Pressure swing adsorption apparatus for hydrogen purification from decomposed ammonia gas and hydrogen purification method using the same

Patent metadata

Field	Value
Publication number	US-12508535-B2
Application number	US-202218013538-A
Country	US
Kind code	B2
Filing date	Apr 11, 2022
Priority date	Dec 31, 2021
Publication date	Dec 30, 2025
Grant date	Dec 30, 2025

Abstract

The present disclosure relates to a pressure swing adsorption apparatus for hydrogen purification from decomposed ammonia gas and a hydrogen purification method using the same, and more particularly, the pressure swing adsorption apparatus of the present disclosure includes a plurality of adsorption towers including a pretreatment unit and a hydrogen purification unit wherein the adsorption towers of the pretreatment unit and the hydrogen purification unit are packed with different adsorbents, thereby achieving high purity hydrogen purification from mixed hydrogen gas produced after ammonia decomposition, making it easy to replace the adsorbent for ammonia removal, minimizing the likelihood that the lifetime of the adsorbent in the hydrogen purification unit is drastically reduced by a very small amount of ammonia, and actively responding to a large change in ammonia concentration in the raw material.Additionally, a hydrogen purification method using the pressure swing adsorption apparatus of the present disclosure physically adsorbs and removes impurities such as moisture (H2O), ammonia (NH3) and nitrogen (N2) included in mixed hydrogen gas produced after ammonia decomposition below extremely small amounts, thereby achieving high purity hydrogen purification with improved selective adsorption of moisture, ammonia and nitrogen and maximized hydrogen recovery rate and productivity. In addition, since the temperature swing adsorption process is not introduced, there is no need for a heat source for regeneration, thereby reducing the driving cost.

First claim

The invention claimed is:

1 . A pressure swing adsorption apparatus for hydrogen purification from decomposed ammonia gas, the pressure swing adsorption apparatus comprising:
a plurality of adsorption towers in a pretreatment unit, connected to a raw material feed pipe and a plurality of adsorption towers in a hydrogen purification unit; a vacuum pump connected to the adsorption towers to keep the adsorption towers in a vacuum state; a hydrogen storage tank to capture purified hydrogen from the adsorption towers; and a plurality of valves to open/close a plurality of pipes connected to the adsorption towers, the vacuum pump and the hydrogen storage tank, wherein each adsorption tower in the pretreatment unit is packed with a first adsorbent and a second adsorbent, which are distinct in material, forming a multilayer structure, to selectively adsorb and remove moisture and ammonia included in mixed hydrogen gas produced after ammonia decomposition fed through the raw material feed pipe, and wherein each adsorption tower in the hydrogen purification unit is packed with a third adsorbent to purify hydrogen by selectively adsorbing nitrogen included in the mixed hydrogen gas free of moisture and ammonia from the pretreatment unit.

2 . A pressure swing adsorption apparatus for hydrogen purification from decomposed ammonia gas, the pressure swing adsorption apparatus comprising:
a plurality of adsorption towers in a pretreatment unit, connected to a raw material feed pipe and a plurality of adsorption towers in a hydrogen purification unit; a vacuum pump connected to the adsorption towers to keep the adsorption towers in a vacuum state; a hydrogen storage tank to capture purified hydrogen from the adsorption towers; and a plurality of valves to open/close a plurality of pipes connected to the adsorption towers, the vacuum pump and the hydrogen storage tank, wherein at least two adsorption towers of the pretreatment unit are arranged in parallel, and each of the at least two adsorption towers is packed with a first adsorbent and a second adsorbent in a multilayer structure to selectively adsorb and remove moisture and ammonia included in mixed hydrogen gas produced after ammonia decomposition fed through the raw material feed pipe, and wherein at least four adsorption towers of the hydrogen purification unit are arranged in parallel, and each of the at least four adsorption towers is packed with a third adsorbent to purify hydrogen by selectively adsorbing nitrogen included in the mixed hydrogen gas free of moisture and ammonia from the pretreatment unit.

3 . The pressure swing adsorption apparatus for hydrogen purification from decomposed ammonia gas according to claim 1 , wherein the first adsorbent is packed at a lower layer region in each adsorption tower of the pretreatment unit, and includes at least one of first activated alumina or silica gel capable of removing moisture.

4 . The pressure swing adsorption apparatus for hydrogen purification from decomposed ammonia gas according to claim 1 , wherein an amount of the first adsorbent packed in each adsorption tower of the pretreatment unit is 5 to 40 wt %.

5 . The pressure swing adsorption apparatus for hydrogen purification from decomposed ammonia gas according to claim 1 , wherein the second adsorbent is packed at an upper layer region in each adsorption tower of the pretreatment unit, and includes at least one selected from the group consisting of metal impregnated activated carbon, silica gel and second activated alumina capable of removing ammonia.

6 . The pressure swing adsorption apparatus for hydrogen purification from decomposed ammonia gas according to claim 5 , wherein the metal impregnated activated carbon is activated carbon impregnated with at least one metal selected from the group consisting of Mg, Ca, Mn and Cu.

7 . The pressure swing adsorption apparatus for hydrogen purification from decomposed ammonia gas according to claim 5 , wherein an amount of metal impregnated in the metal impregnated activated carbon is 1 to 10 wt %.

8 . The pressure swing adsorption apparatus for hydrogen purification from decomposed ammonia gas according to claim 1 , wherein an amount of the second adsorbent packed in the adsorption tower of the pretreatment unit is 60 to 95 wt %.

9 . The pressure swing adsorption apparatus for hydrogen purification from decomposed ammonia gas according to claim 1 , wherein the third adsorbent includes at least one selected from the group consisting of zeolite Lix, zeolite CaX, zeolite NaX, zeolite NaA and zeolite CaA.

10 . The pressure swing adsorption apparatus for hydrogen purification from decomposed ammonia gas according to claim 1 , wherein the first adsorbent is packed at a lower layer region in the adsorption tower of the pretreatment unit, and includes first activated alumina or silica gel capable of removing moisture,
wherein the first adsorbent is packed in an amount of 10 to 35 wt % relative to the second adsorbent in each adsorption tower of the pretreatment unit, wherein the second adsorbent is packed at an upper layer region in each adsorption tower of the pretreatment unit, and includes metal impregnated activated carbon capable of removing ammonia, wherein the second adsorbent is packed in an amount of 65 to 90 wt % relative to the first adsorbent in each adsorption tower of the pretreatment unit, wherein the metal impregnated activated carbon includes magnesium (Mg) impregnated activated carbon or calcium (Ca) impregnated activated carbon, wherein an amount of metal impregnated in the metal impregnated activated carbon is 1 to 8 wt %, and wherein the third adsorbent includes at least one of zeolite LiX or zeolite CaX.

11 . A hydrogen purification method using the pressure swing adsorption apparatus according to claim 1 including the plurality of adsorption towers in the pretreatment unit, connected to a raw material feed pipe and the plurality of adsorption towers in the hydrogen purification unit, connected to the raw material feed pipe; the vacuum pump connected to the adsorption towers to keep the adsorption towers in a vacuum state; the hydrogen storage tank to capture purified hydrogen from the adsorption towers; and the plurality of valves to open/close the plurality of pipes connected to the adsorption towers, the vacuum pump and the hydrogen storage tank, the hydrogen purification method comprising the steps of:
feeding mixed hydrogen gas produced after ammonia decomposition into thean adsorption tower of the pretreatment unit through the raw material feed pipe;
selectively adsorbing and removing moisture by allowing the fed mixed hydrogen gas to pass through a first adsorbent packed at a lower layer region of the adsorption tower in the pretreatment unit;
selectively adsorbing and removing ammonia by allowing mixed hydrogen gas free of moisture to pass through a second adsorbent packed at an upper layer region of the adsorption tower in the pretreatment unit;
feeding mixed hydrogen gas free of ammonia into an adsorption tower of the hydrogen purification unit;
selectively adsorbing and removing nitrogen by allowing the fed mixed hydrogen gas free of ammonia to pass through a third adsorbent packed in the adsorption tower in the hydrogen purification unit to acquire the purified hydrogen; and
capturing the acquired hydrogen in the hydrogen storage tank.

12 . The hydrogen purification method using the pressure swing adsorption apparatus according to claim 11 , wherein the step of selectively adsorbing and removing ammonia comprises adsorbing and removing ammonia such that an amount of ammonia in the mixed hydrogen gas free of moistu

Assignees

• Korea Inst Energy Res

Inventors

• Yoon Hyung-Chul
• Han Sang-Sup
• Beum Hee-Tae
• Cho Kanghee
• Kim Sun Hyung
• Ju Hyung Kuk

Classifications

• C01B2203/0495

  the impurity being water · CPC title

• C01B2203/043

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

• C01B2203/0266

  containing a decomposition step · CPC title

• C01B3/56 Primary

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

• C01B3/047

  Decomposition of ammonia · CPC title