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US3361832A Expired / Lapsed US ⏱️ 0.0 years remaining

Conversion of acids to alcohols

Assignee: ExxonMobil Technology and Engineering Co
•
Filing: 1963-08-13
•
Granted: 1968-01-02
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Expires: 1983-08-13
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Abstract

No abstract record available.

Inventors

  • 👤 Pine Lloyd Albert
  • 👤 Ellert Henry George

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-01 19:14
CPC Classifications
C; C07; C07C; C07C29/00; C07C29/132; C07C29/136; C07C29/147; C07C29/149; C07C67/00; C07C67/08

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 214 words
A PROCESS FOR THE CONVERSION OF A C1 TO C30 ORGANIC ACID OR ITS ANHYDRIDE WHEREIN THE ACID IS SELECTED FROM THE GROUP CONSISTING OF UNSUBSTITUTED AND SUBSTITUTED ALIPHATIC CARBOXYLIC ACIDS, UNSUBSTITUTED AND SUBSTITUTED AROMATIC CARBOXYLIC ACIDS AND AMINO ACIDS AND WHEREIN THE SUBSTITUENT IS SELECTED FROM THE GROUP CONSISTING OF HYDROXY GROUPS AND HALOGEN ATOMS TO AN ALCOHOL HAVING THE SAME NUMBER OF CARBON ATOMS WHICH COMPRISES CONTRACTING SAID ACID OR ANHYDRIDE WITH A C1 TO C6 ALKANOL AT TEMPERATURES OF ABOUT 200 TO 600*F. AND PRESSURES OF ABOUT 200 TO 600 P.S.I.G. IN THE PRESENCE OF A CATALYST CONTAINING A CATALYTIC AMOUNT OF A MOLYBDENUM SULFIDE IN A FIRST REACTION STAGE TO PRODUCE AN ESTERIFIED PRODUCT CORRESPONDING TO SAID ORGANIC ACID AND SAID ALKANOL, INTRODUCING AT LEAST A PORTION OF SAID ESTERIFIED PRODUCT INTO A SECOND REACTON STAGE, CONTACTING SAID ESTERIFIED PRODUCT WITH HYDROGEN IN SAID SECOND STAGE IN THE PRESENCE OF A CATALYST CONTAINING A CATALYTIC AMOUNT OF MOLYBDENUM SULFIDE AT TEMPERATURES OF ABOUT 300 TO 600*F. AND PRESSURES OF ABOUT 500 TO 5,000 P.S.I.G. TO PRODUCE AN ALCOHOL PRODUCT-COMPRISING MIXTURE, SEPARATING THE ALCOHOL PRODUCT FROM SUCH MIXTURE AND SEPARATING AND RECYCLING AT LEAST A PORTION OF SAID C1 TO C6 ALKANOL CONTAINED IN SAID MIXTURE TO THE FIRST REACTION STAGE.
Claim 2
Dependent Claim 214 words
A PROCESS FOR THE CONVERSION OF A C1 TO C30 ORGANIC ACID OR ITS ANHYDRIDE WHEREIN THE ACID IS SELECTED FROM THE GROUP CONSISTING OF UNSUBSTITUTED AND SUBSTITUTED ALIPHATIC CARBOXYLIC ACIDS, UNSUBSTITUTED AND SUBSTITUTED AROMATIC CARBOXYLIC ACIDS AND AMINO ACIDS AND WHEREIN THE SUBSTITUENT IS SELECTED FROM THE GROUP CONSISTING OF HYDROXY GROUPS AND HALOGEN ATOMS TO AN ALCOHOL HAVING THE SAME NUMBER OF CARBON ATOMS WHICH COMPRISES CONTRACTING SAID ACID OR ANHYDRIDE WITH A C1 TO C6 ALKANOL AT TEMPERATURES OF ABOUT 200 TO 600*F. AND PRESSURES OF ABOUT 200 TO 600 P.S.I.G. IN THE PRESENCE OF A CATALYST CONTAINING A CATALYTIC AMOUNT OF A MOLYBDENUM SULFIDE IN A FIRST REACTION STAGE TO PRODUCE AN ESTERIFIED PRODUCT CORRESPONDING TO SAID ORGANIC ACID AND SAID ALKANOL, INTRODUCING AT LEAST A PORTION OF SAID ESTERIFIED PRODUCT INTO A SECOND REACTON STAGE, CONTACTING SAID ESTERIFIED PRODUCT WITH HYDROGEN IN SAID SECOND STAGE IN THE PRESENCE OF A CATALYST CONTAINING A CATALYTIC AMOUNT OF MOLYBDENUM SULFIDE AT TEMPERATURES OF ABOUT 300 TO 600*F. AND PRESSURES OF ABOUT 500 TO 5,000 P.S.I.G. TO PRODUCE AN ALCOHOL PRODUCT-COMPRISING MIXTURE, SEPARATING THE ALCOHOL PRODUCT FROM SUCH MIXTURE AND SEPARATING AND RECYCLING AT LEAST A PORTION OF SAID C1 TO C6 ALKANOL CONTAINED IN SAID MIXTURE TO THE FIRST REACTION STAGE.
Claim 3
Dependent Claim 146 words
A PROCESS FOR THE PRODUCTION OF NEO-HEPTANOL FROM NEO-HEPTANOIC ACID WHICH COMPRISES CONTACTING EQUIMOLAR AMOUNTS OF NEO-HEPTANOIC ACID WITH METHANOL AT TEMPERATURES OF 200 TO 600*F. AND PRESSURES OF 200 TO 600 P.S.I.G. IN THE PRESENCE OF A CATALYST CONTAINING A CATALYTIC AMOUNT OF AN 8-10% MOLYBDENUM SULFIDE ON ACTIVATED CARBON IN A FIRST REACTION VESSEL TO PRODUCE METHYL NEOHEPTANOATE, INTRODUCING AT LEAST A PORTION OF SAID METHYL NEO-HEPTANOATE INTO A SECOND REACTION VESSEL, CONTACTING SAID METHYL NEO-HEPTANOATE WITH HYDROGEN IN SAID SECOND VESSEL AT TEMPERATURES OF 300 TO 600*F, AND PRESSURES OF 500 TO 5,000 P.S.I.G. IN THE PRESENCE OF A CATALYST CONTAINING A CATALYTIC AMOUNT OF 8-10% MOLYBDENUM SULFIDE ON ACTIVATED CARBON TO PRODUCE A NEO-HEPTANOL COMPRISING MIXTURE, SEPARATING SAID NEO-HEPTANOL FROM SAID MIXTURE AND SEPARATING AND RECYCLING AT LEAST A PORTION OF THE METHANOL CONTAINED IN SAID MIXTURE TO THE FIRST REACTON VESSEL.
Claim 4
Dependent Claim 146 words
A PROCESS FOR THE PRODUCTION OF NEO-HEPTANOL FROM NEO-HEPTANOIC ACID WHICH COMPRISES CONTACTING EQUIMOLAR AMOUNTS OF NEO-HEPTANOIC ACID WITH METHANOL AT TEMPERATURES OF 200 TO 600*F. AND PRESSURES OF 200 TO 600 P.S.I.G. IN THE PRESENCE OF A CATALYST CONTAINING A CATALYTIC AMOUNT OF AN 8-10% MOLYBDENUM SULFIDE ON ACTIVATED CARBON IN A FIRST REACTION VESSEL TO PRODUCE METHYL NEOHEPTANOATE, INTRODUCING AT LEAST A PORTION OF SAID METHYL NEO-HEPTANOATE INTO A SECOND REACTION VESSEL, CONTACTING SAID METHYL NEO-HEPTANOATE WITH HYDROGEN IN SAID SECOND VESSEL AT TEMPERATURES OF 300 TO 600*F, AND PRESSURES OF 500 TO 5,000 P.S.I.G. IN THE PRESENCE OF A CATALYST CONTAINING A CATALYTIC AMOUNT OF 8-10% MOLYBDENUM SULFIDE ON ACTIVATED CARBON TO PRODUCE A NEO-HEPTANOL COMPRISING MIXTURE, SEPARATING SAID NEO-HEPTANOL FROM SAID MIXTURE AND SEPARATING AND RECYCLING AT LEAST A PORTION OF THE METHANOL CONTAINED IN SAID MIXTURE TO THE FIRST REACTON VESSEL.

References Cited (Backward Citations)

US3173959A Cited
US2440678A Cited
US2584531A Cited
US2813911A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1971-01-01 1971-07-03 1972-01-02 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1975-01-01 1975-07-03 1976-01-02 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1979-01-01 1979-07-03 1980-01-02 $7700.00 Window Closed / Lapsed

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