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US4247486A Expired / Lapsed US ⏱️ 0.0 years remaining

Cyclic hydroformylation process

Assignee: Union Carbide Corp
•
Filing: 1977-03-11
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Granted: 1981-01-27
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Expires: 1997-03-11
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Abstract

Abstract Hydroformylating alpha-olefins in a cyclic homogeneous liquid phase process utilizing a modified rhodium catalyst, the improvement which involves utilizing a gas recycle to maintain the liquid level in the reaction and control build-up of high molecular weight components.

Inventors

  • 👤 Everard A. V. Brewester
  • 👤 Roy L. Pruett

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 18:05
CPC Classifications
C; C07; C07C; C07C45/00; C07C45/49; C07C45/50; Y; Y02; Y02P; Y02P20/00; Y02P20/50; Y02P20/582

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 196 words
The continuous process of producing aldehydes by the hydroformylation of alpha-olefins containing 2 to about 5 carbon atoms comprising: establishing a liquid body of a homogeneous mixture containing olefin, aldehyde products and higher boiling aldehyde condensation products continuously formed therein, a soluble rhodium catalyst complexed with carbon monoxide and a triarylphosphine, and at least ten moles of free triarylphosphine for each mole of rhodium metal; supplying to the liquid body a gaseous recycle stream comprising hydrogen and the olefin; supplying make-up quantities of carbon monoxide, hydrogen and olefin to the liquid body; maintaining the temperature of the liquid body at about 50° C. to about 140° C., the total pressure at less than about 400 psia, the carbon monoxide partial pressure at less than about 50 psia and the hydrogen partial pressure at less than about 200 psia; removing from said liquid body an amount of vaporous mixture comprising said olefin, hydrogen, vaporized aldehyde product, and an amount of vaporized aldehyde condensation products essentially equal to the rate of their formation in said body whereby the size of said body is maintained at a predetermined value; and recovering aldehyde product and aldehyde condensation product from said
Claim 2
Dependent Claim 196 words
The continuous process of producing aldehydes by the hydroformylation of alpha-olefins containing 2 to about 5 carbon atoms comprising: establishing a liquid body of a homogeneous mixture containing olefin, aldehyde products and higher boiling aldehyde condensation products continuously formed therein, a soluble rhodium catalyst complexed with carbon monoxide and a triarylphosphine, and at least ten moles of free triarylphosphine for each mole of rhodium metal; supplying to the liquid body a gaseous recycle stream comprising hydrogen and the olefin; supplying make-up quantities of carbon monoxide, hydrogen and olefin to the liquid body; maintaining the temperature of the liquid body at about 50° C. to about 140° C., the total pressure at less than about 400 psia, the carbon monoxide partial pressure at less than about 50 psia and the hydrogen partial pressure at less than about 200 psia; removing from said liquid body an amount of vaporous mixture comprising said olefin, hydrogen, vaporized aldehyde product, and an amount of vaporized aldehyde condensation products essentially equal to the rate of their formation in said body whereby the size of said body is maintained at a predetermined value; and recovering aldehyde product and aldehyde condensation product from said
Claim 3
Dependent Claim 11 words
The process of claim 1 wherein the gaseous recycle stream comprises
Claim 4
Dependent Claim 11 words
The process of claim 2 wherein the gaseous recycle stream comprises
Claim 5
Dependent Claim 9 words
The process of claim 2 wherein the triarylphosphine is
Claim 6
Dependent Claim 13 words
The process of claim 1 wherein the total pressure is less than 350
Claim 7
Dependent Claim 14 words
The process of claim 2 wherein the hydrogen to carbon monoxide is at a
Claim 8
Dependent Claim 12 words
The process of claim 2 wherein the temperature is from about 60°
Claim 9
Dependent Claim 10 words
The process of claim 1 wherein the alpha-olefin is 1-butene.

References Cited (Backward Citations)

US3239566A Cited
GB1228201A Cited
GB1387657A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-01-27 1984-07-28 1985-01-27 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-01-27 1988-07-28 1989-01-27 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-01-27 1992-07-28 1993-01-27 $7700.00 Window Closed / Lapsed

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