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Применить Всего найдено 4. Отображено 4.
06-07-2011 дата публикации

Method for liquefying natural gas through double-expansion of high-temperature and low-temperature nitrogen gas

Номер: CN0101614464B
Принадлежит:

The invention discloses a method for liquefying natural gas through double-expansion of high-temperature and low-temperature nitrogen gas, which comprises the followings steps: pressurizing and cooling the nitrogen gas to obtain high-pressure nitrogen gas of 2.2 to 3.6 MPa; introducing the high-pressure nitrogen gas and raw natural gas into a main heat exchanger so that the gas is cooled to a temperature of between 70 DEG C below zero and 30 DEG C below zero by using low-pressure nitrogen gas at the outlet of a low-temperature expander, then extracting one stream of the cooled gas and introducing the cooled gas into a high-temperature expander for expansion refrigeration, and then returning the gas to a position of which the temperature is between 100 DEG C below zero and 80 DEG C below zero in the main heat exchanger; and continuously cooling the other stream of the gas to a temperature of between 110 DEG C below zero and 70 DEG C below zero, then introducing the gas into the low-temperature ...

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30-12-2009 дата публикации

Method for liquefying natural gas through double-expansion of high-temperature and low-temperature nitrogen gas

Номер: CN0101614464A
Принадлежит:

The invention discloses a method for liquefying natural gas through double-expansion of high-temperature and low-temperature nitrogen gas, which comprises the followings steps: pressurizing and cooling the nitrogen gas to obtain high-pressure nitrogen gas of 2.2 to 3.6 MPa; introducing the high-pressure nitrogen gas and raw natural gas into a main heat exchanger so that the gas is cooled to a temperature of between 70 DEG C below zero and 30 DEG C below zero by using low-pressure nitrogen gas at the outlet of a low-temperature expander, then extracting one stream of the cooled gas and introducing the cooled gas into a high-temperature expander for expansion refrigeration, and then returning the gas to a position of which the temperature is between 100 DEG C below zero and 80 DEG C below zero in the main heat exchanger; and continuously cooling the other stream of the gas to a temperature of between 110 DEG C below zero and 70 DEG C below zero, then introducing the gas into the low-temperature ...

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17-08-2011 дата публикации

Method for liquefying high-low pressure nitrogen double-expansion natural gas

Номер: CN0101608859B
Принадлежит:

The invention discloses a method for liquefying high-low pressure nitrogen double-expansion natural gas, which comprises the following steps: compressing and cooling nitrogen gas, and then introducing the nitrogen gas into the pressurizing end of a low-pressure pressurizing machine for pressurization; after cooling the nitrogen gas to a temperature of between 30 and 45 DEG C by a second after cooler, introducing the nitrogen gas into the pressurizing end of a high-pressure pressurizing machine to obtain high-pressure nitrogen gas which is cooled to a temperature of between 30 and 45 DEG C by a first after cooler; introducing the cooled high-pressure nitrogen gas into a main heat exchanger, cooling the nitrogen gas and raw natural gas to a temperature of 70 DEG C below zero and 30 DEG C below zero by the low-pressure nitrogen gas at the outlet of a low-pressure expander, taking out a current of the nitrogen gas which is introduced into a high-pressure expander for expansion refrigeration ...

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23-12-2009 дата публикации

Method for liquefying high-low pressure nitrogen double-expansion natural gas

Номер: CN0101608859A
Принадлежит:

The invention discloses a method for liquefying high-low pressure nitrogen double-expansion natural gas, which comprises the following steps: compressing and cooling nitrogen gas, and then introducing the nitrogen gas into the pressurizing end of a low-pressure pressurizing machine for pressurization; after cooling the nitrogen gas to a temperature of between 30 and 45 DEG C by a second after cooler, introducing the nitrogen gas into the pressurizing end of a high-pressure pressurizing machine to obtain high-pressure nitrogen gas which is cooled to a temperature of between 30 and 45 DEG C by a first after cooler; introducing the cooled high-pressure nitrogen gas into a main heat exchanger, cooling the nitrogen gas and raw natural gas to a temperature of 70 DEG C below zero and 30 DEG C below zero by the low-pressure nitrogen gas at the outlet of a low-pressure expander, taking out a current of the nitrogen gas which is introduced into a high-pressure expander for expansion refrigeration ...

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