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Method for liquefying and rectifying coalbed methane containing oxygen

A coalbed methane and rectification technology, which is applied in the field of liquefaction and rectification of oxygen-containing coalbed methane, can solve the problems of low methane recovery rate, low product recovery rate, difficult operation, etc., and achieve safe and reliable operation process and low power consumption of process flow , easy operation effect

Active Publication Date: 2010-12-22
LIAONING CIMC HASHENLENG GAS LIQUEFACTION EQUIP CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, the adsorption method often leads to a decrease in the product recovery rate. The membrane separation method uses the pressure difference as the driving force. The separation effect is affected by various factors such as the membrane permeability coefficient and the permeation area. It is not easy to operate, and high pressure will bring safety hazards. Through searching , the literature on coalbed methane deoxidation using these two methods is very rare
[0004] After searching the existing technology, it is found that the Chinese patent CN101613627A proposes to use the combustion method to make the methane in the coalbed gas react with oxygen to generate carbon dioxide and water, and reduce the oxygen concentration in the coalbed gas to below 0.2%. This method can Effective removal of oxygen in oxygen-containing coalbed methane with a concentration of 1%-15%, but the impurity gas of carbon dioxide produced by combustion also needs to be removed, which increases equipment investment and energy consumption
[0005] Further search found that in the Chinese patent CN200952872Y, a fractionation tower is used to remove oxygen in coalbed methane under low temperature conditions, but this patent does not consider the explosion limit problem in the separation process, and the safety of the operation process is not guaranteed
Chinese patent CN101531559A adopts low-temperature rectification method to remove oxygen in coalbed methane, and ensures the safety of operation by pre-rough deoxidation of raw material gas. Chinese patent CN101531560A also adopts low-temperature rectification method to remove oxygen in coalbed methane, through Control the temperature of the most explosive position in the rectification process to ensure operational safety, but for the lower concentration of coalbed methane, the methane recovery rate of these two patents is very low, resulting in low energy utilization

Method used

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Examples

Experimental program
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Embodiment 1

[0020] For oxygen-containing coalbed methane with methane, nitrogen and oxygen components of 68.89%, 24.57% and 6.54% respectively, the liquefaction and rectification process includes the following steps:

[0021] Step 1. CBM is firstly compressed to 1.8MPa by compressors K-100 and K-101, and then enters heat exchanger LNG-100 for pre-cooling to -90°C. The pre-cooled CBM is cooled in cooler E-102 , and then enter the heat exchanger LNG-101 for further cooling and liquefaction. The liquefied coal bed gas is decompressed to 0.2MPa through the throttle valve VLV-100 and then enters the rectification tower T-100. The pressure separated from the top of the rectification tower is 0.19 The impurity gas of MPa, the liquid product LNG of 0.195MPa is obtained at the bottom. In order to reduce the energy consumption of the entire liquefaction and rectification process, the low-temperature impurity gas flowing out from the top of the tower first returns to the secondary heat exchanger for...

Embodiment 2

[0025] For low-concentration oxygen-containing coalbed methane with methane content of 42% and air content of 58%.

[0026] Step 1. CBM is compressed to 1.1MPa by compressors K-100 and K-101, and then enters heat exchanger LNG-100 for pre-cooling to -90°C. The pre-cooled CBM is cooled in cooler E-102. Then enter the secondary heat exchanger LNG-101 for further cooling and liquefaction. The liquefied coal bed gas is decompressed to 0.2MPa through the throttle valve VLV-100 and then enters the rectification tower. Impurity gas, the liquid product LNG of 0.195MPa is obtained at the bottom. In order to reduce the energy consumption of the entire liquefaction and rectification process, the low-temperature impurity gas flowing out from the top of the tower first returns to the secondary heat exchanger for cooling recovery, and the impurity gas coming out of the secondary heat exchanger passes through the throttle valve VLV- 101 The pressure drop is 0.11MPa, and the gas from the thr...

Embodiment 3

[0030] For low-concentration oxygen-containing coalbed methane containing 80.7%, 16.77% and 2.53% of methane, nitrogen and oxygen respectively.

[0031] Steps 1 and 2 are the same as steps 1 and 2 in Example 1

[0032] Step 3. The analysis results of the explosion limit theory and the HYSYS simulation results confirm that there is no need for preliminary deoxygenation of the feed gas, and the entire liquefaction and rectification process can be guaranteed by controlling the output of the bottom product of the rectification tower at 0.7882 kmol / h The operation safety of the process, while the methane recovery rate is as high as 97.66%, and the product purity is as high as 99.99%.

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Abstract

The invention relates to a method for liquefying and rectifying coalbed methane containing oxygen in the technical field of fuel gas purification. In the invention, after the coalbed methane containing oxygen is liquefied, impurity nitrogen and oxygen in the coalbed methane are separated off through a rectifying column so as to obtain a high-purity liquid product from the bottom of the column; the operation safety of a process flow is analyzed by applying an explosion limit theory, and an operation process which is easiest to cause explosion is determined; effective measures are taken to guarantee the operation safety of the operation process which is easiest to cause explosion so as to ensure that the operation of the whole process flow is safe and reliable; and a higher methane recovery rate can be also guaranteed so as to improve the energy utilization ratio.

Description

technical field [0001] The invention relates to a method in the technical field of gas purification, in particular to a method for liquefaction and rectification of oxygen-containing coal bed gas. Background technique [0002] Coal bed methane is a new type of clean energy. It is an unconventional natural gas associated with coal and self-generated and stored in coal seams in the form of adsorption. The potential of my country's coalbed methane resources is huge. Its development and utilization can increase new clean energy, reduce dependence on imported energy, effectively reduce greenhouse gas emissions, and can also reduce or avoid gas explosion accidents, which has a safety effect. [0003] There are two types of coalbed methane available for development and utilization. One is the coalbed methane extracted before coal mine mining. This gas has a methane content of more than 95% and has high utilization value. It can be directly pressurized for pipeline network transport...

Claims

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Application Information

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IPC IPC(8): F25J3/02
Inventor 李秋英巨永林
Owner LIAONING CIMC HASHENLENG GAS LIQUEFACTION EQUIP CO LTD
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