US4098684A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Purification of liquid n-paraffins containing carbonyl sulfide and other sulfur compounds
Assignee: Chevron USA Inc
•
Filing: 1976-11-29
•
Granted: 1978-07-04
•
Expires: 1996-11-29
Abstract
Abstract COS and other sulfur compounds such as H2S or mercaptans are removed as impurities from liquid n-paraffin feedstocks by selective adsorption of the sulfur compounds using a dual bed of molecular sieves wherein the first bed contains the 13X variety sieves and the sequential bed contains a molecular sieve having an effective pore diameter of about 4 A.
Inventors
- 👤 Robert A. Innes
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-24 21:06
CPC Classifications
C; C10; C10G; C10G25/00; C10G25/02; C10G25/03; C10G25/05; B; B01; B01D; B01D15/00; B01J; B01J20/00; B01J20/02; B01J20/10; B01J20/16; B01J20/18; B01J20/28; B01J20/28014; B01J20/28052; Y; Y10; Y10S; Y10S208/00; Y10S208/02
Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
116 words
A process for the removal of COS and at least one other sulfur containing compound from a paraffinic feedstock containing at least 10 percent n-paraffins and wherein COS is present in said feedstock initially or is formed during the process, which process comprises passing said feedstock in the liquid phase through an adsorption zone containing two different adsorbent materials, the first portion of the zone containing an activated zeolitic molecular sieve having a pore diameter large enough to adsorb benzene and the second portion of the adsorption zone containing an activated sodium zeolite A having an effective pore diameter of about 4 A; and recovering from said adsorption zone a product substantially free of sulfur compounds.
Claim 2
Dependent Claim
116 words
A process for the removal of COS and at least one other sulfur containing compound from a paraffinic feedstock containing at least 10 percent n-paraffins and wherein COS is present in said feedstock initially or is formed during the process, which process comprises passing said feedstock in the liquid phase through an adsorption zone containing two different adsorbent materials, the first portion of the zone containing an activated zeolitic molecular sieve having a pore diameter large enough to adsorb benzene and the second portion of the adsorption zone containing an activated sodium zeolite A having an effective pore diameter of about 4 A; and recovering from said adsorption zone a product substantially free of sulfur compounds.
Claim 3
Dependent Claim
24 words
A process according to claim 1 wherein the paraffinic feedstock contains at least 20% n-paraffins having from 3 to 10 carbon atoms per molecule.
Claim 4
Dependent Claim
23 words
A process according to claim 2 wherein the feedstock contains at least one n-paraffin having from 3 to 5 carbon atoms per molecule.
Claim 5
Dependent Claim
22 words
A process in accordance with claim 3 wherein said first portion of the zone contains a bed of a 13X molecular sieve.
Claim 6
Dependent Claim
12 words
A process in accordance with claim 4 wherein the feedstock is pentane.
Claim 7
Dependent Claim
12 words
A process in accordance with claim 4 wherein the feedstock is propane.
Claim 8
Dependent Claim
24 words
A process in accordance with claim 4 wherein the feedstock is a mixture of paraffins having from 3 to 5 carbon atoms per molecule.
Claim 9
Dependent Claim
16 words
A process in accordance with claim 3 wherein the COS is present initially in the feedstock.
Claim 10
Dependent Claim
18 words
A process according to claim 3 wherein the sulfur compounds consist of COS and at least one mercaptan.
Claim 11
Dependent Claim
66 words
A process according to claim 1 wherein (a) the feedstock is passed through said adsorption zone until breakthrough of sulfur compounds in the product exceeds a desired level; (b) regenerating said adsorbent materials in said adsorption zone following step (a); and (c) repeating the step (a) of passing said feedstock in the liquid phase through said adsorption zone after said regenerating step (b) has been completed.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1981-07-03 | 1982-01-02 | 1982-07-04 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1985-07-03 | 1986-01-02 | 1986-07-04 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1989-07-03 | 1990-01-02 | 1990-07-04 | $7700.00 | Window Closed / Lapsed |