IP Library Granted Patent US 7,244,857
Granted Patent B2
US 7,244,857 · App. 10/713,805 · Granted Jul 17, 2007

Method of making hydroxyalkyl amide containing reduced level of unreacted alkanolamine

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Quick Facts
Patent No.
US 7,244,857
App. No.
10/713,805
Granted
Jul 17, 2007
Kind
B2
Abstract

A method for reacting alkanolamine with ester in the presence of a metal silicate compound and, optionally, a catalyst, to produce a hydroxyalkyl amide composition with a decreased level of alkanolamine and residual catalyst.

Claims (65)

1. A method for reacting at least one primary and/or secondary alkanolamine with at least one ester, optionally, in the presence of catalyst, to provide a reaction mixture containing hydroxyalkyl amide and unreacted alkanolamine, wherein the improvement comprises, carrying out the reaction of an alkanolamine selected from the group consisting of ethanolamine, propanolamine, isopropanolamine, butanolamine, isobutanolamine, methylethanolamine, butylethanolamine, diethanolamine, dipropanolamine, diisopropanolamine, dibutanolamine, diisobutanolamine, and mixtures thereof and ester in the presence of at least one metal silicate or treating the reaction mixture with at least one metal silicate, the metal of the metal silicate being a metal of Group IIA or Group IIIA of the Periodic Table.

2. The method of claim 1 wherein the parent acid of the ester contains from about 4 to about 22 carbon atoms and the parent alkanol of the ester contains from 1 to about 10 carbon atoms.

3. The method of claim 2 wherein the ester is a fatty acid methyl ester or mixture of fatty acid methyl esters.

4. The method of claim 2 wherein the parent acid of the ester is a fatty acid derived from canola oil, castor oil, cocoa butter, coconut oil, cotton seed oil, olive oil, palm kernel oil, palm kernel (olein), palm kernel (stearine), peanut oil, rapeseed oil, safflower oil, soybean oil, sunflower oil, tall oil, corn oil, butter, lard, tallow, yellow grease, blubber, herring, menhaden, sardine oil, babasso oil and mixtures thereof.

5. The method of claim 4 wherein the parent acid of the ester is a fatty acid derived from coconut oil and the parent alkanol of the ester is methanol.

6. The method of claim 2 wherein the parent acid of the ester is selected from the group consisting of butyric, caproic, caprylic, capric, decenoic, lauric, cis-9-dodecenoic, myristic, myristoleic, cis-9-tetradecenoic, pentadecanoic, palmitic, palmitoleic, cis-9-hexadecenoic, heptadecanoic, heptadecenoic, steric, oleic, linoleic, linolenic, ricinoleic, dihydroxystearic, nonadecanoic, arachidic, cis-9, cis-11-eicosenoic, eicosadienoic, eicosatrienoic, arachidonic, eicosapentaenoic, behenic, erucic, docosadienoic, 4,8,12,15,19-docosapentaenoic, docosahexaenoic, lignoceric, tetracosenoic and mixtures thereof.

7. The method of claim 6 wherein the parent alkanol of the ester is methanol.

8. The method of claim 1 wherein the catalyst is a basic catalyst.

9. The method of claim 8 wherein the basic catalyst is a metal alkoxide or carbonate.

10. The method of claim 9 wherein the metal alkoxide or carbonate is selected from the group consisting of sodium methoxide, sodium ethoxide, sodium propoxide, potassium methoxide, potassium ethoxide, potassium propoxide, potassium carbonate, sodium carbonate, sodium or potassium butoxide, sodium or potassium pentoxide, sodium or potassium hexanoate, sodium carbonate, potassium carbonate, cesium carbonate, calcium carbonate, strontium carbonate, barium carbonate and mixtures thereof.

11. The method of claim 8 wherein the basic catalyst is an organic catalyst selected from the group consisting of tetraalkyl ammonium hydroxide, Ethyl diisopropyl amines, diisopropylethyl amines, 1,8-diazabicyclo[5.4.0] undec-7-ene, 1,5-diazabicyclo[4.3.0] non-5-ene, guanidine and penta methyl guanadine.

12. The method of claim 1 wherein the catalyst is present in an amount of from about 1 to about 100 wt. percent of catalyst concentrate in solvent.

13. The method of claim 12 wherein the catalyst is present in an amount of from about10 to about 50 wt. percent of catalyst concentrate in solvent.

14. The method of claim 13 wherein the catalyst is present in an amount of from about 20 to about 30 wt. percent of catalyst concentrate in solvent.

15. The method of claim 10 wherein the metal alkoxide or carbonate catalyst is present in an amount of from about 0.05 to about 1.00 wt. percent.

16. The method of claim 15 wherein the metal alkoxide or carbonate catalyst is present in an amount of from about 0.25 to about 0.75 wt. percent.

17. The method of claim 16 wherein the metal alkoxide or carbonate catalyst is present in an amount of from about 0.40 to about 0.60 wt. percent.

18. The method of claim 11 wherein the organic catalyst is present in an amount of from about 0.05 to about 1.00 wt. percent.

19. The method of claim 18 wherein the organic catalyst is present in an amount of from about 0.25 to about 0.75 wt. percent.

20. The method of claim 19 wherein the organic catalyst is present in an amount of from about 0.40 to about 0.60 wt. percent.

21. The method of claim 1 wherein the metal silicate is of the general formula xM a O b :ySiO 2 :zH 2 O wherein M is any metal of Group IA, Group HA or Group IIIA of The Periodic Table, x and y are in a molar ratio of from about 1.5:1 to about 1:3.6 and z is equal to x, a is 1 or 2 and b is 1–3.

22. The method of claim 21 wherein in the formula of the metal silicate, x is 1, y is 2.6 and z is 1.

23. The method of claim 21 wherein the metal in the metal silicate is magnesium, calcium, aluminum, sodium.

24. The method of claim 22 wherein the metal in the metal silicate is magnesium, calcium, aluminum, sodium.

25. The method of claim 21 wherein the metal silicate is present at a level of from about 1 to about 50 wt. percent of hydroxyalkyl amide reaction mixture.

26. The method of claim 21 wherein the metal silicate is present at a level of from about 10 to about 20 wt. percent of hydroxyalkyl amide reaction mixture.

27. The method of claim 22 wherein the metal silicate is present at a level of from about 1 to about 50 wt. percent of hydroxyalkyl amide reaction mixture.

28. The method of claim 22 wherein the metal silicate is present at a level of from about 10 to about 20 wt. percent of hydroxyalkyl amide reaction mixture.

29. The method of claim 1 wherein the reaction mixture treated with the metal silicate contains from about 0 to about 0.5 wt. percent unreacted alkanolamine.

30. The method of claim 1 wherein the reaction mixture treated with the metal silicate contains from about 0.05 to about 0.2 wt. percent unreacted alkanolamine.

31. The method of claim 1 wherein the reaction of alkanolamine and ester is carried out in the presence of catalyst and treated with metal silicate with the amount of catalyst being reduced by about 30 percent.

32. The method of claim 1 wherein the reaction of alkanolamine and ester is carried out in the presence of catalyst and treated with metal silicate with the amount of catalyst being reduced by about 60 percent.

33. A method for making a hydroxyalkyl amide which comprises reacting at least one primary and/or secondary alkanolamine with at least one ester, optionally, in the presence of catalyst, to provide a reaction mixture containing hydroxyalkyl amide and unreacted alkanolamine, the reaction of alkanolamine and ester being carried out in the presence of at least one metal silicate or the reaction mixture being treated with at least one metal silicate, the metal of the metal silicate being a metal of Group IA, Group IIA or Group IIIA of the Periodic Table.

34. The method of claim 33 wherein the primary and/or secondary alkanolamine is of the general formula RNHR′ wherein R is hydroxyalkyl of from about 2 to about 10 carbon atoms, hydroxyalkylether and/or combinations thereof, and R′ is hydrogen, alkyl of from 1 to about 10 carbon atoms, hydroxyalkylether and/or combinations thereof or hydroxyalkyl of from 2 to about 10 carbon atoms, hydroxyalkylether and/or combinations thereof.

35. The method of claim 33 wherein the alkanolamine is selected from the group consisting of ethanolamine, propanolamine, isopropanolamine, butanolamine, isobutanolamine, methylethanolamine, butylethanolamine, diethanolamine, dipropanolamine, diisopropanolamine, dibutanolamine, diisobutanolamine, and mixtures thereof.

36. The method of claim 33 wherein the parent acid of the ester contains from about 4 to about 22 carbon atoms and the parent alkanol of the ester contains from 1 to about 10 carbon atoms.

37. The method of claim 36 wherein the ester is a fatty acid methyl ester or mixture of fatty acid methyl esters.

38. The method of claim 33 wherein the parent acid of the ester is a fatty acid derived from canola oil, castor oil, cocoa butter, coconut oil, cotton seed oil, olive oil, palm kernel oil, palm kernel (olein), palm kernel (stearine), peanut oil, rapeseed oil, safflower oil, soybean oil, sunflower oil, tall oil fatty acid, corn oil, butter, lard, tallow, yellow grease, blubber, herring, menhaden, sardine, babasso and mixtures thereof.

39. The method of claim 38 wherein the parent acid of the ester is a fatty acid derived from coconut oil and the parent alkanol of the ester is methanol.

40. The method of claim 36 wherein the parent acid of the ester is selected from the group consisting of butyric, caproic, caprylic, capric, decenoic, lauric, cis-9-dodecenoic, myristic, myristoleic, cis-9-tetradecenoic, pentadecanoic, palmitic, palmitoleic, cis-9-hexadecenoic, heptadecanoic, heptadecenoic, steric, oleic, linoleic, linolenic, ricinoleic, dihydroxystearic, nonadecanoic, arachidic, cis-9, cis-11-eicosenoic, eicosadienoic, eicosatrienoic, arachidonic, eicosapentaenoic, behenic, erucic, docosadienoic, 4,8,12,15,19-docosapentaenoic, docosahexaenoic, lignoceric, tetracosenoic and mixtures thereof.

41. The method of claim 40 wherein the parent alkanol of the ester is methanol.

42. The method of claim 36 wherein the catalyst is a basic catalyst.

43. The method of claim 42 wherein the basic catalyst is a metal alkoxide or carbonate.

44. The method of claim 43 wherein the metal alkoxide or carbonate is selected from the group consisting of sodium methoxide, sodium ethoxide, sodium propoxide, potassium methoxide, potassium ethoxide, potassium propoxide, potassium carbonate, sodium carbonate, sodium or potassium butoxide, sodium or potassium pentoxide, sodium or potassium hexanoate, sodium carbonate, potassium carbonate, cesium carbonate, calcium carbonate, strontium carbonate, barium carbonate and mixtures thereof.

45. The method of claim 42 wherein the basic catalyst is an organic catalyst selected from the group consisting of tetraalkyl ammonium hydroxide, Ethyl di-isopropyl amines, diisopropyl ethyl amines, 1,8-diazabicyclo[5.4.0] undec-7-ene, 1,5-diazabicyclo[4.3.0] non-5-ene, guanidine, penta methyl guanadine.

46. The method of claim 33 wherein the catalyst is present in an amount of from about 1 to about 100 wt. percent of catalyst concentrate in solvent.

47. The method of claim 46 wherein the catalyst is present in an amount of from about 10 to about 50 wt. percent of catalyst concentrate in solvent.

48. The method of claim 47 wherein the catalyst is present in an amount of from about 20 to about 30 wt. percent of catalyst concentrate in solvent.

49. The method of claim 44 wherein the metal alkoxide or carbonate catalyst is present in an amount of from about 0.05 to about 1.00 wt. percent.

50. The method of claim 49 wherein the metal alkoxide or carbonate catalyst is present in an amount of from about 0.25 to about 0.75 wt. percent.

51. The method of claim 50 wherein the metal alkoxide or carbonate catalyst is present in an amount of from about 0.40 to about 0.60 wt. percent.

52. The method of claim 45 wherein the organic catalyst is present in an amount of from about 0.05 to about 1.00 wt. percent.

53. The method of claim 52 wherein the organic catalyst is present in an amount of from about 0.25 to about 0.75 wt. percent.

54. The method of claim 53 wherein the organic catalyst is present in an amount of from about 0.40 to about 0.60 wt. percent.

55. The method of claim 33 wherein the metal silicate is of the general formula xM a O b :ySiO 2 :zH 2 O wherein M is any metal of Group IA, Group IIA or Group IIIA of The Periodic Table, x and y are in a molar ratio of from about 1.5:1 to about 1:3.6 and z is equal to x, a is 1 or 2 and b is 1–3.

56. The method of claim 55 wherein in the formula of the metal silicate x is 1, y is 2.6 and z is 1.

57. The method of claim 55 wherein the metal in the metal silicate is magnesium, calcium, aluminum, sodium.

58. The method of claim 56 wherein the metal in the metal silicate is magnesium.

59. The method of claim 55 wherein the metal silicate is present at a level of from about 1 to about 50 wt. percent of hydroxyalkyl amide reaction mixture.

60. The method of claim 55 wherein the metal silicate is present at a level of from about 10 to about 20 wt. percent of hydroxyalkyl amide reaction mixture.

61. The method of claim 56 wherein the metal silicate is present at a level of from about 1 to about 50 wt. percent of hydroxyalkyl amide reaction mixture.

62. The method of claim 56 wherein the metal silicate is present at a level of from about 10 to about 20 wt. percent of hydroxyalkyl amide reaction mixture.

63. The method of claim 33 wherein the hydroxyalkyl amide contains not more than about 0.5 wt. percent unreacted alkanolamine.

64. The method of claim 33 wherein the reaction of alkanolamine and ester is carried out in the presence of catalyst and treated with metal silicate with the amount of catalyst being reduced by about 30 wt. percent.

65. The method of claim 33 wherein the reaction of alkanolamine and ester is carried out in the presence of catalyst and treated with metal silicate with the amount of catalyst being reduced by about 60 wt. percent.

Assignments (11)
CHANGE OF NAME Recorded Sep 25, 2018
From: CROMPTON CORPORATION
To: CHEMTURA CORPORATION
Reel/Frame 047141/0152 →
RELEASE OF FIRST LIEN INTELLECTUAL PROPERTY SECURITY AGREEMENT Recorded May 11, 2017
From: BANK OF AMERICA, N.A.
To: CHEMTURA CORPORATION; BIOLAB FRANCHISE COMPANY, LLC; BIO-LAB, INC.; CROMPTON COLORS INCORPORATED; CROMPTON HOLDING CORPORATION; GLCC LAUREL, LLC; GREAT LAKES CHEMICAL CORPORATION; GREAT LAKES CHEMICAL GLOBAL, INC.; GT SEED TREATMENT, INC.; HOMECARE LABS, INC.; LAUREL INDUSTRIES HOLDINGS, INC.; RECREATIONAL WATER PRODUCTS, INC.; WEBER CITY ROAD LLC
Reel/Frame 042447/0508 →
RELEASE OF SECOND LIEN INTELLECTUAL PROPERTY SECURITY AGREEMENT Recorded May 11, 2017
From: BANK OF AMERICA, N.A.
To: CHEMTURA CORPORATION; BIOLAB FRANCHISE COMPANY, LLC; BIO-LAB, INC.; CROMPTON COLORS INCORPORATED; CROMPTON HOLDING CORPORATION; GLCC LAUREL, LLC; GREAT LAKES CHEMICAL CORPORATION; GREAT LAKES CHEMICAL GLOBAL, INC.; GT SEED TREATMENT, INC.; HOMECARE LABS, INC.; LAUREL INDUSTRIES HOLDINGS, INC.; RECREATIONAL WATER PRODUCTS, INC.; WEBER CITY ROAD LLC
Reel/Frame 042449/0001 →
SECDOND LIEN INTELLECTUAL PROPERTY SECURITY AGREEMENT Recorded Mar 21, 2011
From: CHEMTURA CORPORATION; BIOLAB FRANCHISE COMPANY, LLC; BIO-LAB, INC.; CROMPTON COLORS INCORORATED; CROMPTON HOLDING CORPORATION; CLCC LAUREL, LLC; GREAT LAKES CHEMICAL CORPORATION; GREAT LAKES CHEMICAL GLOBAL, INC.; GT SEED TREATMENT, INC.; HOMECARE LABS, INC.; HAOMECARE LABS, INC.; LAUREL INDUSTRIES HOLDINGS, INC.; RECREATIONAL WATER PRODUCTS, INC.; WEBER CITY ROAD LLC
To: BANK OF AMERICA, N. A.
Reel/Frame 027881/0347 →
FIRST LIEN INTELLECTUAL PROPERTY SECURITY AGREEMENT. Recorded Mar 21, 2011
From: CHEMTURA CORPORATION; BIOLAB FRANCHISE COMPANY, LLC; BIO-LAB, INC.; CROMPTON COLORS INCORPORATED; CROMPTON HOLDING CORPORATION; GLCC LAUREL, LLC; GREAT LAKES CHEMICAL CORPORATION; GREAT LAKES CHEMICAL GLOBAL, INC.; GT SEED TREATMENT, INC.; HOMECARE LABS, INC.; LAUREL INDUSTRIES HOLDINGS, INC.; RECREATIONAL WATER PRODUCTS, INC.; WEBER CITY ROAD LLC
To: BANK OF AMERICA, N.A.
Reel/Frame 026028/0622 →
INTELLECTUAL PROPERTY SECURITY RELEASE AGREEMENT Recorded Mar 21, 2011
From: CITIBANK, N.A.
To: CHEMTURA CORPORATION; A & M CLEANING PRODUCTS, LLC; ASCK, INC; BIOLAB COMPANY STORE, LLC; AQUA CLEAR INDUSTRIES, LLC; ASEPSIS, INC.; BIOLAB TEXTILES ADDITIVES, LLC; BIOLAB, INC.; CROMPTON COLORS INCORPORATED; CROMPTON MONOCHEM, INC.; CNK CHEMICAL REALTY CORPORATION; CROMPTON HOLDING CORPORATION; GLCC LAUREL, LLC; GREAT LAKES CHEMICAL CORPORATION; GT SEED TREATMENT, INC.; ISCI, INC; GREAT LAKES CHEMICAL GLOBAL, INC.; HOMECARE LABS, INC.; KEM MANUFACTURING CORPORATION; LAUREL INDUSTRIES HOLDINGS, INC.; NAUGATUCK TREATMENT COMPANY; UNIROYAL CHEMICAL COMPANY LIMITED (DELAWARE); MONOCHEM, INC.; RECREATIONAL WATER PRODUCTS, INC.; WEBER CITY ROAD LLC; WRL OF INDIANA, INC.; BIOLAB FRANCHISE COMPANY, LLC
Reel/Frame 026039/0142 →
AMENDED AND RESTATED INTELLECTUAL PROPERTY SECURITY AGREEMENT Recorded Feb 22, 2010
From: CHEMTURA CORPORATION; A & M CLEANING PRODUCTS, LLC; AQUA CLEAR INDUSTRIES, LLC; ASCK, INC.; ASEPSIS, INC.; BIOLAB COMPANY STORE, LLC; BIOLAB FRANCHISE COMPANY, LLC; BIOLAB TEXTILE ADDITIVES, LLC; BIO-LAB, INC.; CNK CHEMICAL REALTY CORPORATION; CROMPTON COLORS INCORPORATED; CROMPTON HOLDING CORPORATION; CROMPTON MONOCHEM, INC.; GLCC LAUREL, LLC; GREAT LAKES CHEMICAL CORPORATION; GREAT LAKES CHEMICAL GLOBAL, INC.; GT SEED TREATMENT, INC.; HOMECARE LABS, INC.; ISCI, INC.; KEM MANUFACTURING CORPORATION; LAUREL INDUSTRIES HOLDINGS, INC.; MONOCHEM, INC.; NAUGATUCK TREATMENT COMPANY; RECREATIONAL WATER PRODUCTS, INC.; UNIROYAL CHEMICAL COMPANY LIMITED (DELAWARE); WEBER CITY ROAD LLC; WRL OF INDIANA, INC.
To: CITIBANK, N.A.
Reel/Frame 023998/0001 →
SECURITY AGREEMENT Recorded May 12, 2009
From: CHEMTURA CORPORATION; A & M CLEANING PRODUCTS, LLC; AQUA CLEAR INDUSTRIES, LLC; ASCK, INC.; ASEPSIS, INC.; BIOLAB TEXTILE ADDITIVES, LLC; BIO-LAB, INC.; CNK CHEMICAL REALTY CORPORATION; CROMPTON HOLDING CORPORATION; CROMPTON COLORS INCORPORATED; CROMPTON MONOCHEM, INC.; GREAT LAKES CHEMICAL CORPORATION; GREAT LAKES CHEMICAL GLOBAL, INC.; GT SEED TREATMENT, INC.; HOMECARE LABS, INC.; ISCI, INC.; KEM MANUFACTURING CORPORATION; LAUREL INDUSTRIES HOLDINGS, INC.; MONOCHEM, INC.; NAUGATUCK TREATMENT COMPANY; RECREATIONAL WATER PRODUCTS, INC.; UNIROYAL CHEMICAL COMPANY LIMITED (DELAWARE); WEBER CITY ROAD LLC; WRL OF INDIANA, INC.; BIOLAB COMPANY STORE, LLC; BIOLAB FRANCHISE COMPANY, LLC; GLCC LAUREL, LLC
To: CITIBANK, N.A.
Reel/Frame 022668/0658 →
RELEASE OF LIEN IN PATENTS Recorded Jul 13, 2005
From: DEUTSCHE BANK AG, NEW YORK BRANCH
To: CROMPTON CORPORATION
Reel/Frame 016513/0745 →
SECURITY AGREEMENT Recorded Nov 10, 2004
From: CROMPTON CORPORATION
To: DEUTSCHE BANK AG NEW YORK BRANCH
Reel/Frame 015370/0467 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 13, 2004
From: FOX, E. BRIAN; LAMBERT, TIMOTHY
To: CROMPTON CORPORATION
Reel/Frame 014982/0939 →