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US3864369A Expired / Lapsed US ⏱️ 0.0 years remaining

Method of Preparing Carboxylic Acid Salts

Assignee: Lion Fat and Oil Co Ltd
•
Filing: 1971-04-30
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Granted: 1975-02-04
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Expires: 1991-04-30
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Abstract

Abstract A method of preparing carboxylic acid salts which comprises subjecting to oxidative dehydrogenation alcoholic oxygen containing organic compounds by heating same with alkali metal oxides or hydroxides in the presence of a catalyst in order to produce the corresponding carboxylic acid salts, wherein said catalyst is obtained by mixing solid carbon with one or more members selected from the group consisting of metals of the Group IB, Group II and Group IV classified in the periodic Table and their inorganic compounds.

Inventors

  • 👤 Hiroshi Isa
  • 👤 Takeo Inagaki
  • 👤 Takeshi Takemoto
  • 👤 Kazuo Endoh

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 02:00
CPC Classifications
C; C07; C07C; C07C51/00; C07C51/16; C07C51/295; C07C51/41

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 167 words
A PROCESS FOR PREPARING CARBOXYLIC ACID SALT FROM ALCOHOLIC OXYGEN-CONTAINING ORGANIC REACTANT SELECTED FROM THE GROUP CONSISTING OF PRIMARY ALCOHOLS, ALDEHYDES, ALDOLS, ESTERS ALKANOLAMINES AND ALUMINUM ALCOHOLATES, COMPRISING REACTING SAID ALCOHOLIC OXYGEN-CONTAINING ORGANIC REACTANT WITH AN ALKALI METAL COMPOUND SELECTED FROM THE GROUP CONSISTING OF ALKALI METAL OXIDES AND HYDROXIDES, UNDER OXIDATIVE DEHYDROGEGENERATION CONDITIONS OF A TEMPERATURE IN THE RANGE OF 150* TO 350*C AND A PRESSURE IN THE RANGE OF 2 TO 100 ATMOSPHERES, IN THE PRESENCE OF FROM 0.01 TO 10% BY WEIGHT, BASED ON THE WEIGHT OF SAID ALCOHOLIC OXYGEN-CONTAINING REACTANT, OF CATALYST CONSISTING ESSENTIALLY OF A MIXTURE OF (A) AT LEAST ONE MEMBER SELECTED FROM THE GROUP CONSISTING OF ZINC, COPPER, THE OXIDES OF METALS OF GROUP IB, GROUP II AND GROUP IV OF THE PERIODIC TABLE, ZINC CHLORIDE AND ZINC HYDROXIDE, AND (B) SOLID CARBONS HAVING A SURFACE AREA IN THE RANGE OF FROM 25 TO 1,700 M2/G, THE WEIGHT RATIO OF (A):(B) BEING IN THE RANGE OF ABOUT 100:1 TO 1:100.
Claim 2
Dependent Claim 167 words
A PROCESS FOR PREPARING CARBOXYLIC ACID SALT FROM ALCOHOLIC OXYGEN-CONTAINING ORGANIC REACTANT SELECTED FROM THE GROUP CONSISTING OF PRIMARY ALCOHOLS, ALDEHYDES, ALDOLS, ESTERS ALKANOLAMINES AND ALUMINUM ALCOHOLATES, COMPRISING REACTING SAID ALCOHOLIC OXYGEN-CONTAINING ORGANIC REACTANT WITH AN ALKALI METAL COMPOUND SELECTED FROM THE GROUP CONSISTING OF ALKALI METAL OXIDES AND HYDROXIDES, UNDER OXIDATIVE DEHYDROGEGENERATION CONDITIONS OF A TEMPERATURE IN THE RANGE OF 150* TO 350*C AND A PRESSURE IN THE RANGE OF 2 TO 100 ATMOSPHERES, IN THE PRESENCE OF FROM 0.01 TO 10% BY WEIGHT, BASED ON THE WEIGHT OF SAID ALCOHOLIC OXYGEN-CONTAINING REACTANT, OF CATALYST CONSISTING ESSENTIALLY OF A MIXTURE OF (A) AT LEAST ONE MEMBER SELECTED FROM THE GROUP CONSISTING OF ZINC, COPPER, THE OXIDES OF METALS OF GROUP IB, GROUP II AND GROUP IV OF THE PERIODIC TABLE, ZINC CHLORIDE AND ZINC HYDROXIDE, AND (B) SOLID CARBONS HAVING A SURFACE AREA IN THE RANGE OF FROM 25 TO 1,700 M2/G, THE WEIGHT RATIO OF (A):(B) BEING IN THE RANGE OF ABOUT 100:1 TO 1:100.
Claim 3
Dependent Claim 30 words
The process of claim 1, wherein the amount of said catalyst is in the range of 0.2 - 4 wt.%, based on the weight of the alcoholic oxygen containing reactant.
Claim 4
Dependent Claim 19 words
The process of claim 1, wherein said weight ratio of (a):(b) is within the range between 10:1 and 1:10.
Claim 5
Dependent Claim 26 words
The process of claim 1, wherein said catalyst is selected from the group consisting of the oxides of Pb, Zn, Cu, Mg, Cd, Ti, and SN.
Claim 6
Dependent Claim 23 words
The process of claim 1, wherein said catalyst member is selected from the group consisting of Zn, and the oxide and hydroxide thereof.
Claim 7
Dependent Claim 18 words
The process of claim 1, wherein said primary alcohols and aldehydes have 1 - 40 carbon atoms, respectively.
Claim 8
Dependent Claim 18 words
The process of claim 1, wherein said oxidative dehydrogenation is conducted at a temperature between 230*C. and 300*C.
Claim 9
Dependent Claim 31 words
A process according to claim 1, wherein the ingredients of the reaction system consist essentially of said organic reactant, said alkali metal compound in a substantially anhydrous state and said catalyst.

References Cited (Backward Citations)

US2027378A Cited
US2930801A Cited
US3365476A Cited
US3449413A Cited
US3387029A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1978-02-03 1978-08-05 1979-02-04 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1982-02-03 1982-08-05 1983-02-04 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1986-02-03 1986-08-05 1987-02-04 $7700.00 Window Closed / Lapsed

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