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Adsorption material for olefins, gas chromatography column, method of selectively removing olefins from a mixture of hydrocarbons

Assignee: PerkinElmer Health Sciences BV
•
Filing: 1985-06-04
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Granted: 1987-03-24
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Expires: 2005-06-04
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Abstract

Abstract This invention relates to an adsorption material for olefins, a gas chromatography column and a method for removing olefins from a mixture with saturated hydrocarbons by gas chromatography. The adsorption material according to the invention is a thermostable, macroporous resin having strongly acid ion exchange groups to which silver ions are linked. The resin has an average pore diameter of 10-100 nm, an internal surface area of 10-100 m 2 /g and 5-15% cross-linking.

Inventors

  • 👤 Edward G. Boeren
  • 👤 Richard B. van Henegouwen

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-23 19:22
CPC Classifications
C; C07; C07C; C07C7/00; C07C7/135; B; B01; B01J; B01J39/00; B01J39/26; B01J45/00; B01J47/00; B01J47/016

Claims Analysis

Total Claims: 25
Claim 1
Independent Claim 50 words
An adsorption material for olefins, comprising a thermostable resin containing strongly acid ion exchange groups to which Ag + ions are linked, characterized in that the resin is a macroporous resin with an average pore diameter of 10-100 nm, an internal area of 10-100 m 2 /g and 5-15% cross-linking.
Claim 2
Dependent Claim 50 words
An adsorption material for olefins, comprising a thermostable resin containing strongly acid ion exchange groups to which Ag + ions are linked, characterized in that the resin is a macroporous resin with an average pore diameter of 10-100 nm, an internal area of 10-100 m 2 /g and 5-15% cross-linking.
Claim 3
Dependent Claim 21 words
An adsorption material as claimed in claim 1, characterized in that the strongly acid ion exchange groups are sulfonic acid groups.
Claim 4
Dependent Claim 19 words
An adsorption material as claimed in claim 1, characterized in that the resin is a polystyrene cross-linked with divinylbenzene.
Claim 5
Dependent Claim 21 words
An adsorption material as claimed in claim 1, characterized in that the particles have sizes in the range of 0.037-0.84 mm.
Claim 6
Dependent Claim 19 words
An adsorption material as claimed in claim 1, characterized in that the resin has a porosity of about 25%.
Claim 7
Dependent Claim 20 words
An adsorption material as claimed in claim 1, characterized in that the resin has a pore diameter of 30-100 nm.
Claim 8
Dependent Claim 23 words
An adsorption material as claimed in claim 1, characterized in that the resin has an internal area of about 25 m 2 /g.
Claim 9
Dependent Claim 17 words
An adsorption material as claimed in claim 1, characterized in that the resin has approximately 8% cross-linking.
Claim 10
Dependent Claim 24 words
A gas chromatography column filled with an adsorption material for olefins as defined in claims 1, 2, 3, 4, 5, 6, 7, or 8.
Claim 11
Dependent Claim 21 words
An adsorption material as claimed in claim 1, characterized in that the resin has a pore diameter of about 40 nm.
Claim 12
Independent Claim 135 words
A method of selectively removing olefins from a mixture of hydrocarbons comprising olefins and saturated hydrocarbons, in which the mixture to be separated is passed through a column containing an adsorption material for olefins comprising a thermostable resin with strongly acid ion exchange groups to which Ag + ions are linked, characterized by removing a group of olefins of different carbon numbers selectively and reversibly from a gaseous complex mixture of hydrocarbons comprising olefins and saturated hydrocarbons of different carbon numbers by gas chromatography, by using a gas chromatography column containing a macroporous, thermostable resin having strongly acid ion exchange groups to which Ag + ions are linked as an olefin adsorption material, which macroporous resin has an average pore diameter of 10-100 nm, an internal area of 10-100 m 2 /g and 5-15% cross-linking.
Claim 13
Independent Claim 135 words
A method of selectively removing olefins from a mixture of hydrocarbons comprising olefins and saturated hydrocarbons, in which the mixture to be separated is passed through a column containing an adsorption material for olefins comprising a thermostable resin with strongly acid ion exchange groups to which Ag + ions are linked, characterized by removing a group of olefins of different carbon numbers selectively and reversibly from a gaseous complex mixture of hydrocarbons comprising olefins and saturated hydrocarbons of different carbon numbers by gas chromatography, by using a gas chromatography column containing a macroporous, thermostable resin having strongly acid ion exchange groups to which Ag + ions are linked as an olefin adsorption material, which macroporous resin has an average pore diameter of 10-100 nm, an internal area of 10-100 m 2 /g and 5-15% cross-linking.
Claim 14
Dependent Claim 20 words
A method as claimed in claim 11, characterized in that the strongly acid ion exchange groups are sulfonic acid groups.
Claim 15
Dependent Claim 18 words
A method as claimed in claim 11, characterized in that the resin is a polystyrene cross-linked with divinylbenzene.
Claim 16
Dependent Claim 20 words
A method as claimed in claim 11, characterized in that the particles have sizes in the range of 0.037-0.84 mm.
Claim 17
Dependent Claim 18 words
A method as claimed in claim 11, characterized in that the resin has a porosity of about 25%.
Claim 18
Dependent Claim 19 words
A method as claimed in claim 11, characterized in that the resin has a pore diameter of 30-100 nm.
Claim 19
Dependent Claim 22 words
A method as claimed in claim 11, characterized in that the resin has an internal area of about 25 m 2 /g.
Claim 20
Dependent Claim 16 words
A method as claimed in claim 11, characterized in that the resin has about 8% cross-linking.
Claim 21
Dependent Claim 25 words
A method as claimed in claim 11, characterized by selectively removing the olefins from a hydrocarbon mixture containing olefins and paraffins having 5-11 carbon atoms.
Claim 22
Dependent Claim 30 words
A method as claimed in claim 11, characterized by absorbing the olefins at a temperature of about 100° C. and a pressure of from about 100 to about 400 kPa.
Claim 23
Dependent Claim 21 words
A method as claimed in claim 11, characterized by desorbing the adsorbed olefins by raising the temperature to about 150° C.
Claim 24
Dependent Claim 26 words
A method as claimed in claim 21, characterized by desorbing the adsorbed olefins in the reverse direction and discharging them from the column as a group.
Claim 25
Dependent Claim 20 words
A method as claimed in claim 11, characterized in that the resin has a pore diameter of about 40 nm.

References Cited (Backward Citations)

US2865970A Cited
US3219717A Cited
US3357158A Cited
US3969344A Cited
US3790475A Cited
US3940972A Cited
US4043905A Cited
US4140653A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1990-03-23 1990-09-22 1991-03-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1994-03-23 1994-09-22 1995-03-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1998-03-23 1998-09-22 1999-03-24 $7700.00 Window Closed / Lapsed

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