IP Library Granted Patent US 9,657,232
Granted Patent B2
US 9,657,232 · App. 14/356,781 · Granted May 23, 2017

Process for producing hydrocarbons

View Patent ↗
Loading inventors, assignments & file history…
Monitor This Case
Get email alerts when status or documents change.
Order Certified Copies
Most orders are placed with the USPTO same day — all within 24 business hours.
Order via The Patent Place →
Pre-filled with this patent's details
Quick Facts
Patent No.
US 9,657,232
App. No.
14/356,781
Granted
May 23, 2017
Kind
B2
Abstract

A process for converting biomass to products is described. Biomass is contacted with hydrogen in the presence of a fluidized bed of hydropyrolysis catalyst in a reactor vessel under hydropyrolysis conditions; and products and char are removed from the reactor vessel. The products leave the fluidized bed at an exit bed velocity, the char has a settling velocity that is less than the exit bed velocity and hydropyrolysis catalyst has a settling velocity that is greater than the exit bed velocity.

Claims (14)

1. A process for converting biomass to products comprising:

a. contacting the biomass with hydrogen in the presence of a fluidized bed of fresh hydropyrolysis catalyst in a reactor vessel under hydropyrolysis conditions;

b. removing products and char from the reactor vessel;

c. carrying out the contacting and removing steps for a period of time such that the fresh hydropyrolysis catalyst attrits in the fluidized bed to form small catalyst particles;

d. removing at least a portion of the small catalyst particles with the products and char wherein the products leave the fluidized bed at an exit bed velocity, the char has a settling velocity that is less than the exit bed velocity, the fresh hydropyrolysis catalyst has a settling velocity that is greater than the exit bed velocity, and the small catalyst particles have a settling velocity that is less than the exit bed velocity;

e. separating the products to remove the carbon monoxide and light hydrocarbons from the remainder of the products; and

f. passing the remainder of the products to a hydroconversion reactor wherein the remainder of the products are contacted with a hydroconversion catalyst under suitable hydroconversion conditions to produce a condensable liquid hydrocarbon product that has less than 1% oxygen.

2. A process as claimed in claim 1 wherein the settling velocity of the char is less than 90% of the exit bed velocity.

3. A process as claimed in claim 1 wherein the settling velocity of the char is less than 75% of the exit bed velocity.

4. A process as claimed in claim 1 wherein the settling velocity of the hydropyrolysis catalyst is greater than 110% of the exit bed velocity.

5. A process as claimed in claim 1 wherein the settling velocity of the hydropyrolysis catalyst is greater than 150% of the exit bed velocity.

6. A process as claimed in claim 1 wherein the settling velocity of the small catalyst particles is less than 90% of the exit bed velocity.

7. A process as claimed in claim 1 wherein the settling velocity of the small catalyst particles is less than 75% of the exit bed velocity.

8. A process as claimed in claim 1 where the small catalyst particles are separated out by a filter while the char is separated by a cyclone.

Assignments (2)
CHANGE OF NAME Recorded Mar 7, 2022
From: SHELL OIL COMPANY
To: SHELL USA, INC.
Reel/Frame 059694/0819 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jul 16, 2014
From: FELIX, LARRY GORDON; LINCK, MARTIN BRENDAN; MARKER, TERRY LOUISE; DEL PAGGIO, ALAN ANTHONY; ROBERTS, MICHAEL JOHN
To: SHELL OIL COMPANY
Reel/Frame 033323/0483 →