Methane gas concentration method

Patent metadata

Field	Value
Publication number	US-9944575-B2
Application number	US-201414772489-A
Country	US
Kind code	B2
Filing date	Feb 27, 2014
Priority date	Mar 4, 2013
Publication date	Apr 17, 2018
Grant date	Apr 17, 2018

Abstract

Adsorption towers are filled with adsorbents that adsorb methane gas in coal mine gas and perform a PSA cycle. For each of adsorption towers, a plurality of different pressure states of the internal pressure of the adsorption tower are set as an intermediate pressure state. As a pressure equalization step, an initial pressure equalization step of transferring the gas in one of the adsorption towers that is in a high pressure state to another one of the adsorption towers that is in an intermediate pressure state, and a final pressure equalization step of transferring the gas in one of the adsorption towers that is in the high pressure-side intermediate pressure state to another one of the adsorption towers that is in the low pressure state are performed.

First claim

The invention claimed is:

1. A methane gas concentration method comprising providing four or more adsorption towers each filled with an adsorbent that adsorbs methane gas in a methane-containing gas and performing, for each of the adsorption towers, a PSA cycle comprising the following steps:
(a) an adsorption step of receiving a supply of the methane-containing gas in a high pressure state near atmospheric pressure from a lower portion of an adsorption tower, adsorbing the methane gas on the adsorbent, and releasing non-adsorbed gas composed mainly of air from an upper portion of the adsorption tower;
(b) a pressure equalization (depressurizing) step of transferring the non-adsorbed gas remaining in the adsorption tower that has finished the adsorption step and is in the high pressure state to another adsorption tower in a lower pressure state so as to bring the inside of the adsorption tower into an intermediate pressure state;
(c) a decompression step of further decompressing the adsorbent in the adsorption tower that has finished the pressure equalization (depressurizing) step to a low pressure state so as to desorb the methane gas adsorbed on the adsorbent, and recovering said methane gas from the lower portion of the adsorption tower;
(d) a pressure equalization (pressurizing) step of receiving, after finishing the decompression step, the non-adsorbed gas from another adsorption tower that is in a higher pressure state so as to bring the inside of the adsorption tower into an intermediate pressure state; and
(e) a pressurizing step of, after an internal pressure of the adsorption tower has been increased by the pressure equalization (pressurizing) step, further supplying a pressurizing air into the adsorption tower from an upper portion of the adsorption tower so as to restore the adsorbent into the high pressure state capable of selectively adsorbing the methane gas,
wherein the adsorbent has a property of selectively adsorbing the methane gas contained in the air in the high pressure state near atmospheric pressure and desorbing the adsorbed methane gas in the low pressure state, and a property of preferentially desorbing the air when desorbing the methane gas,
wherein a plurality of different pressure states of the adsorption tower are set as the intermediate pressure states,
wherein the pressure equalization (depressurizing) step includes:
(b-i) an initial pressure equalization (depressurizing) step of transferring the non-adsorbed gas in the adsorption tower that is in the high pressure state to another one of the adsorption towers that is in an intermediate pressure state at a pressure lower than the high pressure state so as to bring the pressure in the the adsorption tower in the high pressure state into a high pressure-side intermediate pressure state; and
(b-ii) a final pressure equalization (depressurizing) step of transferring the non-adsorbed gas in the adsorption tower that is in the high pressure-side intermediate pressure state at a pressure higher than the low pressure state to another one of the adsorption towers that is in the low pressure state so as to bring the pressure in the adsorption tower in the high pressure-side intermediate pressure state into a low pressure-side intermediate pressure state,
wherein the pressure equalization (pressurizing) step includes:
(d-i) an initial pressure equalization (pressurizing) step of receiving the non-adsorbed gas in one of the adsorption towers that is in the high pressure-side intermediate pressure state into the adsorption tower that is in the low pressure state so as to bring the pressure in the adsorption tower in the low pressure state into the low pressure-side intermediate pressure state; and
(d-ii) a final pressure equalization (pressurizing) step of receiving, into the adsorption tower that is in the low pressure-side intermediate pressure state, the non-adsorbed gas in another one of the adsorption towers that is in the high pressure state so as to bring the pressure in the adsorption tower in the low pressure-side intermediate pressure state into the high pressure-side intermediate pressure state, and
wherein the transferring of the non-adsorbed gas from one of the adsorption towers that performs the pressure equalization (depressurizing) step to another one of the adsorption towers that performs the pressure equalization (pressurizing) step consists of transferring the non-adsorbed gas from an upper portion of the one of the adsorption towers performing the pressure equalization (depressurizing) to an upper portion of the another one of the adsorption towers performing the pressure equalization (pressurizing).

2. The methane gas concentration method according to claim 1 ,
wherein the pressure equalization (depressurizing) step is composed of an initial pressure equalization (depressurizing) step and a final pressure equalization (depressurizing) step, and the pressure equalization (pressurizing) step is composed of an initial pressure equalization (pressurizing) step and a final pressure equalization (pressurizing) step,
the non-absorbed gas discharged from the upper portion of one of the adsorption towers in the initial pressure equalization (depressurizing) step is supplied to the upper portion of another one of the adsorption towers that performs the final pressure equalization (pressurizing), and
the non-absorbed gas discharged from the upper portion of one of the adsorption towers in the final pressure equalization (depressurizing) step is supplied to another one of the adsorption towers that performs the initial pressure equalization (pressurizing) step.

3. The methane gas concentration method according to claim 1 , wherein the methane-containing gas comprises at least one gas selected from coal mine gas, biogas, reformed gas, and natural gas.

4. The methane gas concentration method according to claim 1 , wherein the adsorbent contains at least one selected from the group consisting of activated carbon, zeolite, silica gel, and an organometallic complex having an average pore diameter of 4.5 to 15 Å as measured by the MP method and having a methane gas adsorption amount under atmospheric pressure and at 298 K of 20 Nml/g or more.

Assignees

• Osaka Gas Co Ltd

Inventors

• Kawashima Shota
• Utaki Takahisa

Classifications

• B01D53/047

  Pressure swing adsorption · CPC title

• B01J20/18

  Synthetic zeolitic molecular sieves · CPC title

• C10L3/101

  Removal of contaminants · CPC title

• C10L2290/58

  Control or regulation of the fuel preparation of upgrading process · CPC title

• Y02P20/156

  Methane [CH4] · CPC title