Patent US5656202A successfully refreshed from Google Patents.
← Back to Patent Explorer
US5656202A Expired / Lapsed US ⏱️ 0.0 years remaining

Method for making overbased PVC stabilizer

Assignee: Galata Chemicals LLC
•
Filing: 1995-06-20
•
Granted: 1997-08-12
•
Expires: 2015-06-20
📄 Original PDF 🌐 Google Patents 🔄 Sync Now

Abstract

Abstract An overbased mixture of aliphatic and aromatic carboxylates salts useful in making low-fogging thermal stabilizers for PVC is made by reacting zinc oxide with fatty acid and such as stearic acid, then adding aromatic acids, and then adding and reacting one or both of magnesium oxide and calcium oxide, under controlled heating conditions to maintain fluidity while minimizing side reactions, and then conditioning the reaction product to remove volatiles.

Inventors

  • 👤 Lawrence R. Brecker
  • 👤 Radu Bacaloglu
  • 👤 Michael Fisch
  • 👤 Mukund Shah
  • 👤 Otto Loeffler

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 06:44
CPC Classifications
C; C08; C08K; C08K5/00; C08K5/04; C08K5/09; C08K5/098

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 340 words
A process for producing an overbased mixture of carboxylate salts of one or more aromatic acids selected from the group consisting of benzoic acid and benzoic acid substituted with one, two or three alkyl groups each of which contain from 1 to 6 carbon atoms, and one or more aliphatic fatty acids containing about 12 to 30 carbon atoms with zinc and of magnesium, comprising: (a) dissolving zinc oxide in a molten acid precursor composed of at least a stoichiometrically equivalent quantity of said one or more aliphatic fatty acids wherein up to about 10 mole percent of the amount of said one or more aliphatic fatty acids present is replaced by one or more of said aromatic acids, in the presence of water in an amount up to about 10 wt %, said amount of water being effective to increase the rate of reaction of said zinc oxide with said one or more aliphatic fatty acids, under conditions effective to achieve complete reaction between said zinc oxide and said acid precursor to maximize formation of the corresponding zinc carboxylate while minimizing formation of other reaction products and to provide thereby a liquid reaction product; (b) adding said one or more aromatic acids to said liquid reaction product under conditions effective to maintain it in the liquid state while minimizing side reactions between said zinc carboxylate and said aromatic acids, wherein the mole ratio of said one or more aromatic acids to aliphatic carboxylates is 0.5:1 to 2:1; (c) adding magnesium oxide, either magnesium hydroxide, or mixtures thereof to the product of step (b), in an amount effective to provide a stoichiometric excess thereof up to about 5 wt. % based on the carboxylate, under conditions effective to achieve complete reaction of said one or more aromatic acids with said added compound or compounds to form said mixture of carboxylate salts while minimizing formation of side reaction products; and (d) conditioning the product of step (c) under conditions effective to volatilize and remove therefrom unreacted products and side reaction products.
Claim 2
Dependent Claim 340 words
A process for producing an overbased mixture of carboxylate salts of one or more aromatic acids selected from the group consisting of benzoic acid and benzoic acid substituted with one, two or three alkyl groups each of which contain from 1 to 6 carbon atoms, and one or more aliphatic fatty acids containing about 12 to 30 carbon atoms with zinc and of magnesium, comprising: (a) dissolving zinc oxide in a molten acid precursor composed of at least a stoichiometrically equivalent quantity of said one or more aliphatic fatty acids wherein up to about 10 mole percent of the amount of said one or more aliphatic fatty acids present is replaced by one or more of said aromatic acids, in the presence of water in an amount up to about 10 wt %, said amount of water being effective to increase the rate of reaction of said zinc oxide with said one or more aliphatic fatty acids, under conditions effective to achieve complete reaction between said zinc oxide and said acid precursor to maximize formation of the corresponding zinc carboxylate while minimizing formation of other reaction products and to provide thereby a liquid reaction product; (b) adding said one or more aromatic acids to said liquid reaction product under conditions effective to maintain it in the liquid state while minimizing side reactions between said zinc carboxylate and said aromatic acids, wherein the mole ratio of said one or more aromatic acids to aliphatic carboxylates is 0.5:1 to 2:1; (c) adding magnesium oxide, either magnesium hydroxide, or mixtures thereof to the product of step (b), in an amount effective to provide a stoichiometric excess thereof up to about 5 wt. % based on the carboxylate, under conditions effective to achieve complete reaction of said one or more aromatic acids with said added compound or compounds to form said mixture of carboxylate salts while minimizing formation of side reaction products; and (d) conditioning the product of step (c) under conditions effective to volatilize and remove therefrom unreacted products and side reaction products.
Claim 3
Dependent Claim 13 words
The process of claim 1 wherein magnesium oxide is added in step (c).
Claim 4
Dependent Claim 37 words
The process of claim 1 wherein in steps (a) and (c), oxide is added in successive portions and the temperature of the material to which the oxide is added is increased over the course of said addition.
Claim 5
Dependent Claim 39 words
The process of claim 2 wherein in step (a) the temperature of said acid precursor is increased from about 100° C. when addition of zinc oxide is begun, to about 160° C. after addition of zinc oxide is discontinued.
Claim 6
Dependent Claim 38 words
The process of claim 2 wherein in step (c) the temperature of said product of step (b) is increased from about 160° C. when addition thereto is begun, to about 180° C.-190° C. after said addition is discontinued.
Claim 7
Dependent Claim 16 words
The process of claim 1 wherein said one or more aliphatic fatty acids is stearic acid.
Claim 8
Dependent Claim 29 words
The process of claim 1 wherein said one or more aromatic acids are selected from the group consisting of benzoic acid, all isomers of toluic acid, and mixtures thereof.
Claim 9
Dependent Claim 29 words
The process of claim 6 wherein said one or more aromatic acids are selected from the group consisting of benzoic acid, all isomers of toluic acid, and mixtures thereof.
Claim 10
Dependent Claim 13 words
The process of claim 8 wherein magnesium oxide is added in step (c).

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 2000-08-11 2001-02-10 2001-08-12 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 2004-08-11 2005-02-10 2005-08-12 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 2008-08-11 2009-02-10 2009-08-12 $7700.00 Window Closed / Lapsed

Assigned Categories & Tags

No categories assigned to this patent yet.

Assign Category Tag