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公开(公告)号:KR100292555B1
公开(公告)日:2001-06-01
申请号:KR1019990001743
申请日:1999-01-21
Applicant: 한국에너지기술연구원
IPC: B01D53/047
Abstract: 본발명은높은생산성을갖는수소압력변동흡착공정에관한것으로, CO, CH, CO, 탄화수소등이포함된수소함유혼합가스로부터고순도수소를정제하는압력변동흡착공정의생산성을높이기위한운전방법에관한것이다. 본발명의구성은 3개이상의흡착탑을사용하여압력변동흡착법으로고순도의수소를정제하는방법에있어서한주기의공정구성은순차적으로; 흡착단계, 부분균압단계, 세정제공단계, 향류감압단계, 세정단계, 부분균압단계, 제품가스축압단계로구성되며, 부분균압단계에있는두 흡착탑의압력은두 탑의압력이같아지기전에부분균압단계를종료하여서뒤에오는세정제공단계에서충분한병류감압배출가스가세정단계에있는탑의세정가스로활용되어흡착제의유효흡착량을증가시켜공정의생산성을향상시켰다.
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公开(公告)号:KR1020000051347A
公开(公告)日:2000-08-16
申请号:KR1019990001743
申请日:1999-01-21
Applicant: 한국에너지기술연구원
IPC: B01D53/047
CPC classification number: B01D53/047 , B01D53/96 , C01B3/508
Abstract: PURPOSE: A process of pressure swing absorption of hydrogen is provided which improves the productivity of pressure swing absorption process of purifying hydrogen with high purity from the hydrogen containing mixed gas containing CO2, CH4, CO, hydrocarbon and the like. CONSTITUTION: A process of pressure swing absorption of hydrogen comprises steps of: (i) an absorption step of removing impurities from high pressure raw material gas supplied to an absorption tank and obtaining product hydrogen with high purity from a tank outlet; (ii) a partial pressure homogenization step of supplying the exhausted hydrogen to another absorption tank with decompressing the absorption finished tank in parallel to the flow of the raw material gas; (iii) a washing supply step of further decompressing the partial pressure homogenization step finished absorption tank and supplying the exhausted gas to washing gas of an absorption tank in the washing step; (iv) a permanent current flow decompressing step of decompressing the absorption tank at an atmospheric pressure with a permanent current to further remove the impurities absorbed at the absorption tank after finishing the washing supply step; (v) a washing step of removing absorbed impurities by introducing gas exhausted from another tank in the washing supply step; (vi) a partial pressure homogenization step of pressurizing the tank by introducing the gas exhausted from the another absorption tank in the partial pressure homogenization step through the outlet portion of the tank with a permanent current; and (vii) a product gas pressurizing step of pressurizing the pressure of the absorption tank by introducing a part of the product hydrogen which has finished the partial homogenization step with a permanent current.
Abstract translation: 目的:提供氢的压力挥发吸收过程,其提高从含有CO 2,CH 4,CO,烃等的含氢混合气体中纯化氢的高压纯化的变压吸收过程的生产率。 构成:氢气的变压吸收过程包括以下步骤:(i)从供给到吸收罐的高压原料气体中除去杂质的吸收步骤,从罐出口获得高纯度的产物氢; (ii)分压均质化步骤,将排出的氢气供给另一个吸收罐,使吸收成品罐与原料气体流平行地减压; (iii)洗涤供给步骤,进一步减压分压均质化步骤成品吸收罐,并在洗涤步骤中将排出的气体供给吸收罐的洗涤气体; (iv)永久电流减压步骤,在大气压下用永久电流对吸收罐进行减压,以进一步除去在完成洗涤供应步骤之后在吸收罐处吸收的杂质; (v)通过在洗涤供给步骤中引入从另一个罐排出的气体来除去吸收的杂质的洗涤步骤; (vi)通过在所述分压均质化步骤中从所述另一吸收罐排出的气体通过所述罐的所述出口部分以永久电流进行加压的分压均质化步骤; 和(vii)通过将已经完成了部分均化步骤的一部分产物氢引入永久电流来对吸收罐的压力加压的产品气体加压步骤。
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