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US3849288A Expired / Lapsed US ⏱️ 0.0 years remaining

Manufacture of transformer oils

Assignee: Mobil Oil AS
•
Filing: 1973-03-26
•
Granted: 1974-11-19
•
Expires: 1993-03-26
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Abstract

Abstract Transformer oils are manufactured by catalytic hydrogenation of selected petroleum charge stocks under critical temperature conditions.

Inventors

  • 👤 D Milstein
  • 👤 D Hill

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-03 00:47
CPC Classifications
C; C10; C10G; C10G71/00

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 172 words
A PROCESS FOR MANUFACTURING A TRANSFORMER OIL WHICH CONSISTS ESSENTIALLY OF SELECTING A NAPHTHENIC DISTILLAT BOILING IN THE RANGE OF ABOUT 450*F. TO ABOUT 775*F., CHARACTERIZED BY AN AROMATIC CONTENT LESS THAN 30 PERCENT, AN ALKANE CONTENT LESS THAN 5 PERCENT, THE BALANCE BEING SUBSTANTIALLY ALLNAPHTHENES AND HAVING A FLASH POINT NOT LESS THAN ABOUT 275*F., A VISCOSITY AT 100*F. OF FROM ABOUT 55 TO ABOUT 75 SUS AND A SPECIFFIC GRAVITY OF ABOUT 0.865 TO ABOUT 0.905; CONTACTING SAID DISTILLATE WITH HYDROGEN IN THE PRESENCE OF A HYDROGENATION CATALYST AT A TEMPERATURE OF ABOUT 550*F. AT A PRESSURE IN THE RANGE FROM ABOUT 200 TO ABOUT 5,000 PSIG. AT A SPACE VELOCITY BETWEEN ABOUT 0.2 AND ABOUT 5 VOLUMES PER HOUR PER VOLUME OF CATALYST AND A HYDROGEN CIRCULATION RATE FROM ABOUT 250 TO ABOUT 15,000 S.C.F PER BARREL PERCLOATING THE RESULTING HYDROTREATED OIL THROUGH CLAY, UTILIZING A VOLUME RATIO OF OIL TO CLAY BETWEEN ABOUT 5 AND ABOUT 10 AND RECOVERING FROM SUCH OPERATION A PRODUCT CONSTITUTING A TRANSFORMER OIL.
Claim 2
Dependent Claim 172 words
A PROCESS FOR MANUFACTURING A TRANSFORMER OIL WHICH CONSISTS ESSENTIALLY OF SELECTING A NAPHTHENIC DISTILLAT BOILING IN THE RANGE OF ABOUT 450*F. TO ABOUT 775*F., CHARACTERIZED BY AN AROMATIC CONTENT LESS THAN 30 PERCENT, AN ALKANE CONTENT LESS THAN 5 PERCENT, THE BALANCE BEING SUBSTANTIALLY ALLNAPHTHENES AND HAVING A FLASH POINT NOT LESS THAN ABOUT 275*F., A VISCOSITY AT 100*F. OF FROM ABOUT 55 TO ABOUT 75 SUS AND A SPECIFFIC GRAVITY OF ABOUT 0.865 TO ABOUT 0.905; CONTACTING SAID DISTILLATE WITH HYDROGEN IN THE PRESENCE OF A HYDROGENATION CATALYST AT A TEMPERATURE OF ABOUT 550*F. AT A PRESSURE IN THE RANGE FROM ABOUT 200 TO ABOUT 5,000 PSIG. AT A SPACE VELOCITY BETWEEN ABOUT 0.2 AND ABOUT 5 VOLUMES PER HOUR PER VOLUME OF CATALYST AND A HYDROGEN CIRCULATION RATE FROM ABOUT 250 TO ABOUT 15,000 S.C.F PER BARREL PERCLOATING THE RESULTING HYDROTREATED OIL THROUGH CLAY, UTILIZING A VOLUME RATIO OF OIL TO CLAY BETWEEN ABOUT 5 AND ABOUT 10 AND RECOVERING FROM SUCH OPERATION A PRODUCT CONSTITUTING A TRANSFORMER OIL.
Claim 3
Dependent Claim 26 words
The process of claim 1 wherein said naphthenic distillate has a boiling range of about 525*to 700*F. and an aromatics content of 18 to 25 percent.
Claim 4
Dependent Claim 54 words
The process of claim 1 wherein said contacting takes place at a pressure in the range from about 250 to about 1,000 psig, at a space velocity of about 0.5 to about 2 volumes per hour per volume of catalyst and a hydrogen circulation rate from about 500 to about 2,000 s.c.f. per barrel.
Claim 5
Dependent Claim 47 words
The process of claim 1 wherein said catalyst contains about 1 to about 10 weight percent of an iron group metal, expressed as the oxide, and about 5 to about 25 weight percent of a Group VI B metal, expressed as the oxide, deposited on a carrier.
Claim 6
Dependent Claim 14 words
The process of claim 1 wherein said viscosity at 100*F. is about 58 SUS.
Claim 7
Dependent Claim 19 words
The process of claim 1 wherein said naphthenic distillate has a boiling range of about 580*F. to about 680*F.
Claim 8
Dependent Claim 11 words
The transformer oil product resulting from the process of claim 1.
Claim 9
Dependent Claim 14 words
The process of claim 4 wherein said catalyst is nickel molybdate deposited on alumina.

References Cited (Backward Citations)

No citation records indexed.

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1977-11-18 1978-05-20 1978-11-19 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1981-11-18 1982-05-20 1982-11-19 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1985-11-18 1986-05-20 1986-11-19 $7700.00 Window Closed / Lapsed

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