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US4286972A Expired / Lapsed US ⏱️ 0.0 years remaining

Vapor phase adsorption using nonstoichiometric carbon-sulfur compounds

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1978-01-03
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Granted: 1981-09-01
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Expires: 1998-01-03
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Abstract

Abstract Nonstoichiometric carbon-sulfur compounds have been found to be effective adsorbents for separating organic vapors from a gaseous mixture. Separation of aromatic compounds from gaseous mixtures is particularly effective using such compounds. The spent adsorbent may then be regenerated.

Inventors

  • 👤 David W. Savage
  • 👤 Chin H. Chang
  • 👤 John M. Longo

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 13:51
CPC Classifications
B; B01; B01J; B01J20/00; B01J20/02; B01J20/20; B01D; B01D53/00; B01D53/02

Claims Analysis

Total Claims: 23
Claim 1
Independent Claim 56 words
A process for regenerating a nonstoichiometric carbon-sulfur compound of the formula C x S, where x ranges from about 4 to about 15, the adsorptive capacity of said compound having become reduced due to the adsorption of organic vapors thereon, which comprises removing at least a portion of said adsorbed vapors from said nonstoichiometric carbon-sulfur compound.
Claim 2
Dependent Claim 56 words
A process for regenerating a nonstoichiometric carbon-sulfur compound of the formula C x S, where x ranges from about 4 to about 15, the adsorptive capacity of said compound having become reduced due to the adsorption of organic vapors thereon, which comprises removing at least a portion of said adsorbed vapors from said nonstoichiometric carbon-sulfur compound.
Claim 3
Dependent Claim 14 words
The process of claim 1 wherein x ranges from about 4 to about 10.
Claim 4
Dependent Claim 35 words
The process of claim 1 wherein the C x S has a surface area ranging between 300 and 2500 square meters per gram and a pore volume of at least 0.2 cubic centimeters per gram.
Claim 5
Dependent Claim 20 words
The process of claim 1 wherein said removal is effected by contacting said nonstoichiometric carbon-sulfur compound with a stripping gas.
Claim 6
Dependent Claim 23 words
The process of claim 4 wherein said stripping gas is selected from the group consisting of steam, inert gas, alcohols and mixtures thereof.
Claim 7
Dependent Claim 11 words
The process of claim 5 wherein said stripping gas comprises steam.
Claim 8
Dependent Claim 24 words
the process of claim 1 wherein said removal is effected by heating said compound to a temperature between about 70° and about 1200° F.
Claim 9
Dependent Claim 18 words
The process of claim 7 wherein said compound is heated to a temperature between 150° and 700° F.
Claim 10
Dependent Claim 15 words
The process of claim 7 wherein an inert gas is used as a heat carrier.
Claim 11
Dependent Claim 18 words
The process of claim 1 wherein said removal is effected by contacting said compound with a liquid solvent.
Claim 12
Dependent Claim 12 words
The process of claim 10 wherein said liquid solvent is a hydrocarbon.
Claim 13
Dependent Claim 29 words
The process of claim 11 wherein said liquid solvent is a branched hydrocarbon having at least one trisubstituted carbon atom, at least one tetra-substituted carbon atom or mixtures thereof.
Claim 14
Dependent Claim 19 words
The process of claim 10 wherein the temperature during said contacting ranges from about 70° to about 700° F.
Claim 15
Dependent Claim 21 words
The process of claim 10 wherein the organic vapors removed from said nonstoichiometric carbon-sulfur compound are recovered from said liquid solvent.
Claim 16
Dependent Claim 98 words
A process for removing organic vapors from a gaseous mixture which comprises (a) contacting said mixture with a nonstoichiometric carbon-sulfur compound of the formula C x S, where x ranges from 4 to about 15, said compound having a surface area of at least 300 square meters per gram, for a period of time sufficient to adsorb at least a portion of said organic vapors from said mixture onto said compound, thereby reducing the adsorptive capacity of said compound, (b) regenerating said nonstoichiometric carbon-sulfur compound by removing at least a portion of said organic vapors from said compound.
Claim 17
Dependent Claim 98 words
A process for removing organic vapors from a gaseous mixture which comprises (a) contacting said mixture with a nonstoichiometric carbon-sulfur compound of the formula C x S, where x ranges from 4 to about 15, said compound having a surface area of at least 300 square meters per gram, for a period of time sufficient to adsorb at least a portion of said organic vapors from said mixture onto said compound, thereby reducing the adsorptive capacity of said compound, (b) regenerating said nonstoichiometric carbon-sulfur compound by removing at least a portion of said organic vapors from said compound.
Claim 18
Dependent Claim 13 words
The process of claim 15 wherein x ranges from 4 to about 10.
Claim 19
Dependent Claim 36 words
The process of claim 15 wherein the C x S has a surface area ranging from 300 to about 2500 square meters per gram and a pore volume of at least 0.2 cubic centimeters per gram.
Claim 20
Dependent Claim 27 words
The process of claim 15 wherein said organic vapors are selected from the group consisting of aromatic hydrocarbons, phenolic hydrocarbons, halogenated hydrocarbons, nitrated hydrocarbons and mixtures thereof.
Claim 21
Dependent Claim 20 words
The process of claim 18 wherein said removal is effected by contacting said carbon-sulfur compound with a liquid hydrocarbon solvent.
Claim 22
Dependent Claim 41 words
The process of claim 15 wherein the contacting in (a) is effected at a pressure ranging from about 300 to about 1500 psia and the regeneration in (b) is effected at a pressure ranging between about 0 to about 200 psia.
Claim 23
Dependent Claim 23 words
The process of claim 15 wherein the pressure ratio of the contacting in (a) to the regeneration in (b) is at least 2:1.

References Cited (Backward Citations)

US2823765A Cited
US3634028A Cited
US3470677A Cited
US3596438A Cited
US3660967A Cited
US3844739A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-08-31 1985-03-02 1985-09-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-08-31 1989-03-02 1989-09-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-08-31 1993-03-02 1993-09-01 $7700.00 Window Closed / Lapsed

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