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US4695402A Expired / Lapsed US ⏱️ 0.0 years remaining

Organophilic clay gellants and process for preparation

Assignee: Elementis Specialties Inc
•
Filing: 1985-08-20
•
Granted: 1987-09-22
•
Expires: 2005-08-20
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Abstract

Abstract Improved organophilic clay gellants can be prepared by a process wherein the smectite-type clay is subjected to shearing in order to break apart the agglomerates and/or the smectite-type clay can be reacted with organic cation and, possibly organic anion, under dilute reaction conditions. The reaction product is recovered using gentle drying conditions. Depending in large part on its composition, the organophilic clay gellant may be used to thicken a variety of organic compositions. In a preferred aspect, the organophilic clay gellant can be directly added to polyester compositions in order to efficiently and effectively increase the viscosity thereof or can be first formed into a pregel under low shear conditions to yield even higher efficiencies.

Inventors

  • 👤 Claude M. Finlayson
  • 👤 Charles A. Cody
  • 👤 Steven J. Kemnetz
  • 👤 William W. Reichert
  • 👤 Edward D. Magauran
  • 👤 Johnny R. Johnson

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 15:23
CPC Classifications
C; C01; C01B; C01B33/00; C01B33/20; C01B33/36; C01B33/38; C01B33/44; C08; C08K; C08K3/00; C08K3/34; C08K3/346; C08K9/00; C08K9/04; C09; C09D; C09D11/00; C09D11/02; C09D11/03; C09D7/00; C09D7/40; C09D7/43; C09K; C09K3/00; C09K8/00; C09K8/02; C09K8/04; C09K8/14; C09K8/145; C10; C10M; C10M113/00; C10M113/16; C10M2201/00; C10M2201/14; C10M2215/00; C10M2215/02; C10M2215/04; C10M2215/24; C10M2215/26

Claims Analysis

Total Claims: 94
Claim 1
Independent Claim 137 words
A process for preparing an organophilic clay gellant comprising: (a) subjecting a slurry of smectite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay to high shear conditions whereby clay agglomerates are separated, said smectite-type clay having been previously treated to remove non-clay impurities; (b) reacting the smectite-type clay with organic cation in an amount ranging from about 90 to about 150% of the cation exchange capacity of the smectite-type clay whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic cation thereby forming an organiphilic clay gellant; (c) separating the organophilic clay gellant from the slurry; and (d) drying the organophilic clay gellant under conditions selected such that the temperature of the wet organophilic clay gellant does not exceed about 50° C.
Claim 2
Dependent Claim 137 words
A process for preparing an organophilic clay gellant comprising: (a) subjecting a slurry of smectite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay to high shear conditions whereby clay agglomerates are separated, said smectite-type clay having been previously treated to remove non-clay impurities; (b) reacting the smectite-type clay with organic cation in an amount ranging from about 90 to about 150% of the cation exchange capacity of the smectite-type clay whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic cation thereby forming an organiphilic clay gellant; (c) separating the organophilic clay gellant from the slurry; and (d) drying the organophilic clay gellant under conditions selected such that the temperature of the wet organophilic clay gellant does not exceed about 50° C.
Claim 3
Dependent Claim 21 words
The process of claim 1 wherein the smectite-type clay is selected from the group consisting of bentonite, hectorite and mixtures thereof.
Claim 4
Dependent Claim 21 words
The process of claim 1 wherein the slurry contains from about 0.5 to about 80% by weight of the smectite-type clay.
Claim 5
Dependent Claim 21 words
The process of claim 3 wherein the slurry contains from about 0.5 to about 3.0% by weight of the smectite-type clay.
Claim 6
Dependent Claim 34 words
The process of claim 1 wherein the sheared clay exhibits an increase in capacity of from about 10 to about 50% as determined by the methylene blue spot test when compared to unsheared clay.
Claim 7
Dependent Claim 28 words
The process of claim 1 wherein the sheared clay exhibits a reduction in median particle size of from about 10 to about 80% when compared to unsheared clay.
Claim 8
Dependent Claim 33 words
The process of claim 1 wherein the high shear conditions are achieved by passing the slurry at least one time through a Manton-Gaulin homogenizer operating at from about 500 to about 8,000 psi.
Claim 9
Dependent Claim 34 words
The process of claim 1 wherein the smectite-type clay is reacted with organic cation in an amount ranging from about 100 to about 130% of the cation exchange capacity of the smectite type clay.
Claim 10
Dependent Claim 27 words
The process of claim 1 wherein the organic cation contains at least one lineal or branched, saturated or unsaturated alkyl group having 12 to 22 carbon atoms.
Claim 11
Dependent Claim 135 words
The process of claim 9 wherein the organic cation is at least one of ##STR2## wherein X is a nitrogen or phosphous, Y is sulfur, R 1 is a lineal or branched, saturated or unsaturated alkyl group having 12 to 22 carbon atoms and R 2 , R 3 and R 4 are independently selected from (a) lineal or branched alkyl groups having 1 to 22 carbon atoms; (b) aralkyl group which are benzyl and substituted benzyl moieties including fused ring moieties having lineal or branched 1 to 22 carbon atoms in the alkyl portion of the structure: (c) aryl groups such as phenyl and substituted phenyl including fused ring aromatic substituents; (d) beta, gamma unsaturated groups having six or less carbon atoms or hydroxylalkyl groups having 2 to 6 carbon atoms; and (e) hydrogen.
Claim 12
Dependent Claim 56 words
The process of claim 1 wherein an organic anion having a pKa less than about 11.0 is mixed with the smectite-type clay and the organic cation, said organic anion being present in amount such that the milliequivalent ratio of the organic cation to organic anion is in the range of from about 1.7:1.0 to about 28:1.0.
Claim 13
Dependent Claim 29 words
The process of claim 1 wherein the organophilic clay gellant is dried in an airstream having a temperature in the range of from about 25° to about 50° C.
Claim 14
Dependent Claim 22 words
The process of claim 12 wherein the airstream has a temperature in the range of from about 35° to about 45° C.
Claim 15
Dependent Claim 31 words
The process of claim 1 wherein the organophilic clay gellant is dried in a fluidized bed having incoming air temperature in the range of from about 25° to about 125° C.
Claim 16
Dependent Claim 24 words
The process of claim 14 wherein the fluidized bed has incoming air temperature in the range of from about 25° to about 100° C.
Claim 17
Dependent Claim 15 words
The process of claim 1 wherein the organophilic clay gellant is dried by freeze drying.
Claim 18
Dependent Claim 32 words
The process of claim 1 wherein the slurry is diluted prior to reaction with organic cation such that slurry contains from about 0.5 to about 2.5% by weight of the smectitetype clay.
Claim 19
Dependent Claim 27 words
The process of claim 17 wherein the slurry is diluted such that the slurry contains from about 0.5 to about 2.0% by weight of the smectite-type clay.
Claim 20
Dependent Claim 11 words
The organophilic clay gellant made by the process of claim 1.
Claim 21
Dependent Claim 132 words
A process for preparing an organophilic clay gellant comprising: (a) preparing a slurry of smectite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay wherein the slurry contains from about 0.5 to 2.5% by weight of the smectite-type clay; (b) reacting the smectite-type clay with organic c:ation in an amount ranging from about 90 to about 150% of the cation exchange capacity of the smectite-type clay whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic carion thereby forming an organophilic clay gellant; (c) separating the organophilic clay gellant from the slurry; and (d) drying the organophilic clay gellant under conditions selected such that the temperature of the wet organophilic clay gellant does not exceed about 50° C.
Claim 22
Dependent Claim 132 words
A process for preparing an organophilic clay gellant comprising: (a) preparing a slurry of smectite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay wherein the slurry contains from about 0.5 to 2.5% by weight of the smectite-type clay; (b) reacting the smectite-type clay with organic c:ation in an amount ranging from about 90 to about 150% of the cation exchange capacity of the smectite-type clay whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic carion thereby forming an organophilic clay gellant; (c) separating the organophilic clay gellant from the slurry; and (d) drying the organophilic clay gellant under conditions selected such that the temperature of the wet organophilic clay gellant does not exceed about 50° C.
Claim 23
Dependent Claim 30 words
The process of claim 20 wherein the slurry is prepared by forming a slurry containing greater than about 3.0% by weight of the smectite-type clay and then diluting the slurry.
Claim 24
Dependent Claim 22 words
The process of claim 21 wherein the diluted slurry contains from about 0.5 to about 2.0% by weight of the smectite-type clay.
Claim 25
Dependent Claim 33 words
The process of claim 20 wherein the smectite-type clay is reacted with organic cation in an amount ranging from about 100 to about 130% of the cation exchange capacity of the smectite-type clay.
Claim 26
Dependent Claim 27 words
The process of claim 20 wherein the organic cation contains at least one lineal or branched, saturated or unsaturated alkyl group having 12 to 22 carbon atoms
Claim 27
Dependent Claim 126 words
The process of claim 24 wherein the organic cation is at least one of ##STR3## wherein R 1 is a lineal or branched, saturated or unsaturated alkyl group having 12 to 22 carbon atoms and R 2 , R 3 and R 4 are independently selected from (a) lineal or branched alkyl groups having 1 to 22 carbon atoms; (b) aralkyl group which are benzyl and substituted benzyl moieties including fused ring moieties having lineal or branched 1 to 22 carbon atoms in the alkyl portion of the structure; (c) aryl groups such as phenyl and substituted phenyl including fused ring aromatic substituents; (d) beta, gamma unsaturated groups having 6 or less carbon atoms or hydroxylalkyl groups having 2 to 6 carbon atoms; and (e) hydrogen.
Claim 28
Dependent Claim 56 words
The process of claim 20 wherein an organic anion having a pKa less than about 11.0 is mixed with the smectite-type clay and the organic cation, said organic anion being present in amount such that the milliequivalent ratio of the organic cation to organic anion is in the range of from about 1.7:1.0 to about 28:1.0.
Claim 29
Dependent Claim 29 words
The process of claim 20 wherein the organophilic clay gellant is dried in an airstream having a temperature in the range of from about 25° to about 50° C.
Claim 30
Dependent Claim 22 words
The process of claim 27 wherein the airstream has a temperature in the range of from about 35° to about 45° C.
Claim 31
Dependent Claim 30 words
The process of claim 20 wherein the organophilic clay gellant is dried in a fluidized bed having a temperature in the range of from about 25° to about 125° C.
Claim 32
Dependent Claim 23 words
The process of claim 29 wherein the fluidized bed has a temperature in the range of from about 25° to about 100° C.
Claim 33
Dependent Claim 15 words
The process of claim 20 wherein the organophilic clay gellant is dried by freeze drying.
Claim 34
Dependent Claim 11 words
The organophilic clay gellant made by the process of claim 20.
Claim 35
Dependent Claim 118 words
A process for preparing an organophilic clay gellant comprising: (a) subjecting a slurry of smectite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay to high shear conditions whereby clay agglomerates are separated, said smectite-type clay having been previously treated to remove non-clay impurities; (b) reacting the smectite-type clay with organic cation in an amount ranging from about 90 to about 150% of the cation exchange capacity of the smectite-type clay whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic cation thereby forming an organophilic clay gellant; (c) separating the organophilic clay gellant from the slurry; and (d) drying the organophilic clay gellant.
Claim 36
Dependent Claim 118 words
A process for preparing an organophilic clay gellant comprising: (a) subjecting a slurry of smectite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay to high shear conditions whereby clay agglomerates are separated, said smectite-type clay having been previously treated to remove non-clay impurities; (b) reacting the smectite-type clay with organic cation in an amount ranging from about 90 to about 150% of the cation exchange capacity of the smectite-type clay whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic cation thereby forming an organophilic clay gellant; (c) separating the organophilic clay gellant from the slurry; and (d) drying the organophilic clay gellant.
Claim 37
Dependent Claim 36 words
The process of claim 33 wherein the sheared clay exhibits an increase in cation exchange capacity of from about 10 to about 50% as determined by the methylene blue spot test when compared to unsheared clay.
Claim 38
Dependent Claim 36 words
The process of claim 34 wherein the sheared clay exhibits an increase in cation exchange capacity of from about 15 to about 40% as determined by the methylene blue spot test when compared to unsheared clay.
Claim 39
Dependent Claim 28 words
The process of claim 33 wherein the sheared clay exhibits a reduction in median particle size of from about 10 to about 80% when compared to unsheared clay.
Claim 40
Dependent Claim 28 words
The process of claim 36 wherein the sheared clay exhibits a reduction in median particle size of from about 20 to about 60% when compared to unsheared clay.
Claim 41
Dependent Claim 33 words
The process of claim 33 wherein the high shear conditions are achieved by passing the slurry at least one time through a Manton-Gaulin homogenizer operating at from about 500 to about 8,000 psi.
Claim 42
Dependent Claim 33 words
The process of claim 33 wherein the smectite-type clay is reacted with organic cation in an amount ranging from about 100 to about 130% of the cation exchange capacity of the smectite-type clay.
Claim 43
Dependent Claim 56 words
The process of claim 33 wherein an organic anion having a pKa less than about 11.0 is mixed with the smectite-type clay and the organic cation, said organic anion being present in amount such that the milliequivalent ratio of the organic cation to organic anion is in the range of from about 3.0:1.0 to about 12:1.0.
Claim 44
Dependent Claim 22 words
The process of claim 33 wherein the airstream has a temperature in the range of from about 35° to about 45° C.
Claim 45
Dependent Claim 15 words
The process of claim 33 wherein the organophilic clay gellant is dried by freeze drying.
Claim 46
Dependent Claim 32 words
The process of claim 33 wherein the slurry is diluted prior to reaction with organic cation such that slurry contains from about 0.5 to about 1.5% by weight of the smectitetype clay.
Claim 47
Dependent Claim 254 words
A process for preparing an organophilic clay gellant for polyester compositions comprising: (a) subjecting a slurry of smectite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay to high shear conditions whereby clay agglomerates are separated, said smectite-type clay having been previously treated to remove non-clay impurities; (b) reacting the smectite-type clay with organic cation containing at least one lineal or branched, saturated or unsaturated alkyl group having 12 to 22 carbon atoms, at least one lineal or branched,saturated or unsaturated alkyl group having 1 to 12 carbon atoms and at least one aralkyl group having lineal or branched 1 to 12 carbons in the alkyl portion, said organic cation being in an amount ranging from about 90 to about 150% cf the cation exchange capacity of the smectite-type clay and organic anion having a pKa less than about 11.0 in an amount such that the milliequivalents ratio of the organic cation to the organic anion is in the range of from about 1.7:1.0 to about 28:1.0 whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic cation and at least some of the organic anion forms a complex with organic cation which is intercalated with the smectite-type clay thereby forming an organophilic clay gellant; (c) separating the organophilic clay gellant from the slurry; and (d) drying the organophilic clay gellant under conditions selected such that the temperature of the wet organophilic clay gellant does not exceed about 50° C.
Claim 48
Dependent Claim 254 words
A process for preparing an organophilic clay gellant for polyester compositions comprising: (a) subjecting a slurry of smectite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay to high shear conditions whereby clay agglomerates are separated, said smectite-type clay having been previously treated to remove non-clay impurities; (b) reacting the smectite-type clay with organic cation containing at least one lineal or branched, saturated or unsaturated alkyl group having 12 to 22 carbon atoms, at least one lineal or branched,saturated or unsaturated alkyl group having 1 to 12 carbon atoms and at least one aralkyl group having lineal or branched 1 to 12 carbons in the alkyl portion, said organic cation being in an amount ranging from about 90 to about 150% cf the cation exchange capacity of the smectite-type clay and organic anion having a pKa less than about 11.0 in an amount such that the milliequivalents ratio of the organic cation to the organic anion is in the range of from about 1.7:1.0 to about 28:1.0 whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic cation and at least some of the organic anion forms a complex with organic cation which is intercalated with the smectite-type clay thereby forming an organophilic clay gellant; (c) separating the organophilic clay gellant from the slurry; and (d) drying the organophilic clay gellant under conditions selected such that the temperature of the wet organophilic clay gellant does not exceed about 50° C.
Claim 49
Dependent Claim 21 words
The process of claim 44 wherein the smectite-type clay is selected from the group consisting of bentonite, hectorite and mixtures thereof.
Claim 50
Dependent Claim 21 words
The process of claim 44 wherein the slurry contains from about 0.5 to about 80% by weight of the smectite-type clay.
Claim 51
Dependent Claim 33 words
The process of claim 44 wherein the high shear conditions are achieved by passing the slurry at least one time through a Manton-Gaulin homogenizer operating at from about 500 to about 8,000 psi.
Claim 52
Dependent Claim 33 words
The process of claim 44 wherein the smectite-type clay is reacted with organic cation in an amount ranging from about 100 to about 130% of the cation exchange capacity of the smectite-type clay.
Claim 53
Dependent Claim 13 words
The process of claim 44 wherein the organic cation contains a benzyl group.
Claim 54
Dependent Claim 19 words
The process of claim 49 wherein the organic cation is ammonium and further contains at least one methyl group.
Claim 55
Dependent Claim 15 words
The process of claim 50 wherein the organic cation is benzyl dimethyl hydrogenated tallow ammonium
Claim 56
Dependent Claim 29 words
The process of claim 44 wherein the organic anion is derived from at least one member selected from the group consisting of carboxylic acids, sulfonic acids and alkyl sulfates
Claim 57
Dependent Claim 22 words
The process of claim 52 wherein the organic anion is selected from the group consisting of stearate, lauryl sulfate and mixtures thereof.
Claim 58
Dependent Claim 11 words
The process of claim 53 wherein the organic anion is stearate.
Claim 59
Dependent Claim 249 words
A process for preparing an organophilic clay gellant for polyester compositions comprising: (a) preparing a slurry of smectite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay wherein the slurry contains from about 0.5 to about 2.5% by weight of the smectite-type clay; (b) adding to the slurry organic cation containing at least one lineal or branched, saturated or unsaturated alkyl group having 12 to 22 carbon atoms, at least one lineal or branched, saturated or unsaturated alkyl group having 1 to 12 carbon atoms and at least one aralkyl group having lineal or branched 1 to 12 carbons in the alkyl portion, said organic cation being in an amount ranging from about 90 to about 150% of the cation exchange capacity of the smectite-type clay and organic anion having a pKa less than about 11.0 in an amount such that the milliequivalent ratio of the organic cation to the organic anion is in the range of from about 1.7:1.0 to about 28:1.0 whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic cation and at least some of the organic anion forms a complex with organic cation which is intercalated with the smectite-type clay thereby forming an organophilic clay gellant; (c) separating the organophilic clay gellant from the slurry; and (d) drying the organophilic clay gellant under conditions selected such that the temperature of the wet organophilic clay does not exceed about 50° C.
Claim 60
Dependent Claim 249 words
A process for preparing an organophilic clay gellant for polyester compositions comprising: (a) preparing a slurry of smectite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay wherein the slurry contains from about 0.5 to about 2.5% by weight of the smectite-type clay; (b) adding to the slurry organic cation containing at least one lineal or branched, saturated or unsaturated alkyl group having 12 to 22 carbon atoms, at least one lineal or branched, saturated or unsaturated alkyl group having 1 to 12 carbon atoms and at least one aralkyl group having lineal or branched 1 to 12 carbons in the alkyl portion, said organic cation being in an amount ranging from about 90 to about 150% of the cation exchange capacity of the smectite-type clay and organic anion having a pKa less than about 11.0 in an amount such that the milliequivalent ratio of the organic cation to the organic anion is in the range of from about 1.7:1.0 to about 28:1.0 whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic cation and at least some of the organic anion forms a complex with organic cation which is intercalated with the smectite-type clay thereby forming an organophilic clay gellant; (c) separating the organophilic clay gellant from the slurry; and (d) drying the organophilic clay gellant under conditions selected such that the temperature of the wet organophilic clay does not exceed about 50° C.
Claim 61
Dependent Claim 30 words
The process of claim 55 wherein the slurry is prepared by forming a slurry containing greater than about 3.0% by weight of the smectite-type clay and then diluting the slurry.
Claim 62
Dependent Claim 21 words
The process of claim 56 wherein the slurry contains from about 0.50 to about 2.0% by weight of the smectitetype clay.
Claim 63
Dependent Claim 21 words
The process of claim 55 wherein the smectite-type clay is selected from the group consisting of bentonite, hectorite and mixtures thereof.
Claim 64
Dependent Claim 33 words
The process of claim 55 wherein the smectite-type clay is reacted with organic cation in an amount ranging from about 100 to about 130% of the cation exchange capacity of the smectite-type clay.
Claim 65
Dependent Claim 13 words
The process of claim 55 wherein the organic cation contains a benzyl group.
Claim 66
Dependent Claim 19 words
The process of claim 60 wherein the organic cation is ammonium and further contains at least one methyl group.
Claim 67
Dependent Claim 15 words
The process of claim 61 wherein the organic cation is benzyl dimethyl hydrogenated tallow ammonium
Claim 68
Dependent Claim 29 words
The process of claim 55 wherein the organic anion is derived from at least one member selected from the group consisting of carboxylic acids, sulfonic acids and alkyl sulfates.
Claim 69
Dependent Claim 22 words
The process of claim 63 wherein the organic anion is selected from the group consisting of stearate, lauryl sulfate and mixtures thereof.
Claim 70
Dependent Claim 11 words
The process of claim 64 wherein the organic anion is stearate.
Claim 71
Dependent Claim 274 words
A process for preparing an organophilic clay gellant for polyester compositions comprising: (a) subjecting a slurry of smcctite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay to high shear conditions whereby clay agglomerates are separated, said smectite-type clay having been previously treated to remove non-clay impurities; (b) diluting the sheared slurry such that the slurry contains from about 0.5 to about 2.5% by weight of the smectitetype clay; (c) adding to the slurry organic cation containing at least one lineal or branched, saturated or unsaturated alkyl group having 12 to 22 carbon atoms, at least one lineal or branched, saturated or unsaturated alkyl group having 1 to 12 carbon atoms and at least one aralkyl group having lineal or branched 1 to 12 carbons in the alkyl portion, said organic cation being in an amount ranging from about 90 to about 150% of the cation exchange capacity of the smectite-clay and organic anion having a pKa less than about 11.0 in an amount such that the milliequivalent ratio of the organic cation tothe organic anion is in the range of from about 1.7:1.0 to about 28:1.0 whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic cation and at least some of the organic anion forms a complex with organic cation which is intercalated with the smectite-type clay thereby forming an organophilic clay gellant; (d) separating the organophilic clay gellant from the slurry; and (d) drying the organophilic clay gellant under conditions selected such that the temperature of the wet organophilic clay gellant does not exceed about 50° C.
Claim 72
Dependent Claim 274 words
A process for preparing an organophilic clay gellant for polyester compositions comprising: (a) subjecting a slurry of smcctite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay to high shear conditions whereby clay agglomerates are separated, said smectite-type clay having been previously treated to remove non-clay impurities; (b) diluting the sheared slurry such that the slurry contains from about 0.5 to about 2.5% by weight of the smectitetype clay; (c) adding to the slurry organic cation containing at least one lineal or branched, saturated or unsaturated alkyl group having 12 to 22 carbon atoms, at least one lineal or branched, saturated or unsaturated alkyl group having 1 to 12 carbon atoms and at least one aralkyl group having lineal or branched 1 to 12 carbons in the alkyl portion, said organic cation being in an amount ranging from about 90 to about 150% of the cation exchange capacity of the smectite-clay and organic anion having a pKa less than about 11.0 in an amount such that the milliequivalent ratio of the organic cation tothe organic anion is in the range of from about 1.7:1.0 to about 28:1.0 whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic cation and at least some of the organic anion forms a complex with organic cation which is intercalated with the smectite-type clay thereby forming an organophilic clay gellant; (d) separating the organophilic clay gellant from the slurry; and (d) drying the organophilic clay gellant under conditions selected such that the temperature of the wet organophilic clay gellant does not exceed about 50° C.
Claim 73
Dependent Claim 21 words
The process of claim 66 wherein the smectite-type clay is selected from the group consisting of bentonite, hectorite amd mixtures thereof.
Claim 74
Dependent Claim 21 words
The process of claim 66 wherein the slurry contains from about 0.5 to about 2.0% by weight of the smectite-type clay.
Claim 75
Dependent Claim 34 words
The process of claim 66 wherein the sheared clay exhibits an increase in capacity of from about 10 to about 50% as determined by the methylene blue spot test when compared to unsheared clay.
Claim 76
Dependent Claim 28 words
The process of claim 66 wherein the sheared clay exhibits a reduction in median particle size of from about 10 to about 80% when compared to unsheared clay.
Claim 77
Dependent Claim 33 words
The process of claim 66 wherein the high shear conditions are achieved by passing the slurry at least one time through a Manton-Gaulin homogenizer operating at from about 500 to about 8,000 psi.
Claim 78
Dependent Claim 13 words
The process of claim 66 wherein the organic cation contains a benzyl group.
Claim 79
Dependent Claim 19 words
The process of claim 72 wherein the organic cation is ammonium and further contains at least one methyl group.
Claim 80
Dependent Claim 15 words
The process of claim 73 wherein the organic cation is benzyl dimethyl hydrogenated tallow ammonium
Claim 81
Dependent Claim 29 words
The process of claim 74 wherein the organic anion is derived from at least one member selected from the group consisting of carboxylic acids, sulfonic acids and alkyl sulfates.
Claim 82
Dependent Claim 22 words
The process of claim 75 wherein the organic anion is selected from the group consisting of stearate, lauryl sulfate and mixtures thereof.
Claim 83
Dependent Claim 11 words
The process of claim 76 wherein the organic anion is stearate.
Claim 84
Dependent Claim 29 words
The process of claim 66 wherein the organophilic clay gellant is dried in an airstream having a temperature in the range of from about 25° to about 50° C.
Claim 85
Dependent Claim 30 words
The process of claim 66 wherein the organophilic clay gellant is dried in a fluidized bed having a temperature in the range of from about 25° to about 125° C.
Claim 86
Dependent Claim 15 words
The process of claim 66 wherein the organophilic clay gellant is dried by freeze drying.
Claim 87
Dependent Claim 202 words
An organophilic clay gellant for polyester compositions comprising the reaction product of: (a) a smectite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay; (b) organic cation containing at least one lineal or branched, saturated or unsaturated alkyl group having 12 to 22 carbon atoms, at least one lineal or branched, saturated or unsaturated alkyl group having 1 to 12 carbon atoms and at least one aralkyl group having lineal or branched 1 to 12 carbons in the alkyl portion, said organic cation being in an amount ranging from about 100 to about 130% of the cation exchange capacity of the clay; and (c) organic anion having a pKa less than about 11.0 in an amount such that the milliequivalent ratio of the organic cation to the organic anion is in the range of from about 4.0:1.0 to about 6.0:1.0 whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic cation and at least some of the organic anion forms a complex with the organic cation which is intercalated with the smectite-type clay, wherein the organophilic clay gellant is capable of being directly added into the polyester composition.
Claim 88
Dependent Claim 202 words
An organophilic clay gellant for polyester compositions comprising the reaction product of: (a) a smectite-type clay having a cation exchange capacity of at least 75 milliequivalents per 100 grams of clay; (b) organic cation containing at least one lineal or branched, saturated or unsaturated alkyl group having 12 to 22 carbon atoms, at least one lineal or branched, saturated or unsaturated alkyl group having 1 to 12 carbon atoms and at least one aralkyl group having lineal or branched 1 to 12 carbons in the alkyl portion, said organic cation being in an amount ranging from about 100 to about 130% of the cation exchange capacity of the clay; and (c) organic anion having a pKa less than about 11.0 in an amount such that the milliequivalent ratio of the organic cation to the organic anion is in the range of from about 4.0:1.0 to about 6.0:1.0 whereby at least some of the cation exchange sites of the smectite-type clay are substituted with organic cation and at least some of the organic anion forms a complex with the organic cation which is intercalated with the smectite-type clay, wherein the organophilic clay gellant is capable of being directly added into the polyester composition.
Claim 89
Dependent Claim 13 words
The organophilic clay gellant of claim 81 wherein the organic cation is ammonium.
Claim 90
Dependent Claim 15 words
The organophilic clay gellant of claim 82 wherein the organic cation contains a benzyl group.
Claim 91
Dependent Claim 17 words
The organophilic clay gellant of claim 83 wherein the organic cation is benzyl dimethyl hydrogenated tallow ammonium.
Claim 92
Dependent Claim 24 words
The organophilic clay gellant of claim 84 wherein the organic anion is selected from the group consisting of stearate, lauryl sulfate and mixtures thereof.
Claim 93
Dependent Claim 13 words
The organophilic clay gellant of claim 85 wherein the organic anion is stearate.
Claim 94
Dependent Claim 13 words
The organophilic clay gellant of claim 86 wherein the smectite-type clay is bentonite.

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