Molten salt catalytic compositions and methods for the cracking of carbon-containing feedstocks

Patent metadata

Field	Value
Publication number	US-11834397-B1
Application number	US-202318153163-A
Country	US
Kind code	B1
Filing date	Jan 11, 2023
Priority date	May 29, 2020
Publication date	Dec 5, 2023
Grant date	Dec 5, 2023

Abstract

A catalyst composition includes a metal catalyst dispersed in a molten eutectic mixture of alkali metal or alkaline earth metal carbonates or hydroxides. A process for the catalytic cracking of hydrocarbons includes contacting in a reactor system a carbon-containing feedstock with at least one catalyst in the presence of oxygen to generate olefinic and/or aromatic compounds; and collecting the olefinic and/or aromatic compounds; wherein: the at least one catalyst includes a metal catalyst dispersed in a molten eutectic mixture of alkali metal or alkaline earth metal carbonates or hydroxides. A process for preparing the catalyst includes mixing metal catalyst precursors selected from transition metal compounds and rare-earth metal compounds and a eutectic mixture of alkali metal or alkaline earth metal carbonates or hydroxides and heating it. A use of the catalyst in the catalytic cracking process of hydrocarbons.

First claim

What is claimed is:

1. A process for the catalytic cracking of a carbon-containing feedstock, the process comprising:
contacting, in a reactor system, the carbon-containing feedstock with a heterogeneous catalyst composition, said contacting occurring in the presence of an oxidant, to generate a product chemical compound; and
collecting the product chemical compound,
wherein:
the heterogeneous catalyst composition comprises a metal catalyst dispersed in a molten salt matrix comprising a eutectic mixture of alkali metal or alkaline earth metal carbonates or hydroxides; and
the metal catalyst comprises a transition metal compound and a rare-earth metal compound.

2. The process of claim 1 , which is an autothermal process.

3. The process of claim 1 , wherein the contacting is conducted at a temperature of about 750° C. or less.

4. The process of claim 1 , which is a continuous process, a semi-continuous process, or a batch process.

5. The process of claim 1 , wherein the product chemical compound comprises light olefins, α-olefins, terminal dienes, substituted and unsubstituted aromatic compounds, aldehydes, oxygenates, or a combination thereof.

6. The process of claim 1 , wherein the product chemical compound comprises ethene, propene, 1-butene, 2-methyl-but-1-ene, 1-n-pentene, 1-n-hexene, 2-methyl-pent-1-ene, 3-methyl-pent-1-ene, 1,3-butadiene, 1,3-pentadiene, 1,4-pentadiene, 1,3-hexadiene, 1,4-hexadiene, 1,5-hexadiene, benzene, toluene, ethylbenzene, xylenes, styrene, α-methylstyrene, naphthalene, anthracene, or a combination thereof.

7. The process of claim 1 , wherein the carbon-containing feedstock comprises a polymer comprising polyethylene, polypropylene, polyisobutylene, polybutadiene, polystyrene, poly-α-methylstyrene, polacrylates, poly(meth)acrylates, polyvinylchloride, polyethylene terephthalate, or a mixture of any two or more thereof.

8. The process of claim 1 , wherein the carbon-containing feedstock comprises a refinery range hydrocarbon comprising asphalt, vacuum resid, heavy residual oil, paraffin wax, pyrolysis wax, lubricating oil, diesel, kerosene, naphtha, gasoline, or a combination thereof.

9. The process of claim 1 , wherein the carbon-containing feedstock comprises a refinery range hydrocarbon comprising n-hexane.

10. The process of claim 1 , wherein the carbon-containing feedstock comprises a refinery range hydrocarbon comprising n-hexadecane.

11. The process of claim 1 , wherein the carbon-containing feedstock comprises lignin, fatty acid, plant-based oil, municipal solid waste, paper waste, or a mixture of any two or more thereof.

12. The process of claim 1 , wherein the oxidant comprises at least one member selected from the group consisting of O 2 , NO x , SO x , a nitrate salt, hydrogen peroxide, an organic peroxide, and a non-metal element oxide, such as boron oxide, nitrogen oxide, phosphorus oxide, sulfur oxide, chlorine oxide, and bromine oxide.

13. The process of claim 1 , wherein the oxidant is oxygen and is introduced to the reactor as a purified O 2 stream, air, or a mixture of O 2 or air with a diluent, wherein the diluent is methane, carbon dioxide, nitrogen, argon, helium, or a mixture thereof.

14. The process of claim 1 , wherein the reactor system comprises a single reactor or at least a first reactor and a second reactor in series.

15. The process of claim 1 , wherein the reactor system comprises a single reactor, and the heterogeneous catalyst is contacted with the carbon-containing feedstock.

16. The process of claim 1 , wherein the reactor system comprises a first reactor and a second reactor in series, and a heterogeneous catalyst composition in the first reactor is the same as or different than a heterogeneous catalyst composition in the second reactor.

17. The process of claim 1 , wherein the heterogeneous catalyst composition is prepared outside of the reactor system; then loaded into the reactor system to carry out the catalytic cracking of hydrocarbons.

18. The process of claim 1 , wherein the heterogeneous catalyst is prepared inside the reactor system, by loading the reactor system volume with a catalyst precursor mixture and heating it internally at the process temperature, and wherein the catalyst precursor mixture comprises a salt matrix comprising a eutectic mixture of alkali metal or alkaline earth metal carbonates or hydroxides and a metal catalyst precursor comprising a transition metal compound and a rare-earth metal compound.

19. The process of claim 18 , wherein the metal catalyst precursor comprises a carbonate of Ce.

20. The process of claim 18 , wherein the metal catalyst precursor comprises Cu and Ce carbonates, and the salt matrix comprises a mixture of Li, Na, and K carbonates or hydroxides.

21. The process of claim 18 , wherein the metal catalyst precursor comprises a mixture of Cu 2 (OH) 2 CO 3 and Ce 2 (CO 3 ) 3 ·xH 2 O, and the salt matrix comprises of a mixture of Li 2 CO 3 , Na 2 CO 3 , and K 2 CO 3 .

22. The process of claim 18 , wherein the metal catalyst precursor comprises a mixture of CuCO 3 and Ce(CO 3 ) 2 , and the salt matrix comprises of a mixture of Li 2 CO 3 , Na 2 CO 3 , and K 2 CO 3 .

23. The process of claim 1 , wherein the metal catalyst comprises Cu and Ce in a mol % ratio of about 0.10-0.20:1.00, respectively.

Assignees

• Braskem America Inc

Inventors

• Pushkarev Vladimir
• Kilgore Uriah
• Ambrass Charles
• Mitchell Scott
• Khurana Ishant

Classifications

• C07C4/025 Primary

  Oxidative cracking, autothermal cracking or cracking by partial combustion · CPC title

• C10G1/086

  Characterised by the catalyst used · CPC title

• C10G11/02

  characterised by the catalyst used · CPC title

• C10G27/04

  with oxygen or compounds generating oxygen · CPC title

• C10G2300/1092

  C2-C4 olefins · CPC title