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US3905948A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for the preparation of petroleum resins

Assignee: Societa Italiana Resine SpA SIR
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Filing: 1973-12-26
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Granted: 1975-09-16
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Expires: 1993-12-26
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Abstract

Abstract A process for the preparation of petroleum resins from hydrocarbon fractions containing olefins and diolefins, having a boiling range of from about 30* to 300*C, which comprises A. SUBJECTING SAID HYDROCARBON FRACTION TO PRE-POLYMERIZATION WITH TRANSFORMATION INTO HIGH-BOILING PRODUCTS IN QUANTITIES EQUAL TO OR SMALLER THAN ABOUT 20 PERCENT BY WEIGHT WITH RESPECT TO THE FRACTION ITSELF; B. SUBJECTING THE RESIDUAL HYDROCARBON FRACTION, AFTER SEPARATION OF THE HIGH-BOILING PRODUCTS, TO POLYMERIZATION IN THE PRESENCE OF Friedel-Crafts catalysts with conversion into polymer of a quantity equal to or smaller than about 40 percent by weight with respect to the hydrocarbon fraction fed to the pre-polymerization, and C. RECOVERING THE PETROLEUM RESIN FROM THE POLYMERIZATION PRODUCTS.

Inventors

  • 👤 Silvio Vargiu
  • 👤 Edoardo Carpaneti
  • 👤 Beppino Passalenti
  • 👤 Pietro Paparatto

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 19:30
CPC Classifications
C; C08; C08F; C08F240/00

Claims Analysis

Total Claims: 5
Claim 1
Independent Claim 230 words
A PROCESS FOR THE PREPARATION OF PETROLEUM RESINS FROM HYDROCARBON FRACTIONS CONTAINING OLEFIN AND DIOLEFINS HAVING A BOILING RANGE OF FROM ABOUT 120* TO 220*C WHICH COMPRISES A. SUBJECTING SAID HYDROCARBON FRACTION TO PREPOLYMERIZATION IN THE PRESENCE OF 2-10 PARTS BY WEIGHT ACTIVATED CLAYS/100 PARTS OF THE FRACTION ITSELF AT 25* - 35*C FOR 20-40 MINUTES WITH TRANSFORMATION INTO HIGGH-BOILING PRODUCTS IN QUANTITIES EQUAL TO ABOUT 1-10 PERCENT BY WEIGHT WITH RESPECT TO THE FRACTION ITSELF B. SEPARATING THE PREPOLYMERIZATION PRODUCT FROM THE ACTIVATED CLAYS TO OBTAIN A HYDROCARBON SOLUTION TO THEPOLYMER, C. DISTILLING SAID HYDROCARBON SOLUTION TO OBTAIN A RESIDUAL HYDROCARBON FRACTON HAVING A MAXIMUM BOILING POINT OF 210* - 230*C, D. SUBJECTING THE RESIDUAL HYDROCARBN FRACTION TO POLYMERIZATION IN THE PRESENCE OF 0.1 - 1.0 PARTS BY WEIGHT TO 100 PARTS BY WEIGHT OF THE FRACTION OF FRIECEL-CRAFTS CATALYST AT 25* - 70*C FOR 20-90 MINUTES WITH CONVERSATION INTO POLYMER OF A QUALITY EQUAL TO OR SMALLER THAN ABOUT 40 PERCENT BY WEIGHT WITH RESPECT TO THE HYDROCARBON FRACTION FED TO THE PREPOLYMERIZATION, E. TREATING THE PRODUCT FROM STEP (D) WITH ACTIVE EARTHS IN A QUALITY OF 2-10 PARTS OF SAID PRODUCT FOR 1-60 MINUTES AT 10* -60, F. SEPARATING SAID PRODUUCT FROM THE ACTIVE EARTHS AND G. DISTILLING SAIDD PRODUCT TO REMOVE LOW-BOILING CONSTITUENTS THEREFROM AND RECOVERING PETROLEUM RESIN FROM THEPOLYMERIZATION PRODUCT HAVING AT 125* - 130*C.
Claim 2
Dependent Claim 230 words
A PROCESS FOR THE PREPARATION OF PETROLEUM RESINS FROM HYDROCARBON FRACTIONS CONTAINING OLEFIN AND DIOLEFINS HAVING A BOILING RANGE OF FROM ABOUT 120* TO 220*C WHICH COMPRISES A. SUBJECTING SAID HYDROCARBON FRACTION TO PREPOLYMERIZATION IN THE PRESENCE OF 2-10 PARTS BY WEIGHT ACTIVATED CLAYS/100 PARTS OF THE FRACTION ITSELF AT 25* - 35*C FOR 20-40 MINUTES WITH TRANSFORMATION INTO HIGGH-BOILING PRODUCTS IN QUANTITIES EQUAL TO ABOUT 1-10 PERCENT BY WEIGHT WITH RESPECT TO THE FRACTION ITSELF B. SEPARATING THE PREPOLYMERIZATION PRODUCT FROM THE ACTIVATED CLAYS TO OBTAIN A HYDROCARBON SOLUTION TO THEPOLYMER, C. DISTILLING SAID HYDROCARBON SOLUTION TO OBTAIN A RESIDUAL HYDROCARBON FRACTON HAVING A MAXIMUM BOILING POINT OF 210* - 230*C, D. SUBJECTING THE RESIDUAL HYDROCARBN FRACTION TO POLYMERIZATION IN THE PRESENCE OF 0.1 - 1.0 PARTS BY WEIGHT TO 100 PARTS BY WEIGHT OF THE FRACTION OF FRIECEL-CRAFTS CATALYST AT 25* - 70*C FOR 20-90 MINUTES WITH CONVERSATION INTO POLYMER OF A QUALITY EQUAL TO OR SMALLER THAN ABOUT 40 PERCENT BY WEIGHT WITH RESPECT TO THE HYDROCARBON FRACTION FED TO THE PREPOLYMERIZATION, E. TREATING THE PRODUCT FROM STEP (D) WITH ACTIVE EARTHS IN A QUALITY OF 2-10 PARTS OF SAID PRODUCT FOR 1-60 MINUTES AT 10* -60, F. SEPARATING SAID PRODUUCT FROM THE ACTIVE EARTHS AND G. DISTILLING SAIDD PRODUCT TO REMOVE LOW-BOILING CONSTITUENTS THEREFROM AND RECOVERING PETROLEUM RESIN FROM THEPOLYMERIZATION PRODUCT HAVING AT 125* - 130*C.
Claim 3
Dependent Claim 21 words
A process as recited in claim 1, wherein aluminium trichloride, aluminium tribromide and boron trifluoride are used as the Friedel-Crafts catalysts.
Claim 4
Dependent Claim 39 words
A process as recited in claim 1, wherein in the polymerization a quantity of polymer of from about 20 to 35 parts by weight per 100 parts by weight of the hydrocarbon fraction fed to the pre-polymerization is formed.
Claim 5
Dependent Claim 9 words
Petroleum resins obtained by the process of claim 1.

References Cited (Backward Citations)

US2779750A Cited
US2837491A Cited
US2946775A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-09-15 1979-03-17 1979-09-16 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-09-15 1983-03-17 1983-09-16 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-09-15 1987-03-17 1987-09-16 $7700.00 Window Closed / Lapsed

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