发明名称 Wet start-up method for hydrogenation unit, energy-saving hydrogenation process and hydrogenation apparatus
摘要 The present invention relates to a wet start-up method for hydrogenation unit, an energy-saving hydrogenation process, and a hydrogenation apparatus. The method involves heating a start-up activating oil to a specific temperature and flowing the heated oil through a bed of hydrogenation catalyst bed, so that the temperature at the catalyst bed layer is increased to 180±10° C. or above by means of heat exchange and the reaction heat generated from activation in the start-up method.
申请公布号 US9574141(B2) 申请公布日期 2017.02.21
申请号 US201314068506 申请日期 2013.10.31
申请人 CHINA PETROLEUM & CHEMICAL CORPORATION;Fushun Research Institute of Petroleum and Petrochemicals, SINOPEC 发明人 Zeng Ronghui;Liu Tao;Fang Xiangchen;Han Zhaoming;Zhang Xuehui;Sun Shike;Peng Chong;Guo Rong;Liu Jihua;Li Benzhe
分类号 C10G49/24 主分类号 C10G49/24
代理机构 Novick, Kim & Lee, PLLC 代理人 Novick, Kim & Lee, PLLC ;Xue Allen
主权项 1. A wet start-up method for hydrogenation unit, comprising the following steps: (a) utilizing a low-temperature heat source to heat up a start-up activating oil, feeding the heated start-up activating oil and a circulating hydrogen into a hydrogenation unit, wherein the hydrogenation unit contains a sulfurized type hydrogenation catalyst, and the sulfurized type hydrogenation catalyst is activated; (b) stopping the use of the low-temperature heat source, utilizing the reaction heat generated from the activating reaction of the sulfurized type hydrogenation catalyst to heat up materials in the hydrogenation unit to 180±10° C., and then introducing an olefin-rich gas and/or olefin-rich light distillate oil into the hydrogenation unit to carry out olefin hydrogenation reaction; (c) utilizing the reaction heat generated from the olefin hydrogenation reaction to further heat up the materials in the hydrogenation unit to 230±10° C., and keeping the temperature constant for at least 4 h; (d) heating the materials in the hydrogenation unit further to a temperature higher than 240° C., reducing the amount of the olefin-rich gas and/or olefin-rich light distillate oil gradually, replacing the start-up activating oil with a feedstock gradually, and utilizing the reaction heat generated from the feedstock hydrogenation reaction to heat up the materials in the hydrogenation unit until the target temperature is reached.
地址 Beijing CN