发明名称 Multiple bed temperature controlled adsorption
摘要 The systems and processes disclosed herein relate generally to multi bed temperature controlled adsorption for use in the recovery of sorbates that are removed from process streams by adsorption. Multi bed temperature controlled adsorber systems can include three or more temperature controlled adosrbers that operate in parallel. Each temperature controlled adsorber through a series of steps including an adsorption step, a first bed to bed interchange, a regeneration step, and a second bed to bed interchange.
申请公布号 US8936727(B2) 申请公布日期 2015.01.20
申请号 US200912399057 申请日期 2009.03.06
申请人 UOP LLC 发明人 Dunne Stephen R.;Wegerer David A.
分类号 B01D15/24;B01D15/00;B01J20/34;B01D53/04;B01D53/26;B01J20/18;B01J20/28;B01J20/32 主分类号 B01D15/24
代理机构 代理人
主权项 1. A process for sorbate removal in the adsorption treatment of a process stream, the process comprising: providing said process stream to four temperature controlled adsorbers that operate in parallel, where each temperature controlled adsorber includes one or more adsorption flow passages, wherein said process stream flows through said adsorption flow passages and one or more heat transfer flow passages, wherein each of said one or more adsorption flow passages is adjacent to at least one of said one or more heat transfer flow passages and the one or more adsorption flow passages contain an adsorptive material coating on an adsorbent layer that defines each of said one or more adsorption flow passages wherein said adsorbent layer has a thickness from about 0.035 cm to 0.058 cm and wherein said adsorbent layer comprises a polymer and a 3A or 4A zeolite; cycling each temperature controlled adsorber through a continuous_series of steps including an adsorption step, a first bed to bed interchange of heat transfer fluid, a regeneration step, and a second bed to bed interchange of heat transfer fluid wherein during said first bed to bed interchange of heat transfer fluid and said second bed to bed interchange of heat transfer fluid heat is recovered from said one or more adsorption flow passages and wherein each temperature controlled adsorber is simultaneously undergoing a different step; removing the sorbate from the process stream during the step of adsorption and removing said sorbate from said adsorption flow passages during said regeneration step wherein said sorbate is water.
地址 Des Plaines IL US