Florida Gas Transmission Company, LLC
Fourth Revised Volume No. 1
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Effective Date: 04/01/2010, Docket: RP10-21-000, Status: Effective
Second Revised Sheet No. 206A Second Revised Sheet No. 206A
Superseding: First Revised Sheet No. 206A
GENERAL TERMS AND CONDITIONS
(continued)
required postings of additional standards applicable to the Western Division
shall meet the following:
i) Transporter shall attempt to provide as much notice as possible, but in any
event, such additional standards shall be posted at least 24 hours in
advance of their implementation;
ii) Such standards shall apply for only so long as necessary to bring the
blended gas stream entering into the Market Area (as measured at
Transporter's Compressor Station No. 12, just downstream of the Western
Division/Market Area demarcation point) into compliance with the standards
in Section 2.B, and such posting shall indicate the expected duration of
such limitation;
iii) Transporter shall post only those standards necessary to bring the blended
gas stream into compliance with Section 2.B; and,
iv) Such standards shall be applied on a not unduly discriminatory basis.
B. Gas delivered into Transporter's pipeline system at point(s) of receipt in
Transporter's Market Area and gas entering the Market Area from the Western Division
(as measured at Transporter's Compressor Station No. 12) shall, in addition to the
provisions contained in Section 2.A.1 through 2.A.8, conform to the following quality
standards:
1. shall have a methane composition of not less than eighty-five (85) mole percent;
2. shall have an ethane composition of not more than ten (10) mole percent;
3. shall have a propane composition of not more than two and three-quarters (2.75)
mole percent;
4. shall have a combined composition of not more than one and two tenths (1.2) mole
percent of isobutane and normal butane and pentanes and heavier hydrocarbons; and
a Hydrocarbon Dew point not to exceed 25 degrees Fahrenheit;
5. shall have a minimum temperature, and a physical means to maintain such minimum
temperature; such minimum temperature to be determined on a case-by-case basis,
considering the pipeline operating conditions at, and downstream of, the receipt
location, such as: (i) gas flow and the ability to blend gas streams, (ii) the
magnitude of the pressure drop at the point of the interconnection, and (iii) any
potentially adverse impact to, or unsafe condition on, Transporter's or customers'
facilities downstream of the interconnection, such as those occurring from the
receipt of excessively cold gas or liquid hydrocarbon fallout;
6. shall have a Btu content of not more than eleven hundred and ten (1110) Btu per
cubic foot;
7. shall have a Wobbe Index absolute limit from 1340 to 1396 (calculated using Higher
Heating Value (HHV), dry, under standard conditions at 14.73 psia at 60 degrees
Fahrenheit) based on the following mathematical definition and in accordance with
Section 4 of these GT&C;
HHV/SQRT SGgas
Where:
HHV = Higher Heating Value (Btu/scf)
SGgas = Specific Gravity
Sqrt = Square Root of
and shall be subject to a limitation on the rate of change of two percent (2%) of
Wobbe per six-minute interval; and,
8. shall not contain more than one percent (1%) carbon dioxide by volume nor
any injected carbon dioxide as a dilutant; and
9. shall contain not more than two (2) grains of total sulphur per one
hundred (100) cubic feet of gas.