US4585843A
Expired / Lapsed
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Exothermic reactions
Assignee: Ciba Specialty Chemicals Water Treatments Ltd
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Filing: 1984-11-30
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Granted: 1986-04-29
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Expires: 2004-11-30
Abstract
Abstract An exothermic gel polymerization process conducted in the presence of water is initiated at a low temperature, is held for most of the process at a higher temperature by including in the medium a particulate heat sink material, such as sodium sulphate decahydrate, that is substantially insoluble in the medium and which undergoes an endothermic phase change and is then allowed to rise to a higher temperature. Either as a result of the endothermic change, or as a result of a subsequent exothermic change, at the end of the process the heat sink material is again solid particulate material substantially insoluble in the medium and so the product is a dispersion of the material in a polymer gel. The polymer is water soluble.
Inventors
- 👤 Peter Flesher
- 👤 David Farrar
- 👤 Ian M. Johnson
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 20:06
CPC Classifications
C; C08; C08F; C08F20/00; B; B01; B01J; B01J19/00; B01J19/0006; B01J19/0013; C09; C09K; C09K5/00; C09K5/02; C09K5/06; C09K5/063; B01J2219/00; B01J2219/00049; B01J2219/00051; B01J2219/00121; B01J2219/00123; B01J2219/00126; B01J2219/00168; B01J2219/00184; B01J2219/00189
Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
186 words
A bulk gel polymerization process for producing a water soluble polymer by exothermic bulk gel polymerisation of a reaction mixture that comprises 100 parts polymerisable monoethylenically unsaturated monomers dissolved in 33 to 250 parts added free water and that contains a heat sink material that is in a first thermodynamic state, is particulate and is substantially insoluble in the reaction mixture, in which the polymerisation reaction is initiated at a temperature T 1 at which the heat sink material remains in its first thermodynamic state, the temperature of the reaction mixture rises exothermically to T 2 at which the heat sink material undergoes an endothermic change of state to a second thermodynamic state by absorbing the exothermic heat of polymerisation and the amount of heat sink material is such that when the all the heat sink material is in the second thermodynamic state, the temperature rises exothermically to T 3 , and in which the process includes the step of converting the heat sink material from the first thermodynamic state to a final thermodynamic state in which it is particulate and substantially insoluble in liquid medium.
Claim 2
Dependent Claim
186 words
A bulk gel polymerization process for producing a water soluble polymer by exothermic bulk gel polymerisation of a reaction mixture that comprises 100 parts polymerisable monoethylenically unsaturated monomers dissolved in 33 to 250 parts added free water and that contains a heat sink material that is in a first thermodynamic state, is particulate and is substantially insoluble in the reaction mixture, in which the polymerisation reaction is initiated at a temperature T 1 at which the heat sink material remains in its first thermodynamic state, the temperature of the reaction mixture rises exothermically to T 2 at which the heat sink material undergoes an endothermic change of state to a second thermodynamic state by absorbing the exothermic heat of polymerisation and the amount of heat sink material is such that when the all the heat sink material is in the second thermodynamic state, the temperature rises exothermically to T 3 , and in which the process includes the step of converting the heat sink material from the first thermodynamic state to a final thermodynamic state in which it is particulate and substantially insoluble in liquid medium.
Claim 3
Dependent Claim
29 words
A bulk gel polymerization process according to claim 1 in which the temperature of the reaction medium is held at a substantially constant temperature T 2 during the process.
Claim 4
Dependent Claim
33 words
A bulk gel polymerization process according to claim 1 in which the temperature of the reaction mixture is held at a substantially constant temperature T 2 for at least 50% of the polymerisation.
Claim 5
Dependent Claim
44 words
A bulk gel polymerization process according to claim 1 in which 5 to 50% of the polymerisation occurs during the temperature rise between T 1 and T 2 and 5 to 25% of the polymerisation occurs during the temperature rise to T 3 .
Claim 6
Dependent Claim
42 words
A bulk gel polymerization process according to claim 1 in which T 1 is in the range 0° to 20° C., T 2 is in the range 25° to 60° C. and T 3 is in the range 60° to 100° C.
Claim 7
Dependent Claim
20 words
A bulk gel polymerization process according to claim 1 in which the polymerisation reaction is initiated by a Redox initiator.
Claim 8
Dependent Claim
43 words
A bulk gel polymerization process according to claim 1 in which the monomers comprise monomers selected from acrylamide and acrylic acid and the amount of water is from 75 to 250 parts per 100 parts of monomers selected from acrylamide and acrylic acid.
Claim 9
Dependent Claim
105 words
A bulk gel polymerization process according to claim 1 in which a further heat sink material in a first thermodynamic state in which it is particulate and insoluble in the reaction mixture is included in the reaction mixture, and this material can undergo an endothermic change of state at a temperature T 4 higher than T 2 and in which process, when all the first heat sink material is in its second thermodynamic state, the temperature of the reaction mixture rises from T 2 to T 4 at which the further heat sink material undergoes an endothermic change of state to its second thermodynamic state.
Claim 10
Dependent Claim
38 words
A bulk gel polymerization process according to claim 8 in which, when all the further heat sink material is in its second thermodynamic state, the temperature of the reaction mixture rises from T 4 to a higher temperature.
Claim 11
Dependent Claim
20 words
A bulk gel polymerization process according to claim 1 in which the heat sink material is an ionic crystalline material.
Claim 12
Dependent Claim
34 words
A bulk gel polymerization process according to claim 1 in which the heat sink material is the hydrate of an inorganic salt, and the phase change is a change in the degree of hydration.
Claim 13
Dependent Claim
25 words
A bulk gel polymerization process according to claim 1 in which the heat sink material is selected from sodium sulphate decahydrate and sodium acetate trihydrate.
Claim 14
Dependent Claim
29 words
A bulk gel polymerization process according to claim 8 in which the heat sink material consists of sodium sulphate decahydrate and further heat sink material is sodium acetate trihydrate.
Claim 15
Dependent Claim
57 words
A bulk gel polymerization process according to claim 3 in which the polymerization reaction is initiated by a redox initiator, T 1 is in the range of 0 to 20 degrees C, T 2 is in the range of 25 to 60 degrees C and T 3 is in the range of 60 to 100 degrees C.
Claim 16
Dependent Claim
37 words
A bulk gel polymerization process according to claim 14 in which the monomers comprise monomers selected from acrylamide and acrylic acid and the amount of water is from 75 to 250 parts per 100 parts of monomers.
References Cited (Backward Citations)
US2846421A
Cited
US4335237A
Cited
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1989-04-28 | 1989-10-28 | 1990-04-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1993-04-28 | 1993-10-28 | 1994-04-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1997-04-28 | 1997-10-28 | 1998-04-29 | $7700.00 | Window Closed / Lapsed |