发明名称 BIOMASS TREATMENT FOR HYDROTHERMAL HYDROCATALYTIC CONVERSION
摘要 A selective removal of chlorine and phosphorus that are detrimental to subsequent hydrothermal hydrocatalytic conversion from the biomass feed prior to carrying out catalytic hydrogenation/hydrogenolysis/hydrodeoxygenation of the biomass in a manner that does not reduce the effectiveness of the hydrothermal hydrocatalytic treatment while minimizing the amount of water used in the process is provided.
申请公布号 US2015167237(A1) 申请公布日期 2015.06.18
申请号 US201414574530 申请日期 2014.12.18
申请人 SHELL OIL COMPANY 发明人 POWELL Joseph Broun;CHHEDA Juben Nemchand
分类号 D21C11/00;C13K1/02;C07C1/24;C07C29/132 主分类号 D21C11/00
代理机构 代理人
主权项 1. A method for selective removal of chlorine and phosphorus from a cellulosic biomass solids, said method comprising a plurality of vessels: a. providing each of said vessels with one of detrimental species-containing cellulosic biomass solids; b. introducing a quantity of a base solution having a pH of greater than 9 from an inlet into a first vessel of said plurality of vessels containing said detrimental species-containing cellulosic biomass solids at a temperature in the range of about 0° C. to about 60° C.; c. repeating step (b) for a second vessel of said plurality of vessels; d. introducing a quantity of aqueous solution having a pH of at most 8 from an inlet into said first vessel of said plurality of vessels treated according to step (b) thereby discharging the basic water effluent; e. repeating step (d) for the second vessel of said plurality of vessels treated according to step (c); f. introducing a quantity of gas or organic solution from an inlet into the first vessel of said plurality of vessels treated according to step (d) and discharging the aqueous effluent; g. repeating step (f) for the second vessel of said plurality of vessels treated according to step (e); h. recycling at least a portion of the discharged aqueous effluent as a portion of the base solution; i. transferring at least a portion of the biomass treated according to steps (f) and (g) to a digestion and/or reaction vessel; j. wherein at least 2 of the vessels are undergoing at least one of the steps (b) through (i) at the same time; and k. wherein the amount of the total basic water effluent from the plurality of vessels is in the range of from about 3 parts to about 0.5 parts relative to about 1 part of detrimental species—containing cellulosic biomass solids (dry basis).
地址 Houston TX US