发明名称 System and method for conditioning a hardwood pulp liquid hydrolysate
摘要 A system and method for hardwood pulp liquid hydrolysate conditioning includes a first evaporator receives a hardwood mix extract and outputting a quantity of vapor and extract. A hydrolysis unit receives the extract, hydrolyzes and outputs to a lignin separation device, which separates and recovers a quantity of lignin. A neutralization device receives extract from the lignin separation device and a neutralizing agent, producing a mixture of solid precipitate and a fifth extract. The solid precipitate is removed from the fifth extract. A second evaporator removes a quantity of acid from the fifth extract in a vapor form. This vapor may be recycled to improve total acid recovery or discarded. A desalination device receives the diluted extract, separates out some of the acid and salt and outputs a desalinated solution.
申请公布号 US9068291(B2) 申请公布日期 2015.06.30
申请号 US201314079049 申请日期 2013.11.13
申请人 Red Shield Acquisition, LLC;University of Maine System Board of Trustees 发明人 Waite Darrell;Arnold Richard;St. Pierre James;Pendse Hemant P.;Ceckler William H.
分类号 D21C11/00;C13K13/00;C13K1/02;D21C11/10 主分类号 D21C11/00
代理机构 Hayes Soloway PC 代理人 Hayes Soloway PC
主权项 1. A hardwood pulp liquid hydrolysate conditioning system comprising: a first evaporator receiving a first extract derived from a quantity of hardwood mix and outputting a first quantity of vapor and a second extract; a hydrolysis unit positioned to receive the second extract and output a third extract; at least one lignin separation device positioned to receive the third extract from the hydrolysis unit, wherein the at least one lignin separation device separates and recovers a quantity of lignin from the third extract and outputs a fourth extract; a neutralization device positioned to receive a fourth extract, the neutralization device having a neutralizing agent input, wherein the neutralization device adjusts a pH of the fourth extract to form a quantity of solid precipitate and a fifth extract; a precipitate removal device positioned to receive the quantity of solid precipitate and the fifth extract from the neutralization device, wherein the precipitate removal device separates the quantity of solid precipitate from the fifth extract; a second evaporator positioned to receive the fifth extract from the precipitate removal device, wherein the second evaporator removes a first quantity of acid from the fifth extract, wherein the second evaporator outputs a second quantity of vapor having the first quantity of acid, and wherein the second evaporator outputs a sixth extract; and a desalination device, positioned to receive the sixth extract, wherein the desalination device removes a quantity of salt, heavy metal, residual acid, and lignin from the sixth extract and outputs a seventh extract comprising a desalinated solution containing sugar.
地址 Old Town ME US