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US3979280A Expired / Lapsed US ⏱️ 0.0 years remaining

Separation of unsaturated compounds from liquid hydrocarbon mixtures containing same

Assignee: Wintershall Dea International AG
•
Filing: 1974-12-12
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Granted: 1976-09-07
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Expires: 1994-12-12
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Abstract

Abstract Unsaturated hydrocarbons are separated from liquid mixtures containing same by adsorbing the unsaturated compound using a metal-loaded macroporous exchange resin and desorbing the unsaturated compound using a normally gaseous hydrocarbon.

Inventors

  • 👤 Maximilian Dielacher
  • 👤 Uwe Hansen

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 08:49
CPC Classifications
C; C07; C07C; C07C7/00; C07C7/12

Claims Analysis

Total Claims: 12
Claim 1
Independent Claim 109 words
In a process for the separation of unsaturated compounds from liquid hydrocarbon mixtures containing same by contacting the mixture with a metal ion laden cation exchange resin having a specific surface area of at least 1 m 2 /g and an average pore diameter of greater than 10 A, the improvement which comprises adsorbing said unsaturated compounds on a macroporous dehydrated cation exchange resin laden with monovalent silver or copper ions and subsequently displacing said unsaturated compounds in liquid phase from said resin at a temperature between about 10° and 40°C. and a pressure between about 1 and 30 atmospheres using a normally gaseous olefin as the desorption medium.
Claim 2
Dependent Claim 109 words
In a process for the separation of unsaturated compounds from liquid hydrocarbon mixtures containing same by contacting the mixture with a metal ion laden cation exchange resin having a specific surface area of at least 1 m 2 /g and an average pore diameter of greater than 10 A, the improvement which comprises adsorbing said unsaturated compounds on a macroporous dehydrated cation exchange resin laden with monovalent silver or copper ions and subsequently displacing said unsaturated compounds in liquid phase from said resin at a temperature between about 10° and 40°C. and a pressure between about 1 and 30 atmospheres using a normally gaseous olefin as the desorption medium.
Claim 3
Dependent Claim 33 words
A process according to claim 1, characterized by using cation exchange resins having a specific surface area greater than 40 m 2 /gram and an average pore diameter of lesser than 250 A.
Claim 4
Dependent Claim 17 words
A process according to claim 1 characterized by using propene or butene as the normally gaseous olefin.
Claim 5
Dependent Claim 30 words
A process according to any of claim 1 characterized by operating in a temperature range of from 10° to 25°C and under superatmospheric pressures of between 1 and 5 atmospheres.
Claim 6
Dependent Claim 34 words
A process according to claim 1 characterized by separating monoolefins having from 4 to 25 carbon atoms as the unsaturated compounds from hydrocarbon mixtures containing saturated hydrocarbons having from 4 to 25 carbon atoms.
Claim 7
Dependent Claim 20 words
A process according to claim 1 characterized by separating aromatics as the unsaturated compounds from hydrocarbon mixtures containing saturated hydrocarbons.
Claim 8
Dependent Claim 24 words
A process according to claim 3 characterized by operating at a temperature between 10° and 25°C and a pressure between 1 and 5 atmospheres.
Claim 9
Dependent Claim 33 words
A process according to claim 3 characterized by using a cation exchange resin having a specific surface area between 500 and 750 square meter/gram and an average pore diameter between 40 and 60A.
Claim 10
Dependent Claim 16 words
A process according to claim 4 characterized in that the resin is loaded with silver ions.
Claim 11
Dependent Claim 16 words
A process according to claim 4 characterized in that the resin is loaded with copper ions.
Claim 12
Dependent Claim 19 words
A process according to claim 1 characterized in that the resin is a sulfonated divinyl benzene cross-linked polystyrene resin.

References Cited (Backward Citations)

US2449402A Cited
US2865970A Cited
US3409691A Cited
US3922217A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-09-07 1980-03-08 1980-09-07 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-09-07 1984-03-08 1984-09-07 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-09-07 1988-03-08 1988-09-07 $7700.00 Window Closed / Lapsed

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