发明名称 Method for preparing vinyl chloride from acetylene and dichlorethane
摘要 Provided is a method for preparing vinyl chloride with acetylene and dichlorethane for large-scale industrial production. Acetylene, dichlorethane vapor and hydrogen chloride gas at a molar ratio of 1:(0.3-1.0):(0-0.20) are mixed; the raw mixed gas is preheated; the preheated raw mixed gas passes through a reactor containing a catalyst and reacts; the resultant mixed gas is cooled to 30-50° C. and pressurized to 0.4-1.0 MPa, and then cooled to ambient temperature, and further frozen to −25-15° C. for liquefaction isolation, and unliquefied gas is recycled and reused; liquefied liquid is sent to a rectifying tower for rectification, and vinyl chloride monomers meeting polymerization requirements are obtained. The present invention has the advantages of eliminating mercury contamination completely, simplifying the reactor structure, recycling hydrogen chloride and acetylene, reducing waterwash process, avoiding mass production of waste acid and improving utilization of chlorine.
申请公布号 US9371259(B2) 申请公布日期 2016.06.21
申请号 US201214406931 申请日期 2012.07.12
申请人 SHANGHAI ADVANCED RESEARCH INSTITUTE, CHINESE ACADEMY OF SCIENCES;ZHONGKE YIGONG (SHANGHAI) CHEMICAL TECHNOLOGY CO., LTD. 发明人 Jiang Biao;Zhong Jinguang
分类号 C07C17/07;C07C17/08;C07C17/25;C07C17/354 主分类号 C07C17/07
代理机构 Novick, Kim & Lee, PLLC 代理人 Novick, Kim & Lee, PLLC ;Xue Allen
主权项 1. A method for preparing vinyl chloride, comprising: 1) mixing acetylene, dichlorethane vapor and optionally hydrogen chloride gas to obtain a raw mixed gas, wherein the raw mixed gas has a molar ratio of acetylene:dichlorethane:hydrogen chloride gas at 1:(0.3-1.0):(0-0.20); 2) preheating the raw mixed gas to a preheating temperature to obtain a preheated raw mixed gas; 3) feeding the preheated raw mixed gas into a reactor containing a catalyst; 4) cooling an effluent gas from the reactor to 30-50° C., pressurizing the effluent gas to 0.4-1.0 MPa, and cooling the pressurized effluent gas to ambient temperature, and further cooling the pressurized effluent gas from ambient temperature to −25-15° C. to obtain a liquid; and 5) feeding the liquid to a rectifying tower for rectification, and obtaining vinyl chloride from the rectifying tower.
地址 Shanghai CN
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