Process for the preparation of aromatic compounds

Patent metadata

Field	Value
Publication number	US-10927498-B2
Application number	US-201515508963-A
Country	US
Kind code	B2
Filing date	Sep 22, 2015
Priority date	Sep 22, 2014
Publication date	Feb 23, 2021
Grant date	Feb 23, 2021

Abstract

A process for the preparation of small aromatic compounds from black liquor comprising:
providing black liquor that derives from alkaline treatment of wood chips; subjecting the black liquor to a pyrolysis treatment to yield a pyrolysed black liquor gas and a solid mass comprising char and salts in a first reactor, wherein the salts substantially derive from the treatment of black liquor; contacting at least part of the pyrolysed black liquor gas with a catalyst in a second reactor, which is different from the first reactor to provide a conversion treatment to yield a conversion product; and recovering small aromatic compounds from the conversion product.

First claim

The invention claimed is:

1. A process for the preparation of small aromatic compounds from black liquor comprising:
adding hardwood chips and an alkaline solution to a digester and contacting the hardwood chips with the alkaline solution thereby digesting the hardwood chips to yield a cellulose pulp and a black liquor;
adding the black liquor to a first reactor and subjecting the black liquor to a pyrolysis treatment to yield a pyrolysed black liquor gas and a solid mass comprising char and salts wherein the salts substantially derive from the treatment of black liquor;
separating the pyrolysed black liquor gas and the solid mass and contacting at least part of the pyrolysed black liquor gas with a catalyst in a second reactor, wherein the second reactor is different from the first reactor, to provide a conversion treatment to yield a conversion product; and
recovering small aromatic compounds from the conversion product with a condenser to form a condensed stream comprising small aromatic compounds.

2. The process according to claim 1 , wherein the pyrolysis treatment is carried out without the addition of a catalyst.

3. The process according to claim 1 , wherein the pyrolysis treatment of black liquor is carried out at a temperature of 350° C. to 700° C. at a pressure of between 0.1 to 6 bar(a).

4. The process according to claim 1 , wherein at least a part of the solid mass is collected and heated to a temperature that is sufficiently high to recover the salt in the solid mass.

5. The process according to claim 1 , wherein the conversion treatment involves the conversion of complex aromatic compounds to small aromatic compounds, the conversion of oxygen containing aromatic and oxygen containing aliphatic compounds to small aromatic compounds without oxygen atoms, and/or the conversion of hydrocarbons.

6. The process according to claim 1 , wherein the conversion treatment occurs at a temperature between 200° C. and 1000° C.

7. The process according to claim 1 , wherein in the conversion treatment the catalyst is present in a weight ratio of pyrolysed black liquor gas to catalyst in the range of 5:1 to 1:20.

8. The process according to claim 1 , wherein the catalyst is a zeolitic catalyst selected from aluminosilicates, SAPOs, silicalites, and a combination thereof.

9. The process according to claim 1 , wherein the catalyst is acidic and is made acidic by ion exchange with ammonium salts and subsequent calcination.

10. The process according to claim 1 , wherein the catalyst has a silica to alumina ratio from 5 to 300.

11. The process according to claim 1 , wherein the catalyst has a largest internal pore size in the range of 4.5 to 12 Å.

12. The process according to claim 1 , wherein the catalyst is selected from the group consisting of ferrierite, zeolite beta, zeolite Y, zeolite X, mordenite, zeolite A, and a combination thereof.

13. The process according to claim 1 , wherein the catalyst is bound by means of a binder to form a bound catalyst, and wherein the binder is selected from the group consisting of alumina, silica, silica alumina, titania, zirconia, kaolin and a mixture thereof.

14. The process according to claim 13 , wherein the amount of binder in the bound catalyst is in the range of 0 to 80% by wt, based on the weight of the bound catalyst.

15. The process according to claim 1 , wherein the conversion treatment is carried out in a fixed bed, moving bed or fluidized bed.

16. The process according to claim 1 , wherein the recovering of aromatic compounds occurs by subjecting the condensed stream comprising small aromatic compounds to fractionation.

Assignees

• Huntsman Int Llc

Inventors

• Heeres André
• Schenk Niels Jan
• Zeeuw Arend-Jan
• De Waele Bart
• Kamminga Kornelis Jan

Classifications

• C10G51/04

  including only thermal and catalytic cracking steps · CPC title

• C10G3/00

  Production of liquid hydrocarbon mixtures from oxygen-containing organic materials, e.g. fatty oils, fatty acids (production from non-melting solid oxygen-containing carbonaceous materials C10G1/00) · CPC title

• C10G1/00 Primary

  Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal (mechanical winning of oil from oil-shales, oil-sand, or the like B03B) · CPC title

• C10G1/002 Primary

  in combination with oil conversion- or refining processes · CPC title

• D21C11/125 Primary

  Decomposition of the pulp liquors in reducing atmosphere or in the absence of oxidants, i.e. gasification or pyrolysis · CPC title