Methods of deoxygenating bio-based material and production of bio-based terephtalic acid and olefinic monomers

Patent metadata

Field	Value
Publication number	US-11525094-B2
Application number	US-201414782879-A
Country	US
Kind code	B2
Filing date	Apr 8, 2014
Priority date	Apr 8, 2013
Publication date	Dec 13, 2022
Grant date	Dec 13, 2022

Abstract

The present invention relates to a method of deoxygenating tall oil pitch, yielding aliphatic and aromatic hydrocarbons. The invention even comprises turning the aliphates into polymerizable olefins by steam cracking, and turning the aromates into polymerizable terephthalic acid by oxygenation and, as necessary, rearrangement. The monomers can be used for the production of polymers of partially or completely biologic origin. According to the invention, tall oil pitch is first heated to turn it into liquid, which is then fed into a catalyst bed and catalytically deoxygenated with hydrogen. The deoxygenation catalyst is preferably a Ni—Mo catalyst and, in addition, a cracking catalyst can be used, such as an acidic zeolite catalyst. The deoxygenated product stream is cooled down so as to obtain a liquid, which is distilled for separation of the aliphatic and aromatic hydrocarbons for use in the production of the respective monomers and finally polymers.

First claim

The invention claimed is:

1. A method of deoxygenating tall oil pitch, wherein
tall oil pitch obtained as a non-distillable residue from vacuum or steam distillation of crude tall oil, which contains a share of fatty and resin acids and/or their derivatives, is heated to a temperature sufficient to turn it liquid;
said liquid is fed into a catalyst bed formed by a solid bed material, to bring it into contact with hydrogen and at least two catalysts in said catalyst bed, said catalysts including a NiMo deoxygenation catalyst and a cracking catalyst which are different from each other and located sequentially apart from each other in the catalyst bed;
the feed is catalytically deoxygenated with hydrogen;
the feed is cracked by means of the cracking catalyst; and
a gaseous effluent from the bed is cooled down, to yield a liquid product, which comprises aliphatic and aromatic hydrocarbons and which has been substantially completely deoxygenated:

wherein conversion of the oxygenous components of the feed to hydrocarbons is above 99%.

2. The method of claim 1 , wherein the tall oil pitch is heated to the temperature of at least 55° C. to turn it liquid.

3. The method of claim 1 wherein the liquid yield is divided into a fraction rich in aliphatic hydrocarbons and a fraction rich in aromatic hydrocarbons.

4. The method of claim 1 wherein one of the catalysts of the deoxygenation stage is a catalyst comprising NiMoS.

5. The method of claim 1 wherein one of the catalysts of the cracking stage is acidic.

6. The method of claim 5 wherein the acidic catalyst is a ZSM-5 zeolite catalyst.

7. The method of claim 1 wherein the deoxygenation is carried out at a temperature of 300-450° C.

8. The method of claim 7 wherein the deoxygenation is carried out by raising the temperature so as to be within 320-370° C. at the start of the process and within 370-430° C. at the end of the process.

9. The method of claim 1 wherein the deoxygenation is carried out at a pressure of 50-100 bars.

10. The method of claim 1 wherein the weight hourly space velocity (WHSV) in the catalyst bed is 0.2-1.0 1/h.

11. The method of claim 1 wherein water contained in the liquid yield is separated from the produced liquid hydrocarbons.

12. The method of claim 1 wherein one or more aromatic hydrocarbons that can be converted into terephthalic acid are separated from the reaction yield by distillation.

13. The method of claim 1 wherein the aromatic hydrocarbon that is separated from the reaction yield is o-xylene, m-xylene or p-xylene, or a cymene.

14. A method of producing bio-based terephthalic acid, wherein
tall oil pitch obtained as a non-distillable residue from vacuum or steam distillation of crude tall oil, which tall oil pitch contains a share of fatty and resin acids and/or their derivatives, is heated to a temperature sufficient to turn it liquid;
said liquid is fed into a catalyst bed formed by a solid bed material, to bring it into contact with hydrogen and at least two catalysts in said catalyst bed, said catalysts including a NiMo deoxygenation catalyst and a cracking catalyst which are different from each and located sequentially apart from each other in the catalyst bed;
the feed is catalytically deoxygenated with hydrogen;
the feed is cracked by means of the cracking catalyst;
a gaseous effluent from the bed is cooled down, to yield a liquid intermediate product, which comprises aliphatic and aromatic hydrocarbons and which has been substantially completely deoxygenated;
an aromatic hydrocarbon that can be converted into terephthalic acid is separated from said intermediate product; and
the separated hydrocarbon is subjected to oxygenation and a possible rearrangement reaction, so that terephthalic acid is obtained as the end product;

wherein conversion of the oxygenous components of the feed to hydrocarbons is above 99%.

15. The method of claim 14 wherein oxygenation of the separated hydrocarbon is carried out with a chemical or biochemical oxidizer.

16. The method of claim 15 wherein the oxidizer is chromic acid.

17. The method of claim 14 wherein p-xylene is separated from the said intermediate product and oxidized into terephthalic acid.

18. The method of claim 14 wherein o-xylene is separated from the said intermediate product and oxidized into phthalic acid, which thereafter is converted by means of the Raecke or Henkel rearrangement reaction into terephthalic acid.

19. The method of claim 18 wherein the conversion into terephthalic acid is carried out by using a salt catalyst.

20. The method of claim 19 , wherein the salt catalyst is a cobalt-magnesium salt.

21. The method of claim 14 wherein in the rearrangement, the reaction mixture is heated to a temperature of at least 300° C., in an inert gas atmosphere.

22. The method of claim 21 wherein the reaction mixture is heated to a temperature of 330-500° C.

23. A method of producing olefinic monomers for the production of a polymer, wherein
tall oil pitch obtained as a non-distillable residue from vacuum or steam distillation of crude tall oil, which tall oil pitch contains a share of fatty and resin acids and/or their derivatives, is heated to a temperature sufficient to turn it liquid;
said liquid is fed into a catalyst bed formed by a solid bed material, to bring it into contact with hydrogen and at least two catalysts in said catalyst bed, said catalysts including a NiMo deoxygenation catalyst and a cracking catalyst which are different from each and located sequentially apart from each other in the catalyst bed—the feed is catalytically deoxygenated with hydrogen;
the feed is cracked by means of the cracking catalyst;
a gaseous effluent from the bed is cooled down, to yield a liquid intermediate product, which comprises aliphatic and aromatic hydrocarbons and which has been substantially completely deoxygenated;
a fraction rich in aliphatic hydrocarbons is separated from said intermediate product; and
said fraction is subjected to steam cracking to obtain a product, which contains polymerizable olefins;

wherein conversion of the oxygenous components of the feed to hydrocarbons is above 99%.

24. The method of claim 23 , wherein ethylene and/or propylene are produced by the steam cracking.

Assignees

• Stora Enso Oyj

Inventors

• Räsänen Jari
• Harlin Ali
• Aaltonen Olli
• Linnekoski Juha
• Anthonykutty Jinto

Classifications

• C10G2300/1014

  of vegetal origin · CPC title

• C08G63/183

  Terephthalic acids · CPC title

• C07C63/26

  1,4 - Benzenedicarboxylic acid · CPC title

• Y02P30/20

  using bio-feedstock · CPC title

• C10G3/50 Primary

  in the presence of hydrogen, hydrogen donors or hydrogen generating compounds · CPC title