公开(公告)号：US20170239634A1

公开(公告)日：2017-08-24

申请号：US15436029

申请日：2017-02-17

Applicant: PHILLIPS 66 COMPANY

Inventor： Dustin L. DALLUGE ,  Steven E. LUSK ,  Samuel T. JONES ,  Johnathan T. GORKE

IPC: B01J8/00 ,  C10C5/00 ,  C10B53/02 ,  B01J8/02

CPC classification number: B01J8/10 ,  B01J8/0045 ,  B01J8/005 ,  B01J8/082 ,  B01J8/087 ,  C10B49/16 ,  C10B53/02 ,  C10C5/00 ,  Y02E50/14 ,  Y02P20/145

Abstract: The present disclosure relates generally to two-stage biomass pyrolysis systems configured to maximize pyrolysis vapor yield from a lignocellulosic biomass while being conducive to commercial-scale throughput of lignocellulosic biomass. The system includes a reactor first stage comprising at least one auger pyrolyzes a lignocellulosic feedstock at a temperature and residence time that produces pyrolysis vapors derived predominantly from cellulose and hemi-cellulose fractions of the feedstock. A reactor second stage is configured to partially-pyrolyzed feedstock from the reactor first stage at a higher temperature for an additional residence time to produce additional pyrolysis vapors that are predominantly derived from of lignin. Certain embodiments arrange multiple reactor first stages around a single reactor second stage.

公开(公告)号：US20170240814A1

公开(公告)日：2017-08-24

申请号：US15435990

申请日：2017-02-17

Applicant: PHILLIPS 66 COMPANY

Inventor： Dustin L. DALLUGE ,  Steven E. LUSK ,  Samuel T. JONES ,  Johnathan T. GORKE

IPC: C10B53/02 ,  C10B5/00 ,  C10B49/06 ,  C10B57/06 ,  C10B49/18 ,  C10B7/10 ,  C10B3/00

CPC classification number: C10B53/02 ,  C10B49/16 ,  C10B57/06 ,  Y02E50/14 ,  Y02P20/145

Abstract: The present disclosure relates generally to a two-stage biomass pyrolysis processes that maximize pyrolysis vapor yield from a lignocellulosic biomass while being conducive to commercial-scale throughput of biomass. A lignocellulosic feedstock is first pyrolyzed in a reactor first stage comprising at least one auger at a temperature and residence time that produces pyrolysis vapors derived predominantly from cellulose and hemi-cellulose fractions of the feedstock. Partially-pyrolyzed feedstock from the reactor first stage is then pyrolyzed in a reactor second stage at a higher temperature for an additional residence time to produce additional pyrolysis vapors that are predominantly derived from lignin. Certain embodiments arrange multiple reactor first stages around a single reactor second stage.