Process for converting syngas to aromatics and catalyst system suitable therefor

US10196325B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-10196325-B2
Application numberUS-201514965099-A
CountryUS
Kind codeB2
Filing dateDec 10, 2015
Priority dateJan 15, 2015
Publication dateFeb 5, 2019
Grant dateFeb 5, 2019

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  1. Title

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  2. Abstract

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

The present invention relates to a multistage process and catalyst system therefor to convert syngas to aromatics. In a first stage, syngas is converted to a C 1 -C 4 alcohol mixture by contacting syngas with a first catalyst comprising rhodium or copper at moderate temperature. In a second stage, the C 1 -C 4 alcohol mixture is converted into an aromatic product by contact with a second catalyst comprising a molecular sieve and at least one Group 8-14 element, the molecular sieve having a Constraint Index about 1 to 12 and a silica to alumina ratio of about 10 to 100 at effective conversion conditions. The final aromatic product is rich in benzene, toluene, and xylenes (e.g. greater than 50% aromatics on a hydrocarbon basis).

First claim

Opening claim text (preview).

What is claimed is: 1. A multistage process for converting syngas to aromatics comprising: (a) contacting syngas in a first reactor with a first catalyst comprising rhodium or copper to produce a C1-C4 alcohol mixture at a gas hourly space velocity (GHSV) of at least 500 hr 1 , wherein the GHSV is the liters of syngas per hour flowing through the first reactor divided by the liters of the first catalyst within the first reactor; and (b) contacting said C1-C4 alcohol mixture in a second reactor with a second catalyst comprising a molecular sieve to produce an aromatic product, wherein said molecular sieve is a ZSM-5 zeolite having a silica to alumina ratio of about 10 to 100, and wherein the second catalyst comprises said ZSM-5 zeolite physically mixed with gallium and zinc substantially in the form of mixed oxides thereof. 2. The process of claim 1 , wherein the reaction of syngas with the first catalyst in step (a) to produce said C 1 -C 4 alcohol mixture has a yield of at least 50%. 3. The process of claim 1 , wherein said C 1 -C 4 alcohol mixture contains at least 10% by weight of a methanol, ethanol and propanol mixture. 4. The process of claim 3 , wherein said methanol, ethanol and propanol mixture contains at least 50% by weight of ethanol and propanol. 5. The process of claim 1 , wherein said syngas has a volume ratio of hydrogen to carbon monoxide of 20:1 to 0.1:1. 6. The process of claim 1 , wherein said first catalyst comprises Rh—Mn/SiO 2 . 7. The process of claim 1 , wherein step (a) is carried out at a reaction temperature of 260 to 300° C. 8. The process of claim 1 , wherein said aromatic product contains at least 50% by weight of a benzene, toluene and xylene mixture on a hydrocarbon basis. 9. The process of claim 8 , wherein said benzene, toluene and xylene mixture contains at least 20% by weight of xylenes on a hydrocarbon basis. 10. The process of claim 1 , wherein step (b) is carried out at a reaction temperature of 350 to 450° C. 11. The process of claim 1 , wherein step (b) is carried out at a reaction pressure of 0.1 to 2.8 MPaa. 12. The process of claim 1 , wherein step (b) is carried out at a weight hourly space velocity of 0.1 to 20. 13. The process of claim 1 , further comprising separating at least a portion of said aromatic product to form a C 8 product stream and at least one of a C 7− stream and a C 9+ stream. 14. The process of claim 1 , wherein the first catalyst comprises Rhodium (Rh), Manganese (Mn), Iron (Fe), M 1 , and M 2 , wherein M 1 comprises one or both of Lithium (Li) and Sodium (Na), and wherein M 2 comprises one or both of Ruthenium (Ru) and Iridium (Ir). 15. The process of claim 14 , wherein the first catalyst comprises 0.1 to 3 wt. % Rh, and wherein: the weight ratio of Mn/Rh in the first catalyst is 0.5-12; the weight ratio of Fe/Rh in the first catalyst is 0.01-0.5; the weight ratio of M 1 /Rh in the first catalyst is 0.04-0.2; and the weight ratio of M 2 /Rh in the first catalyst is 0.1-1.0.

Assignees

Inventors

Classifications

  • Benzene · CPC title

  • containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead · CPC title

  • C07C1/20Primary

    starting from organic compounds containing only oxygen atoms as heteroatoms · CPC title

  • Xylenes · CPC title

  • Toluene · CPC title

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What does patent US10196325B2 cover?
The present invention relates to a multistage process and catalyst system therefor to convert syngas to aromatics. In a first stage, syngas is converted to a C 1 -C 4 alcohol mixture by contacting syngas with a first catalyst comprising rhodium or copper at moderate temperature. In a second stage, the C 1 -C 4 alcohol mixture is converted into an aromatic product by contact with a second cata…
Who is the assignee on this patent?
Exxonmobil Chemical Patents Inc
What technology area does this patent fall under?
Primary CPC classification C07C1/20. Mapped technology areas include Chemistry & Metallurgy.
When was this patent published?
Publication date Tue Feb 05 2019 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 1 related publication on this page (citations in our corpus or others sharing the same primary CPC).