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

A natural gas, high and low pressure technology, applied in the field of high and low pressure nitrogen double expansion natural gas liquefaction, to achieve the effect of good liquefaction effect and high liquefaction rate

Active Publication Date: 2011-08-17
HANGZHOU FORTUNE CRYOGENIC EQUIP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, there is no high-low pressure nitrogen expansion refrigeration liquefaction process. Here we mainly introduce the high-low pressure nitrogen double-expansion natural gas liquefaction process. This process is a kind of nitrogen double-expansion process.

Method used

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

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0019] The high and low pressure nitrogen double expansion natural gas liquefaction method comprises the following steps:

[0020] a. Nitrogen is compressed to 2.0MPa and cooled to 30°C;

[0021] b. After the nitrogen gas obtained in step a enters the booster end of the low-pressure booster 2 for pressurization, it is cooled to 30°C by the second aftercooler 4, and then enters the booster end of the high-pressure booster 1 to obtain 3.6MPa high-pressure nitrogen. , 3.6MPa high-pressure nitrogen is cooled to 30°C by the first aftercooler 3;

[0022] c. The cooled high-pressure nitrogen gas enters the main heat exchanger 9 and 1.0MPaMpa raw natural gas is cooled to -30°C by the 0.4MPa low-pressure nitrogen gas at the outlet of the low-pressure expander 6, and then one stream is drawn out and sent to the high-pressure expander 5 for high-pressure expansion Machine 5 expands and refrigerates at a high pressure of 4.0MPa and a high temperature of -50°C, with an expansion ratio of ...

Embodiment 2

[0025] The high and low pressure nitrogen double expansion natural gas liquefaction method comprises the following steps:

[0026] a. Nitrogen is compressed to 3.0MPa and cooled to 45°C;

[0027] b. After the nitrogen gas obtained in step a enters the booster end of the low-pressure booster 2 for pressurization, it is cooled to 45°C by the second aftercooler 4, and then enters the booster end of the high-pressure booster 1 to obtain 5.3MPa high-pressure nitrogen. , 5.3MPa high-pressure nitrogen is cooled to 45°C by the first aftercooler 3;

[0028] c. The cooled high-pressure nitrogen gas enters the main heat exchanger 9 and 1.0MPa ~ 10Mpa raw natural gas is cooled to -70°C by the 0.6MPa low-pressure nitrogen gas at the outlet of the low-pressure expander 6, and then one stream is drawn out and sent to the high-pressure expander 5. The high-pressure expander 5 expands and cools at a high pressure of 4.0 MPa and a high temperature of -50°C, with an expansion ratio of 3, and th...

Embodiment 3

[0031] The high and low pressure nitrogen double expansion natural gas liquefaction method comprises the following steps:

[0032] a. Nitrogen is compressed to 2.5MPa and cooled to 35°C;

[0033] b. After the nitrogen gas obtained in step a enters the booster end of the low-pressure booster 2 for pressurization, it is cooled to 35°C by the second aftercooler 4, and then enters the booster end of the high-pressure booster 1 to obtain 4.0MPa high-pressure nitrogen. , 4.0MPa high-pressure nitrogen is cooled to 35°C by the first aftercooler 3;

[0034] c. The cooled high-pressure nitrogen gas enters the main heat exchanger 9 and the 1.6Mpa raw natural gas is cooled to -40°C by the 0.5MPa low-pressure nitrogen gas at the outlet of the low-pressure expander 6, and then a stream is drawn out and sent to the high-pressure expander 5 for high-pressure expansion Machine 5 expands and refrigerates at high pressure 4.0MPa and high temperature -50°C, with an expansion ratio of 2.5, and th...

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Abstract

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 and then is introduced into the low-pressure expander for expansion refrigeration to obtain low-pressure nitrogen gas, and simultaneously cooling, liquefying and super-cooling the raw natural gas by the low-pressure nitrogen gas continuously and then leading out the raw natural gas from the main heat exchanger; and throttling the raw natural gas led out of the main heat exchanger by a throttle valve, separating the raw natural gas by a separation tank to obtain liquefied natural gas which is introduced into a storage tank, and returning the gas into the main heat exchanger for recovering cold. The method is applicable to high-low pressure areas and has high liquefaction rate which can reach 100 percent.

Description

technical field [0001] The invention relates to a natural gas liquefaction method, in particular to a high-low pressure nitrogen double-expansion natural gas liquefaction method. Background technique [0002] With the development of society, the amount of oil reserves is decreasing, and the greenhouse effect is becoming more and more obvious; people's requirements for green energy are also becoming stronger and stronger, so natural gas has been widely used. However, the extracted natural gas is all gaseous, and it is almost impossible to transport it, which greatly restricts its use. The liquefaction ratio of natural gas is 591. If the natural gas is liquefied, the volume will be reduced by 591 times, and transportation will become possible. Therefore, a large number of natural gas liquefaction devices have appeared. The liquefaction process of natural gas mainly includes nitrogen expansion refrigeration process, nitrogen-methane expansion refrigeration process, mixed worki...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): F25J1/02C10L3/10
CPCF25J1/0022F25J1/004F25J1/0221F25J2210/42F25J2230/42F25J2270/16
Inventor 葛水福葛浩华葛浩俊任智军李丰明冯金列洪艳红阮家林许立国向云华蒋吉林黄孝文田曙光陈海大黄荣陈龙余发军
Owner HANGZHOU FORTUNE CRYOGENIC EQUIP CO LTD
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