US3674086A - Method of transporting oil or gas in frozen tundra - Google Patents

Method of transporting oil or gas in frozen tundra Download PDF

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US3674086A
US3674086A US61982A US3674086DA US3674086A US 3674086 A US3674086 A US 3674086A US 61982 A US61982 A US 61982A US 3674086D A US3674086D A US 3674086DA US 3674086 A US3674086 A US 3674086A
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gas
oil
pipe
pipeline
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US61982A
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Alden W Foster
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ALDEN W FOSTER
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ALDEN W FOSTER
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F16ENGINEERING ELEMENTS AND UNITS; GENERAL MEASURES FOR PRODUCING AND MAINTAINING EFFECTIVE FUNCTIONING OF MACHINES OR INSTALLATIONS; THERMAL INSULATION IN GENERAL
    • F16LPIPES; JOINTS OR FITTINGS FOR PIPES; SUPPORTS FOR PIPES, CABLES OR PROTECTIVE TUBING; MEANS FOR THERMAL INSULATION IN GENERAL
    • F16L9/00Rigid pipes
    • F16L9/18Double-walled pipes; Multi-channel pipes or pipe assemblies
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B36/00Heating, cooling, insulating arrangements for boreholes or wells, e.g. for use in permafrost zones
    • E21B36/003Insulating arrangements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17DPIPE-LINE SYSTEMS; PIPE-LINES
    • F17D1/00Pipe-line systems
    • F17D1/08Pipe-line systems for liquids or viscous products
    • F17D1/084Pipe-line systems for liquids or viscous products for hot fluids

Definitions

  • ABSTRACT [52] U.S.Cl .T ..165/1,l6l/45,6 l/35, A method of preventing softening or thawing of the per- 12/260 mafrost zone while producing or transporting hot oil or gas [51] Int. Cl ..F25d 23/12 therethmugh in which a
  • i fi d hydrocarbon gas f bl [58] Field Of Search ..l65/45; 62/260; 61/35, 36 natural gas is passed between the zone and the hot oil.
  • gas may be circulated in a suitable system.
  • This invention relates to a method of oil and gas recovery from the earth and more particularly to a method of producing or transporting hot oil or gas through frozen tundra such as the Alaskan permafrost layer.
  • my method involves passing a liquefied hydrocarbon gas through suitable apparatus, preferably one which enables circulation of the gas, down through an annulus formed between two concentric strings of pipe or casing in an oil or gas well, and up through an annulus between the inner one of said strings and a third concentric string.
  • the gas is circulated to that depth necessary to provide complete protection of the permafrost zone.
  • the hot oil may be transported in the inner of two concentric pipes with the liquefied hydrocarbon gas being passed through an annulus between the pipes. In either case, the flow of the hydrocarbon gas is parallel to the flow of the oil or gas being produced or transported. Under some circumstances, it may be desirable to place insulation around the outer surface of the pipeline.
  • 3,220,470 disclose certain refrigerants to be useful for maintaining earth in a frozen condition
  • a method such as mine utilizing liquefied hydrocarbon gases methane, ethane, butane, propane, ethylene, and others which are abundantin the Arctic region, as a means for maintaining the permafrost zone in a frozen condition in areas near oil and gas wells or pipelines.
  • hydrocarbon gases include natural gas, which may be liquefied at temperatures down to 260 F, substantially below any temperature envisioned by the prior art.
  • FIG. 1 is a diagrammatic elevation view partly in section of apparatus useful in carrying out my method
  • the gas is circulated as shown by the arrows in FIG. 2 is a sectional view in reduced scale taken on lines II-II of FIG. I;
  • FIG. 3 is a sectional view of a portion of a transfer oil-and gas pipeline between pumping stations which illustrates my invention.
  • a part of a conventional oil producing string 1 extends from a reservoir (not shown) located below a permafrost zone 2 of the frozen tundra.
  • the string 1 is suitably connected to an oil collecting means, such as a storage tank or to other equipment, e.g., a gas separator, for preliminary processing.
  • a suitable apparatus for performing my method in a well comprises jacketing the oil producing string 1 with a first pipe or casing 3 which is positioned concentrically with respect to string 1.
  • a second pipe or casing 4 is positioned concentrically withrespect to the string 1 and casing 3.
  • the lower end of casing 4 is cemented in the well, as at 4a.
  • Casings 3 and 4 are con-, nected at the surface to conventional liquification equipment 5 and are of sufficient length to penetrate the earth to a depth greater than the depth of the permafrost zone, where they are suitably joined in fluid communication with one another to form a continuous circulation system.
  • FIG. 1 and suitable check valves 6 are provided to prevent reversal of the cycle. Stated otherwise, referring to FIG. I, a
  • liquid hydrocarbon gas is circulated from liquefaction equipment 5 down through the annulus 7 between the wall of casing 4 and the wall of casing 3. Thereafter, the gas passes around the lowerend of easing 3and rises in the annulus 8 between the wall of easing 3 and the producing pipe I.
  • the condition of the hydrocarbon gas at any point in its cycle is a function of its temperature and pressure. As the gas circulates in the system, it may gradually change from liquid to vapor state due to its close proximity to the hot oil which is produced through pipe 1. If the gas is cooled to a sufficiently low temperature prior to pumping it into the well, it may be maintained in the liquid state throughout the cycle; however, the extent to which the gas can be cooled is limited by the cost of liquefying it and because excessive heat transfer from the hot oil to the gas would tend to impede the flow of the oil being produced.
  • the temperature of the oil may be in the range of l50l80 F, but for the protection afforded by the circulation of the liquefied gas, it-is certain that the permafrost zone would be softened or melted, leading to the complications previously described, by heat transfer from the high temperature oil produced.
  • a laterally extending pipeline for transferring hot oil and gas comprises a transfer pipe 10 having a concentrically disposed jacket or pipe 11.
  • Hot oil flows through the transfer pipe 10 while a liquefied hydrocarbon gas is passed through annulus 12 formed by the walls of pipe 10 and pipe 11 to protect the frozen permafrost zone 13 from the effects of the substantially higher temperature of the hot oil.
  • insulation 14 is placed on the outer surface of pipe 11.
  • Hydrocarbon gases preferably liquefied natural gas
  • liquefied natural gas comprise the medium for protecting the permafrost from the softening effect of the hot oil being produced or transferred. While any hydrocarbon gas may be used, for instance, propane, ethylene, etc., the large supply of natural gas in the Arctic region suggests its use for economic reasons.
  • liquefaction of natural gas may be accomplished in accordance with known techniques with a minimum of specialized equipment.
  • a method of transporting oil or gas at elevated temperatures in a pipeline through a permafrost zone of earth comprising:
  • hydrocarbon gas is one of methane, ethane, butane, ethylene, and propane.
  • a method as set forth in claim 4 in which a plurality of lengths of pipe are disposed end to end to provide a continuous pipeline.

Abstract

A method of preventing softening or thawing of the permafrost zone while producing or transporting hot oil or gas therethrough in which a liquefied hydrocarbon gas, preferably natural gas, is passed between the zone and the hot oil. The gas may be circulated in a suitable system.

Description

0 United States Patent [151 Foster Y July.4, 1972 [54] METHOD OF TRANSPORTING OIL 0 [56] References Cited GAS [N FROZEN TUNDRA UNlTED STATESPATENTS [72] lnventor: Alden W. Foster, 1207 Beaver St., 3,564,862 9/1969 Hashemi et al. ..62/260 Sewickley, Pa. l5l43 I 1 Primary Examiner-Charles Sukalo Attorney-Webb, Burden, Robinson & Webb [21] AP No.1 61,982
r [57] ABSTRACT [52] U.S.Cl .T ..165/1,l6l/45,6 l/35, A method of preventing softening or thawing of the per- 12/260 mafrost zone while producing or transporting hot oil or gas [51] Int. Cl ..F25d 23/12 therethmugh in which a |i fi d hydrocarbon gas f bl [58] Field Of Search ..l65/45; 62/260; 61/35, 36 natural gas is passed between the zone and the hot oil. The
gas may be circulated in a suitable system.
6 Claims, 3 Drawing Figures GAS I TANK Fm LIQUEFACTION EQUIPMENT GAS OUT
METHOD OF TRANSPORTING OIL R GAS IN FROZEN TUNDRA This invention relates to a method of oil and gas recovery from the earth and more particularly to a method of producing or transporting hot oil or gas through frozen tundra such as the Alaskan permafrost layer.
Substantial difficulty has been encountered when producing oil and gas at elevated temperaturesfrom subsurface reservoirs in cold climates. As the hot oil or gas passes throughthe permafrost zone, its heat softens or melts the zone which may result in destruction of the oil or gas producing strings or buckling of the surface rigs used in producing oil or gas, or pipelines for transporting it, unless special precautions are taken.
Ihave invented a novel method for preventing the thawing or softening of the permafrost zone which surrounds the upper portion of the casing or string of oil and gas wells drilled, or oil, gas or oil product pipelines laid, in extremely cold climates, such as the Arctic region, where the permafrost zone extends to depths of 1,000 feet or more below the surface. In the case of wells, my method involves passing a liquefied hydrocarbon gas through suitable apparatus, preferably one which enables circulation of the gas, down through an annulus formed between two concentric strings of pipe or casing in an oil or gas well, and up through an annulus between the inner one of said strings and a third concentric string. The gas is circulated to that depth necessary to provide complete protection of the permafrost zone. In the case of oil or gas pipelines, the hot oil may be transported in the inner of two concentric pipes with the liquefied hydrocarbon gas being passed through an annulus between the pipes. In either case, the flow of the hydrocarbon gas is parallel to the flow of the oil or gas being produced or transported. Under some circumstances, it may be desirable to place insulation around the outer surface of the pipeline.
Although prior patents, for example, Balch US. Pat. No.
3,220,470, disclose certain refrigerants to be useful for maintaining earth in a frozen condition, I am not aware of any prior patent or publication which proposes a method such as mine utilizing liquefied hydrocarbon gases methane, ethane, butane, propane, ethylene, and others which are abundantin the Arctic region, as a means for maintaining the permafrost zone in a frozen condition in areas near oil and gas wells or pipelines. Such hydrocarbon gases include natural gas, which may be liquefied at temperatures down to 260 F, substantially below any temperature envisioned by the prior art.
An understanding of my invention will be facilitated by the consideration of the following description taken with the accompanying drawings in which:
FIG. 1 is a diagrammatic elevation view partly in section of apparatus useful in carrying out my method;
Preferably, the gas is circulated as shown by the arrows in FIG. 2 is a sectional view in reduced scale taken on lines II-II of FIG. I; and
FIG. 3 is a sectional view of a portion of a transfer oil-and gas pipeline between pumping stations which illustrates my invention.
In FIGS. 1 and 2, a part of a conventional oil producing string 1 extends from a reservoir (not shown) located below a permafrost zone 2 of the frozen tundra. The string 1 is suitably connected to an oil collecting means, such as a storage tank or to other equipment, e.g., a gas separator, for preliminary processing.
A suitable apparatus for performing my method in a well comprises jacketing the oil producing string 1 with a first pipe or casing 3 which is positioned concentrically with respect to string 1. A second pipe or casing 4 is positioned concentrically withrespect to the string 1 and casing 3. The lower end of casing 4 is cemented in the well, as at 4a. Casings 3 and 4 are con-, nected at the surface to conventional liquification equipment 5 and are of sufficient length to penetrate the earth to a depth greater than the depth of the permafrost zone, where they are suitably joined in fluid communication with one another to form a continuous circulation system.
FIG. 1 and suitable check valves 6 are provided to prevent reversal of the cycle. Stated otherwise, referring to FIG. I, a
liquid hydrocarbon gas is circulated from liquefaction equipment 5 down through the annulus 7 between the wall of casing 4 and the wall of casing 3. Thereafter, the gas passes around the lowerend of easing 3and rises in the annulus 8 between the wall of easing 3 and the producing pipe I.
The condition of the hydrocarbon gas at any point in its cycle is a function of its temperature and pressure. As the gas circulates in the system, it may gradually change from liquid to vapor state due to its close proximity to the hot oil which is produced through pipe 1. If the gas is cooled to a sufficiently low temperature prior to pumping it into the well, it may be maintained in the liquid state throughout the cycle; however, the extent to which the gas can be cooled is limited by the cost of liquefying it and because excessive heat transfer from the hot oil to the gas would tend to impede the flow of the oil being produced. Since the temperature of the oil may be in the range of l50l80 F, but for the protection afforded by the circulation of the liquefied gas, it-is certain that the permafrost zone would be softened or melted, leading to the complications previously described, by heat transfer from the high temperature oil produced.
In a second embodiment, shown in FIG. 3, a laterally extending pipeline for transferring hot oil and gas comprises a transfer pipe 10 having a concentrically disposed jacket or pipe 11. Hot oil flows through the transfer pipe 10 while a liquefied hydrocarbon gas is passed through annulus 12 formed by the walls of pipe 10 and pipe 11 to protect the frozen permafrost zone 13 from the effects of the substantially higher temperature of the hot oil. Where desirable, insulation 14 is placed on the outer surface of pipe 11. An additional advantage of such a pipeline is that not only may the oil be transported, but the gas itself may bemovcd considerable distances in the pipeline, for example, from Alaska to the United States.
Hydrocarbon gases, preferably liquefied natural gas, comprise the medium for protecting the permafrost from the softening effect of the hot oil being produced or transferred. While any hydrocarbon gas may be used, for instance, propane, ethylene, etc., the large supply of natural gas in the Arctic region suggests its use for economic reasons. In addition, liquefaction of natural gas may be accomplished in accordance with known techniques with a minimum of specialized equipment.
Although refrigerants have been used before to maintain soil in frozen condition, to my knowledge, liquefied hydrocarbon gases have not been used in oil and gas producing and transporting operations in which the oil or gas is at such a high temperature as to effect softening or even melting of the permafrost zone. The extremely low temperatures of the liquefied hydrocarbon gases virtually insure complete protection of the permafrost layer during production and'transportation of oil or gas at elevated temperatures.
Iclaim:
l. A method of transporting oil or gas at elevated temperatures in a pipeline through a permafrost zone of earth comprising:
A. Surrounding that part of a first pipe which extends through the permafrost zone with a second pipe to form an annulus between said pipes;
B. Passing a liquified hydrocarbon gas through said annulus in a path parallel to the path of oil or gas passing through said first pipe; and
C. Maintaining the temperature of said hydrocarbon gas sufficiently low to prevent heat transfer from said oil or gas to said permafrost zone.
2. A method as set forth in claim 1 in which the hydrocarbon gas is one of methane, ethane, butane, ethylene, and propane.
3. A method as set forth in claim 1 in which the hydrocarbon gas is natural gas.
D. Maintaining the temperature of the hydrocarbon gas sufficientlylow to prevent the'permafrost zone adjacent the pipe from softening.
5. A method as set forth in claim 4 in which the temperature of the liquid natural gas is maintained by passing it throug pumping stations located along the pipeline.
6. A method as set forth in claim 4 in which a plurality of lengths of pipe are disposed end to end to provide a continuous pipeline.

Claims (5)

  1. 2. A method as set forth in claim 1 in which the hydrocarbon gas is one of methane, ethane, butane, ethylene, and propane.
  2. 3. A method as set forth in claim 1 in which the hydrocarbon gas is natural gas.
  3. 4. A method of protecting a permafrost zone from softening under the influence of heat from oil or gas being transported in a pipeline therethrough comprising: A. Extending a length of pipe to form a part of the pipeline substantially horizontally in said zone; B. Surrounding the pipe with a jacket to provide an annulus between the pipe and the jacket; C. Passing a liquified hydrocarbon gas through said annulus in a path parallel to the path of oil or gas passing in the pipe; and D. Maintaining the temperature of the hydrocarbon gas sufficiently low to prevent the permafrost zone adjacent the pipe from softening.
  4. 5. A method as set forth in claim 4 in which the temperature of the liquid natural gas is maintained by passing it through pumping stations located along the pipeline.
  5. 6. A method as set forth in claim 4 in which a plurality of lengths of pipe are disposed end to end to provide a continuous pipeline.
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Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3730201A (en) * 1971-03-16 1973-05-01 K Lefever Transmission of mixed petroleum products through a frozen medium
US3768547A (en) * 1971-02-04 1973-10-30 Dow Chemical Co Arrangement to control heat flow between a member and its environment
US3777502A (en) * 1971-03-12 1973-12-11 Newport News Shipbuilding Dry Method of transporting liquid and gas
US3840035A (en) * 1971-03-15 1974-10-08 K Lefever Transmission of petroleum products through a frozen medium
US3859800A (en) * 1973-03-15 1975-01-14 Dow Chemical Co Air convection device 2 a.g. for permafrost stabilization
US3882937A (en) * 1973-09-04 1975-05-13 Union Oil Co Method and apparatus for refrigerating wells by gas expansion
US3943965A (en) * 1973-09-07 1976-03-16 Matelena John J Pipeline for transporting petroleum products through tundra
US3984059A (en) * 1973-03-13 1976-10-05 Robert Henry Davies Liquid handling
US4607488A (en) * 1984-06-01 1986-08-26 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Ground congelation process and installation
US20130319532A1 (en) * 2012-06-04 2013-12-05 Elwha LLC, a limited liability company of the State of Delaware Fluid recovery in chilled clathrate transportation systems
US20130319531A1 (en) * 2012-06-04 2013-12-05 Elwha Llc Chilled clathrate transportation system
EP2730831A1 (en) * 2012-11-08 2014-05-14 Linde Aktiengesellschaft Pipeline apparatus
US9310023B2 (en) 2013-06-20 2016-04-12 The Boeing Company Methods and systems for distributing inert gas in an aircraft
WO2019123008A2 (en) 2017-12-20 2019-06-27 Acergy France SAS Insulation of pipe-in-pipe systems

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3564862A (en) * 1969-09-12 1971-02-23 Hadi T Hashemi Method and apparatus for supporing a pipeline in permafrost environment

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3564862A (en) * 1969-09-12 1971-02-23 Hadi T Hashemi Method and apparatus for supporing a pipeline in permafrost environment

Cited By (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3768547A (en) * 1971-02-04 1973-10-30 Dow Chemical Co Arrangement to control heat flow between a member and its environment
US3777502A (en) * 1971-03-12 1973-12-11 Newport News Shipbuilding Dry Method of transporting liquid and gas
US3840035A (en) * 1971-03-15 1974-10-08 K Lefever Transmission of petroleum products through a frozen medium
US3730201A (en) * 1971-03-16 1973-05-01 K Lefever Transmission of mixed petroleum products through a frozen medium
US3984059A (en) * 1973-03-13 1976-10-05 Robert Henry Davies Liquid handling
US3859800A (en) * 1973-03-15 1975-01-14 Dow Chemical Co Air convection device 2 a.g. for permafrost stabilization
US3882937A (en) * 1973-09-04 1975-05-13 Union Oil Co Method and apparatus for refrigerating wells by gas expansion
US3943965A (en) * 1973-09-07 1976-03-16 Matelena John J Pipeline for transporting petroleum products through tundra
US4607488A (en) * 1984-06-01 1986-08-26 L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude Ground congelation process and installation
US20130319532A1 (en) * 2012-06-04 2013-12-05 Elwha LLC, a limited liability company of the State of Delaware Fluid recovery in chilled clathrate transportation systems
US20130319538A1 (en) * 2012-06-04 2013-12-05 Elwha LLC, a limited liability company of the State of Delaware Direct cooling of clathrate flowing in a pipeline system
US20130319531A1 (en) * 2012-06-04 2013-12-05 Elwha Llc Chilled clathrate transportation system
US9303819B2 (en) * 2012-06-04 2016-04-05 Elwha Llc Fluid recovery in chilled clathrate transportation systems
US9464764B2 (en) * 2012-06-04 2016-10-11 Elwha Llc Direct cooling of clathrate flowing in a pipeline system
US9822932B2 (en) * 2012-06-04 2017-11-21 Elwha Llc Chilled clathrate transportation system
EP2730831A1 (en) * 2012-11-08 2014-05-14 Linde Aktiengesellschaft Pipeline apparatus
US8893748B2 (en) 2012-11-08 2014-11-25 Linde Aktiengesellschaft Pipeline for high pressure cryogenic applications
US9310023B2 (en) 2013-06-20 2016-04-12 The Boeing Company Methods and systems for distributing inert gas in an aircraft
WO2019123008A2 (en) 2017-12-20 2019-06-27 Acergy France SAS Insulation of pipe-in-pipe systems

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