← Back to Patent Explorer
US3867475A Expired / Lapsed US ⏱️ 0.0 years remaining

Isoparaffin alkylation

Assignee: Texaco Inc
•
Filing: 1973-03-21
•
Granted: 1975-02-18
•
Expires: 1993-03-21
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract A strong acid catalyzed alkylation process wherein an isoparaffin is alkylated with an alkylating agent such as olefin hydrocarbon, alkyl sulfates, in the liquid phase, at a superatmospheric pressure and a temperature in the range of from below zero to about 100*F., and wherein gaseous carbon dioxide is dissolved in the strong acid catalyst.

Inventors

  • 👤 John H Estes
  • 👤 Edward L Cole

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-28 15:49
CPC Classifications
C; C07; C07C; C07C2/00; C07C2/54; C07C2/56; C07C2/58; C07C2/62; C07C2527/00; C07C2527/02; C07C2527/03; C07C2527/053; C07C2527/054

Claims Analysis

Total Claims: 6
Claim 1
Independent Claim 158 words
IN AN ALKYLATION PROCESS WHEREIN ISOPARAFFIN HYDROCARBON SELECTED FROM THE GROUP CONSISTING OF ISOBUTANE, ISOPENTANE AND MIXTURES THEREOF IS ALKYLATED WITH AN ALKYLATING AGENT SELECTED FROM THE GROUP CONSISTING OF PROPYLENE, BUTYLENES, PENTYLENES, THEIR SULFATES, AND MIXTURES THEREOF IN THE LIQUID PHASE, IN THE PRESENCE OF AN ACID CATALYST SELECTED FROM THE GROUP CONSISTING OF SULFURIC ACID, FLUOROSULFONIC ACID, AND MIXTURES THEREOF AT A TEMPERATURE IN THE RANGE OF ABOUT ZERO TO ABOUT 100*F AND A SUPERATMOSPHERIC PRESSURE, THE IMPROVEMENT WHICH COMPRISES: A. TREATING SAID ACID CATALYST WITH CARBON DIOXIDE TO FORM AN ACID CATALYST HAVING A WEIGHT RATIO OF CARBON DIOXIDE TO ACID OF AT LEAST 0.1/100 AT A TEMPERATURE IN THE RANGE OF ABOUT ZERO TO ABOUT 100*F AND A SUPERATMOSPHERIC PRESSURE IN THE RANGE OF FROM ABOUT 50 PSIG TO ABOUT 1000 PSIG, AND B. ALKYLATING SAID ISOPARAFFIN HYDROCARBON WITH SAID ALKYLATING AGENT IN THE PRESENCE THE CARBON DIOXIDE TREATED ACID CATALYST OF STEP (A).
Claim 2
Dependent Claim 158 words
IN AN ALKYLATION PROCESS WHEREIN ISOPARAFFIN HYDROCARBON SELECTED FROM THE GROUP CONSISTING OF ISOBUTANE, ISOPENTANE AND MIXTURES THEREOF IS ALKYLATED WITH AN ALKYLATING AGENT SELECTED FROM THE GROUP CONSISTING OF PROPYLENE, BUTYLENES, PENTYLENES, THEIR SULFATES, AND MIXTURES THEREOF IN THE LIQUID PHASE, IN THE PRESENCE OF AN ACID CATALYST SELECTED FROM THE GROUP CONSISTING OF SULFURIC ACID, FLUOROSULFONIC ACID, AND MIXTURES THEREOF AT A TEMPERATURE IN THE RANGE OF ABOUT ZERO TO ABOUT 100*F AND A SUPERATMOSPHERIC PRESSURE, THE IMPROVEMENT WHICH COMPRISES: A. TREATING SAID ACID CATALYST WITH CARBON DIOXIDE TO FORM AN ACID CATALYST HAVING A WEIGHT RATIO OF CARBON DIOXIDE TO ACID OF AT LEAST 0.1/100 AT A TEMPERATURE IN THE RANGE OF ABOUT ZERO TO ABOUT 100*F AND A SUPERATMOSPHERIC PRESSURE IN THE RANGE OF FROM ABOUT 50 PSIG TO ABOUT 1000 PSIG, AND B. ALKYLATING SAID ISOPARAFFIN HYDROCARBON WITH SAID ALKYLATING AGENT IN THE PRESENCE THE CARBON DIOXIDE TREATED ACID CATALYST OF STEP (A).
Claim 3
Dependent Claim 62 words
The process of claim 1 wherein the treating step (a) temperature is in the range of about 20*F to about 75*F, the pressure is in the range of about 50 psig to about 1000 psig, and the acid catalyst is contacted with carbon dioxide in a weight ratio of carbon dioxide to acid in the range of about 0.3/100 to about 5/100.
Claim 4
Dependent Claim 23 words
The process of claim 2 wherein treated acid catalyst from step (a) contains from about 0.3 to about 0.8 weight percent carbon dioxide.
Claim 5
Dependent Claim 27 words
The process of claim 3 wherein isoparaffin reactant is isobutane and the alkylating agent is selected from the group consisting of propylene, butylenes, pentylenes and mixtures thereof.
Claim 6
Dependent Claim 12 words
The process of claim 4 wherein the acid catalyst is sulfuric acid.

References Cited (Backward Citations)

US2286184A Cited
US2468529A Cited
US2520391A Cited
US3531546A Cited
US3489818A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-02-17 1978-08-19 1979-02-18 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-02-17 1982-08-19 1983-02-18 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-02-17 1986-08-19 1987-02-18 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag