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US4275243A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for producing hydroxybutyraldehyde

Assignee: Tosoh Corp
•
Filing: 1979-08-27
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Granted: 1981-06-23
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Expires: 1999-08-27
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Abstract

Abstract An organic tri-substituted phosphine having a boiling point of at least 200 DEG C. and a reaction medium having a boiling point of at least 200 DEG C. are used in a hydroformylation of allyl alcohol with carbon monoxide and hydrogen in the presence of a rhodium complex catalyst. The concentration of the organic phosphine is 5x10-4 to 0.3 mol. per 1 liter of the reaction medium. The reaction medium is distilled at lower than 80 DEG C. under a reduced pressure and the bottom residue as the catalyst solution is recycled. The hydroformylation can be repeated by using the bottom residue as the catalyst solution.

Inventors

  • 👤 Toshihiro Saito
  • 👤 Shoji Arai
  • 👤 Yukihiro Tsutsumi

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 14:22
CPC Classifications
C; C07; C07C; C07C45/00; C07C45/49; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/584

Claims Analysis

Total Claims: 8
Claim 1
Independent Claim 120 words
In a process for producing hydroxybutyraldehyde by reacting allyl alcohol with carbon monoxide and hydrogen in a reaction medium in the presence of a rhodium complex catalyst having an organic tri-substituted phosphine, the improvement wherein the organic tri-substituted phosphine and the reaction medium have a boiling point higher than 200° C., the phosphine is used at a concentration of 5×10 -4 to 0.3 mol. per 1 liter of the reaction medium in the hydroformylation and then a distillative separation of the reaction mixture is carried out in the absence of oxygen at a temperature of 20° C. to 80° C. under a reduced pressure to separate the reaction product from the solution of the rhodium complex in the reaction medium.
Claim 2
Dependent Claim 120 words
In a process for producing hydroxybutyraldehyde by reacting allyl alcohol with carbon monoxide and hydrogen in a reaction medium in the presence of a rhodium complex catalyst having an organic tri-substituted phosphine, the improvement wherein the organic tri-substituted phosphine and the reaction medium have a boiling point higher than 200° C., the phosphine is used at a concentration of 5×10 -4 to 0.3 mol. per 1 liter of the reaction medium in the hydroformylation and then a distillative separation of the reaction mixture is carried out in the absence of oxygen at a temperature of 20° C. to 80° C. under a reduced pressure to separate the reaction product from the solution of the rhodium complex in the reaction medium.
Claim 3
Dependent Claim 121 words
In a process for producing hydroxybutyraldehyde by reacting allyl alcohol with carbon monoxide and hydrogen in a reaction medium in the presence of a rhodium complex catalyst having an organic trisubstituted phosphine, the improvement wherein the organic trisubstituted phosphine and the reaction medium have a boiling point higher than 200° C., the phosphine is used at a concentration of 5×10 -4 to 0.3 mol. per 1 liter of the reaction medium in the hydroformylation, and then a distillative separation of the reaction mixture is carried out in the absence of oxygen at a temperature lower than 80° C. and at a pressure of 1-20 mmHg, to separate the reaction product from the solution of the rhodium complex in the reaction medium.
Claim 4
Dependent Claim 121 words
In a process for producing hydroxybutyraldehyde by reacting allyl alcohol with carbon monoxide and hydrogen in a reaction medium in the presence of a rhodium complex catalyst having an organic trisubstituted phosphine, the improvement wherein the organic trisubstituted phosphine and the reaction medium have a boiling point higher than 200° C., the phosphine is used at a concentration of 5×10 -4 to 0.3 mol. per 1 liter of the reaction medium in the hydroformylation, and then a distillative separation of the reaction mixture is carried out in the absence of oxygen at a temperature lower than 80° C. and at a pressure of 1-20 mmHg, to separate the reaction product from the solution of the rhodium complex in the reaction medium.
Claim 5
Dependent Claim 31 words
The process of claims 1 or 2, wherein said rhodium complex catalyst is used at a concentration ranging from 0.1 to 15 mg atom per 1 liter of the reaction medium.
Claim 6
Dependent Claim 39 words
The process of claims 1 or 2, wherein said organic trisubstituted phosphine has the formula PR 3 , wherein the total number of carbon atoms in the 3R's in said formula PR 3 is in the range of 10-30.
Claim 7
Dependent Claim 31 words
The process of claims 1 or 2, wherein the organic phosphine is used at a ratio of 5 to 200 atoms of phosphorous to 1 atom of rhodium of said catalyst.
Claim 8
Dependent Claim 71 words
The process of claims 1 or 2, wherein said reaction medium is selected from the group consisting of saturated hydrocarbons having at least 12 carbon atoms, aromatic hydrocarbons having at least 9 carbon atoms, alcohols having at least 9 carbon atoms, ethers having at least 10 carbon atoms, ether or ether glycols of polyhydric alcohols having at least 7 carbon atoms, esters having at least 9 carbon atoms, and mixtures thereof.

References Cited (Backward Citations)

US3515757A Cited
US3511880A Cited
US3946082A Cited
GB1493154A Cited
US4064145A Cited
JPS5278809A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-06-22 1984-12-22 1985-06-23 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-06-22 1988-12-22 1989-06-23 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-06-22 1992-12-22 1993-06-23 $7700.00 Window Closed / Lapsed

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