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Optimization of heat removal in a gas phase fluidized bed process for polyethylene production using ethane to increase the heat capacity of the fluidized bed gas

机译:使用乙烷提高聚乙烯在流化床气相生产中的热容量,以提高流化床气体的热容

摘要

A process for preparation of polyethylene from feed ethylene in which the impurity acetylene is catalytically hydrogenated to ethylene, impurity ethylene is partially converted to ethane, and the remaining ethylene is polymerized to polyethylene in the gas phase in a fluidized bed reactor is new. A process for preparation of polyethylene from feed ethylene including (a) a hydrogenation stage (a) in which the feed ethylene containing impurities and secondary components such as acetylene and ethane, with removal of the acetylene by catalytic hydrogenation with hydrogen to ethylene, and partial conversion of the ethylene to ethane, and a polymerization stage (b) in which the ethylene remaining in stage (a) is converted to polyethylene in the gas phase in a fluidized bed (FB) reactor, with feeding in of the FB gas so that on entry into the reactor the ethene and 20-70 vol.% of the ethane relative to the total volume of fluidized bed gas and also other components are included, and in (a) in addition to the ethane present in the feed-ethylene the ethylene is so far converted to ethane that in stage (b) the established concentration can be maintained. An Independent claim is also included for: (1) A FB reactor setup including: (a) a hydrogenation reactor (1) with an ethylene feed pipe (2) and a hydrogen feed pipe (3), and (b) a fluidized bed reactor (10),a catalyst feed (11), a polyethylene outlet (3), separators (14) and (7), and gas line (22).
机译:由进料乙烯制备聚乙烯的方法是新的,其中将杂质乙炔催化氢化为乙烯,将杂质乙烯部分转化为乙烷,并将剩余的乙烯在流化床反应器中在气相中聚合为聚乙烯。由进料乙烯制备聚乙烯的方法,包括(a)加氢步骤(a),其中进料乙烯包含杂质和诸如乙炔和乙烷的第二组分,并通过用氢催化加氢成乙烯除去乙炔,并进行部分将乙烯转化为乙烷,以及聚合步骤(b),其中将阶段(a)中残留的乙烯在气相中在流化床(FB)反应器中转化为聚乙烯,并进料FB气体,从而进入反应器时,相对于流化床气体的总体积,乙烯和20-70%(体积)的乙烷以及其他组分也包括在内,并且在(a)中,除了进料乙烯中存在的乙烷外,到目前为止,乙烯已转化为乙烷,因此在步骤(b)中可以保持设定的浓度。还包括以下方面的独立权利要求:(1)FB反应器装置,包括:(a)带有乙烯进料管(2)和氢气进料管(3)的氢化反应器(1),以及(b)流化床反应器(10),催化剂进料(11),聚乙烯出口(3),分离器(14)和(7)以及气体管线(22)。

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