Patent US3990256A successfully refreshed from Google Patents.
US3990256A
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Method of transporting gas
Assignee: ExxonMobil Technology and Engineering Co
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Filing: 1973-02-26
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Granted: 1976-11-09
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Expires: 1993-02-26
Abstract
Abstract A method of distributing natural gas by pipeline comprising pumping liquefied natural gas (LNG) for a predetermined portion of the desired distance, applying processes in which the refrigeration value of the gas is utilized and the high boiling point components are separated, and then vaporizing the remaining liquid prior to its being further transported by pipeline in the gaseous phase.
Inventors
- 👤 Walter G. May
- 👤 Donald E. Shaneberger
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-05 18:19
CPC Classifications
F; F17; F17C; F17C9/00; F17C9/02; F17C9/04; F17D; F17D1/00; F17D1/02; F17D1/04; F25; F25J; F25J3/00; F25J3/02; F25J3/0204; F25J3/0209; F25J3/0214; F25J3/0228; F25J3/0233; F25J3/0242; F17C2221/00; F17C2221/03; F17C2221/032; F17C2221/033; F17C2223/00; F17C2223/01; F17C2223/0146; F17C2223/0153; F17C2223/0161; F17C2227/00; F17C2227/01; F17C2227/0128; F17C2227/0135; F17C2227/03; F17C2227/0367; F17C2227/0388; F17C2227/0393; F17C2265/00; F17C2265/01; F17C2265/015; Y; Y10; Y10T; Y10T137/00; Y10T137/0318; Y10T137/0324; Y10T137/0329; Y10T137/0352; Y10T137/0391
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
190 words
A method of transporting natural gas comprising: a. liquefying and subcooling the natural gas at a base station; b. pressurizing the liquefied natural gas at said base station to a pressure sufficient to prevent vaporization of said liquefied natural gas due to heat in leakage during transport; c. transporting said liquefied natural gas by pipeline for a predetermined distance until a predetermined approach to the boiling point of said gas is reached; d. repressuring said liquefied natural gas to suppress vaporization; e. repeating steps (c) and (d) until a predetermined optimum temperature and pressure is reached coincident with the arrival of said liquefied natural gas at an intermediate vaporizing station; f. receiving said liquefied natural gas at said intermediate station; g. repressuring and vaporizing said liquefied natural gas completely at the intermediate station to predetermined pressure and temperature suitable for distributing vaporized gas thereby avoiding reliquefaction facilities and including processes which use the refrigeration value of said liquefied natural gas and thereby add heat to said gas; and h. transporting said vaporized natural gas by pipeline from the intermediate station to the terminal station from which the gas is distributed.
Claim 2
Independent Claim
190 words
A method of transporting natural gas comprising: a. liquefying and subcooling the natural gas at a base station; b. pressurizing the liquefied natural gas at said base station to a pressure sufficient to prevent vaporization of said liquefied natural gas due to heat in leakage during transport; c. transporting said liquefied natural gas by pipeline for a predetermined distance until a predetermined approach to the boiling point of said gas is reached; d. repressuring said liquefied natural gas to suppress vaporization; e. repeating steps (c) and (d) until a predetermined optimum temperature and pressure is reached coincident with the arrival of said liquefied natural gas at an intermediate vaporizing station; f. receiving said liquefied natural gas at said intermediate station; g. repressuring and vaporizing said liquefied natural gas completely at the intermediate station to predetermined pressure and temperature suitable for distributing vaporized gas thereby avoiding reliquefaction facilities and including processes which use the refrigeration value of said liquefied natural gas and thereby add heat to said gas; and h. transporting said vaporized natural gas by pipeline from the intermediate station to the terminal station from which the gas is distributed.
Claim 3
Independent Claim
212 words
A method of transporting natural gas comprising: a. liquefying and subcooling the natural gas at a base station; b. pressuring the liquefied natural gas at said base station to a pressure sufficient to prevent vaporization of said liquefied natural gas due to heat in leakage during transport; c. transporting said liquefied natural gas by pipeline for a predetermined distance until a predetermined approach to the boiling point of said gas is reached; d. repressuring said liquefied natural gas to suppress vaporization; e. repeating steps (c) and (d) until a predetermined optimum temperature and pressure is reached coincident with the arrival of said liquefied natural gas at an intermediate vaporizing station; f. receiving said liquefied natural gas at said intermediate station; g. separating said liquefied natural gas at said intermediate station into fractions, at least one of said fractions consisting essentially of methane; h. repressuring and completely vaporizing said fraction consisting essentially of methane at a predetermined pressure and temperature suitable for distributing vaporized gas and wherein this step and step (g) include cold recovery processes for minimizing the energy required in the separation and vaporization processes; and i. transporting said vaporized fraction consisting essentially of methane by pipeline from the intermediate station to the terminal station from which the gas is distributed.
Claim 4
Independent Claim
212 words
A method of transporting natural gas comprising: a. liquefying and subcooling the natural gas at a base station; b. pressuring the liquefied natural gas at said base station to a pressure sufficient to prevent vaporization of said liquefied natural gas due to heat in leakage during transport; c. transporting said liquefied natural gas by pipeline for a predetermined distance until a predetermined approach to the boiling point of said gas is reached; d. repressuring said liquefied natural gas to suppress vaporization; e. repeating steps (c) and (d) until a predetermined optimum temperature and pressure is reached coincident with the arrival of said liquefied natural gas at an intermediate vaporizing station; f. receiving said liquefied natural gas at said intermediate station; g. separating said liquefied natural gas at said intermediate station into fractions, at least one of said fractions consisting essentially of methane; h. repressuring and completely vaporizing said fraction consisting essentially of methane at a predetermined pressure and temperature suitable for distributing vaporized gas and wherein this step and step (g) include cold recovery processes for minimizing the energy required in the separation and vaporization processes; and i. transporting said vaporized fraction consisting essentially of methane by pipeline from the intermediate station to the terminal station from which the gas is distributed.
References Cited (Backward Citations)
US2958205A
Cited
US3656312A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1979-11-09 | 1980-05-10 | 1980-11-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1983-11-09 | 1984-05-10 | 1984-11-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1987-11-09 | 1988-05-10 | 1988-11-09 | $7700.00 | Window Closed / Lapsed |