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US4170605A
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Synthesis of ethylene glycol from carbon monoxide and hydrogen using a ruthenium complex catalyst and a pyridine base ligand
Assignee: Gulf Research and Development Co
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Filing: 1978-04-06
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Granted: 1979-10-09
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Expires: 1998-04-06
Abstract
Abstract A process for selectively producing ethylene glycol which comprises contacting carbon monoxide and hydrogen with a ruthenium complex catalyst and a pyridine base ligand.
Inventors
- 👤 Roger C. Williamson
- 👤 Thaddeus P. Kobylinski
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-31 09:46
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/15; C07C29/151; C07C29/1512; C07C29/1514; C07C29/153; C07C29/156; C07C29/157
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
148 words
In a process for the selective production of ethylene glycol from carbon monoxide and hydrogen in the presence of a catalyst, the improvement which comprises contacting carbon monoxide and hydrogen with a catalyst consisting essentially of a catalytic amount of a ruthenium complex catalyst selected from the group consisting of ruthenium tris (acetylacetonate), ruthenium trihydroxide, and mixtures thereof; and a pyridine base ligand, wherein the carbon monoxide and hydrogen are in a molar ratio of from about 1:10 to about 10:1, the ruthenium complex catalyst concentration is from about 1×10 -6 gm moles/liter to about 1 gm mole/liter based on the reaction mixture, the ruthenium complex catalyst and ligand are in a molar ratio of from about 1:1 to about 1:10, the reaction pressure is from about 10,000 psig to about 50,000 psig, and the reaction temperature is in the range of about 100° to about 600° C.
Claim 2
Dependent Claim
148 words
In a process for the selective production of ethylene glycol from carbon monoxide and hydrogen in the presence of a catalyst, the improvement which comprises contacting carbon monoxide and hydrogen with a catalyst consisting essentially of a catalytic amount of a ruthenium complex catalyst selected from the group consisting of ruthenium tris (acetylacetonate), ruthenium trihydroxide, and mixtures thereof; and a pyridine base ligand, wherein the carbon monoxide and hydrogen are in a molar ratio of from about 1:10 to about 10:1, the ruthenium complex catalyst concentration is from about 1×10 -6 gm moles/liter to about 1 gm mole/liter based on the reaction mixture, the ruthenium complex catalyst and ligand are in a molar ratio of from about 1:1 to about 1:10, the reaction pressure is from about 10,000 psig to about 50,000 psig, and the reaction temperature is in the range of about 100° to about 600° C.
Claim 3
Dependent Claim
24 words
The process according to claim 1 wherein the carbon monoxide and hydrogen are in a molar ratio of from about 1:3 to about 3:1.
Claim 4
Dependent Claim
14 words
The process of claim 1 wherein the ruthenium complex catalyst is ruthenium tris (acetylacetonate).
Claim 5
Dependent Claim
29 words
The process of claim 1 wherein the ruthenium complex catalyst concentration is from about 3×10 -4 gm moles/liter to about 3×10 -2 gm moles/liter based on the reaction mixture.
Claim 6
Dependent Claim
23 words
The process of claim 1 wherein the ligand is selected from the group consisting of 2-hydroxypyridine, 2-aminopyridine, or 2(methylamino) pyridine and mixtures thereof.
Claim 7
Dependent Claim
11 words
The process according to claim 1 wherein the ligand is 2-hydroxypyridine.
Claim 8
Dependent Claim
24 words
The process of claim 5 wherein the ruthenium complex catalyst and ligand are in a molar ratio of from about 1:1 to about 1:5.
Claim 9
Dependent Claim
23 words
The process according to claim 1 including a solvent selected from the group consisting of alcohols, ethers, paraffins or aromatics and mixtures thereof.
Claim 10
Dependent Claim
11 words
The process according to claim 8 wherein the solvent is propanol.
Claim 11
Dependent Claim
24 words
The process of claim 8 wherein the ruthenium complex catalyst and solvent are in a molar ratio of from about 1:10 to about 10:1.
Claim 12
Dependent Claim
24 words
The process of claim 8 wherein the ruthenium complex catalyst and solvent are in a molar ratio of from about 1:5 to about 5:1.
Claim 13
Dependent Claim
22 words
The process according to claim 1 having a pressure of from about 20,000 psig (136.60 MPa) to about 30,000 psig (204.90 MPa).
Claim 14
Dependent Claim
17 words
The process of claim 1 having a temperature of from about 180° C. to about 300° C.
Claim 15
Dependent Claim
20 words
The process according to claim 1 having a reaction time period of from about 0.5 hour to about 10 hours.
Claim 16
Dependent Claim
20 words
The process according to claim 1 having a reaction time period of from about 1 hour to about 5 hours.
References Cited (Backward Citations)
US2549470A
Cited
US3957857A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1982-10-08 | 1983-04-09 | 1983-10-09 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1986-10-08 | 1987-04-09 | 1987-10-09 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1990-10-08 | 1991-04-09 | 1991-10-09 | $7700.00 | Window Closed / Lapsed |