JP2008519210A5 - - Google Patents
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- JP2008519210A5 JP2008519210A5 JP2007538975A JP2007538975A JP2008519210A5 JP 2008519210 A5 JP2008519210 A5 JP 2008519210A5 JP 2007538975 A JP2007538975 A JP 2007538975A JP 2007538975 A JP2007538975 A JP 2007538975A JP 2008519210 A5 JP2008519210 A5 JP 2008519210A5
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Claims (35)
実質的に気相状態の天然ガスを第１の場所で輸送容器に荷積みするステップと、
前記輸送容器内の前記天然ガスを冷却して、実質的に液化天然ガスに変換するステップと、
前記液化ガスを前記輸送容器の断熱コンテナ内に貯蔵するステップと、
前記輸送容器の前記液化天然ガスを第１の場所から第２の場所に輸送するステップと、
前記輸送容器の前記液化天然ガスを加熱して実質的に気相に戻すステップと、
前記天然ガスを第２の場所で前記容器から荷降ろしするステップと、を備えている、
ことを特徴とする方法。 A method for transporting liquefied natural gas, comprising:
Loading substantially natural gas in a gas phase into a shipping container at a first location;
Cooling the natural gas in the transport container to convert it to substantially liquefied natural gas;
Storing the liquefied gas in an insulated container of the transport container;
Transporting the liquefied natural gas in the transport container from a first location to a second location;
Heating the liquefied natural gas in the transport container back to a substantially gas phase;
Unloading the natural gas from the container at a second location,
A method characterized by that.
請求項１に記載の方法。 The step of cooling the natural gas and the step of heating the liquefied natural gas are each performed by utilizing a gas processing facility;
The method of claim 1.
請求項２に記載の方法。 The same gas treatment facility is utilized both in cooling the natural gas and heating the liquefied natural gas;
The method of claim 2.
請求項１に記載の方法。 The vessel is a vessel selected from the group consisting of a vessel vessel, a barge vessel, a land-trailer vessel,
The method of claim 1.
前記天然ガスと熱交換流体との間の熱接触によって前記天然ガスを冷却する第１の熱交換器と、
前記熱交換流体が前記第１の熱交換器を貫流した後に圧縮され一時的に加温されるコンプレッサと、
圧縮された前記熱交換流体が冷却される第２の熱交換器と、
圧縮された前記熱交換流体が更に冷却され、前記第１の熱交換器を通って戻る前に減圧されるエキスパンダーと、
を備えるガス処理施設を利用することによって行われる、
請求項１に記載の方法。 Cooling the natural gas comprises:
A first heat exchanger that cools the natural gas by thermal contact between the natural gas and a heat exchange fluid;
A compressor that is compressed and temporarily warmed after the heat exchange fluid flows through the first heat exchanger;
A second heat exchanger in which the compressed heat exchange fluid is cooled;
An expander in which the compressed heat exchange fluid is further cooled and depressurized before returning through the first heat exchanger;
By using a gas processing facility comprising
The method of claim 1.
前記天然ガスと熱交換流体との間の熱接触によって前記天然ガスを加温する第１の熱交換器と、
前記熱交換流体が前記第１の熱交換器を貫流した後に加温される第２の熱交換器と、
熱交換流体運動装置と、
を備えたガス処理施設を利用することによって行われる、
請求項１に記載の方法。 Heating the natural gas comprises:
A first heat exchanger that heats the natural gas by thermal contact between the natural gas and a heat exchange fluid;
A second heat exchanger that is heated after the heat exchange fluid has flowed through the first heat exchanger;
A heat exchange fluid motion device;
By using a gas processing facility with
The method of claim 1.
請求項６に記載の方法。 The heat exchange fluid motion device comprises a compressor that is compressed and further warmed after the heat exchange fluid has flowed through the second heat exchanger and before returning through the first heat exchanger. ing,
The method of claim 6.
請求項６に記載の方法。 The fluid motion device comprises a pump disposed in-line between the first and second heat exchangers to compress a liquefied heat exchange fluid;
The method of claim 6.
請求項６に記載の方法。 The second heat exchanger heats the heat exchange fluid by thermal contact between the heat exchange fluid and at least one of seawater, air, and a combustion source at ambient ocean temperature;
The method of claim 6.
請求項６に記載の方法。 The heat exchange fluid is heated by thermal contact with an intermediate fluid, and the intermediate fluid itself is heated by a combustion source outside the second heat exchanger.
The method of claim 6.
請求項５または６に記載の方法。 The heat exchange fluid comprises lower hydrocarbons,
The method according to claim 5 or 6.
（ａ）前記天然ガスと冷媒として働く熱交換流体との間の熱接触によって前記天然ガスを冷却する第１の熱交換器と、
前記冷媒が前記第１の熱交換器を貫流した後に圧縮されて一時的に加温されるコンプレッサと、
前記圧縮された冷媒が冷却される第２の熱交換器と、
前記圧縮された冷媒が更に前記第１の熱交換器を通って戻る前に冷却され減圧されるエキスパンダーと、を提供することによって前記天然ガスを冷却し、
（ｂ）前記天然ガスと前記熱交換流体との間の熱接触によって前記天然ガスを加温する前記第１の熱交換器と、
前記熱交換流体が前記第１の熱交換器を貫流した後に加温される前記第２の熱交換器と、
流体運動装置と、を提供することによって前記天然ガスを加熱する、
単一のガス処理施設を利用することによって各々行われる、
ことを特徴とする請求項１に記載の方法。 Cooling the natural gas and heating the liquefied natural gas;
(A) a first heat exchanger that cools the natural gas by thermal contact between the natural gas and a heat exchange fluid that acts as a refrigerant;
A compressor that is compressed and temporarily warmed after the refrigerant flows through the first heat exchanger;
A second heat exchanger in which the compressed refrigerant is cooled;
Cooling the natural gas by providing an expander that is cooled and depressurized before the compressed refrigerant further returns through the first heat exchanger;
(B) the first heat exchanger that heats the natural gas by thermal contact between the natural gas and the heat exchange fluid;
The second heat exchanger heated after the heat exchange fluid has flowed through the first heat exchanger;
Heating the natural gas by providing a fluid motion device;
Each done by utilizing a single gas processing facility,
The method according to claim 1.
請求項１２に記載の方法。 The fluid motion device comprises a compressor that is compressed and further warmed after the heat exchange fluid has flowed through the second heat exchanger and before returning through the first heat exchanger.
The method of claim 12.
請求項１２に記載の方法。 The fluid motion device comprises a pump disposed in-line between the first and second heat exchangers to pressurize the liquefied heat exchange fluid;
The method of claim 12.
請求項１２に記載の方法。 The heat exchange fluid that cools the natural gas and the heat exchange fluid that heats the natural gas are at least partially different;
The method of claim 12.
前記輸送容器用のガス移送システムを提供するステップと、
前記天然ガスを選択的に冷却し加熱するガス処理施設を前記輸送容器に提供するステップと、
基本的に気相状態にある前記天然ガスを前記ガス移送システムを通って前記輸送容器に荷積みするステップと、
前記天然ガスが実質的に液化状態にある低温まで前記天然ガスを冷却するように前記ガス処理施設を通って前記天然ガスを貫流させるステップと、
輸送中に前記液化天然ガスを収容するために前記輸送容器に格納構造体を提供するステップと、を備えている、
ことを特徴とする方法。 A method for transporting liquefied natural gas in a transport container, comprising:
Providing a gas transfer system for the transport container;
Providing the transport container with a gas treatment facility for selectively cooling and heating the natural gas;
Loading the natural gas in a gas phase state into the transport container through the gas transfer system;
Flowing the natural gas through the gas processing facility to cool the natural gas to a low temperature at which the natural gas is substantially in a liquefied state;
Providing a containment structure in the transport container for containing the liquefied natural gas during transport,
A method characterized by that.
前記ガス移送システムを通って前記輸送容器から前記天然ガスを荷降ろしするステップと、を更に含む、
請求項１６に記載の方法。 Through the gas processing facility to heat the natural gas from a temperature at which the natural gas is in a substantially liquefied state to a temperature at which the natural gas is at least partially converted back to the gas phase and returned. Pumping natural gas; and
Unloading the natural gas from the transport container through the gas transfer system;
The method of claim 16.
請求項１６に記載の方法。 The transport container is a container selected from the group consisting of a ship container, a barge container, and a land transport trailer container;
The method of claim 16.
請求項１６に記載の方法。 The gas transfer system comprises a connection for receiving a buoy line and thereby placing the gas processing facility in fluid communication with a marine jumper line;
The method of claim 16.
請求項１６に記載の方法。 The gas transfer system comprises a connection for receiving a line for placing the gas treatment facility in fluid communication with a hose;
The method of claim 16.
請求項１６に記載の方法。 The containment structure is a plurality of pressure vessels for maintaining the liquefied natural gas in a pressurized state;
The method of claim 16.
前記天然ガスが熱交換流体と熱的に接触する少なくとも１つの熱交換器と、
前記熱交換流体を圧縮する少なくとも１つのコンプレッサと、を備えている、
請求項１６に記載の方法。 The gas processing facility is:
At least one heat exchanger in which the natural gas is in thermal contact with a heat exchange fluid;
And at least one compressor for compressing the heat exchange fluid.
The method of claim 16.
前記天然ガスと熱交換流体との間の熱接触によって天然ガスを冷却する第１の熱交換器と、
前記熱交換流体が前記第１の熱交換器を貫流した後に圧縮されるコンプレッサと、
圧縮された熱交換流体が冷却される第２の熱交換器と、
圧縮された熱交換流体が減圧され、前記第１の熱交換器を通って戻る前に更に冷却されるエキスパンダーと、
を提供することによって前記天然ガスを冷却する、
請求項１６に記載の方法。 The gas treatment facility is
A first heat exchanger that cools the natural gas by thermal contact between the natural gas and a heat exchange fluid;
A compressor that is compressed after the heat exchange fluid has flowed through the first heat exchanger;
A second heat exchanger in which the compressed heat exchange fluid is cooled;
An expander in which the compressed heat exchange fluid is depressurized and further cooled before returning through the first heat exchanger;
Cooling the natural gas by providing
The method of claim 16.
前記天然ガスと熱交換流体との間の熱接触によって前記天然ガスを加温する第１の熱交換器と、
前記熱交換流体が前記第１の熱交換器を貫流した後に加温される第２の熱交換器と、
流体運動装置と、
を提供することによって前記天然ガスを加熱する、
請求項１６に記載の方法。 The gas treatment facility is
A first heat exchanger that heats the natural gas by thermal contact between the natural gas and a heat exchange fluid;
A second heat exchanger that is heated after the heat exchange fluid has flowed through the first heat exchanger;
A fluid motion device;
Heating the natural gas by providing
The method of claim 16.
請求項２４に記載の方法。 The second heat exchanger heats the heat exchange fluid by thermal contact between the heat exchange fluid and seawater, air, and a combustion source at ambient ocean temperature;
25. A method according to claim 24.
請求項２４に記載の方法。 The heat exchange fluid is heated by thermal contact with an intermediate fluid, and the intermediate fluid itself is heated by a combustion source outside the second heat exchanger;
25. A method according to claim 24.
（ａ）前記天然ガスと冷媒として働く熱交換流体との間の熱接触によって前記天然ガスを冷却する第１の熱交換器と、
前記冷媒が前記第１の熱交換器を貫流した後に圧縮されて一時的に加温されるコンプレッサと、
前記圧縮された冷媒が冷却される第２の熱交換器と、
前記圧縮された冷媒が前記第１の熱交換器を通って戻る前に更に減圧され更に冷却されるエキスパンダーと、
を提供することによって前記天然ガスを冷却し、
（ｂ）前記天然ガスと前記熱交換流体との間の熱接触によって前記天然ガスを加温する前記第１の熱交換器と、
前記熱交換流体が前記第１の熱交換器を貫流した後に加温される前記第２の熱交換器と、
前記熱交換流体が前記第２の熱交換器を貫流した後及び前記第１の熱交換器を通って戻る前に圧縮され更に加温される前記コンプレッサと、を提供することによって前記天然ガスを加熱する、
請求項１６に記載の方法。 The gas treatment facility is
(A) a first heat exchanger that cools the natural gas by thermal contact between the natural gas and a heat exchange fluid that acts as a refrigerant;
A compressor that is compressed and temporarily warmed after the refrigerant flows through the first heat exchanger;
A second heat exchanger in which the compressed refrigerant is cooled;
An expander that is further reduced in pressure and further cooled before the compressed refrigerant returns through the first heat exchanger;
Cooling the natural gas by providing
(B) the first heat exchanger that heats the natural gas by thermal contact between the natural gas and the heat exchange fluid;
The second heat exchanger heated after the heat exchange fluid has flowed through the first heat exchanger;
The compressor by which the heat exchange fluid is compressed and further heated after flowing through the second heat exchanger and before returning through the first heat exchanger. To heat,
The method of claim 16.
基本的に気相状態の容器との間で天然ガスを荷積み及び荷降ろしするためのガス移送システムと、
（ｉ）前記天然ガスが気相状態にある温度から、前記天然ガスが実質的に液化状態にある低温まで前記天然ガスを冷却すること、
（ｉｉ）天然ガスが実質的に液化状態にある温度から、前記天然ガスが気相に変換して戻る温度まで前記天然ガスを加熱すること、
を選択的に行うためのガス処理施設と、
前記ガス処理施設に給電するための発電機と、
輸送中に前記液化天然ガスを収容するための格納構造体と、を備えている、
ことを特徴とする容器。 A container for transporting liquefied natural gas,
A gas transfer system for loading and unloading of natural gas to and from a container in essentially a gas phase;
(I) cooling the natural gas from a temperature at which the natural gas is in a gas phase state to a low temperature at which the natural gas is substantially in a liquefied state;
(Ii) heating the natural gas from a temperature at which the natural gas is substantially in a liquefied state to a temperature at which the natural gas is converted back to a gas phase;
Gas processing facility for selectively performing,
A generator for supplying power to the gas processing facility;
A containment structure for containing the liquefied natural gas during transportation,
A container characterized by that.
請求項２８に記載の容器。 The vessel is a vessel selected from the group consisting of a vessel vessel, a barge vessel, and a land transport trailer vessel;
The container according to claim 28.
前記天然ガスが格納構造体内に貯蔵されるときに前記容器を推進するよう動力を供給すること、および、
前記天然ガスが冷却又は加熱されるときに前記ガス処理施設に給電すること、
を選択的に行う、
請求項２８に記載の容器。 The generator is
Providing power to propel the container when the natural gas is stored in a containment structure; and
Supplying power to the gas treatment facility when the natural gas is cooled or heated;
Selectively,
The container according to claim 28.
請求項３０に記載の容器。 Auxiliary compressor for circulating and cooling the heat exchange fluid while the transport vessel is transporting LNG to recondensate any natural gas that vaporizes during transport or to maintain a low temperature in the gas treatment facility Further comprising
The container according to claim 30.
沖合天然ガス生産システムから実質的に未処理の流体を受け取る輸送容器用ガス移送システムを提供するステップと、
他のあらゆる生成流体から生成されたガスを分離するための流体処理システムを提供するステップと、
前記天然ガス生産システムから生産された流体を荷積みするステップと、
前記生産されたガスを液化天然ガスに変換するために前記輸送容器にガス処理設備を提供するステップと、
前記ガス処理施設を通ってガスを貫流させて前記天然ガスを周囲温度から天然ガスが実質的に液化相である低温まで冷却するようにするステップと、
輸送中に前記液化天然ガスを収容するため前記容器に格納構造体を提供するステップと、
前記容器の前記液化天然ガスを加熱して実質的に気相に再変換するステップと、備えている、
ことを特徴とする方法。 A method for transporting liquefied natural gas on a ship, comprising:
Providing a transport container gas transfer system for receiving substantially unprocessed fluid from an offshore natural gas production system;
Providing a fluid treatment system for separating gas produced from any other product fluid;
Loading the fluid produced from the natural gas production system;
Providing a gas processing facility to the transport vessel to convert the produced gas to liquefied natural gas;
Allowing gas to flow through the gas treatment facility to cool the natural gas from ambient temperature to a low temperature where the natural gas is substantially in a liquefied phase;
Providing a containment structure in the container for containing the liquefied natural gas during transport;
Heating the liquefied natural gas in the vessel to substantially reconvert it to the gas phase,
A method characterized by that.
請求項３２記載の方法。 Further comprising providing a separate containment structure in the container for containing any manufactured liquid hydrocarbons during transport;
The method of claim 32.
請求項３２に記載の方法。 The gas is unloaded into a gas storage device at an export location;
The method of claim 32.
請求項３４に記載の方法。 The gas storage device is an underground salt dome gas storage cave,
35. The method of claim 34.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US62538804P | 2004-11-05 | 2004-11-05 | |
| PCT/US2005/037245 WO2006052392A2 (en) | 2004-11-05 | 2005-10-17 | Lng transportation vessel and method for transporting hydrocarbons |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2008519210A JP2008519210A (en) | 2008-06-05 |
| JP2008519210A5 true JP2008519210A5 (en) | 2008-12-04 |
Family
ID=34956490
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2007538975A Pending JP2008519210A (en) | 2004-11-05 | 2005-10-17 | LNG transport container and method for transporting hydrocarbons |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20080127673A1 (en) |
| JP (1) | JP2008519210A (en) |
| KR (1) | KR20070085611A (en) |
| CA (1) | CA2585211A1 (en) |
| WO (1) | WO2006052392A2 (en) |
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