GB2188930A - Preparation of higher alcohols - Google Patents
Preparation of higher alcohols Download PDFInfo
- Publication number
- GB2188930A GB2188930A GB8708608A GB8708608A GB2188930A GB 2188930 A GB2188930 A GB 2188930A GB 8708608 A GB8708608 A GB 8708608A GB 8708608 A GB8708608 A GB 8708608A GB 2188930 A GB2188930 A GB 2188930A
- Authority
- GB
- United Kingdom
- Prior art keywords
- methanol
- hydrogen
- carbon monoxide
- catalyst
- carbon
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/32—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring increasing the number of carbon atoms by reactions without formation of -OH groups
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
A process for the production of higher alcohols in which the feedstock is a gas containing hydrogen, methanol and carbon monoxide in which the hydrogen to carbon monoxide ratio is below 0.33.
Description
SPECIFICATION
Feedstock process
Processes for the manufacture of compounds containing two or more carbon atoms, particularly alcohols (higher alcohols), from synthesis gas mixtures, i.e. mixtures containing carbon monoxide, hydrogen, and possibly carbon dioxide, do not usually give high yields of individual compounds.
One of the purposes of this invention is to raisethe yields of individual compounds when converting a one carbon atom feedstock into a product containing two or more carbon atoms.
The invention comprises using methanol as part of the feedstock and feeding this to the catalyst along with synthesis gas which is high in carbon monoxide content. The hydrogen to carbon monoxide ratio is below 0.33, preferably below 0.25, on entry to the catalyst.
Two extremes of this invention are the feeding of methanol in a carrier gas containing hydrogen and carbon monoxidewhich intotocomprisesthe feedstockto the catalyst. Alternatively some or all of the carbon monoxide/hydrogen carrier gas is recycled within a catalyst containing loop and the methanol is injected into the recycled gas before it contacts the catalyst.
Quantitatively the methanol could be injected into such a carrier gas whose composition was such that if contacted underthe prevailing conditions with a methanol synthesis catalyst further methanol would be produced.
Alternatively, methanol could be introduced into such a barrier gas such that the concentration of methanol present in the carbon monoxide/hydrogen carrier gas is greater than 25% of the (calculated) equilibrium methanol concentration the same conditions.
Advantages ofthis invention are that the exothermic heat formation of methanol is not added to any exotherm of any compounds formed, and that the product distribution is altered in thatthe starting point is, in part, now methanol ratherthan just carbon monoxide/dioxide and hydrogen.
1. A process forthe production of higher alcohols from a gas containing hydrogen, carbon monoxide and methanol in which the hydrogen to carbon monoxide ratio is below 0.33.
2. Higheralcoholswhen produced by means of this invention.
**WARNING** end of DESC field may overlap start of CLMS **.
Claims (2)
1. A process forthe production of higher alcohols from a gas containing hydrogen, carbon monoxide and methanol in which the hydrogen to carbon monoxide ratio is below 0.33.
2. Higheralcoholswhen produced by means of this invention.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB8608746A GB8608746D0 (en) | 1986-04-10 | 1986-04-10 | Feedstock process |
Publications (3)
Publication Number | Publication Date |
---|---|
GB8708608D0 GB8708608D0 (en) | 1987-05-13 |
GB2188930A true GB2188930A (en) | 1987-10-14 |
GB2188930B GB2188930B (en) | 1990-04-04 |
Family
ID=10595985
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8608746A Pending GB8608746D0 (en) | 1986-04-10 | 1986-04-10 | Feedstock process |
GB8708608A Expired - Lifetime GB2188930B (en) | 1986-04-10 | 1987-04-10 | Preparation of higher alcohols |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB8608746A Pending GB8608746D0 (en) | 1986-04-10 | 1986-04-10 | Feedstock process |
Country Status (1)
Country | Link |
---|---|
GB (2) | GB8608746D0 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0311297A2 (en) * | 1987-10-08 | 1989-04-12 | Coal Industry (Patents) Limited | Alcohol synthesis process |
-
1986
- 1986-04-10 GB GB8608746A patent/GB8608746D0/en active Pending
-
1987
- 1987-04-10 GB GB8708608A patent/GB2188930B/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0311297A2 (en) * | 1987-10-08 | 1989-04-12 | Coal Industry (Patents) Limited | Alcohol synthesis process |
EP0311297A3 (en) * | 1987-10-08 | 1990-01-03 | Coal Industry (Patents) Limited | Alcohol synthesis process |
Also Published As
Publication number | Publication date |
---|---|
GB8708608D0 (en) | 1987-05-13 |
GB2188930B (en) | 1990-04-04 |
GB8608746D0 (en) | 1986-05-14 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PCNP | Patent ceased through non-payment of renewal fee |