Pressure swing adsorption process and pressure swing adsorption apparatus

Patent metadata

Field	Value
Publication number	US-10933366-B2
Application number	US-201816193323-A
Country	US
Kind code	B2
Filing date	Nov 16, 2018
Priority date	Nov 17, 2017
Publication date	Mar 2, 2021
Grant date	Mar 2, 2021

Abstract

According to an exemplary embodiment of the present invention, a pressure swing adsorption process of a hydrogen production system is provided. The hydrogen production system includes a desulfurization process for removing sulfur components from raw natural gas; a reforming reaction process for producing a reformed gas containing hydrogen generated by the reaction of natural gas through the desulfurization process and steam; and a pressure swing adsorption process of concentrating the hydrogen using a pressure swing adsorption from the reformed gas. In a desorption step of the pressure swing adsorption process, a cocurrent depressurization and a countercurrent depressurization are simultaneously performed.

First claim

What is claimed is:

1. A pressure swing adsorption process of a hydrogen production system comprising:
a desulfurization process for removing sulfur components from a raw natural gas;
a reforming reaction process for producing a reformed gas containing hydrogen generated by the reaction of the natural gas through the desulfurization process and steam; and
a pressure swing adsorption process of concentrating the hydrogen using a pressure swing adsorption from the reformed gas,
wherein the pressure swing adsorption process is performed using a plurality of adsorption beds,
wherein the pressure swing adsorption process includes:
an adsorption step of adsorbing impurities while introducing the reformed gas into a first adsorption bed pressurized with an adsorption pressure to produce a hydrogen product;
a first pressure equalization step, a first cleaning and supplying step, a second cleaning and supplying step, and a second pressure equalization step which are sequentially performed after the adsorption step and perform a cocurrent depressurization of the first adsorption bed; and
a desorption step which is performed after the second pressure equalization step, depressurizes an internal pressure of the first adsorption bed to a desorption pressure, and performs a recovery of remaining hydrogen and desorption of the impurities, and

wherein in the desorption step, a cocurrent depressurization and a countercurrent depressurization are simultaneously performed.

2. The pressure swing adsorption process of claim 1 , wherein in the first pressure equalization step, the first adsorption bed is in communication with a second adsorption bed which is to be subjected to a pressurization step to pressurize the second adsorption bed, and the first adsorption bed is cocurrent-depressurized,
wherein in the first cleaning and supplying step, a hydrogen gas remaining in the first adsorption bed is supplied to a third adsorption bed after completion of the desorption step, and the first adsorption bed is cocurrent-depressurized,
wherein in the second cleaning and supplying step, the hydrogen gas remaining in the first adsorption bed and a hydrogen gas recovered in the desorption step are supplied to the third adsorption bed as a cleaning gas, and the first adsorption bed is cocurrent-depressurized, and
wherein in the second pressure equalization step, after the second cleaning and supplying step, only the first adsorption bed and the third adsorption bed are in communication with each other, and the first adsorption bed is cocurrent-depressurized.

3. The pressure swing adsorption process of claim 1 , wherein the pressure swing adsorption process uses an adsorption bed in which a lower end thereof, which is a direction into which the reformed gas is introduced, is filled with activated carbon, and an upper end thereof is filled with zeolite.

4. The pressure swing adsorption process of claim 1 , wherein a depressurization pressure of the first adsorption bed after completion of the first pressure equalization step, the first cleaning and supplying step, the second cleaning and supplying step, and the second pressure equalization step is 10 to 30% of the adsorption pressure.

5. The pressure swing adsorption process of claim 1 , wherein the cocurrent depressurization and the countercurrent depressurization in the desorption step are performed at a pressure of 1 to 20% of the adsorption pressure.

6. The pressure swing adsorption process of claim 1 , wherein the reformed gas contains 3 to 6% of methane, 1 to 4% of carbon monoxide, 10 to 30% of carbon dioxide, and 65 to 85% of hydrogen by volume.

7. A pressure swing adsorption apparatus of a hydrogen production system comprising:
a desulfurizing apparatus for removing sulfur components from a raw natural gas;
a reforming reaction apparatus for producing a reformed gas including hydrogen produced by a reaction of the natural gas through the desulfurizing apparatus and steam; and
a pressure swing adsorption apparatus for concentrating the hydrogen using a pressure swing adsorption from the reformed gas,
wherein the pressure swing adsorption apparatus includes an adsorption bed and two or more buffer tanks connected to a lower end and an upper end of the adsorption bed, respectively,
wherein the pressure swing adsorption apparatus is configured to adsorb impurities while introducing the reformed gas into the adsorption bed pressurized with an adsorption pressure to produce a hydrogen product,
wherein the pressure swing adsorption apparatus is further configured to sequentially perform, after adsorbing impurities, a first pressure equalization step, a first cleaning and supplying step, a second cleaning and supplying step, and a second pressure equalization step, and a cocurrent depressurization of the adsorption bed,
wherein the pressure swing adsorption apparatus is further configured to perform a desorption step after the second pressure equalization step, depressurization of an internal pressure of the adsorption bed to a desorption pressure, and a recovery of remaining hydrogen and desorption of the impurities, and
wherein the pressure swing adsorption apparatus is further configured to simultaneously perform a cocurrent depressurization and a countercurrent depressurization.

8. The pressure swing adsorption apparatus of claim 7 , wherein the adsorption bed has the lower end thereof, into which the reformed gas is introduced, filled with activated carbon, and the upper end thereof filled with zeolite.

9. The pressure swing adsorption apparatus of claim 7 , wherein the pressure swing adsorption apparatus further includes a water gas transition reaction apparatus for removing carbon monoxide in the reformed gas.

Assignees

• Korea Inst Energy Res

Inventors

• Park Jong-Ho
• Beum Hee-Tae
• Han Sang-Sup
• Cho Dong-Woo
• Cho Kanghee

Classifications

• C01B2203/048

  the impurity being an organic compound · CPC title

• C01B2203/0475

  the impurity being carbon dioxide · CPC title

• C01B2203/047

  the impurity being carbon monoxide · CPC title

• C01B2203/043

  Regenerative adsorption process in two or more beds, one for adsorption, the other for regeneration · CPC title

• C01B3/56 Primary

  by contacting with solids; Regeneration of used solids · CPC title