Method for thermal conversion of ketoacids and hydrotreament to hydrocarbons

Patent metadata

Field	Value
Publication number	US-10364396-B2
Application number	US-201615276144-A
Country	US
Kind code	B2
Filing date	Sep 26, 2016
Priority date	Mar 26, 2014
Publication date	Jul 30, 2019
Grant date	Jul 30, 2019

Abstract

The present disclosure relates to thermal conversion of ketoacids, including methods for increasing the molecular weight of ketoacids, the method including the steps of providing in a reactor a feedstock comprising at least one ketoacid. The feedstock is then subjected to one or more C-C-coupling reaction(s) by heating the feedstock to temperature of 200-500° C. in the absence of a catalyst.

First claim

What is claimed is:

1. A method for increasing the molecular weight of ketoacids, the method comprising:
a) providing in a reactor a feedstock containing at least 80 wt % of at least one ketoacid; and
b) subjecting the feedstock to one or more C-C-coupling reaction(s) to produce a C-C-coupling reaction product;
wherein the one or more C-C-coupling reaction(s) are conducted by heating the feedstock to a temperature of 205-400° C. in an absence of a catalyst, and wherein the one or more C-C-coupling reaction(s) are conducted mainly in the liquid phase.

2. The method according to claim 1 , wherein the feedstock is heated to a temperature of 245-350° C.

3. The method according to claim 1 , wherein the one or more C-C-coupling reaction(s) are conducted in a single reactor.

4. The method according to claim 1 , wherein the one or more C-C-coupling reaction(s) are conducted at a pressure of between 10-100 bar.

5. The method according to claim 1 , wherein the feedstock contains at least 90 wt-% of at least one ketoacid.

6. The method according to claim 1 , wherein the feedstock further comprises an ester of a ketoacid.

7. The method according to claim 1 , wherein the feedstock comprises levulinic acid.

8. The method according to claim 1 , further comprising subjecting the C-C-coupling reaction product to a hydrodeoxygenation step and optionally an isomerization step to produce a hydrocarbon product.

9. The method according to claim 8 , wherein the hydrodeoxygenation step is conducted in the presence of a hydrodeoxygenation catalyst comprising a hydrogenation metal on a support.

10. The method according to claim 8 , wherein the method comprises subjecting the C-C-coupling reaction product to a hydrodeoxygenation step and an isomerization step, and wherein said isomerization step is conducted in the presence of an isomerization catalyst.

11. The method according to claim 1 , wherein the C-C-coupling reaction(s) are conducted at a pressure of between 10-50 bar.

12. The method according to claim 2 , wherein the C-C-coupling reaction(s) are conducted at a pressure of between 10-100 bar.

Assignees

• Neste Oyj

Inventors

• Myllyoja Jukka
• Piilola Rami

Classifications

• C10L1/026

  for compression ignition · CPC title

• C10G2400/04

  Diesel oil · CPC title

• C10G50/00

  Production of liquid hydrocarbon mixtures from lower carbon number hydrocarbons, e.g. by oligomerisation · CPC title

• C10G3/42

  Catalytic treatment · CPC title

• C10G3/40

  Thermal non-catalytic treatment · CPC title