IP Library Granted Patent US 10,093,602
Granted Patent B2
US 10,093,602 · App. 15/519,843 · Granted Oct 9, 2018

Process for the conversion of saccharide-containing feedstock

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Quick Facts
Patent No.
US 10,093,602
App. No.
15/519,843
Granted
Oct 9, 2018
Kind
B2
Abstract

The invention provides a process for the catalytic conversion of a saccharide-containing feedstock in a reactor, wherein saccharide-containing feedstock is provided to the reactor as a feed stream through a feed pipe and is contacted with a catalyst system in the reactor and wherein, as the saccharide-containing feedstock is fed through the feed pipe, a solvent stream, initially comprising essentially no saccharide, is fed along the internal walls of the feed pipe.

Claims (11)

1. A process for the catalytic conversion of a saccharide-containing feedstock in a reactor to a glycol, wherein saccharide-containing feedstock is provided to the reactor as a feed stream through a feed pipe having a first section and a second section and is contacted with a catalyst system in the reactor and wherein, as the saccharide-containing feedstock is fed through the second section of the feed pipe, a solvent stream, initially comprising essentially no saccharide, is fed along the internal walls of the second section of the feed pipe to provide a co-axial flow of the solvent stream around the saccharide-containing feedstock.

2. A process according to claim 1 , wherein the solvent stream is provided to the internal walls of the second section of the feed pipe through a permeable section of the first section of the feed pipe.

3. A process according to claim 1 , wherein the solvent stream and the saccharide-containing feedstock are provided to the second section of the feed pipe through concentric pipes in order to provide the co-axial flow.

4. A process according to claim 1 , wherein the temperature of the saccharide-containing feedstock is initially below the degradation temperature of the saccharide and the temperature of the solvent stream is initially higher than the degradation temperature of the saccharide.

5. A process according to claim 1 , wherein the saccharide containing feedstock is also contacted with hydrogen in the reactor.

6. A process according to claim 1 , wherein the catalytic conversion of a saccharide-containing feedstock comprises the conversion of said feedstock into ethylene glycol and 1,2-propylene glycol in the presence of a catalyst system.

7. A process according to claim 6 , wherein the catalyst system comprises at least two active catalytic components comprising, as a first active catalyst component, one or more materials selected from transition metals from groups 8, 9 or 10 or compounds thereof, with catalytic hydrogenation capabilities; and, as a second active catalyst component, one or more materials selected from tungsten, molybdenum and compounds and complexes thereof.

8. A process according to claim 1 , wherein the solvent comprises water.

9. A process according to claim 1 , wherein the saccharide-containing feedstock comprises one or more of glucose, sucrose and starch.

10. A process according to claim 1 , wherein the temperature in the reactor is in the range of from 150 to 250° C. and the pressure in the reactor is in the range of from 1 to 16 MPa.

11. A process for the catalytic conversion of a saccharide-containing feedstock in a reactor, wherein saccharide-containing feedstock is provided to the reactor as a feed stream through a feed pipe and is contacted with a catalyst system in the reactor and wherein, as the saccharide-containing feedstock is fed through the feed pipe, a solvent stream, initially comprising essentially no saccharide, is fed along the internal walls of the feed pipe, wherein the temperature of the saccharide-containing feedstock is initially below the degradation temperature of the saccharide and the temperature of the solvent stream is initially higher than the degradation temperature of the saccharide.

Assignments (3)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 15, 2025
From: SHELL OIL COMPANY
To: TECHNIP ENERGIES FRANCE
Reel/Frame 072574/0615 →
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 11, 2018
From: VAN DER HEIDE, EVERT; HUIZENGA, PIETER
To: SHELL OIL COMPANY
Reel/Frame 046316/0637 →