IP Library Granted Patent US 8,269,046
Granted Patent B2
US 8,269,046 · App. 11/195,577 · Granted Sep 18, 2012

Cyclic bisamides useful in formulating inks for phase-change printing

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Quick Facts
Patent No.
US 8,269,046
App. No.
11/195,577
Granted
Sep 18, 2012
Kind
B2
Abstract

Cyclic bisamides may be used to formulate inks for jet ink printing. The cyclic bisamide may be prepared from a cyclic diamine and acylic monocarboxylic acids. Conversely, the cyclic bisamide may be prepared from a cyclic diacid and acylic monoamines. The performance properties of the product may be enhanced by adding some additional difunctional reactant(s), e.g., diacid or diamine. A blend of bisamides may provide better performance properties than either of the component bisamides alone, where the blend includes at least one cyclic bisamide. The bisamides, in combination with an image-forming material, and optionally in combination with other materials, is taken to a molten form and the applied to a substrate to provide a printed substrate.

Claims (64)

1. A process of making a cyclic bisamide of structure I

comprising reacting under amidification conditions reactants comprising a diamine of structure (IV)

and a monocarboxylic acid of the formula R 1 —COOH, wherein at least one n is an integer from 1 to 2, and at least one n is 0 or an integer from 1 to 2, m is 0 or 1 to provide a cyclopentyl ring or cyclohexyl ring, and R 1 is a C1-C75 alkyl group, the reactants further comprising a difunctional reactant selected from (a) H 2 N—R 2 —NH 2 where R 2 is selected (i) from a polyether group having a plurality of —OR 3 — groups where R 3 is a C3-C10 aliphatic hydrocarbyl, and (ii) a C2-C36 hydrocarbyl group and (b) HOOC—R 4 —COOH where R 4 is a C2-C34 hydrocarbyl group, where the composition has a melt viscosity at 130° C. of less than 100 cPs.

2. The process of claim 1 wherein the diamine of structure (IV) is 1,2-diaminocyclohexane.

3. The process of claim 1 wherein the reactants comprise HOOC—R 4 —COOH, which represents dimer acid.

4. The process of claim 1 wherein the reactants comprise H 2 N—R 2 —NH 2 where R 2 is a polyether group having a plurality of —OR 3 — groups where R 3 is a C2-C3 aliphatic hydrocarbyl.

5. The process of claim 4 wherein the difunctional reactant of formula H 2 N—R 2 —NH 2 has a formula weight of less than 3,000 g/mol.

6. The process of claim 1 wherein the reactants comprise H 2 N—R 2 —NH 2 where R 2 is a C2-C36 hydrocarbyl group.

7. The process of claim 6 wherein the reactants comprise H 2 N—R 2 —NH 2 and H 2 N—R 2 —NH 2 represents a second cyclic diamine of structure (IV)

wherein n is 0 or an integer from 1 to 2, m is 0 or 1 to provide a cyclopentyl ring or cyclohexyl ring.

8. The process of claim 1 wherein the reactants comprise both a difunctional reactant of formula H 2 N—R 2 —NH 2 where R 2 is selected (i) from a polyether group having a plurality of —OR 3 — groups where R 3 is a C2-C10 aliphatic hydrocarbyl, and (ii) a C2-C36 hydrocarbyl group, and a difunctional reactant of formula HOOC—R 4 —COOH where R 4 is a C2-C34 hydrocarbyl group.

9. The process of claim 8 wherein the difunctional reactant of formula H 2 N—R 2 —NH 2 represents a second cyclic diamine of structure (IV)

10. The process of claim 9 wherein the difunctional reactant of formula HOOC—R 4 —COOH represents dimer acid.

11. The process of claim 1 wherein the difunctional reactant comprises carboxylic acid groups, and carboxylic acid groups from the difunctional reactant constitute less than 25 equivalent percent of the total of the carboxylic acid groups present in the reactants.

12. The process of claim 1 wherein the difunctional reactant comprises amine groups, and the amine groups from the difunctional reactant constitute less than 25 equivalent percent of the total of the amine groups present in the reactants.

13. The process of claim 1 having a clarity that is greater than the corresponding composition prepared without the difunctional reactant(s).

14. A process of making a cyclic bisamide of structure (I)

comprising reacting under amidification conditions reactants comprising a diamine of structure (IV)

and a monocarboxylic acid of the formula R 1 —COOH, wherein n is 0 or an integer from 1 to 2, m is 0 or 1 to provide a cyclopentyl ring or cyclohexyl ring, and R 1 is selected from the group consisting of C1-C10 and C15-C30 alkyl groups, the reactants further comprising a difunctional reactant selected from (a) H 2 N—R 2 —NH 2 where R 2 is selected (i) from a polyether group having a plurality of —OR 3 — groups where R 3 is a C3-C10 aliphatic hydrocarbyl, and (ii) a C2-C36 hydrocarbyl group and (b) HOOC—R 4 —COOH where R 4 is a C2-C34 hydrocarbyl group, where the composition has a melt viscosity at 130° C. of less than 100 cPs.

15. The process of claim 14 wherein the diamine of structure (IV) is 1,2-diaminocyclohexane.

16. The process of claim 14 wherein the reactants comprise HOOC—R 4 —COOH, which represents dimer acid.

17. The process of claim 14 wherein the reactants comprise H 2 N—R 2 —NH 2 where R 2 is a polyether group having a plurality of —OR 3 — groups where R 3 is a C2-C3 aliphatic hydrocarbyl.

18. The process of claim 17 wherein the difunctional reactant of formula H 2 N—R 2 —NH 2 has a formula weight of less than 3,000 g/mol.

19. The process of claim 14 wherein the reactants comprise H 2 N—R 2 —NH 2 where R 2 is a C2-C36 hydrocarbyl group.

20. The process of claim 19 wherein the reactants comprise H 2 N—R 2 —NH 2 and H 2 N—R 2 —NH 2 represents a second cyclic diamine of structure (IV)

wherein n is 0 or an integer from 1 to 2, m is 0 or 1 to provide a cyclopentyl ring or cyclohexyl ring.

21. The process of claim 14 wherein the reactants comprise both a difunctional reactant of formula H 2 N—R 2 —NH 2 where R 2 is selected (i) from a polyether group having a plurality of —OR 3 — groups where R 3 is a C2-C10 aliphatic hydrocarbyl, and (ii) a C2-C36 hydrocarbyl group, and a difunctional reactant of formula HOOC—R 4 —COOH where R 4 is a C2-C34 hydrocarbyl group.

22. The process of claim 21 wherein the difunctional reactant of formula H 2 N—R 2 —NH 2 represents a second cyclic diamine of structure (IV)

23. The process of claim 22 wherein the difunctional reactant of formula HOOC—R 4 —COOH represents dimer acid.

24. The process of claim 14 wherein the difunctional reactant comprises carboxylic acid groups, and carboxylic acid groups from the difunctional reactant constitute less than 25 equivalent percent of the total of the carboxylic acid groups present in the reactants.

25. The process of claim 14 wherein the difunctional reactant comprises amine groups, and the amine groups from the difunctional reactant constitute less than 25 equivalent percent of the total of the amine groups present in the reactants.

26. The process of claim 14 having a clarity that is greater than the corresponding composition prepared without the difunctional reactant(s).

27. A process of making a cyclic bisamide of structure (II)

comprising reacting under amidification conditions reactants comprising a diamine of structure (IV)

and a monocarboxylic acid of the formula R 1 —COOH, wherein n is 0 or an integer from 1 to 2, m is 0 to provide a cyclopentyl ring, and R 1 is a C1-C75 alkyl group, the reactants further comprising a difunctional reactant selected from (a) H 2 N—R 2 —NH 2 where R 2 is selected (i) from a polyether group having a plurality of —OR 3 — groups where R 3 is a C3-C10 aliphatic hydrocarbyl, and (ii) a C2-C36 hydrocarbyl group and (b) HOOC—R 4 —COOH where R 4 is a C2-C34 hydrocarbyl group, where the composition has a melt viscosity at 130° C. of less than 100 cPs.

28. The process of claim 27 wherein the diamine of structure (IV) is 1,2-diaminocyclopentane.

29. The process of claim 27 wherein the reactants comprise HOOC—R 4 —COOH, which represents dimer acid.

30. The process of claim 27 wherein the reactants comprise H 2 N—R 2 —NH 2 where R 2 is a polyether group having a plurality of —OR 3 — groups where R 3 is a C2-C3 aliphatic hydrocarbyl.

31. The process of claim 30 wherein the difunctional reactant of formula H 2 N—R 2 —NH 2 has a formula weight of less than 3,000 g/mol.

32. The process of claim 27 wherein the reactants comprise H 2 N—R 2 —NH 2 where R 2 is a C2-C36 hydrocarbyl group.

33. The process of claim 32 wherein the reactants comprise H 2 N—R 2 —NH 2 and H 2 N—R 2 —NH 2 represents a second cyclic diamine of structure (IV)

wherein n is 0 or an integer from 1 to 2, m is 0 or 1 to provide a cyclopentyl ring or cyclohexyl ring.

34. The process of claim 27 wherein the reactants comprise both a difunctional reactant of formula H 2 N—R 2 —NH 2 where R 2 is selected (i) from a polyether group having a plurality of —OR 3 — groups where R 3 is a C2-C10 aliphatic hydrocarbyl, and (ii) a C2-C36 hydrocarbyl group, and a difunctional reactant of formula HOOC—R 4 —COOH where R 4 is a C2-C34 hydrocarbyl group.

35. The process of claim 34 wherein the difunctional reactant of formula H 2 N—R 2 —NH 2 represents a second cyclic diamine of structure (IV)

36. The process of claim 35 wherein the difunctional reactant of formula HOOC—R 4 .COOH represents dimer acid.

37. The process of claim 27 wherein the difunctional reactant comprises carboxylic acid groups, and carboxylic acid groups from the difunctional reactant constitute less than 25 equivalent percent of the total of the carboxylic acid groups present in the reactants.

38. The process of claim 27 wherein the difunctional reactant comprises amine groups, and the amine groups from the difunctional reactant constitute less than 25 equivalent percent of the total of the amine groups present in the reactants.

39. The process of claim 27 having a clarity that is greater than the corresponding composition prepared without the difunctional reactant(s).

40. A process of making a cyclic bisamide of structure (I)

comprising reacting under amidification conditions reactants comprising diamine of structure (IV)

and a monocarboxylic acid of the formula R 1 —COOH, wherein n is 0 or an integer from 1 to 2, m is 0 or 1 to provide a cyclopentyl ring or cyclohexyl ring, and R 1 is a C1-C75 alkyl group, the reactants further comprising a difunctional reactant selected from (a) H 2 N—R 2 —NH 2 where R 2 is selected (i) from a polyether group having a plurality of —OR 3 — groups where R 3 is a C3-C10 aliphatic hydrocarbyl, and (ii) a C2-C36 hydrocarbyl group and (b) HOOC—R 4 —COOH where R 4 is a C2-C34 hydrocarbyl group, where the composition has a melt viscosity at 130° C. of less than 100 cPs; and wherein the diamine of structure (IV) is a 1,3 diamine when m is 0, and a 1,3 or 1,4 diamine when m is 1.

41. The process of claim 40 wherein the diamine of structure (IV) is 1,3-diaminocyclohexane.

42. The process of claim 40 wherein the reactants comprise HOOC—R 4 —COOH, which represents dimer acid.

43. The process of claim 40 wherein the reactants comprise H 2 N—R 2 —NH 2 where R 2 is a polyether group having a plurality of —OR 3 — groups where R 3 is a C2-C3 aliphatic hydrocarbyl.

44. The process of claim 43 wherein the difunctional reactant of formula H 2 N—R 2 —NH 2 has a formula weight of less than 3,000 g/mol.

45. The process of claim 40 wherein the reactants comprise H 2 N—R 2 —NH 2 where R 2 is a C2-C36 hydrocarbyl group.

46. The process of claim 45 wherein the reactants comprise H 2 N—R 2 —NH 2 , and H 2 N—R 2 —NH 2 represents a second cyclic diamine of structure (IV)

wherein n is 0 or an integer from 1 to 2, m is 0 or 1 to provide a cyclopenty 1 ring or cyclohexy 1 ring.

47. The process of claim 40 wherein the reactants comprise both a difunctional reactant of formula H 2 N—R 2 —NH 2 where R 2 is selected (i) from a polyether group having a plurality of —OR 3 — groups where R 3 is a C2-C10 aliphatic hydrocarbyl, and (ii) a C2-C36 hydrocarbyl group, and a difunctional reactant of formula HOOC—R 4 —COOH where R 4 is a C2-C34 hydrocarbyl group.

48. The process of claim 47 wherein the difunctional reactant of formula H 2 N—R 2 —NH 2 represents a second cyclic diamine of structure (IV)

49. The process of claim 48 wherein the difunctional reactant of formula HOOC—R 4 —COOH represents dimer acid.

50. The process of claim 40 wherein the difunctional reactant comprises carboxylic acid groups, and carboxylic acid groups from the difunctional reactant constitute less than 25 equivalent percent of the total of the carboxylic acid groups present in the reactants.

51. The process of claim 40 wherein the difunctional reactant comprises amine groups, and the amine groups from the difunctional reactant constitute less than 25 equivalent percent of the total of the amine groups present in the reactants.

52. The process of claim 40 having a clarity that is greater than the corresponding composition prepared without the difunctional reactant(s).

Assignments (16)
RELEASE OF SECURITY INTEREST IN INTELLECTUAL PROPERTY COLLATERAL AT REEL/FRAME NO. 33146/0361 Recorded Jan 6, 2016
From: GOLDMAN SACHS BANK USA
To: ARIZONA CHEMICAL COMPANY LLC
Reel/Frame 037451/0169 →
RELEASE OF SECURITY INTEREST IN PATENT RIGHTS Recorded Jan 6, 2016
From: ANTARES CAPITAL LP, AS SUCCESSOR TO GENERAL ELECTRIC CAPITAL CORPORATION
To: ARIZONA CHEMICAL COMPANY LLC
Reel/Frame 037451/0057 →
ASSIGNMENT OF INTELLECTUAL PROPERTY SECURITY AGREEMENT Recorded Oct 9, 2015
From: GENERAL ELECTRIC CAPITAL CORPORATION, AS RETIRING AGENT
To: ANTARES CAPITAL LP, AS SUCCESSOR AGENT
Reel/Frame 036827/0443 →
SECURITY INTEREST Recorded Jun 12, 2014
From: ARIZONA CHEMICAL COMPANY LLC
To: GENERAL ELECTRIC CAPITAL CORPORATION, AS FIRST LIEN COLLATERAL AGENT
Reel/Frame 033146/0333 →
RELEASE OF SECURITY INTEREST Recorded Jun 12, 2014
From: GENERAL ELECTRIC CAPITAL CORPORATION, AS COLLATERAL AGENT
To: ARIZONA CHEMICAL COMPANY LLC
Reel/Frame 033146/0278 →
SECURITY INTEREST Recorded Jun 12, 2014
From: ARIZONA CHEMICAL COMPANY LLC
To: GOLDMAN SACHS BANK USA, AS SECOND LIEN COLLATERAL AGENT
Reel/Frame 033146/0361 →
SECURITY AGREEMENT Recorded Jan 7, 2012
From: ARIZONA CHEMICAL COMPANY, LLC
To: GENERAL ELECTRIC CAPITAL CORPORATION, AS COLLATERAL AGENT
Reel/Frame 027497/0465 →
RELEASE OF SECURITY INTEREST Recorded Jan 6, 2012
From: GENERAL ELECTRIC CAPITAL CORPORATION
To: ARIZONA CHEMICAL COMPANY, LLC
Reel/Frame 027489/0030 →
SECURITY AGREEMENT Recorded Feb 2, 2011
From: ARIZONA CHEMICAL COMPANY, LLC
To: GENERAL ELECTRIC CAPITAL CORPORATION, AS COLLATERAL AGENT
Reel/Frame 025734/0383 →
RELEASE OF SECURITY INTEREST IN INTELLECTUAL PROPERTY COLLATERAL (FIRST LIEN) Recorded Jan 31, 2011
From: GOLDMAN SACHS CREDIT PARTNERS, L.P.
To: ARIZONA CHEMICAL COMPANY
Reel/Frame 025719/0265 →
RELEASE OF SECURITY INTEREST IN INTELLECTUAL PROPERTY COLLATERAL (SECOND LIEN) Recorded Jan 31, 2011
From: WILMINGTON TRUST FSB (SUCCESSOR TO CAPITALSOURCE FINANCE LLC)
To: ARIZONA CHEMICAL COMPANY
Reel/Frame 025720/0248 →
CHANGE OF NAME Recorded Nov 24, 2010
From: ARIZONA CHEMICAL COMPANY
To: ARIZONA CHEMICAL COMPANY, LLC
Reel/Frame 025406/0597 →
CHANGE OF NAME Recorded Aug 30, 2010
From: CAPITALSOURCE FINANCE LLC
To: WILMINGTON TRUST FSB
Reel/Frame 024944/0501 →
FIRST LIEN PATENT SECURITY AGREEMENT Recorded Mar 20, 2007
From: ARIZONA CHEMICAL COMPANY
To: GOLDMAN SACHS CREDIT PARTNERS, L.P.
Reel/Frame 019035/0392 →
SECOND LIEN PATENT SECURITY AGREEMENT Recorded Mar 20, 2007
From: ARIZONA CHEMICAL COMPANY
To: CAPITAL SOURCE FINANCE, LLC
Reel/Frame 019035/0423 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 11, 2006
From: PAVLIN, MARK S.
To: ARIZONA CHEMICAL COMPANY
Reel/Frame 018373/0731 →