date: June 29, 2009
MAGELLAN PIPELINE ADDITIVE SPECIFICATIONS
Magellan will permit the types and concentrations of additives detailed below; all other types and
concentrations or additives are prohibited.
Gasoline Additive Specifications
The following additive specifications apply to all grades except
aviation products, LPG’s, and Natural Gasoline, for the grades
noted in each section.
(H, I, J8, L, Q, and W Grade)
Gum Inhibitors and Metal
Deactivators
Gasoline shipments may, but are not required to, contain any of
the following gum inhibitors and/or metal deactivators:
N, N'di-secondary butyl ortho-phenylenediamine
N, N'di-secondary butyl para-phenylenediamine
N, N'disalicylidene-1,2 propanediamine
N, N'di(1-ethyl-3-methylpentyl)-para-phnylenediamine
N, N'di-isopropyl-para-phenylenediamine
N, n'bis-(1, 4-demethylpentyl)-p-phenylenediamine n-Butyl para-aminophenol
2-6-di-tert-butylphenol
2,4,6-tri-tert-butylphenol
Ortho-tert-butylphenol
UOP 12P
UOP 3455
Innospec AO-36
Ethanox 4776
Tolad 3905
Nalco 88BU-118
Tolad 4695
UOP 12S
UOP 5S
Innospec AO-37
Ethanox 4720
Tolad 3910
Unichem 7529
UOP 17P
Innospec AO-31
Ethyl 733
Ethanox 4740
Specaid 8Q202
Pitt-Consol M-56
Specaid 8Q206
Revision Date: October 22, 2014
Gasoline, Fuel Oil and Diesel Fuel Additive
Corrosion Inhibitors
Products requiring compliance with NACE standard TM0172 may
contain any of the following corrosion inhibitors:
Nalco 5403
Nalco Visco 3554
Apollo PRI-19
UOP Unicor
Innospec DCI-6A
Tolad 245
HiTech 580
Nalco EC5407A
Nalco 5405
Lubrizol 541
Innospec DCI-4A
UOP Unicor J
Hitec E-534
Tolad 4410
Spec-Aid 8Q5127
Baypros 853
UOP Unicor PL
Unichem 7504
Tolad 249
Unichem 7501
Tolad 9715
Tolad 9719
Spec-Aid 8Q123ULS
Spec-Aid 8Q110ULS
Fuel Oil and Diesel Fuel
Additives
Stability
Fuel oil and/or diesel fuel shipments may contain one or more of the
following stability additives as required to achieve compliance with
the stability characteristics outlined in the applicable grade
specification.
Innospec FOA-3
UOP Polyflo-121
UOP Polyflo-122
UOP Polyflo-128
Tolad 9022
Chemtec 7220
Spec-Aid 8Q403ULS
Tolad 9076
Unichem 7530
Spec-Aid 8Q401
Specaid 8Q72
Nalco 5303
Nalco 5301
UOP Polyflo-195
Revision Date: October 22, 2014
Cold Flow Additives
Fuel oil and/or diesel fuel shipments requiring additives to achieve
compliance with low temperature properties may, but are not
required to contain one or more of the following pour point
depressant additives:
Hitec 4541
Innospec 2152
Betz Q5201
Hitec 4518
Exxon ECA 7305
UOP Polyflo 6000
Dyes
Innospec PDD-7450
Spec-Aid 8Q5201
Paradyne 25
Unichem 8094
Nalco 5375
Spec-Aid 8Q72ULS
Tolad 3005
Tolad 3030
Betz 8Q12
Hitec 4566
Spec-Aid 8Q14ULS
X5 Grade High Sulfur Fuel Oil is the only product in Magellan
Pipeline that requires dye at the origin. Applicable dyes and
required treat rates are listed in the X5 grade product specifications.
XR Grade Low Sulfur Fuel Oil is dyed at the Magellan rack.
Revision Date: October 22, 2014
Seasonal Gasoline Volatility Classes
Shipments From Origin
Reid Vapor Pressure, D5191 1/
March 1 - September 15
DVPE using EPA formula 2/
September 16 – February 28 DVPE using D5191 formula
Distillation, ASTM D 86 3/
10% Evaporated F, max
50% Evaporated F, min
50% Evaporated F, max
90% Evaporated F, max
Final Boiling Point F, max 4/
Residue, vol % max
Driveability Index, D4814, max 3/
Class AA Class A
158
158
170
170
250
250
374
374
430
430
2
2
Class B Class C
149
140
170
170
245
240
374
365
430
430
2
2
1250
1250
1240
Vapor to Liquid Ratio=20:1, F 3,5/ Class 1
D5188, min
140
Class 2
133
Class 3
124
Class D
131
170
235
365
430
2
Class E
122
170
230
365
430
2
1230
1220
1200
Class 4
116
Class 5
105
1/
All gasoline deliveries will not exceed applicable Federal and State requirements.
2/
The calculation required for the EPA compliance period is published in 40 CFR 80.46.
3/
Specifications must be met before blending with denatured fuel ethanol.
4/
The final boiling point of all gasoline deliveries at terminals will be at or below 437 °F as
determined by ASTM D86
5/
D5188 is the referee test method. The alternative equations in D4814
may also be used.
Revision Date: October 22, 2014
Schedule of Origin Volatility Requirements
A GRADE
Colorado
DVPE)
(Class)
Kansas
(DVPE)
(Class)
Illinois
(DVPE)
(Class)
Minnesota
(DVPE)
(Class)
N. Dakota
(DVPE)
(Class)
Oklahoma
(DVPE)
(Class)
Texas
(DVPE)
(Class)
Wisconsin
(DVPE)
(Class)
Wyoming
(DVPE)
(Class)
Jan.
1-15
Jan. Feb. Feb. Mar. Apr.
16-31 1-15 16-29 1-31 1-30
May
1-31
June July
1-30 1-31
Aug. Sept. Sept. Oct.
1-31 1-15 16-30 1-31
Nov.
1-30
Dec.
1-31
15.0
E-5
15.0
E-5
13.5
D-5
13.5
D-5
11.5
C-3
9.0
A-3
9.0
A-3
9.0
A-2
9.0
A-2
9.0
A-2
9.0
A-2
10.0
B-2
11.5
C-3
13.5
D-4
15.0
E-5
13.5
D-5
13.5
D-5
10.0
B-5
10.0
B-5
8.5
A-4
8.5
A-3
9.0
A-3
9.0
A-2
9.0
A-2
9.0
A-2
9.0
A-2
10.0
B-2
11.5
C-3
13.5
D-4
15.0
E-5
13.5
D-5
13.5
D-5
10.0
B-5
10.0
B-5
8.5
A-5
8.5
A-4
9.0
A-4
9.0
A-3
9.0
A-3
9.0
A-3
9.0
A-3
11.5
C-3
13.5
D-4
15.0
E-5
15.0
E-5
13.5
D-5
13.5
D-5
10.0
B-5
10.0
B-5
8.5
A-5
8.5
A-4
9.0
A-4
9.0
A-3
9.0
A-3
9.0
A-3
9.0
A-3
11.5
C-3
13.5
D-4
15.0
E-5
15.0
E-5
13.5
D-5
13.5
D-5
10.0
B-5
10.0
B-5
8.5
A-5
8.5
A-4
9.0
A-4
9.0
A-3
9.0
A-2
9.0
A-2
9.0
A-3
11.5
C-3
13.5
D-4
15.0
E-5
15.0
E-5
13.5
D-5
13.5
D-5
10.0
B-4
10.0
B-4
8.5
A-4
8.5
A-3
9.0
A-3
9.0
A-2
9.0
A-2
9.0
A-2
9.0
A-2
10.0
B-2
11.5
C-3
13.5
D-4
15.0
E-5
13.5
D-4
13.5
C-4
10.0
B-4
10.0
B-4
9.0
A-4
9.0
A-3
9.0
A-3
9.0
A-2
9.0
A-2
9.0
A-2
9.0
A-2
10.0
A-2
11.5
C-3
13.5
D-4
13.5
D-4
13.5
D-5
13.5
D-5
10.0
B-5
10.0
B-5
8.5
A-5
8.5
A-4
9.0
A-4
9.0
A-3
9.0
A-3
9.0
A-3
9.0
A-3
11.5
C-3
13.5
D-4
15.0
E-5
15.0
E-5
15.0
E-5
15.0
E-5
13.5
D-5
13.5
D-5
11.50 9.0
C-3
A-3
9.0
A-3
9.0
A-2
9.0
A-2
9.0
A-2
9.0
A-2
10.0
B-2
11.5
C-3
13.5
D-4
13.5
E-5
NOTE:
Gulf Coast origin changeover dates will precede this schedule by approximately 10 days, depending upon the applicable Explorer Pipeline cycle. Shipments via Explorer Pipeline must meet the specification
applicable to the anticipated West Tulsa delivery date. Gulf Coast shippers will be advised of these dates through seasonal letters.
Revision Date: December 22, 2014
Schedule of Origin Volatility Requirements
A1 GRADE
Jan.
1-15
(DVPE)
(Class)
N/A
Jan. Feb. Feb. Mar. Apr.
16-31 1-15 16-29 1-31 1-30
May
1-31
June July
1-30 1-31
Aug. Sept. Sept. Oct.
1-31 1-15 16-30 1-31
Nov.
1-30
Dec.
1-31
N/A
6.8
A-3
6.8
A-2
6.8
A-2
N/A
N/A
N/A
N/A
N/A
6.8
A-3
6.8
A-2
6.8
A-2
N/A
N/A
NOTE: Gulf Coast origin changeover dates will precede this schedule by approximately 10 days, depending upon the applicable Explorer Pipeline
cycle. Shipments via Explorer Pipeline must meet the specification applicable to the anticipated West Tulsa delivery date. Gulf Coast shippers will be
advised of these dates through seasonal letters.
Revision Date: December 22, 2014
Schedule of Origin Volatility Requirements
South System El Paso Deliveries
A1X GRADE
Jan.
1-31
11.50
C-3
Feb.
1-29
10.00
B-2
Mar.
1-31
9.0
B-2
Apr.
1-15
9.0
B-2
Apr.
16-30
9.0
B-2
May.
1-31
9.00
A-1
June.
1-30
9.00
A-1
July.
1-31
9.00
A-1
Aug.
1-31
9.00
A-1
Sept.
1-15
9.0
B-2
Sept.
16-30
10.00
B-2
Oct. Nov. Dec.
1-30 1-30 1-31
11.50 11.50 11.50
C-3
C-3
C-3
Revision Date: December 22, 2014
Schedule of Origin Volatility Requirements
A5 GRADE
Jan. Feb. Mar.
1-31 1-28 1-30
15.00 13.50 11.50
E-5
D-5 C-3
Apr.
1-30
9.0
A-3
May
1-31
9.0
A-3
June
1-30
9.0
A-2
July
1-31
9.0
A-2
Aug.
1-31
9.0
A-2
Sept.
1-15
9.0
A-2
Sept
16-30
10.00
B-2
Oct.
1-30
11.50
C-3
Nov.
1-31
13.5
D-4
Dec.
1-31
15.00
E-5
Revision Date: August 13, 2014
Schedule of Origin Volatility Requirements
AMS Grade
Colorado
(DVPE)
Jan.
1-31
N/A
Feb.
1-28
N/A
Mar.
1-15
N/A
Mar. Apr. May.
16-31 1-30 1-31
N/A
7.8
7.8
A3
A3
June. July.
1-30 1-31
7.8
7.8
A2
A2
N/A
N/A
N/A
7.8
A-3
7.8
A-3
7.8
A-3
7.8
A-2
N/A
N/A
N/A
7.8
A-3
7.8
A-3
7.8
A-3
7.8
A-2
N/A
N/A
N/A
N/A
7.8
A-3
7.8
A-2
(CLASS)
Aug.
1-31
7.8
A2
Sept. Sept. Oct. Nov.
1-15 16-30 1-31 1-30
7.8
N/A N/A N/A
A-2
Dec.
1-31
N/A
Kansas
(DVPE)
(CLASS)
7.8
A-2
7.8
A-2
7.8
A-2
N/A
N/A
7.8
A-2
7.8
A-2
N/A
7.8
A-2
7.8
A-2
N/A
N/A
N/A
N/A
N/A
Texas
(DVPE)
(Class)
7.8
A-2
N/A
Wyoming
(DVPE)
(Class)
7.8
A-3
7.8
A-2
N/A
N/A
N/A
Revision Date: August 13, 2014
Schedule of Origin Volatility Requirements
AR Grade
Texas
(DVPE)
(CLASS)
Jan. Feb.
1-31 1-20
13.5 13.5
D-4 D-4
Feb.
21-28
11.5
D-4
Mar. Mar. Apr. May. June. July.
1-20 21-31 1-30 1-31 1-30 1-31
9.0
Report Report Report Report Report
A-3 A-3 A-3 A-3 A-3 A-2
Aug. Sept.
1-31 1-15
Report Report
A-2 A-2
Sept.
16-30
10.0
B-2
Oct. Nov. Dec.
1-31 1-30 1-31
11.5 13.5 13.5
C-3
D-4 D-4
NR Grade
Texas
(DVPE)
(CLASS)
Oklahoma
(DVPE)
(Class)
Jan. Feb. Feb. Mar.
1-31 1-20 21-29 1-20
13.5 13.5 13.5 13.5
D-4 D-4 D-4 D-4
Jan.
1-20
15.0
E-5
Jan.
21-31
13.5
D-4
Mar. Apr.
21-31 1-30
Report Report
A-3 A-3
May. June. July.
1-31 1-30 1-31
Report Report Report
A-3 A-3 A-2
Feb. Feb. Feb. Mar. Mar Apr.
1-10 11-29 20-28 1-10 11-30 1-30
13.5 11.5 9.0
9.0 Report Report
D-4 C-3 A-3 A-3 A-3
A-3
May.
1-31
Report
A-3
Aug. Sept. Sept.
1-31 1-15 16-30
Report Report 10.0
A-2 A-2 B-2
June.
1-30
Report
A-2
Oct.
1-31
11.5
C-3
Nov.
1-30
13.5
D-4
Dec.
1-31
13.5
D-4
July. Aug. Sept. Sept. Oct. Nov. Nov. Dec.
1-31 1-31 1-15 16-30 1-31 1-20 21-31 1-31
Report Report Report 11.5 13.5 13.5 15.0 15.0
A-2 A-2
A-2 C-3 D-4 D-4 E-5 E-5
Revision Date: August 13, 2014
Schedule of Origin Volatility Requirements
South System El Paso Deliveries
NEP Grade
Jan.
1-24
11.50
C-3
Jan.
25-31
10.00
B-2
Feb.
1-29
10.00
B-2
Mar.
1-31
10.00
B-2
Apr.
1-15
10.00
B-2
Apr.
16-30
9.00
A-1
May
1-31
9.00
A-1
June
1-30
9.00
A-1
July
1-31
9.00
A-1
Aug.
1-31
10.00
B-2
Sept.
1-30
10.00
B-2
Oct.
1-31
11.50
C-3
Nov.
1-30
11.50
C-3
Dec.
1-31
11.50
C-3
Revision Date: September 17, 2013
Schedule of Origin Volatility Requirements
NOTE: Gulf Coast origin changeover dates will precede this schedule by approximately 10 days, depending upon the applicable Explorer Pipeline
cycle. Shipments via Explorer Pipeline must meet the specification applicable to the anticipated West Tulsa delivery date. Gulf Coast shippers will be
advised of these dates through seasonal letters.
V GRADE
Jan. Jan. Feb. Feb. Mar. Apr. May June July Aug. Sept. Sept. Oct. Nov. Dec.
1-15 16-31 1-15 16-29 1-31 1-30 1-31 1-30 1-31 1-31 1-15 16-30 1-31 1-30 1-31
Kansas
(DVPE)
(CLASS)
Illinois
(DVPE)
(CLASS)
Minnesota,
N. Dakota, Wis
(CLASS)
Oklahoma
(DVPE)
(DVPE)
(CLASS)
Texas
(DVPE)
(CLASS)
15.0 13.5
E-5 D-5
13.5
D-5
13.5
D-5
8.5
A-4
8.5
A-3
9.0
A-3
9.0
A-2
9.0
A-2
9.0
A-2
9.0
A-2
10.0
B-2
11.5
C-3
13.5
D-4
15.0
E-5
15.0 13.5
E-5 D-5
13.5
D-5
13.5
D-5
8.5
A-5
8.5
A-4
9.0
A-4
9.0
A-3
9.0
A-3
9.0
A-3
9.0
A-3
11.5
C-3
13.5
D-4
15.0
E-5
15.0
E-5
15.0
E-5
15.0
E-5
13.5
D-5
13.5
D-5
8.5
A-5
8.5
A-4
9.0
A-4
9.0
A-3
9.0
A-3
9.0
A-3
9.0
A-3
11.5
C-3
13.5
D-4
15.0
E-5
15.0
E-5
15.0 13.5
E-5 D-5
13.5
D-4
13.5
D-4
8.5
A-4
8.5
A-3
9.0
A-3
9.0
A-2
9.0
A-2
9.0
A-2
9.0
A-2
10.0
B-2
11.5
C-3
13.5
D-4
15.0
E-5
13.5 13.5
D-5 D-5
13.5
D-4
11.5
C-4
9.0
A-4
9.0
A-3
9.0
A-3
9.0
A-2
9.0
A-2
9.0
A-2
9.0
A-2
10.0
B-2
11.5
C-3
13.5
D-4
13.5
D-5
Revision Date: January 04, 2015
Schedule of Origin Volatility Requirements
NOTE: Gulf Coast origin changeover dates will precede this schedule by approximately 10 days, depending upon the applicable Explorer Pipeline
cycle. Shipments via Explorer Pipeline must meet the specification applicable to the anticipated West Tulsa delivery date. Gulf Coast shippers will be
advised of these dates through seasonal letters.
V1 GRADE
Colorado
Jan.
1-31
(DVPE) 15.0
(Class) E-5
Feb. Feb. Mar.
1-15 16-28 1-15
15.0 13.5
11.5
D-5
E-5
C-3
Mar.
16-31
11.5
C-3
Apr. May. June. July. Aug. Sept.
1-30 1-31 1-30
1-31 1-31 1-15
9.0
9.0
9.0
9.0
9.0
9.0
A-3 A-3
A-2
A-2
A-2
A-2
Sept.
16-30
10.0
B-2
Oct. Nov. Dec.
1-31 1-30 1-31
11.5 13.5 15.0
C-3 D-4 E-5
15.0
E-5
13.5
D-5
13.5
D-5
11.5
C-3
N/A
N/A
N/A
10.0
B-2
11.5 13.5
C-3 D-4
15.0
E-5
15.0
E-5
13.5
D-5
13.5
D-5
11.5
C-3
N/A
N/A
N/A
10.0
B-2
11.5
C-3
15.0
E-5
15.0
E-5
15.0
D-5
13.5
E-5
11.5
C-3
11.5
C-3
9.0
A-3
Mar.
1-31
11.5
C-5
Apr.
1-30
9.0
A-4
Kansas
(DVPE)
(Class)
N/A
N/A
N/A
N/A
Texas
(DVPE)
(Class)
N/A
N/A
N/A
N/A
13.5
D-4
Wyoming
(DVPE)
(Class)
9.0
A-3
9.0
A-2
9.0
9.0
A-2 A-2
9.0
A-2
10.0
B-2
11.5
C-3
13.5 15.0
D-4 E-5
V2 GRADE
(DVPE)
(CLASS)
Jan. Feb
1-31 1-29
15.0 15.0
E-5
E-5
May
1-31
9.0
A-4
June
1-30
9.0
A-3
July
1-31
9.0
A-3
Aug.
1-31
9.0
A-3
Sept. Sept. Oct.
1-15 16-31 1-31
9.0
11.5 13.5
A-3 C-3
D-4
Nov.
1-30
15.0
E-5
Dec.
1-31
15.0
E-5
Revision Date: January 04, 2015
Schedule of Origin Volatility Requirements
NOTE: Gulf Coast origin changeover dates will precede this schedule by approximately 10 days, depending upon the applicable Explorer Pipeline
cycle. Shipments via Explorer Pipeline must meet the specification applicable to the anticipated West Tulsa delivery date. Gulf Coast shippers will be
advised of these dates through seasonal letters.
V8 GRADE
Oklahoma
Kansas
Jan.
16-31
(DVPE) 15.0
(CLASS) E-5
Feb.
1-15
13.5
D-4
Feb.
16-29
13.5
D-4
Mar.
1-31
13.5
D-4
Apr.
1-15
11.5
C-3
Apr. May
16-30 1-31
N/A N/A
June July
1-30 1-31
N/A N/A
Aug. Sept. Sept. Oct.
1-31 1-15 16-30 1-31
N/A N/A N/A N/A
Nov.
1-30
N/A
Dec.
1-31
N/A
15.0
(CLASS) E-5
15.0
E-5
15.0
E-5
13.5
D-4
11.5
C-3
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
15.0
E-5
15.0
E-5
13.5
D-4
11.5
C-4
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
Jan. Feb. Feb. Mar. Apr.
1-15 1-15 16-29 1-31 1-30
N/A N/A N/A N/A 6.6
A-3
May
1-31
6.6
A-3
June
1-30
6.6
A-2
July
1-31
6.6
A-2
Aug.
1-31
6.6
A-2
Sept.
1-15
6.6
A-2
Sept. Oct.
16-30 1-31
6.6
N/A
A-2
Nov.
1-30
N/A
Dec.
1-31
N/A
Jan. Feb. Feb. Mar. Apr.
1-15 1-15 16-29 1-31 1-30
N/A N/A N/A N/A 6.8
A-3
May
1-31
6.8
A-2
June
1-30
6.8
A-2
July
1-31
6.8
A-2
Aug.
1-31
6.8
A-2
Sept. Sept. Oct.
1-15 16-30 1-31
6.8
N/A N/A
A-2
Nov.
1-30
N/A
Dec.
1-31
N/A
Jan.
1-31
13.5
D-4
Mar.
16-31
6.6
A-3
Apr.
1-31
6.6
A-3
May
1-30
6.6
A-3
June
1-30
6.6
A-3
July
1-31
6.6
A-2
(DVPE)
Minnesota &
Wisconsin
(DVPE)
(CLASS)
V66 Grade
(DVPE)
(CLASS)
V68 GRADE
(DVPE)
(CLASS)
VCB GRADE
(DVPE)
(CLASS)
Jan.
16-31
13.5
D-4
Feb.
1-15
13.5
D-4
Feb.
16-29
11.5
C-4
Mar.
1-15
6.6
A-3
Aug.
1-31
6.6
A-2
Sept. Sept. Oct.
1-15 16-30 1-31
6.6
6.6
11.5
A-2 B-2
C-3
Nov.
1-30
13.5
D-4
Dec.
1-31
13.5
D-4
Revision Date: January 04, 2015
Schedule of Origin Volatility Requirements
NOTE: Gulf Coast origin changeover dates will precede this schedule by approximately 10 days, depending upon the applicable Explorer Pipeline
cycle. Shipments via Explorer Pipeline must meet the specification applicable to the anticipated West Tulsa delivery date. Gulf Coast shippers will be
advised of these dates through seasonal letters.
VMS GRADE
Colorado
(DVPE)
Jan.
1-31
N/A
(Class)
Feb. Mar. Mar. Apr.
1-15 1-15 16-31 1-30
N/A N/A N/A 7.8
A-3
May
1-31
7.8
A-3
June
1-30
7.8
A-2
July
1-31
7.8
A-2
Aug.
1-31
7.8
A-2
Sept. Sept. Oct.
1-15 16-30 1-31
7.8
N/A N/A
A-2
Nov.
1-30
N/A
Dec.
1-31
N/A
Kansas
(DVPE) N/A
(Class)
N/A
N/A
7.8
A-3
7.8
A-3
7.8
A-3
7.8
A-2
7.8
A-2
7.8
A-2
7.8
A-2
N/A
N/A
N/A
N/A
Texas
(DVPE)
N/A
N/A
N/A
7.8
A-3
7.8
A-3
7.8
A-3
7.8
A-2
7.8
A-2
7.8
A-2
7.8
A-2
N/A
N/A
N/A
N/A
N/A
N/A
N/A
N/A
7.8
A-3
7.8
A-3
7.8
A-2
7.8
A-2
7.8
A-2
7.8
A-2
N/A
N/A
N/A
N/A
Apr.
1-30
9.0
A-3
May
1-31
9.0
A-3
June
1-30
9.0
A-2
July
1-31
9.0
A-2
Aug.
1-31
9.0
A-2
Sept. Sept. Oct.
1-15 16-30 1-31
9.0
10.0 11.5
A-2 B-2
C-3
Nov.
1-30
13.5
D-4
Dec.
1-31
13.5
D-5
(Class)
Wyoming
(DVPE)
(Class)
VTX Grade
Jan.
1-31
(DVPE) 13.5
(CLASS) D-5
Feb. Feb. Mar.
1-15 16-29 1-31
13.5 11.5 9.0
D-4 C-4
A-4
Revision Date: January 04, 2015
Schedule of Origin Volatility Requirements
VAZ Grade
Arizona
Jan.
1-31
9.0
A-2
Feb. Mar.
1-29 1-31
9.0
9.0
A-2 A-2
Apr.
1-30
9.0
A-1
May
1-31
9.0
A-1
June
1-30
9.0
A-1
July
1-31
9.0
A-1
Aug.
1-31
9.0
A-1
Sept.
1-30
9.0
A-1
Oct.
1-31
9.0
A-2
Nov.
1-30
9.0
A-2
Dec.
1-31
9.0
A-2
Revision Date: September 14, 2010
A Grade Premium Unleaded Gasoline Specifications
(Conventional Gasoline - This product does not meet the requirements for reformulated gasoline
and may not be used in any reformulated gasoline covered area.)
Product Property
Gravity, ° API
Color
Volatility 2/
Benzene, vol %
Mercaptan Sulfur, wt % 3/
Copper Corrosion
Silver Corrosion
Gum, Existent, mg/100 ml
Oxidation Stability, minutes
Phosphorus, g/gal
Lead, g/gal
Octane
RON
MON
(R+M)/2
Sulfur, ppm 4/
Oxygenates, wt %
Haze Rating 5/
NACE Corrosion
Odor 6/
Test
Method
D287
D3606
D3227
D130
D7667, 7671
D381
D525
D3231
D3237
Origin
Test Results
Minimum
Maximum
Report
Undyed
Deliveries1/
4.9
0.002
1
1
4
5
240
D2699
D2700
0.003
0.010
0.005
0.05
80
0.05
2
3
Report
Report
91.0
D2622
D4815
D4176
TM0172
B+
Nonoffensive
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Gasoline exceeding the origin specification will be accepted from small refineries as defined in 40 CFR
part 80 of the EPA regulations, subject to the special handling fee specified in Magellan Pipelines rules and
regulations tariff.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures,
adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
6/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will
not be accepted for shipment.
Revision Date: October 22, 2014
A1 Grade Premium Unleaded Gasoline Specifications
(Conventional Gasoline – This product does not meet the requirements for reformulated gasoline
and may not be used in any reformulated gasoline covered area.)
Origin
Test
Test Results
Product Property
Method
Minimum
Maximum
Deliveries1/
Gravity, ° API
D287
Report
Color
Undyed
Volatility 2/
Benzene, vol %
D3606
4.9
Mercaptan Sulfur, wt % 3/
D3227
0.002
Copper Corrosion
D130
1
Silver Corrosion
D4814
1
Gum, Existent, mg/100 ml
D381
4
5
Oxidation Stability, minutes
D525
240
Phosphorus, g/gal
D3231
0.003
0.005
Lead, g/gal
D3237
0.010
0.05
Octane
RON
D2699
Report
MON
D2700
Report
(R+M)/2
91.0
Sulfur, ppm 4/
D2622
80
Oxygenates, wt %
D4815
0.05
5/
Haze Rating
D4176
2
3
NACE Corrosion
TM0172
B+
Odor 6/
Nonoffensive
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Gasoline exceeding the origin specification will be accepted from small refineries as defined in 40 CFR
part 80 of the EPA regulations, subject to the special handling fee specified in Magellan Pipelines rules and
regulations tariff.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures,
adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
6/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will
not be accepted for shipment.
Revision Date: November 25, 2014
A1X Grade Premium Unleaded Gasoline Specifications
This is for export only and not for retail use in the United States
Origin
Test
Test Results
Product Property
Method
Minimum
Maximum
Deliveries1/
Gravity, ° API
D287
Report
Color
Undyed
2/
Volatility
Benzene, vol %
D3606
4.9
3/
Mercaptan Sulfur, wt %
D3227
0.002
Copper Corrosion
D130
1
Silver Corrosion
D7667
1
Gum, Existent, mg/100 ml
D381
4
5
Oxidation Stability, minutes
D525
240
Phosphorus, g/gal
D3231
0.003
0.005
Lead, g/gal
D3237
0.010
0.05
Octane
RON
D2699
Report
MON
D2700
Report
(R+M)/2
91.0
Sulfur, ppm 4/
D2622
80
Oxygenates, wt %
D4815
0.05
Haze Rating 5/
D4176
2
3
NACE Corrosion
TM0172
B+
Odor 6/
Nonoffensive
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Gasoline exceeding the origin specification will be accepted from small refineries as defined in 40 CFR
part 80 of the EPA regulations, subject to the special handling fee specified in Magellan Pipelines rules and
regulations tariff.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures,
adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
6/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will
not be accepted for shipment.
Revision Date: November 25, 2014
A0 Grade Premium Unleaded Gasoline Specifications
(Conventional Gasoline - This Product does not meet the requirements for reformulated gasoline
and may not be used in any reformulated gasoline covered area)
Product Property
Gravity, ° API
Color
Volatility 2/
Benzene, vol %
Mercaptan Sulfur, wt % 3/
Copper Corrosion
Silver Corrosion
Gum, Existent, mg/100 ml
Oxidation Stability, minutes
Phosphorus, g/gal
Lead, g/gal
Octane
RON
MON
(R+M)/2
Sulfur, ppm 4/
Oxygenates, wt %
Haze Rating 5/
NACE Corrosion
Odor 6/
Test
Method
D287
D3606
D3227
D130
D4814
D381
D525
D3231
D3237
Origin
Test Results
Minimum
Maximum
Report
Undyed
4.9
0.002
1
1
4
0.003
0.010
5
180
0.005
0.05
80
0.05
2
3
240
D2699
D2700
Deliveries1/
Report
Report
91.0
D2622
D4815
D4176
TM0172
B+
Nonoffensive
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952
is negative.
4/
Gasoline exceeding the origin specification will be accepted from small refineries as
defined in 40 CFR part 80 of the EPA regulations, subject to the special handling fee
specified in Magellan Pipelines rules and regulations tariff.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following
temperatures, adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt %
dicyclopentadiene will not be accepted for shipment.
6/
Revision Date: November 25, 2014
A3 Premium Unleaded Gasoline Specifications
(Conventional Gasoline - This product does not meet the requirements for reformulated gasoline
and may not be used in any reformulated gasoline covered area.)
Product Property
Gravity, °API
Color
Volatility 2/
Benzene, vol %
Mercaptan Sulfur, wt % 3/
Copper Corrosion
Silver Corrosion
Gum, Existent, mg/100 ml
Oxidation Stability, minutes
Phosphorus, g/gal
Lead, g/gal
Octane
RON
MON
(R+M)/2
Sulfur, ppm 4/
Oxygenates, wt %
Haze Rating 5/
NACE Corrosion
Odor 6/
Test
Method
D287
D3606
D3227
D130
D7667,7671
D381
D525
D3231
D3237
D2699
D2700
D2622
D4815
D4176
TM0172
Origin
Test Results
Minimum
Maximum
Report
Undyed
Deliveries1/
4.9
0.002
1
1
4
240
0.003
0.010
5
180
0.005
0.05
94.0
87.0
93.0
80
0.05
2
3
B+
Nonoffensive
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952
is negative.
4/
Gasoline exceeding the origin specification will be accepted from small refineries as
defined in 40 CFR part 80 of the EPA regulations, subject to the special handling fee
specified in Magellan Pipelines rules and regulations tariff.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following
temperatures, adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
6/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt %
dicyclopentadiene will not be accepted for shipment.
Revision Date: November 25, 2014
A5 , AMS Grade 88.5 Sub-Octane Premium Unleaded Gasoline Specifications
(Conventional Gasoline - This product does not meet the requirements for reformulated gasoline
and may not be used in any reformulated gasoline covered area.)
Product Property
Gravity, ° API
Color
Volatility 2/
Benzene, vol %
Mercaptan Sulfur, wt % 3/
Copper Corrosion
Silver Corrosion
Gum, Existent, mg/100 ml
Oxidation Stability, minutes
Phosphorus, g/gal
Lead, g/gal
Octane
RON
MON
(R+M)/2
Sulfur, ppm 4/
Oxygenates, wt %
Haze Rating 5/
NACE Corrosion
Odor 6/
Test
Method
D287
D3606
D3227
D130
D7667,7671
D381
D525
D3231
D3237
Origin
Test Results
Minimum
Maximum
Report
Undyed
Deliveries1/
4.9
0.002
1
1
4
0.003
0.010
5
180
0.005
0.05
80
0.05
2
3
240
D2699
D2700
Report
Report
88.5
D2622
D4815
D4176
TM0172
B+
Nonoffensive
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Gasoline exceeding the origin specification will be accepted from small refineries as defined in 40 CFR
part 80 of the EPA regulations, subject to the special handling fee specified in Magellan Pipelines rules and
regulations tariff.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures,
adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
6/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will
not be accepted for shipment.
Revision Date: November 25, 2014
AR Grade Premium Gasoline Blendstock (RBOB)
For Blending With 10.0% Denatured Fuel Ethanol
(92% Purity) As Defined In ASTM D4806
VOC-Controlled Region 1 Complex Model Phase II
Product Property
Gravity, ° API8/
Color
Volatility 2/9/
Distillation, ASTM D 86
10% Evaporated °F, max
50% Evaporated °F, min
50% Evaporated °F, max
90% Evaporated °F, max
Final Boiling Point °F, max3/
Residue, vol% max
Drivability Index, max
ASTM D4814
Test
Method
D287
Origin
Test Results
Minimum
Maximum
Report
Undyed
Deliveries1/
Class AA Class A Class B Class C Class D Class E
158
158
149
140
131
122
150
150
150
150
150
150
250
250
245
240
235
230
374
374
374
365
365
365
430
430
430
430
430
430
2
2
2
2
2
2
1250
1250 1240
1230
1220
1200
Vapor/Liquid Ratio = 20:1
Class 1 Class 2 Class 3 Class 4 Class 5
°F, min4/
129
122
116
107
102
2/8/
Vapor Pressure, D5191
E200 (vol%)
D86
30
70
E300 (vol%)
D86
70
100
Emission Performance Reduction (%)
-27.0
Mercaptan Sulfur, wt % 3/
D3227
0.002
Copper Corrosion
D130
1
Silver Corrosion
D7667,7671
1
Gum, Existent, mg/100 ml
D381
4
Oxidation Stability, minutes
D525
240
Octane
RON
D2699
Report
MON
D2700
Report
(R+M)/2
93.0
Phosphorus, g/gal
D3231
0.003
Benzene, vol %
D3606
1.3
4/
Aromatics (vol %)
50
Olefins (vol %)
D1319
25
Sulfur, ppm
D2622
80
Oxygen Content wt %5/
D5599
1.5
4.0
Oxygenates, (vol %) 8/
D4815
0.05
6/, 8/
Haze Rating
D4176
2
NACE Corrosion8/
TM0172
B+
Odor 7/, 8/
Nonoffensive
5
180
0.005
3
Revision Date: November 25, 2014
AR Grade Premium Gasoline Blendstock (RBOB) (continued)
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952
is negative.
4/
Refer to test methods in 40 CFR Chapter 1, Part 80.46.
5/
Oxygen content must meet a minimum of 1.5 wt. % and a maximum of 4.0 wt. % after
blending of denatured fuel ethanol.
6/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following
temperatures, adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
7/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt %
dicyclopentadiene will not be accepted for shipment.
8/
Specifications must be met before blending of denatured fuel ethanol except for vapor
pressure during the VOC compliance period, March 20th through October 1st, will be
reported on the blended fuel.
9/
For products blended to meet EPA or state imposed summer VOC requirements, test
must be performed for RVP in accordance with procedure described in 40 CFR, PART
80, Appendix E, Method 3.
**NOTE: This RBOB may not be combined with any other RBOB except RBOB having the
same requirement for oxygenate type and amount. “Base Gasoline” Not for sale to the ultimate
consumer.
**NOTE: Heavy metals are not allowed to be present.
**NOTE: All parameters must be met after blending with denatured fuel ethanol unless noted.
Revision Date: October 22, 2014
AZ2 Grade Arizona Summer Cleaner Burning Gasoline (CBG)
Product Property
Octane RON
MON
(R+M)/2
1/
Oxygen Content (wt%)
RVP (psi) (ASTM)
Benzene (vol%)
Aromatics (vol%)
Olefins (vol%)
Color
Corrosion (Cu) 3 hrs @122F (50C)
Corrosion (Ag) 3 hrs @122F (50C)
2/
Doctor test
or Mercaptan Sulfur (wt.%)
Existent Gum (mg/l00 ml)
GravityAPI @ 60F
Oxidation stability (minutes)
Phosphorous, (gms/gal)
Lead, (gms/gal)
Sulfur (ppm)
NACE
3/
Haze
Odor
ASTM Test
Method
D 2699
D 2700
D 4815
D 5191
D 3606
D 5769
D 1319
D 130
D 7667,7671
D 4952
D 3227
D 381
D 287
D 525
D 3231
D 5059
D 5453
TM0172
D 4176
Olfactory
Test Results
Minimum
Maximum
Report
Report
91.0
0.05
6.4
7.0
1.30
50
25
Undyed
1
1
Negative
0.002
4
Report
240
0.003
0.010
80
B+
2
Non-Offensive
Emissions Performance Reductions (%)
VOC Reduction (%)
NOx Reduction (%)
Volatility
Distil1ation, (F)
E 200(vol%)
E 300(vol%)
End pt
Vapor/Liquid Ratio (V/L °F@ 20)
Drivability Index (DI)
-27.5
-5.5
D 86
30
70
D 2533
D 4814
70
100
430
140
1250
1/ Total oxygen levels shall not exceed de minimus levels. The use of non-hydrocarbon blending components
such as MTBE is prohibited.
2/ Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
3/ Product must be tested at 55F or tank temperature whichever is lower.




Product must be certified using current Arizona CBG regulations from a state of Arizona
registered supplier.
In addition to the above a LPP Product Transfer Document for Arizona CBG must be filled out
and provided to Longhorn Pipe Line Quality Control.
All gasoline must meet latest revision of ASTM D 4814.
Corrosion inhibitors, gum inhibitors and metal deactivators must be approved by Longhorn
Pipeline
Revision Date: October 22, 2014
AZ2 Grade Arizona Summer Cleaner Burning Gasoline (CBG) (continued)



No additives or corrosion inhibitors containing phosphorus may be used in this gasoline.
The shipment of fuels containing Port Fuel Injector (PFl) and intake valve detergent additives is
prohibited. This is a base gasoline, not for sale to the ultimate consumer
Any gasoline exhibiting an offensive and/or containing more than 0.50wt % dicyclopentadiene
will not be accepted for shipment.
Revision Date: October 22, 2014
AZ6 Grade Arizona Winter Cleaner Burning Gasoline (AZRBOB)
Product Property
Octane RON
MON
(R+M)/2
1/
Oxygen Content (wt%)
RVP (psi)
Benzene (vol%)
Aromatics (vol%)
Olefins (vol%)
CARB Predictive Model Calculation
Color
Corrosion (Cu)3 hrs @ 122F(50C)
Corrosion (Ag) 3 hrs @122F (50C)
2/
Doctor test
or Mercaptan sulfur (wt.%)
Existent Gum (mg/100 ml)
Gravity API @ 60F
Oxidation stability (minutes)
Phosphorous (gms/gal)
Lead (gms/gal)
Sulfur (ppm)
NACE
3/
Haze
Odor
Volatility:
Distil1ation, (F)
Vapor/Liquid Ratio (V/L °F@ 20)
Drivability Index (DI)
50%Evap
Max
237
Grade
Z6
1/
2/
3/
ASTM Test
Method
D 2699
D 2700
D 4815
D 5191
D 3606
D 5769
D 1319
D 130
D 7667,7671
D 4952
D 3227
D 381
D 287
D 525
D 3231
D 5059
D 5453
TM0172
D 4176
Olfactory
Test Results
Minimum
Maximum
Report
Report
89.5
0.05
8.0
1.30
33.1
11.1
Pass
Undyed
1
1
Negative
0.002
4
Report
240
0.003
0.010
80
B+
2
Non-Offensive
D 86
D 2533
D 4814
90%Evap
Max
335
End pt
Max
430
V/L DI
Min Max
140 1250
Total oxygen levels shall not exceed de minimums levels. The use of non-hydrocarbon blending
components such as MTBE is prohibited.
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
Product must be tested at 55F or tank temperature whichever is lower.





Product must be certified using current Arizona AZRBOB regulations from a state of Arizona
registered supplier.
In addition to the above a LPP Product Transfer Document for AZRBOB must be filled out and
provided to Longhorn Pipe Line Quality Control.
All gasoline must meet latest revision of ASTM D 4814.
Corrosion inhibitors, gum inhibitors and metal deactivators must be approved by Longhorn
Pipeline
No additives or corrosion inhibitors containing phosphorus may be used in this gasoline.
Revision Date: October 22, 2014
AZ6 Grade Arizona Winter Cleaner Burning Gasoline (AZRBOB) (continued)




The shipment of fuels containing Port Fuel Injector (PFl) and intake valve detergent additives is
prohibited. This is a base gasoline, not for sale to the ultimate consumer
Any gasoline exhibiting an offensive and/or containing more than 0.50wt % dicyclopentadiene
will not be accepted for shipment.
AZRBOB does not comply with the standards for Arizona CBG without the addition of
oxygenate.
This AZRBOB is intended for blending with 10% volume ethanol and may not be combined with
AZRBOB’s requiring oxygenate blending with any other type or amount of oxygenate.
Revision Date: October 22, 2014
D Grade Premium Diesel Fuel Specifications
Product Property
Gravity, °API
Color
Distillation,
IBP, °F
50% Recovered, °F
90% Recovered, °F
Copper Corrosion
Cetane
(1) Cetane Number
OR (2) Cetane Index, A or B
Cetane Index 2/
Flash Point, F
Stability
(1)Thermal, % reflectance
Aging Period (Minutes)
OR (2) Potential Gum, mg/100 ml 3/
Carbon Residue on 10% Bottoms, %
Cloud Point, F
Pour Point, F
Viscosity, cSt at 104 F
Ash, wt %
Haze Rating 5/
NACE Corrosion
Sulfur, ppm 6/
Test
Method
D287
D1500
D86
Origin
Test Results
Minimum Maximum
33.5
39.0
2.0
340
460
540
D130
D613
D4737
D976
D93
2.5
640
1
47.5
47.5
40
145
D6468 (W)
75
D6468 (Y)
82
D6468
90
MPL P. Gum
D524
D2500
D97
D445
1.9
D482
D4176
TM0172
B+
D2622
Deliveries1/
140
15
0.20
4/
4/
4.1
0.01
2
3
*10
Revision Date: December 31, 2008
D Grade Premium Diesel Fuel Specifications (continued)
1/
Delivered products meets all applicable requirements at time and place of delivery
2/
ASTM D976 data is required for low sulfur fuel oils to demonstrate aromatics
compliance per the EPA.
3/
The Potential Gum will be determined by ASTM method D381 modified (Steam Jet
Evaporation at 485 F) after a 16 hour induction period by ASTM method D525
modified. Contact Magellan QC to request a copy of this method.
4/
Month
January
February
March
April
May
June
July
August
September
October
November
December
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at 77 °F or tank
temperature at the time of sampling, whichever is lower.
6/
All results provided must use an EPA qualified instrument.
*Sulfur limit, 11 ppm for interconnecting pipelines.
Pour Point F, max
0
0
0
+10
+10
+10
+10
0
0
0
0
0
Cloud Point F, max
+14
+14
+14
+20
+20
+20
+20
+14
+14
+14
+14
+14
Additional Requirements:
Biodiesel: The use of any biodiesel fuel as a blending component is prohibited.
Dyes: D Grade shipments may not be dyed.
Revision Date: December 31, 2008
E Grade Denatured Fuel Ethanol Specifications
Specification Points
Test Method
Shipments
Apparent Proof, 60°F
Or Density, 60°F
Hydrometer
ASTM D-4052
Report
Report
Water, Volume %, Maximum
ASTM E-203 or E-1064
1.0
Ethanol, Volume %
Minimum
Methanol, Volume %, Maximum
ASTM D-5501
ASTM D-5501
93.5
0.5
Sulfur, ppm (wt/wt), Maximum
ASTM D5453
10
Solvent Washed Gum,
mg/100mL
Maximum
ASTM D-381
Air Jet Method
Potential Sulfate, mass ppm
Maximum
ASTM D7319
Chloride, mg/L
Maximum
ASTM D-7319
Copper, mg/L
Maximum
ASTM D-1688
Method A,
Modified per D-4806
Acidity (as acetic acid), Mass %
Maximum
ASTM D-1613 or D-7795
pHe
Minimum
Maximum
ASTM D-6423
Appearance @ 60°F
Visual Examination
Deliveries
1/
93.0
5.0
4
8
0.08
0.007
6.5
9.0
2/
Denaturant Content and Type
Volume %
Corrosion Inhibitor Additive,
One of the following is
required:
Visibly free of suspended or precipitated
contaminants. Must be clear and bright.
2
Minimum treat rate
6 lbs./1000 bbls.
20 lbs/1000 bbls.
20 lbs./1000 bbls.
20 lbs./1000 bbls.
20 lbs./1000 bbls.
20 lbs./1000 bbls.
13 lbs./1000 bbls.
13 lbs./1000 bbls.
13 lbs/1000 bbls.
13 lbs/1000 bbls.
6 lbs/1000 bbls
3 lbs/1000 bbls.
5 lbs/1000 bbls.
6 lbs/1000 bbls.
Vendor
Innospec
G. E. Betz
Petrolite
Nalco
Betz
Midcontinental
Midcontinental
Petrolite
US Water Services
US Water Services
Ashland
G.E. Power & Water
NALCO
US Water Services
Additive
DCI-11 Plus
Endcor GCC9711
Tolad 3222
5403
ACN 13
MCC5011E
MCC5011PHE
Tolad 3224
Corrpro 654
Corrpro 656
Amergy ECI-6
8Q123ULS
EC5624A Plus
Corrpro Pro NT
Revision Date: October 22, 2014
E Grade Denatured Fuel Ethanol Specifications (continued)
1/ Delivered products meets all applicable requirements at time and place of delivery.
2/ Only approved denaturants listed in D4806. The denaturant range must be within the guidelines
provided for in IRS Notice 2009.06, which is 1.96% to no more than 2.5%.
Revision Date: October 22, 2014
H Grade Normal Butane Specifications
Product Property
Composition, POD or
Chromatography analysis
Liquid vol %
Normal Butane
Isobutane
Pentanes
Propane
Specific Gravity
Vapor Pressure at 100 F, psi
Weathering,
95% Evaporated Temp, F
(Corrected)
Residues,
Non-Volatile Residue at
100F, ml
Oil, No oil stain observation, ml
Sulfur, ppm
Copper Corrosion
Dryness, Inspection
Free Water Content
Test
Method
D2163
Origin
Test Results
Minimum
Maximum
Deliveries1/
95
D1657
D1267
D1837
0.580
3
3
3
0.588
43
36
D2158
D3246
0.05
0.3
30
D1838
1
0
Additives: H grade normal butane shipments must be unstenched and contain no additives.
1/
Delivered products meets all applicable requirements at time and place of delivery.
Revision Date: December 31, 2008
I Grade Iso-Butane Specifications
Product Property
Composition, POD or
Chromatography analysis
Liquid vol %
Isobutane
Propane
Normal Butane
Pentanes
Specific Gravity
Vapor Pressure at 100 F, psi
Weathering,
95% Evaporated Temp, F
(Corrected)
Residues,
Non-Volatile Residue at 100 F, ml
Oil, No oil stain observation, ml
Sulfur,
grains per hundred cubic feet
Copper Corrosion
Dryness, Inspection
Free Water Content
Test
Method
D2163
Origin
Test Results
Minimum
Maximum
Deliveries1/
95
D1657
D1267
D1837
0.560
3.0
5.0
0.5
0.570
62
31
D2158
0.05
0.3
D1266
D1838
15
1
0
Additives: I grade Isobutane shipments must be unstenched and contain no additives.
1/
Delivered products meets all applicable requirements at time and place of delivery.
Revision Date: December 31, 2008
J8 Grade Military Jet Fuel Specifications
Product Property
Color, Saybolt
Total Acid Number, mg KOH/g
Test
Method
D156
D3242
Aromatics, vol. %
Sulfur, ppm
Mercaptan Sulfur, wt %
Doctor Test
Distillation
Initial Boiling Point, °C
10% recovered, °C
20% recovered, °C
50% recovered, °C
90% recovered, °C
Final Boiling Point, °C
Residue, vol %
Loss, vol %
OR
Simulated Distillation
Initial Boiling Point, °C
10% recovered, °C
20% recovered, °C
50% recovered, °C
90% recovered, °C
Final Boiling Point, °C
D1319
D4294
D3227
D4952
D86
Flash Point, C (F)
Density, kg/L at 15 C
Gravity, °API
Freezing Point, C
D93
D4052
D1298
D2386
Origin
Test Results
Minimum
Maximum
Report
0.015
Deliveries1/
25.0
3000
0.002
Negative
Report
205
Report
Report
Report
300
1.5
1.5
D2887
Report
205
Report
Report
Report
300
38 (100)
0.775
37.0
0.840
51.0
-47
Revision Date: January 13, 2012
J8 Grade Military Jet Fuel Specification (continued)
Product Property
Viscosity, at –20 C, cSt.
Net Heat of Combustion, BTU/lb
OR: MJ/kg
Hydrogen Content, wt %
Combustion
(1) Smoke point, mm
OR: (2) Smoke point, mm AND
Naphthalenes, vol %
Cetane Index
Copper Corrosion
Thermal Stability:
Filter pressure drop, mm Hg.
Heater tube deposit rating
Existent Gum, mg/100 ml
Particulate Matter, mg/L
Filtration Time, minutes
Water Reaction, Interface rating
Water Separation Index
Fuel System Icing Inhibitor, vol %
Electrical Conductivity, pS/m
Test
Method
D445
D3338
D4809
D3701
D1322
D1322
D1840
D976
D130
D3241 2/
Origin
Test Results
Minimum
Maximum
8.0
18,400
42.8
13.4
25.0
19.0
3.0
Report
1
25
<3
7.0
1.0
15
D381
D5452 3/
D1094
D3948
D5006 5/
D2624
Deliveries1/
1b
4/
0.10
0.15
6/
6/
Revision Date: January 13, 2012
J8 Grade Military Jet Fuel Specification (continued)
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
ASTM D3241 Thermal Stability test must be conducted at 260 oC for 2.5 hours.
Peacock or abnormal color deposits result in a failure and are not accepted.
3/
A minimum sample size of 3.79 liters (one gallon) shall be filtered. Filtration time will
be determined in accordance with the procedure in Appendix A of MIL-DTL-83133E (or
most current version); this procedure may be used to determine the particulate matter as
an alternate to ASTM D 5452 or ASTM 2276.
4/
The minimum microseparometer rating shall be as follows:
J8 Additives
Antioxidant (AO)*, Metal Deactivator
(MDA)*
AO*, MDA*, and Fuel System Icing
Inhibitor (FSII)
AO*, MDA*, and Corrosion
Inhibitor/Lubricity Improver (CI/LI)
AO*, MDA*, FSII and CI/LI
MSEP Rating, min.
90
85
80
70
* Even though the presence or absence does not change these limits, samples submitted
for specification conformance testing shall contain the same additives present in the
refinery batch. Regardless of which minimum the refiner elects to meet, the refiner shall
report the MSEP rating on a laboratory hand blend of the fuel with all additives required
by the specification.
5/
FSII test shall be performed using the DiEGME scale of the refractometer.
6/
The conductivity must be between 150 and 450 pS/m at ambient temperature or 85 F,
whichever is lower (150 to 700 for JP8+100 shipments that contain thermal stability
improver additive), unless otherwise directed by the procuring activity.
Revision Date: January 13, 2012
J8 Grade Military Jet Fuel Specifications (continued)
Other Requirements
Additives: Shipper must provide the type and amount of each additive used upon request.
Antioxidants: Immediately after processing, and before the fuel is exposed to the atmosphere
(i.e. during rundown into feed/batch tankage), add an approved antioxidant from the following
list in order to prevent the formation of gums and peroxides after manufacture. The
concentration of antioxidant to be added shall be:
a. Not less than 17.2 mg or more than 24.0 mg of active ingredient per liter of fuel (6.0 to
8.4 lb/1000 barrels) to all JP-8 fuel that contains blending stocks that have been hydrogen
treated.
b. At the option of the supplier, not more than 24.0 mg of active ingredient per liter of fuel
(8.4 lb/1000 barrels) may be added to JP-8 fuels that do not contain hydrogen treated
blending stocks.
Approved Antioxidants
a.
b.
c.
d.
e.
f.
2, 6-di-tert-butyl-4-methylphenol
6-tert-butyl-2, 4-dimethylphenol
2, 6-di-tert-butylphenol
75% minimum: 2, 6-di-tert-butylphenol
25% maximum: tert-butyl phenols and tri-tert-butylphenols
72% minimum: 6-tert-butyl-2, 4-dimethylphenol
28% maximum: tert-buty-methylphenols and tert-butyl-dimethylphenols
55% minimum: 2,4-dimethyl-6-tert-butylphenol and
15% minimum: 2,6-di-tert-butyl-4-methylphenol and 30% maximum mixed
methyl and dimethyl tert-butylphenols
Revision Date: January 13, 2012
J8 Grade Military Jet Fuel Specifications (continued)
Metal Deactivator: A metal deactivator, N,N'-disalycylidene-1 ,2-propanediamine, may be
blended into the fuel. The concentration of active material used on initial batching of the fuel at
the refinery shall not exceed 2.0 mg/L. Cumulative addition of metal deactivator when redoping
the fuel, shall not exceed 5.7 mg/L. Metal deactivator additive shall not be used in JP-8 unless
the supplier has obtained written consent from the Procuring Activity and user.
Static Dissipater Additive: An additive shall be blended into the fuels in sufficient
concentration to increase the conductivity of the fuel to within the range specified in the
specifications at the point of injection. The point of injection of the additive shall be determined
by agreement between the purchasing authority and the supplier. The following electrical
conductivity additive is approved: Stadis 450 marketed by Octel America. Inc., Newark, DE
19702.
Corrosion Inhibitor: A corrosion inhibitor conforming to MIL-PRF-25017 shall be blended
into the F-34 (JP-8) grade fuel by the contractor. The corrosion inhibitor additive is optional for
F-35. The amount added shall be equal to or greater that the minimum effective concentration
and shall not exceed the maximum allowable concentration listed in the latest revision of QPL25017. The contractor or transporting agency, or both, shall maintain and upon request shall
make available to the Government evidence that the corrosion inhibitors used are equal in every
respect to the qualification products listed in QPL-25017. The point of injection of the corrosion
inhibitor shall be determined by agreement between the purchasing authority and the supplier.
Fuel System Icing Inhibitor (FSII): The use of a fuel system icing inhibitor shall be mandatory
for NATO F-34 (JP-8) and shall conform to MIL-DTL-85470. The point of injection of the
additive shall be determined by agreement between the Purchasing Authority and the supplier.
Thermal stability improver additive: Due to logistical concern, personnel at the operating
location shall request written approval from the cognizant activity to add a thermal stability
improver additive to the fuel. If approval is given, the concentration of the additive and location
of injection shall be specified by the cognizant service activity found in MIL-DTL-8133E section
3.3.6. JP-8 fuel with an approved thermal stability improver additive at the required
concentration shall be designated as JP-8+100. Thermal stability improver additive shall not be
used in JP-8 without approval, in writing (reference MIL-DTL-83133E section 3.3.6 for
addresses).
Revision Date: January 13, 2012
J8 Grade Military Jet Fuel Specifications (continued)
Qualified thermal stability improver additives:
Additive Name
SPEC AID 8Q462
Qualification
Reference
AFRL/PRSF
Ltr, 9 Dec 97
AeroShell Performance
Additive 101
AFRL.PRSF
Ltr, 13 Jan 98
Manufacturer
BetzDearborn
9669 Grogan Mill Road
PO Box 4300
The Woodlands, TX 77387
Shell Aviation Ltd.
Shell-Mex House
Strand
London WC2R 0ZA
Premixing of Additives: Additives shall not be premixed with other additives before injection
into the fuel so as to prevent possible reactions among the concentrated forms of different
additives.
Workmanship: At the time of Government acceptance, the finished fuel shall be visually free
from undissolved water, sediment, or suspended matter and shall be clear and bright.
Additional Provisions: The Carrier shall not be responsible for the concentration of additives in
J8 grade jet fuel deliveries except as provided for in the tariff.
Revision Date: January 13, 2012
L Grade Propane Specifications
Product Property
Composition
Chromatography analysis
Liquid vol %
Propane
Propylene
Butanes and C4+
Pentanes and C5+
Specific gravity
Vapor pressure at 100 F, psi
Weathering, 95% evaporated
Temp, F (corrected)
Residues,
Nonvolatile residue at 100 F, ml
Oil, no oil stain observation, ml
Sulfur,
grains per hundred cubic feet
Copper Corrosion
Dryness, Valve Freeze, seconds
Test
Method
Origin
Test Results
Minimum
Maximum
Deliveries1/
D2163
90
5.0
2.5
D1657
D1267
D1837
None
0.500
175
0.510
208
-37
D2158
0.05
0.3
D2784
10
D1838
D2713
1
60
Additives: L Grade shipments must be unstenched and contain no additives. Unless
otherwise notified in writing by shipper, L Grade propane deliveries will be odorized at
the rate of 1.5 pounds Ethyl Mercaptan/10,000 gallons.
1/
Delivered products meets all applicable requirements at time and place of delivery.
Revision Date: December 31, 2008
NEP Grade Regular Unleaded Gasoline Specifications
This is for export only and not for retail use in the United States.
Origin
Test
Test Results
Product Property
Method
Minimum
Maximum
Deliveries1/
Gravity, ° API
D287
Report
Color
Undyed
Volatility 2/
Benzene, vol %
D3606
3.0
Mercaptan Sulfur, wt % 3/
D3227
0.002
Copper Corrosion
D130
1
Silver Corrosion
D7667,7671
1
Gum, Existent, (washed) mg/100 ml D381
4
Oxidation Stability, minutes
D525
300
Phosphorus, g/gal
D3231
0.003
Lead, g/gal
D3237
0.010
0.05
Octane
RON
D2699
Report
MON
D2700
82.0
(R+M)/2
87.0
Sulfur, ppm
D2622
1000
Oxygenates, wt %
D4815
0.05
Haze Rating 4/
D4176
2
3
NACE Corrosion
TM0172
B+
Odor 5/
Nonoffensive
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952
is negative.
4/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following
temperatures, adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
5/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt %
dicyclopentadiene will not be accepted for shipment.
Revision Date: October 22, 2014
NR Grade Regular Gasoline Blendstock (RBOB)
For Blending With 10.0% Denatured Fuel Ethanol
(92% Purity) As Defined In ASTM D4806
VOC-Controlled Region 1 Complex Model Phase II
Product Property
Gravity, ° API8/
Color
Volatility 2/9/
Distillation, ASTM D 86
10% Evaporated °F, max
50% Evaporated °F, min
50% Evaporated °F, max
90% Evaporated °F, max
Final Boiling Point °F, max3/
Residue, vol% max
Drivability Index, max
ASTM D4814
Origin
Test
Test Results
Method
Minimum
Maximum
D287
Report
Undyed
Deliveries1/
Class AA Class A Class B Class C Class D Class E
158
158
149
140
131
122
150
150
150
150
150
150
250
250
245
240
235
230
374
374
374
365
365
365
430
430
430
430
430
430
2
2
2
2
2
2
1250
1250 1240
1230
1220
1200
Vapor/Liquid Ratio = 20:1
Class 1 Class 2 Class 3 Class 4 Class 5
4/
°F, min
129
122
116
107
102
Vapor Pressure, D5191 2/8/
E200 (vol%)
D86
30
70
E300 (vol%)
D86
70
100
Emission Performance Reduction (%)
-27.0
Mercaptan Sulfur, wt % 3/
D3227
0.002
Copper Corrosion
D130
1
Silver Corrosion
D7667,7671
1
Gum, Existent, mg/100 ml
D381
4
Oxidation Stability, minutes
D525
240
Octane
RON
D2699
Report
MON
D2700
82.0
(R+M)/2
87.0
Phosphorus, g/gal
D3231
0.003
Benzene, wt. %
D3606
1.3
Aromatics (vol %)4/
50
Olefins (vol %)
D1319
25
Sulfur, ppm
D2622
80
Oxygen Content wt %5/
D5599
1.5
4.0
8/
Oxygenates, (vol %)
D4815
0.05
Haze Rating 6/, 8/
D4176
2
8/
NACE Corrosion
TM0172
B+
Odor 7/, 8/
Nonoffensive
5
0.005
3
Revision Date: October 22, 2014
NR Grade Regular Gasoline Blendstock (RBOB) (continued)
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952
is negative.
4/
Refer to test methods in 40 CFR Chapter 1, Part 80.46.
5/
Oxygen content must meet a minimum of 1.5 wt. % and a maximum of 4.0 wt. % after
blending of denatured fuel ethanol.
6/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following
temperatures, adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
7/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt %
dicyclopentadiene will not be accepted for shipment.
8/
Specifications must be met before blending of denatured fuel except for vapor
pressure during the VOC compliance period, March 20th through October 1st, will be
reported on the blended fuel.
9/
For products blended to meet EPA or state imposed summer VOC requirements, test
must be performed for RVP in accordance with procedure described in 40 CFR, PART
80, Appendix E, Method 3.
**NOTE: This RBOB may not be combined with any other RBOB except RBOB having the
same requirement for oxygenate type and amount. “Base Gasoline” Not for sale to the ultimate
consumer.
**NOTE: Heavy metals are not allowed to be present.
**NOTE: All parameters must be met after blending with denatured fuel ethanol unless noted
Revision Date: October 22, 2014
NZ2 Grade Arizona Summer Cleaner Burning Gasoline (CBG)
Product Property
Octane RON
MON
(R+M)/2
1/
Oxygen Content (wt%)
RVP (psi)
Benzene (vol%)
Aromatics (vol%)
Olefins (vol%)
Color
Corrosion (Cu) 3 hrs @122F (50C)
Corrosion (Ag) 3 hrs @122F (50C)
2/
Doctor test
or Mercaptan Sulfur (wt.%)
Existent Gum (mg/l00 ml)
GravityAPI @ 60F
Oxidation stability (minutes)
Phosphorous, (gms/gal)
Lead, (gms/gal)
Sulfur (ppm)
NACE
3/
Haze
Odor
ASTM Test
Method
D 2699
D 2700
D 4815
D 5191
D 3606
D 5769
D 1319
D 130
D 7667,7671
D 4952
D 3227
D 381
D 287
D 525
D 3231
D 5059
D 5453
TM0172
D 4176
Olfactory
Test Results
Minimum
Maximum
Report
82.0
87.0
0.05
6.4
7.0
1.30
50
25
Undyed
1
1
Negative
0.002
4
Report
240
0.003
0.010
80
B+
2
Non-Offensive
Emissions Performance Reductions (%)
VOC Reduction (%)
NOx Reduction (%)
Volatility
Distil1ation, (F)
E 200(vol%)
E 300(vol%)
End pt
Vapor/Liquid Ratio (V/L °F@ 20)
Drivability Index (DI)
1/
2/
3/
-27.5
-5.5
D 86
30
70
D 2533
D 4814
70
100
430
140
1250
Total oxygen levels shall not exceed de minimus levels. The use of non-hydrocarbon blending components
such as MTBE is prohibited.
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
Product must be tested at 55F or tank temperature whichever is lower.




Product must be certified using current Arizona CBG regulations from a state of Arizona
registered supplier.
In addition to the above a MMP Product Transfer Document for Arizona CBG must be filled out
and provided to Magellan Pipe Line Quality Control.
All gasoline must meet latest revision of ASTM D 4814.
Corrosion inhibitors, gum inhibitors and metal deactivators must be approved by Magellan
Pipeline
Revision Date: October 22, 2014
NZ2 Grade Arizona Summer Cleaner Burning Gasoline (CBG) (continued)




No additives or corrosion inhibitors containing phosphorus may be used in this gasoline.
The shipment of fuels containing Port Fuel Injector (PFl) and intake valve detergent additives is
prohibited. This is a base gasoline, not for sale to the ultimate consumer
Any gasoline exhibiting an offensive and/or containing more than 0.50wt % dicyclopentadiene
will not be accepted for shipment.
This product does not meet the requirements for reformulated gasoline and may not be used in any
reformulated gasoline covered area.
Revision Date: October 22, 2014
NZ6 Grade Arizona Winter Cleaner Burning Gasoline (AZRBOB)
Product Property
Octane RON
MON
(R+M)/2
1/
Oxygen Content (wt%)
RVP (psi)
Benzene (vol%)
Aromatics (vol%)
Olefins (vol%)
CARB Predictive Model Calculation
Color
Corrosion (Cu)3 hrs @ 122F(50C)
Corrosion (Ag) 3 hrs @122F (50C)
2/
Doctor test
or Mercaptan sulfur (wt.%)
Existent Gum (mg/100 ml)
Gravity API @ 60F
Oxidation stability (minutes)
Phosphorous (gms/gal)
Lead (gms/gal)
Sulfur (ppm)
NACE
3/
Haze
Odor
Volatility:
Distil1ation, (F)
Vapor/Liquid Ratio (V/L °F@ 20)
Drivability Index (DI)
50%Evap
Max
237
Grade
NZ6
1/
2/
3/
ASTM Test
Method
D 2699
D 2700
D 4815
D 5191
D 3606
D 5769
D 1319
D 130
D 7667,7671
D 4952
D 3227
D 381
D 287
D 525
D 3231
D 5059
D 5453
TM0172
D 4176
Olfactory
Test Results
Minimum
Maximum
Report
Report
84.0
0.05
8.0
1.30
33.1
11.1
Pass
Undyed
1
1
Negative
0.002
4
Report
240
0.003
0.010
80
B+
2
Non-Offensive
D 86
D 2533
D 4814
90%Evap
Max
335
End pt
Max
430
V/L DI
Min Max
140 1250
Total oxygen levels shall not exceed de minimus levels. The use of non-hydrocarbon blending components
such as MTBE is prohibited.
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
Product must be tested at 55F or tank temperature whichever is lower.





Product must be certified using current Arizona AZRBOB regulations from a state of Arizona
registered supplier.
In addition to the above a MMP Product Transfer Document for AZRBOB must be filled out and
provided to Magellan Pipe Line Quality Control.
All gasoline must meet latest revision of ASTM D 4814.
Corrosion inhibitors, gum inhibitors and metal deactivators must be approved by Magellan
Pipeline
No additives or corrosion inhibitors containing phosphorus may be used in this gasoline.
Revision Date: October 22, 2014
NZ6 Grade Arizona Winter Cleaner Burning Gasoline (AZRBOB) (continued)





The shipment of fuels containing Port Fuel Injector (PFl) and intake valve detergent additives is
prohibited. This is a base gasoline, not for sale to the ultimate consumer
Any gasoline exhibiting an offensive and/or containing more than 0.50wt % dicyclopentadiene
will not be accepted for shipment.
AZRBOB does not comply with the standards for Arizona CBG without the addition of
oxygenate.
This AZRBOB is intended for blending with 10% volume ethanol and may not be combined with
AZRBOB’s requiring oxygenate blending with any other type or amount of oxygenate.
This product does not meet the requirements for reformulated gasoline and may not be used in any
reformulated gasoline covered area.
Revision Date: October 22, 2014
Q Grade Commercial Jet Fuel Specifications
Product Property
Gravity, o API
Total Acidity , mg KOH/g
Freezing Point, oF
Existent Gum, mg/100 ml
Sulfur, ppm
Mercaptan Sulfur, wt % 2/
Color, Saybolt
Copper Corrosion
Water Separation Index
Aromatics, vol %
Net Heat of Combustion, BTU/lb 3/
Flash Point, oF
Viscosity at –4 oF, cSt
Electrical Conductivity, pSm
Thermal Stability:
Filter pressure drop, mm Hg
Heater tube deposit rating
Distillation
10% Recovered, °F
50% Recovered, °F
90% Recovered, °F
Final Boiling Point, °F
Residue, vol %
Loss, vol %
OR
Simulated Distillation
10% Recovered, °F
50% Recovered, °F
90% Recovered, °F
Final Boiling Point, °F
Combustion
(1) Smoke Point, mm
OR (2) Smoke Point, mm
AND Naphthalenes, vol %
Particulate Matter, mg/L
Test
Method
D287
D3242
D2386
D381
D2622
D3227
D156
D130
D3948
D1319
D4809
D56,D93
D445
D2624
D32414/
Origin
Test Results
Minimum
Maximum
37.5
50.5
0.10
-40
5
3000
0.003
+16
1
85
25
18,400
108
8.0
Report
Deliveries1/
37.0 - 51.0
7
+14
75
100
5/
25
<3
D86
396
400
562
1.5
1.5
572
Report
Report
D2887
Report
Report
D1322
D1322
D1840
D5452
25
18
3.0
Report
Revision Date: February 19, 2014
Q Grade Commercial Jet Fuel Specifications (continued)
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952
is negative.
3/
Equation 2 in D3338 may be used as an alternate method.
4/
ASTM D3241 Thermal Stability test must be conducted at 275 oC for 2.5 hours at origin.
Peacock or abnormal color deposits result in a failure and are not accepted.
5/
ASTM D3241 Thermal Stability test results for deliveries will be generated at a
minimum test temperature of 260 °C
Additives:
Antioxidants: Shipments may, but are not required to, contain a maximum of 8.4 pounds
per 1,000 barrels (not including weight of solvent) of the following anti-oxidants:
(1)
N, N-diisopropylparaphenylene diamine.
(2)
75% (min) of 2, 6-ditertiary-butyl phenol plus 25% (max) of tertiary and
tritertiary butyl phenols.
(3)
72% (min) 2, 4-dimethyl-6-tertiary-butyl phenol plus 28% (max) of monomethyl
and dimethyl tertiary-butyl phenols.
(4)
55% (min) 2, 4-dimethyl-6-tertiary-butyl phenol plus 45% (max) of mixed tertiary
and ditertiary butyl phenols.
Metal Deactivators: Shipments may, but are not required to, contain the following metal
deactivators at a maximum of 2.0 lbs per 1,000 barrels (not including weight of solvent):
(1)
n, N-disalicylidene-1, 2-propane diamine.
No other additives are permitted.
The carrier shall not be responsible for the concentration of additives in jet fuel deliveries
at terminals.
Revision Date: September 2, 2010
TA Grade Texas Low Emission Diesel Fuel Specifications
Product Property
Gravity, °API
Distillation
IBP
10% Recovered, F
50% Recovered, F
90% Recovered, F
EP
Copper Corrosion
Cetane
(1) Cetane Number
OR (2) Cetane Index, procedure B
Cetane Index 2/
Flash Point, F
Stability
(1)Thermal, % reflectance
Test
Method
D287
Origin
Test Results
Minimum Maximum
33.0
39.0
D86
Report
340
400
540
610
D130
D613
D4737
D976
D93
D6468 (W)
D6468 (Y)
Aging Period (Minutes)
D6468
OR (2) Potential Color 3/ and
MPL P. Color
4/
Potential Gum, mg/100 ml
MPL P. Gum
OR (3) Oxidation, mg/100 ml
D2274
Carbon Residue on 10% Bottoms, %
D524
Cloud Point, F
D2500
Pour Point, F
D97
Viscosity, cSt at 104 F
D445
Ash, wt %
D482
6/
Haze Rating
D4176
NACE Corrosion
TM0172
7/
Sulfur, ppm
D2622
Total Aromatic Hydrocarbon, Vol%
D5186
Polycyclic Aromatic Hydrocarbon, wt% D5186
Nitrogen, ppm
D4629
Deliveries1/
420
490
640
690
1
48.0
48.0
48
140
125
75
82
90
6
50
2.5
0.35
5/
5/
2.0
4.1
0.01
2
3
B+
*10
10
1.4
10
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
ASTM D976 data is required for low sulfur fuel oils to demonstrate aromatics
compliance per the EPA.
3/
The Potential Color will be determined by ASTM method D1500 on a filtered sample
after a 16 hour induction period by ASTM method D525 modified. Contact Magellan
QC to request a copy of this method.
Revision Date: June 7, 2012
TA Grade Texas Low Emission Diesel Fuel Specifications (continued)
4/
The Potential Gum will be determined by ASTM method D381 modified (Steam Jet
Evaporation at 485 F) after a 16 hour induction period by ASTM method D525
modified. Contact Magellan QC to request a copy of this method.
5/
Month
January
February
March
April
May
June
July
August
September
October
November
December
6/
Compliance with ASTM D4176 will be determined using Procedure 2 at 77 °F or tank
temperature at the time of sampling, whichever is lower.
7/
All results provided must use an EPA qualified instrument.
*Sulfur limit, 11 ppm for interconnecting pipelines.
Pour Point F, max.
0
0
0
+10
+10
+10
+10
+10
0
0
0
0
Cloud Point F, max
+14
+14
+14
+20
+20
+20
+20
+20
+14
+14
+14
+14
Dyes: TC Grade shipments may not be dyed.
Revision Date: June 7, 2012
Sub-Octane Unleaded Gasoline Specifications
Grades: V, V8, V66, V68, VCB, and VTX
(Conventional Gasoline - This product does not meet the requirements for reformulated gasoline
and may not be used in any reformulated gasoline covered area.
The following parameters apply before blending with denatured fuel ethanol.
Product
Test
Origin Limits
Origin Limits
Property
Method
Minimum
Maximum
Deliveries1/
Gravity, ° API
D287, D1298, D4052
Report
Color
Undyed
Distillation 2/
D86
RVP 2/
D5191
Vapor to Liquid Ratio 2/
D5188
2/
Drivability Index
D4814
Copper Corrosion
D130
1
Silver Corrosion
D7667, 7671
1
Gum, Existent, mg/100 ml D381
4
5
Mercaptan Sulfur, wt % 3/
D3227
0.002
Sulfur, ppm
D2622
80
Benzene, vol %
D3606
4.9
Oxidation Stability, minutes D525
240
Haze Rating 4/
D4176
2
3
Oxygenates, wt %
D4815
0.05
Phosphorus, g/gal
D3231
0.003
0.005
Lead, g/gal
D3237
0.010
0.05
NACE Corrosion
TM0172
B+
Odor 5/
Nonoffensive
The following parameter applies either before or before and after blending with denatured
fuel ethanol.
Octane
RON, min
MON, min
(R+M)/2, min
RON, min
MON, min
(R+M)/2, min
D2699
D2700
Base Gasoline
Report
79.0
84.0
D2699
D2700
Base Gasoline and Blend with 10% Ethanol
Report
Report
Report
82.0
83.0
87.0
Revision Date: October 22, 2014
The following parameters apply after blending with denatured fuel ethanol at 10%
Test
Method
Product Property
Distillation,
10% Evap (T10),°F
20% Evap (T20),°F
50% Evap (T50),°F, min
RVP 6/
Origin Limits
D86
Report
Report
150
D5191
Vapor to Liquid Ratio
D5188, min2/7/
Class 1
129
Report
Class 2
122
Class 3
116
Class 4
107
Class 5
102
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Magellan’s Seasonal Gasoline Volatility Classes and Schedule of Origin
Volatility requirements.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952
is negative.
4/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following
temperatures, adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
5/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt %
dicyclopentadiene will not be accepted for shipment.
6/
RVP limits on ethanol blended gasoline are controlled by various federal and state
regulations and waivers, which are generally greater than the limits for base gasoline.
7/
D5188 is the referee test method. The alternate equation in D 4814 may also be used.
Revision Date: October 22, 2014
Sub-Octane Unleaded Gasoline Specifications
V1, VMS Grade 81.5 Sub-Octane Unleaded Gasoline Specifications
(Conventional Gasoline - This product does not meet the requirements for reformulated gasoline
and may not be used in any reformulated gasoline covered area.
The following parameters apply before blending with denatured fuel ethanol.
Product
Test
Origin Limits
Origin Limits
Property
Method
Minimum
Maximum
Deliveries1/
Gravity, ° API
D287, D1298, D4052
Report
Color
Undyed
Distillation 2/
D86
RVP 2/
D5191
2/
Vapor to Liquid Ratio
D5188
Drivability Index 2/
D4814
Copper Corrosion
D130
1
Silver Corrosion
D7667, 7671
1
Gum, Existent, mg/100 ml D381
4
5
3/
Mercaptan Sulfur, wt %
D3227
0.002
Sulfur, ppm
D2622
80
Benzene, vol %
D3606
4.9
Oxidation Stability, minutes D525
240
Haze Rating 4/
D4176
2
3
Oxygenates, wt %
D4815
0.05
Phosphorus, g/gal
D3231
0.003
0.005
Lead, g/gal
D3237
0.010
0.05
NACE Corrosion
TM0172
B+
Odor 5/
Nonoffensive
The following parameter applies either before or before and after blending with denatured
fuel ethanol.
Octane
RON, min
MON, min
(R+M)/2, min
RON, min
MON, min
(R+M)/2, min
D2699
D2700
Base Gasoline
Report
Report
82.0
D2699
D2700
Base Gasoline and Blend with 10% Ethanol
Report
Report
Report
Report
81.5
85.0
Revision Date: October 31, 2014
The following parameters apply after blending with denatured fuel ethanol at 10%
Test
Method
Product Property
Distillation,
10% Evap (T10),°F
20% Evap (T20),°F
50% Evap (T50),°F, min
RVP 6/
Origin Limits
D86
Report
Report
150
D5191
Vapor to Liquid Ratio
D5188, min2/7/
Class 1
129
Report
Class 2
122
Class 3
116
Class 4
Report
Class 5
Report
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Magellan’s Seasonal Gasoline Volatility Classes and Schedule of Origin
Volatility requirements.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952
is negative.
4/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following
temperatures, adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
5/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt %
dicyclopentadiene will not be accepted for shipment.
6/
RVP limits on ethanol blended gasoline are controlled by various federal and state
regulations and waivers, which are generally greater than the limits for base gasoline.
7/
D5188 is the referee test method. The alternate equation in D 4814 may also be used.
Revision Date: October 31, 2014
V2 Grade 85.0 Octane Unleaded Gasoline
(Conventional Gasoline - This product does not meet the requirements for reformulated gasoline
and may not be used in any reformulated gasoline covered area.)
Product Property
Gravity, ° API
Color
Volatility 2/
Benzene, vol%
Mercaptan Sulfur, wt % 3/
Copper Corrosion
Silver Corrosion
Gum, Existent, mg/100 ml
Oxidation Stability, minutes
Phosphorus, g/gal
Lead, g/gal
Octane
RON
MON
(R+M)/2
Sulfur, ppm 4/
Oxygenates, wt %
Haze Rating 5/
NACE Corrosion
Odor 6/
Test
Method
D287
D3606
D3227
D130
D7667,7671
D381
D525
D3231
D3237
Origin
Test Results
Minimum
Maximum
Report
Undyed
Deliveries1/
4.9
0.002
1
1
4
0.003
0.010
5
180
0.005
0.05
80
0.05
2
3
240
D2699
D2700
Report
Report
85.0
D2622
D4815
D4176
TM0172
B+
Nonoffensive
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
Refer to Seasonal Gasoline Volatility Schedule.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952 is negative.
4/
Gasoline exceeding the origin specification will be accepted from small refineries as defined in 40 CFR
part 80 of the EPA regulations, subject to the special handling fee specified in Magellan Pipelines rules and
regulations tariff.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at the following temperatures,
adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
6/
Any gasoline exhibiting an offensive odor and/or containing more than 0.30 wt % dicyclopentadiene will
not be accepted for shipment.
Revision Date: October 22, 2014
W Grade Natural Gasoline Specifications
Product Property
Specific Gravity
Gravity, °API
Reid Vapor Pressure, psi
Distillation,
% Evaporated at 140 F
% Evaporated at 275 F
Final Boiling Point, F
Color
Benzene, vol %
Doctor
Sulfur, ppm
Dryness, Free Water by Inspection
Copper Corrosion
Test
Method
D1657
D287
D5191
NGPA 1138
Origin
Test Results
Minimum
Maximum
0.654
0.685
75.0
85.0
12.0
15.0
25
90
Deliveries1/
85
375
D156
D3606
D484
D2622
+25
1.5
Negative
D130
30
None
1
Additives: W Grade shipments may not contain additives.
1/
Delivered products meets all applicable requirements at time and place of delivery.
Revision Date: December 31, 2008
W2 Denaturant Grade Natural Gasoline Specifications
Test
Product Property
Method
Gravity, °API
D287
Reid Vapor Pressure, psi
D5191
Distillation,
D86
90% Evaporated at Degree F
Final Boiling Point at Degree F
Color
D156
Benzene, vol %
D5580
Aromatics, vol %, max
D5580
Olefins Content, vol %, max
D6550
Doctor
D4952
Sulfur, ppm
D5453
Copper Corrosion
D130
2/
Haze Rating
D4176
NACE Corrosion
TM0172
Origin
Test Results
Minimum
Maximum
75.0
85.0
12
14
Deliveries1/
365
437
+25
1.10
35.0
10.0
Negative
120
1
2
3
B+
Additives: W2 Grade shipments may not contain additives.
1/
2/
Delivered products meets all applicable requirements at time and place of delivery.
Compliance with ASTM D4176 will be determined using Procedure 2 at the following
temperatures, adjusted seasonally:
February 16 – September 30
55 F max
October 1– February 15
45 F max
.
Revision Date: November 25, 2014
X Grade Ultra Low Sulfur Diesel Fuel Specifications
Product Property
Gravity, °API
Color
Distillation
50% Recovered, F
90% Recovered, F
OR
Simulated Distillation
50% Recovered, °F
90% Recovered, °F
Copper Corrosion
Cetane
(1) Cetane Number
OR (2) Cetane Index, procedure A
Cetane Index 2/
Flash Point, F
Stability
(1)Thermal, % reflectance
Aging Period (Minutes)
OR (2) Potential Color 3/ and
Potential Gum, mg/100 ml 4/
OR (3) Oxidation, mg/100 ml
Carbon Residue on 10% Bottoms, %
Cloud Point, F
Pour Point, F
Viscosity, cSt at 104 F
Ash, wt %
Haze Rating 6/
NACE Corrosion
Sulfur, ppm 7/
Test
Method
D287
D1500
D86
Origin
Test Results
Minimum Maximum
Report
2.5
Deliveries1/
3.0
Report
540
640
D2887
Report
572
D130
D613
D4737
D976
D93
40.0
40.0
40
140
D6468 (W)
D6468 (Y)
D6468
75
82
90
MPL P. Color
MPL P. Gum
D2274
D524
D2500
D97
D445
1.9
D482
D4176
TM0172
B+
D2622
672
1
130
6
50
2.5
0.35
5/
5/
4.1
0.01
2
3
*10
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
ASTM D976 data is required for low sulfur fuel oils to demonstrate aromatics
compliance per the EPA.
3/
The Potential Color will be determined by ASTM method D1500 on a filtered sample
after a 16 hour induction period by ASTM method D525 modified. Contact Magellan
QC to request a copy of this method.
Revision Date: June 7, 2012
X Grade Ultra Low Sulfur Diesel Fuel Specifications (continued)
4/
The Potential Gum will be determined by ASTM method D381 modified (Steam Jet
Evaporation at 485 F) after a 16 hour induction period by ASTM method D525
modified. Contact Magellan QC to request a copy of this method.
5/
Month
January
February
March
April
May
June
July
August
September
October
November
December
6/
Compliance with ASTM D4176 will be determined using Procedure 2 at 77 °F or tank
temperature at the time of sampling, whichever is lower.
7/
All results provided must use an EPA qualified instrument.
*Sulfur limit, 11 ppm for interconnecting pipelines.
Pour Point F, max.
0
0
0
+10
+10
+10
+10
+10
0
0
0
0
Cloud Point F, max
+14
+14
+14
+20
+20
+20
+20
+20
+14
+14
+14
+14
Additional Requirements:
Biodiesel: The use of any biodiesel fuel as a blending component is prohibited.
Dyes: X Grade shipments may not be dyed.
Revision Date: June 7, 2012
XH Grade Low Sulfur Diesel Fuel Specifications
Product Property
Gravity, °API
Color
Distillation
50% Recovered, F
90% Recovered, F
OR
Simulated Distillation
50% Recovered, °F
90% Recovered, °F
Copper Corrosion
Cetane
(1) Cetane Number
OR (2) Cetane Index, procedure B
Cetane Index 2/
Flash Point, F
Stability
(1)Thermal, % reflectance
Aging Period (Minutes)
OR (2) Potential Color 3/ and
Potential Gum, mg/100 ml 4/
OR (3) Oxidation, mg/100 ml
Carbon Residue on 10% Bottoms, %
Cloud Point, F
Pour Point, F
Viscosity, cSt at 104 F
Ash, wt %
Haze Rating 6/
NACE Corrosion
Sulfur, ppm 7/
Test
Method
D287
D1500
D86
Origin
Test Results
Minimum Maximum
Report
2.5
Deliveries1/
3.0
Report
540
640
D2887
Report
572
D130
D613
D4737
D976
D93
40.0
40.0
40
140
D6468 (W)
D6468 (Y)
D6468
MPL P. Color
MPL P. Gum
D2274
D524
D2500
D97
D445
D482
D4176
TM0172
D2622
75
82
90
672
1
130
6
50
2.5
0.35
5/
5/
1.9
4.1
0.01
2
3
B+
470
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
ASTM D976 data is required for low sulfur fuel oils to demonstrate aromatics
compliance per the EPA.
3/
The Potential Color will be determined by ASTM method D1500 on a filtered sample
after a 16 hour induction period by ASTM method D525 modified. Contact Magellan
QC to request a copy of this method.
Revision Date: December 31, 2008
XH Grade Low Sulfur Diesel Fuel Specifications (continued)
4/
The Potential Gum will be determined by ASTM method D381 modified (Steam Jet
Evaporation at 485 F) after a 16 hour induction period by ASTM method D525
modified. Contact Magellan QC to request a copy of this method.
5/
Month
January
February
March
April
May
June
July
August
September
October
November
December
6/
Compliance with ASTM D4176 will be determined using Procedure 2 at 77 °F or tank
temperature at the time of sampling, whichever is lower.
7/
All results provided must use an EPA qualified instrument.
Pour Point F, max.
0
0
0
+10
+10
+10
+10
0
0
0
0
0
Cloud Point F, max
+14
+14
+14
+20
+20
+20
+20
+14
+14
+14
+14
+14
Additional Requirements:
Biodiesel: The use of any biodiesel fuel as a blending component is prohibited.
Dyes: XH Grade shipments may not be dyed.
Revision Date: December 31, 2008
XR Grade Low Sulfur Diesel Fuel Specifications
Product Property
Gravity, °API
Color
Distillation
50% Recovered, F
90% Recovered, F
OR
Simulated Distillation
50% Recovered, °F
90% Recovered, °F
Copper Corrosion
Cetane
(1) Cetane Number
OR (2) Cetane Index, procedure B
Cetane Index 2/
Flash Point, F
Stability
(1)Thermal, % reflectance
Aging Period (Minutes)
OR (2) Potential Color 3/ and
Potential Gum, mg/100 ml 4/
OR (3) Oxidation, mg/100 ml
Carbon Residue on 10% Bottoms, %
Cloud Point, F
Pour Point, F
Viscosity, cSt at 104 F
Ash, wt %
Haze Rating 6/
NACE Corrosion
Sulfur, ppm 7/
Test
Method
D287
D1500
D86
Origin
Test Results
Minimum Maximum
Report
2.5
Deliveries1/
3.0
Report
540
640
D2887
Report
572
D130
D613
D4737
D976
D93
40.0
40.0
40
140
D6468 (W)
D6468 (Y)
D6468
MPL P. Color
MPL P. Gum
D2274
D524
D2500
D97
D445
D482
D4176
TM0172
D2622
75
82
90
672
1
130
6
50
2.5
0.35
5/
5/
1.9
4.1
0.01
2
3
B+
470
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
ASTM D976 data is required for low sulfur fuel oils to demonstrate aromatics
compliance per the EPA.
3/
The Potential Color will be determined by ASTM method D1500 on a filtered sample
after a 16 hour induction period by ASTM method D525 modified. Contact Magellan
QC to request a copy of this method.
Revision Date: December 31, 2008
XR Grade Low Sulfur Diesel Fuel Specifications (continued)
4/
The Potential Gum will be determined by ASTM method D381 modified (Steam Jet
Evaporation at 485 F) after a 16 hour induction period by ASTM method D525
modified. Contact Magellan QC to request a copy of this method.
5/
Month
January
February
March
April
May
June
July
August
September
October
November
December
6/
Compliance with ASTM D4176 will be determined using Procedure 2 at 77 °F or tank
temperature at the time of sampling, whichever is lower.
7/
All results provided must use an EPA qualified instrument.
Pour Point F, max.
0
0
0
+10
+10
+10
+10
0
0
0
0
0
Cloud Point F, max
+14
+14
+14
+20
+20
+20
+20
+14
+14
+14
+14
+14
Additional Requirements:
Biodiesel: The use of any biodiesel fuel as a blending component is prohibited.
Dyes: XR Grade shipments require red dye. A minimum of 4.0 PTB (11.5ppm) solid
dye standard Solvent Red 26 or a spectrally equivalent quantity of a diluted dye
formulation must be added to all XR shipments at the Magellan Pipeline loading rack.
Red dye concentrations may be measured using a Petrospec DT100c or equivalent.
Revision Date: December 31, 2008
XU Grade Ultra Low Sulfur Diesel Fuel Specifications
Rocky Mountain System
Origin
Test
Test Results
Product Property
Method
Minimum Maximum
Gravity, °API
D287
Report
Color
D1500
2.5
Distillation
D86
50% Recovered, F
Report
90% Recovered, F
540
640
OR
Simulated Distillation
D2887
50% Recovered, °F
Report
90% Recovered, °F
572
672
Copper Corrosion
D130
1
Cetane
(1) Cetane Number
D613
40.0
OR (2) Cetane Index, procedure A
D4737
40.0
Cetane Index 2/
D976
40
Flash Point, F
D93
134
Stability
(1)Thermal, % reflectance
D6468 (W)
75
D6468 (Y)
82
Aging Period (Minutes)
D6468
90
OR (2) Potential Color 3/ and
Potential Gum, mg/100 ml 4/
OR (3) Oxidation, mg/100 ml
Carbon Residue on 10% Bottoms, %
Cloud Point, F
Pour Point, F
Viscosity, cSt at 104 F
Ash, wt %
Haze Rating 6/
NACE Corrosion
Sulfur, ppm 7/
MPL P. Color
MPL P. Gum
D2274
D524
D2500
D97
D445
1.9
D482
D4176
TM0172
B+
D2622
Deliveries1/
3.0
6
50
2.5
0.35
5/
5/
4.1
0.01
2
3
*10
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
ASTM D976 data is required for low sulfur fuel oils to demonstrate aromatics
compliance per the EPA.
3/
The Potential Color will be determined by ASTM method D1500 on a filtered sample
after a 16 hour induction period by ASTM method D525 modified. Contact Magellan
QC to request a copy of this method.
Revision Date: August 13, 2014
XU Grade Ultra Low Sulfur Diesel Fuel Specifications (continued)
Rocky Mountain System
4/
The Potential Gum will be determined by ASTM method D381 modified (Steam Jet
Evaporation at 485 F) after a 16 hour induction period by ASTM method D525
modified. Contact Magellan QC to request a copy of this method.
5/
Month
January
February
March
April
May
June
July
August
September
October
November
December
6/
Compliance with ASTM D4176 will be determined using Procedure 2 at 77 °F or tank
temperature at the time of sampling, whichever is lower.
7/
All results provided must use an EPA qualified instrument.
*Sulfur limit, 11 ppm for interconnecting pipelines.
Pour Point F, max.
-20
-20
-20
Report
Report
Report
Report
Report
Report
-20
-20
-20
Cloud Point F, max
+5
+5
+5
+20
+20
+20
+20
+20
+20
+5
+5
+5
Additional Requirements:
Biodiesel: The use of any biodiesel fuel as a blending component is prohibited.
Dyes: X Grade shipments may not be dyed.
Revision Date: August 13, 2014
Y Grade No. 1 Diesel Fuel Specifications
Product Property
Gravity, API
Flash Point, F
Pour Point, F
Carbon Residue on 10% Bottoms, %
Sulfur, ppm 2/
Mercaptan Sulfur, wt % 3/
Copper Corrosion
Cetane
(1) Cetane Number
OR (2) Cetane Index, procedure A
Cetane Index 4/
Distillation
10% Recovered, F
90% Recovered, F
OR
Simulated Distillation
10% Recovered, F
90% Recovered, F
Viscosity at 104 F, cSt
Ash, wt %
Haze Rating 5/
NACE Corrosion
Test
Method
D287
D93
D97
D524
D2622
D3227
D130
D613
D4737
D976
D86
Origin
Test Results
Minimum Maximum
35.0
125
160
-25
0.15
*10
0.004
1
Deliveries1/
115
40.0
40.0
40
419
550
D2887
D445
D482
D4176
TM0172
1.3
383
580
2.1
0.01
2
3
B+
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
All results provided must use an EPA qualified instrument.
*Sulfur limit, 11 ppm for interconnecting pipelines.
3/
Mercaptan Sulfur determination is waived if the result of the Doctor Test ASTM D4952
is negative.
4/
ASTM D976 data is required for low sulfur fuel oils to demonstrate aromatics
compliance per the EPA.
5/
Compliance with ASTM D4176 will be determined using Procedure 2 at 77 °F or tank
temperature at the time of sampling, whichever is lower.
Additional Requirements:
Biodiesel: The use of any biodiesel fuel as a blending component is prohibited.
Dyes: Y Grade shipments may not be dyed.
Revision Date: August 13, 2014
ZB Grade Ultra Low Sulfur Biodiesel Fuel Blend Stock Specifications
Product Property
Density, Kg/L
Filtration, Seconds (Modified), max
Flash Point, C
Cloud Point, F
Carbon Residue on 100% Sample,wt %
Sulfur, ppm (mg/g) 2/
Stability (Three Parameters)
Rancimat, (hrs.)
Copper Corrosion
Cetane Number
Distillation
Atmospheric equivalent temperature
90% Recovered, F or
Simulated Distillation, (Modified)
Viscosity at 104 F, cst
Sulfated Ash, wt %
Free Glycerin, wt %
Monoglyceride, wt%
Total Glycerin, wt %
Acid Number, mgKOH/g
Haze Rating @ 60 F
Phosphorus content, wt%
Water & Sediment, vol%
Minimum Delivery Temperature
*Test
Method
D4052
D7501
D93
D2500
D4530
D5453
EN14112
D130
D613
D1160
D2887
D445
D874
D6584
D6584
D6584
D664
D4176
D4951
D2709
MMP
Calcium and Magnesium, combined, ppm (mg/g) EN14538
Sodium & Potassium combined, ppm (mg/g) EN14538
Workmanship 3/
MMP
Origin
Test Results
Minimum Maximum
Report
125
130
36
0.050
15
6
Deliveries1/
3
1
47
680
1.9
680
6.0
0.020
0.020
0.450
0.240
0.40
2
0.001
0.050
0.50
+50
5.0
5.0
Revision Date: July 25, 2012
ZB Grade Ultra Low Sulfur Biodiesel Fuel Blend Stock Specifications (continued)
1/
Delivered products meets all applicable requirements at time and place of delivery.
2/
All results provided must use an EPA qualified instrument.
3/
Workmanship: At the time of acceptance, the finished fuel shall be visually free from
undissolved water, sediment, or suspended matter and shall be clear and bright.
Additives:
BioExtend 30
Eastman - Tenox 21
Kemin BF 320
NALCO EC 5609A
*Alternative methods found in association with D6751 the ASTM specification for
biodiesel are accepted.
Revision Date: July 25, 2012

Product Specifications