发明名称 Catalyst feed control during catalyst transition periods
摘要 Techniques are provided for operating a reactor during a catalyst transition period. The instantaneous reaction rate during a catalyst transition period can be determined using real-time measured process variables, and material balance calculations to provide an instantaneous reaction rate in approximately real time. According to certain embodiments, a material balance can be performed on the reactor system using a continuous ideal stirred tank reactor to determine the fractions of each type of catalyst that are present in the reactor, as well as the overall weight percent of catalyst in the reactor. A controller can then calculate the overall instantaneous reaction rate based on the respective catalyst fractions and the overall weight percent of catalyst in the reactor. The catalyst feed rate can then be adjusted based on the determined instantaneous reaction rate to maintain the instantaneous reaction rate within desired limits during a catalyst transition period.
申请公布号 US8846829(B2) 申请公布日期 2014.09.30
申请号 US201113100675 申请日期 2011.05.04
申请人 Chevron Phillips Chemical Company LP 发明人 Hendrickson Gregory G.
分类号 C08F2/00;C08F2/12;C08F2/34;C08F10/00;B01J8/22;B01J8/18;B01J19/18 主分类号 C08F2/00
代理机构 Fletcher Yoder, P.C. 代理人 Fletcher Yoder, P.C.
主权项 1. A method of operating a reactor during a catalyst transition period, the method comprising: feeding a first catalyst and a second catalyst to the reactor during the catalyst transition period; producing product effluent during the catalyst transition period; determining respective fractions of the first catalyst and the second catalyst in the reactor by performing a material balance on the reactor, based at least on a flow rate of the product effluent exiting the reactor; calculating an overall instantaneous reaction rate based on the respective fractions; and adjusting a feed rate for the second catalyst based on the overall instantaneous reaction rate.
地址 The Woodlands TX US