IP Library Granted Patent US 7,261,879
Granted Patent B2
US 7,261,879 · App. 10/238,758 · Granted Aug 28, 2007

Iodinated anion exchange resin and process for preparing same

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Quick Facts
Patent No.
US 7,261,879
App. No.
10/238,758
Granted
Aug 28, 2007
Kind
B2
Abstract

The present invention relates to iodinated resins. It relates in particular to a process for preparing a polyiodide-resin wherein an anion exchange resin is contacted with a material capable of donating a member absorbable by the resin so as to convert the resin to the polyiodide-resin. The absorbable member is selected from the group consisting of I 2 and polyiodide ion having a valence of −1. In the process, conversion of the anion exchange resin to the polyiodide-resin is effected at elevated temperature and/or elevated pressure, the elevated temperature being about 100° C. or higher, the elevated pressure being greater than atmospheric pressure. The present invention also relates to a substance comprising an iodine (impregnated) resin as produced by the above process.

Claims (116)

1. A process for preparing an iodinated resin,

said iodinated resin being an iodinated anion exchange resin, said iodinated anion exchange resin is in a form selected from the group consisting of chloride Cl − and hydroxyl OH − ,

said process comprising a conversion step, said conversion step comprising contacting an anion exchange resin with a sufficient amount of an iodine-substance absorbable by said anion exchange resin such that said anion exchange resin absorbs said iodine-substance so as to convert said anion exchange resin to said iodinated resin, said iodine-substance being selected from the group consisting of I 2 and polyiodide ions having a valence of −1,

wherein for said conversion step at least a portion of the absorption of iodine-substance is effected at elevated temperature and at elevated pressure, said elevated temperature being a temperature higher than about 100° C. and up to about 210° C., said elevated pressure being a pressure greater than atmospheric pressure and up to about 100 psig.

2. A process as defined in claim 1 wherein said elevated pressure is a pressure of about 2 psig and up to about 100 psig.

3. A process as defined in claim 1 wherein said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

4. A process as defined in claim 1 wherein said elevated pressure is a pressure of up to about 100 psig.

5. A process as defined in claim 1 wherein said elevated pressure is a pressure of from about 5 to about 35 psig.

6. A process as defined in claim 1 wherein said elevated pressure is a pressure of from about 5 to about 20 psig.

7. A process as defined in claim 1 wherein said elevated temperature is a temperature of about 102° C. and up to about 210° C.

8. A process as defined in claim 1 wherein said elevated temperature is a temperature of about 115° C. and up to about 210° C.

9. A process as defined in claim 1 wherein said elevated temperature is a temperature of up to about 150° C.

10. A process as defined in claim 1 wherein said elevated temperature is a temperature of about 115° C. to about 135° C.

11. A process as defined in claim 1 wherein said elevated temperature is a temperature of about 102° C. and up to about 210° C. and said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

12. A process as defined in claim 1 wherein said elevated temperature is a temperature of about 110° C. and up to about 210° C. and said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

13. A process as defined in claim 1 wherein said elevated temperature is a temperature of about 115° C. and up to about 210° C. and said elevated pressure is a pressure of from about 5 to about 35 psig.

14. A process as defined in claim 1 wherein said iodine-substance comprises triiodide ions of formula I 3 − .

15. A process as defined in claim 1 wherein said anion exchange resin is an anion exchange resin having a primary, secondary or tertiary aromatic or aliphatic amino group.

16. A process as defined in claim 1 wherein said anion exchange resin is contacted with a composition comprising a mixture of KI, I 2 and a minor amount of water, and a mole ratio of KI to I 2 initially being about 1.

17. A process as defined in claim 15 wherein said anion exchange resin is in a hydroxyl form OH − , wherein said anion exchange resin is contacted with a composition comprising a mixture of KI, I 2 and a minor amount of water, and a mole ratio of KI to I 2 initially being about 1, wherein said elevated temperature is a temperature of about 102° C. and up to about 210° C. and wherein said elevated pressure is a pressure of about 2 psig and up to about 100 psig.

18. A process for preparing an iodinated resin,

said iodinated resin being an iodinated anion exchange resin, said iodinated anion exchange resin is in a form selected from the grow consisting of chloride Cl − and hydroxyl OH − ,

said process comprising a conversion step, said conversion step comprising contacting an anion exchange resin with a sufficient amount of an iodine-substance absorbable by said anion exchange resin such that said anion exchange resin absorbs said iodine-substance so as to convert said anion exchange resin to said iodinated resin, said iodine-substance being selected from the group consisting of I 2 and polyiodide ions having a valence of −1,

wherein said conversion step comprises an initial conversion stage followed by a second conversion stage, said initial conversion stage comprising contacting said anion exchange resin with said iodine-substance at a temperature of about 100° C. or lower so as to obtain an intermediate composition, said intermediate composition comprising residual absorbable iodine-substance and an intermediate iodinated resin, said second conversion stage comprising subjecting said intermediate composition to elevated temperature and elevated pressure, said elevated temperature being a temperature higher than about 100° C. and up to about 210° C., said elevated pressure being a pressure greater than atmospheric pressure and up to about 100 psig.

19. A process as defined in claim 18 wherein said elevated pressure is a pressure of about 2 psig and up to about 100 psig.

20. A process as defined in claim 18 wherein said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

21. A process as defined in claim 18 wherein said elevated pressure is a pressure of up to about 100 psig.

22. A process as defined in claim 18 wherein said elevated pressure is a pressure of from about 5 to about 35 psig.

23. A process as defined in claim 18 wherein said elevated pressure is a pressure of from about 5 to about 20 psig.

24. A process as defined in claim 18 wherein said elevated temperature is a temperature of about 102° C. and up to about 210° C.

25. A process as defined in claim 18 wherein said elevated temperature is a temperature of about 115° C. and up to about 210° C.

26. A process as defined in claim 18 wherein said elevated temperature is a temperature of up to about 150° C.

27. A process as defined in claim 18 wherein said elevated temperature is a temperature of about 115° C. to about 135° C.

28. A process as defined in claim 18 wherein said elevated temperature is a temperature of about 102° C. and up to about 210° C. and said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

29. A process as defined in claim 18 wherein said elevated temperature is a temperature of about 110° C. and up to about 21 00C. and said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

30. A process as defined in claim 18 wherein said elevated temperature is a temperature of about 115° C. and up to about 210° C. and said elevated pressure is a pressure of from about 5 to about 35 psig.

31. A process as defined in claim 18 wherein said iodine-substance comprises triiodide ions of formula I 3 − .

32. A process as defined in claim 18 wherein said anion exchange resin is an anion exchange resin having a primary, secondary or tertiary aromatic or aliphatic amino group.

33. A process as defined in claim 18 wherein said anion exchange resin is contacted with a composition comprising a mixture of KI, I 2 and a minor amount of water, and a mole ratio of KI to I 2 initially being about 1.

34. A process as defined in claim 18 wherein said anion exchange resin is in a hydroxyl form OH − , wherein said anion exchange resin is contacted with a composition comprising a mixture of KI, I 2 and a minor amount of water, and a mole ratio of KI to I 2 initially being about 1, wherein said elevated temperature is a temperature of about 102° C. and up to about 210° C. and wherein said elevated pressure is a pressure of about 2 psig and up to about 100 psig.

35. A process as defined in claim 18 wherein said initial conversion stage comprises contacting said anion exchange resin with said iodine-substance at a pressure of from about 0 to less than about 2 psig.

36. A process as defined in claim 18 wherein said initial conversion stage comprises contacting said anion exchange resin with said iodine-substance at a temperature of from about 20° C. to about 40° C. and at essentially ambient pressure ranging from a pressure of about 0 psig to less than about 1 psig.

37. A process as defined in claim 18 wherein said initial conversion stage is affected for a time period of about 1 minute or more.

38. A process as defined in claim 18 wherein said initial conversion stage is affected for a time period of from about 1 minute to about 24 hours.

39. A process for preparing an iodinated resin,

said iodinated resin being an iodinated weak base anion exchange resin, said iodinated anion exchange resin is in a form selected from the group consisting of chloride Cl − and hydroxyl OH − ,

said process comprising a conversion step, said conversion step comprising contacting a weak base anion exchange resin with a sufficient amount of an iodine-substance absorbable by said anion exchange resin such that said anion exchange resin absorbs said iodine-substance so as to convert said weak base anion exchange resin to said iodinated weak base anion exchange resin, said iodine-substance being selected from the group consisting of I 2 and polyiodide ions having a valence of −1,

wherein for said conversion step at least a portion of the absorption of iodine-substance is effected at elevated temperature and at elevated pressure, said elevated temperature being a temperature higher than about 100° C. and up to about 210° C., said elevated pressure being a pressure greater than atmospheric pressure and up to about 100 psig.

40. A process as defined in claim 39 wherein said elevated pressure is a pressure of about 2 psig and up to about 100 psig.

41. A process as defined in claim 39 wherein said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

42. A process as defined in claim 39 wherein said elevated pressure is a pressure of up to about 100 psig.

43. A process as defined in claim 39 wherein said elevated pressure is a pressure of from about 5 to about 35 psig.

44. A process as defined in claim 39 wherein said elevated pressure is a pressure of from about 5 to about 20 psig.

45. A process as defined in claim 39 wherein said elevated temperature is a temperature of about 102° C. and up to about 210° C.

46. A process as defined in claim 39 wherein said elevated temperature is a temperature of about 115° C. and up to about 210° C.

47. A process as defined in claim 39 wherein said elevated temperature is a temperature of up to about 150° C.

48. A process as defined in claim 39 wherein said elevated temperature is a temperature of about 115° C. to about 135° C.

49. A process as defined in claim 39 wherein said elevated temperature is a temperature of about 102° C. and up to about 210° C. and said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

50. A process as defined in claim 39 wherein said elevated temperature is a temperature of about 110° C. and up to about 210° C. and said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

51. A process as defined in claim 39 wherein said elevated temperature is a temperature of about 115° C. and up to about 210° C. and said elevated pressure is a pressure of from about 5 to about 35 psig.

52. A process as defined in claim 39 wherein said iodine-substance comprises triiodide ions of formula I 3 − .

53. A process as defined in claim 39 wherein said weak base anion exchange resin is an anion exchange resin having a primary, secondary or tertiary aromatic or aliphatic amino group.

54. A process as defined in claim 39 wherein said weak base anion exchange resin is contacted with a composition comprising a mixture of KI, I 2 and a minor amount of water, and a mole ratio of KI to I 2 initially being about 1.

55. A process as defined in claim 39 wherein said weak base anion exchange resin is in a hydroxyl form OH − , wherein said weak base anion exchange resin is contacted with a composition comprising a mixture of KI, I 2 and a minor amount of water, and a mole ratio of KI to I 2 initially being about 1, wherein said elevated temperature is a temperature of about 102° C. and up to about 210° C. and wherein said elevated pressure is a pressure of about 2 psig and up to about 100 psig.

56. A process for preparing an iodinated resin,

said iodinated resin being an iodinated weak base anion exchange resin, said iodinated anion exchange resin is in a form selected from the group consisting of chloride Cl − and hydroxyl OH − ,

said process comprising a conversion step, said conversion step comprising contacting a weak base anion exchange resin with a sufficient amount of an iodine-substance absorbable by said anion exchange resin such that said weak base anion exchange resin absorbs said iodine-substance so as to convert said weak base anion exchange resin to said iodinated weak base anion exchange resin, said iodine-substance being selected from the group consisting I 2 and polyiodide ions having a valence of −1,

wherein said conversion step comprises an initial conversion stage followed by a second conversion stage, said initial conversion stage comprising contacting said weak base anion exchange resin with said iodine-substance at a temperature of about 100° C. or lower so as to obtain an intermediate composition, said intermediate composition comprising residual absorbable iodine-substance and an intermediate iodinated resin, said second conversion stage comprising subjecting said intermediate composition to elevated temperature and elevated pressure, said elevated temperature being a temperature higher than about 100° C. and up to about 210° C., said elevated pressure being a pressure greater than atmospheric pressure and up to about 100 psig.

57. A process as defined in claim 56 wherein said elevated pressure is a pressure of about 2 psig and up to about 100 psig.

58. A process as defined in claim 56 wherein said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

59. A process as defined in claim 56 wherein said elevated pressure is a pressure of up to about 100 psig.

60. A process as defined in claim 56 wherein said elevated pressure is a pressure of from about 5 to about 35 psig.

61. A process as defined in claim 56 wherein said elevated pressure is a pressure of from about 5 to about 20 psig.

62. A process as defined in claim 56 wherein said elevated temperature is a temperature of about 102° C. and up to about 210° C.

63. A process as defined in claim 56 wherein said elevated temperature is a temperature of about 115° C. and up to about 210° C.

64. A process as defined in claim 56 wherein said elevated temperature is a temperature of up to about 150° C.

65. A process as defined in claim 56 wherein said elevated temperature is a temperature of about 115° C. to about 135° C.

66. A process as defined in claim 56 wherein said elevated temperature is a temperature of about 102° C. and up to about 210° C. and said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

67. A process as defined in claim 56 wherein said elevated temperature is a temperature of about 110° C. and up to about 210° C. and said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

68. A process as defined in claim 56 wherein said elevated temperature is a temperature of about 115° C. and up to about 210° C. and said elevated pressure is a pressure of from about 5 to about 35 psig.

69. A process as defined in claim 56 wherein said iodine-substance comprises triiodide ions of formula I 3 − .

70. A process as defined in claim 56 wherein said weak base anion exchange resin is an anion exchange resin having a primary, secondary or tertiary aromatic or aliphatic amino group.

71. A process as defined in claim 56 wherein said weak base anion exchange resin is contacted with a composition comprising a mixture of KI, I 2 and a minor amount of water, and a mole ratio of KI to I 2 initially being about 1.

72. A process as defined in claim 56 wherein said weak base anion exchange resin is in a hydroxyl form OH − , wherein said weak base anion exchange resin is contacted with a composition comprising a mixture of KI, I 2 and a minor amount of water, and a mole ratio of KI to I 2 initially being about 1, wherein said elevated temperature is a temperature of about 102° C. and up to about 210° C. and wherein said elevated pressure is a pressure of about 2 psig and up to about 100 psig.

73. A process as defined in claim 56 wherein said initial conversion stage comprises contacting said weak base anion exchange resin with said iodine-substance at a pressure of from about 0 to less than about 2 psig.

74. A process as defined in claim 56 wherein said initial conversion stage comprises contacting said weak base anion exchange resin with said iodine-substance at a temperature of from about 20° C. to about 40° C. and at essentially ambient pressure ranging from a pressure of about 0 psig to less than about 1 psig.

75. A process as defined in claim 56 wherein said initial conversion stage is affected for a time period of about 1 minute or more.

76. A process as defined in claim 56 wherein said initial conversion stage is affected for a time period of from about 1 minute to about 24 hours.

77. A process for preparing an iodinated resin,

said iodinated resin being an iodinated anion exchange resin, said iodinated anion exchange resin is in a form selected from the group consisting of chloride Cl − and hydroxyl OH − ,

said process comprising a conversion step, said conversion step comprising contacting an anion exchange resin with a sufficient amount of an iodine-substance absorbable by said anion exchange resin such that said anion exchange resin absorbs said iodine-substance so as to convert said anion exchange resin to said iodinated resin, said iodine-substance being selected from the group consisting of I 2 and polyiodide ions having a valence of −1,

wherein for said conversion step at least a portion of the absorption of iodine-substance is effected at elevated pressure, said elevated pressure being a pressure greater than 2 psig and up to about 100 psig.

78. A process as defined in claim 77 wherein said iodine-substance comprises diatomic iodine I 2 .

79. A process as defined in claim 77 wherein said iodine-substance comprises triiodide ions of formula I 3 − .

80. A process as defined in claim 77 wherein said conversion step is carried out in a closed, air-tight container.

81. A process as defined in claim 80 wherein said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

82. A process as defined in claim 80 wherein said elevated pressure is a pressure of up to about 100 psig.

83. A process as defined in claim 80 wherein said elevated pressure is a pressure of from about 5 to about 35 psig.

84. A process as defined in claim 80 wherein said elevated pressure is a pressure of from about 5 to about 20 psig.

85. A process as defined in claim 80 wherein said anion exchange resin is an anion exchange resin having a primary, secondary or tertiary aromatic or aliphatic amino group.

86. A process as defined in claim 80 wherein said anion exchange resin is contacted with a composition comprising a mixture of KI, I 2 and a minor amount of water, and a mole ratio of KI to I 2 initially being about 1.

87. A process as defined in claim 80 wherein said anion exchange resin is in a hydroxyl form OH − , wherein said anion exchange resin is contacted with a composition comprising a mixture of KI, I 2 and a minor amount of water, and a mole ratio of KI to I 2 initially being about 1, wherein said elevated pressure is a pressure of about 2 psig and up to about 100 psig.

88. A process for preparing an iodinated resin,

said iodinated resin being an iodinated anion exchange resin, said iodinated anion exchange resin is in a form selected from the group consisting of chloride Cl − and hydroxyl OH − ,

said process comprising a conversion step, said conversion step comprising contacting an anion exchange resin with a sufficient amount of an iodine-substance absorbable by said anion exchange resin such that said anion exchange resin absorbs said iodine-substance so as to convert said anion exchange resin to said iodinated resin, said iodine-substance being selected from the group consisting of I 2 and polyiodide ions having a valence of −1,

wherein said conversion step comprises an initial conversion stage followed by a second conversion stage, said initial conversion stage comprising contacting said anion exchange resin with said iodine-substance at a temperature of about 100° C. or lower so as to obtain an intermediate composition, said intermediate composition comprising residual absorbable iodine-substance and an intermediate iodinated resin, said second conversion stage comprising subjecting said intermediate composition to elevated pressure, said elevated pressure being a pressure greater than 2 psig and up to about 100 psig.

89. A process as defined in claim 88 wherein said iodine-substance comprises diatomic iodine I 2 .

90. A process as defined in claim 88 wherein said iodine-substance comprises triiodide ions of formula I 3 − .

91. A process as defined in claim 88 wherein said conversion step is carried out in a closed, air-tight container.

92. A process as defined in claim 91 wherein said elevated pressure is a pressure of about 5 psig and up to about 100 psig.

93. A process as defined in claim 91 wherein said elevated pressure is a pressure of up to about 100 psig.

94. A process as defined in claim 91 wherein said elevated pressure is a pressure of from about 5 to about 35 psig.

95. A process as defined in claim 91 wherein said elevated pressure is a pressure of from about 5 to about 20 psig.

96. A process as defined in claim 91 wherein said anion exchange resin is an anion exchange resin having a primary, secondary or tertiary aromatic or aliphatic amino group.

97. A process as defined in claim 91 wherein said anion exchange resin is contacted with a composition comprising a mixture of KI, I 2 and a minor amount of water, and a mole ratio of KI to I 2 initially being about 1.

98. A process as defined in claim 91 wherein said anion exchange resin is in a hydroxyl form OH − , wherein said anion exchange resin is contacted with a composition comprising a mixture of KI, I 2 and a minor amount of water, and a mole ratio of KI to I 2 initially being about 1, wherein said elevated pressure is a pressure of about 2 psig and up to about 100 psig.

Assignments (16)
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNOR'S EXECUTION DATE ON ORIGINAL COVER SHEET AND NOTICE OF RECORDATION PREVIOUSLY RECORDED ON REEL 026390 FRAME 0371. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Jun 6, 2011
From: TRIOSYN CORP.
To: SAFELIFE/TRIOSYN CORP.
Reel/Frame 026397/0226 →
CHANGE OF NAME Recorded Jun 3, 2011
From: TRIOSYN CORP.
To: SAFELIFE/TRIOSYN CORP.
Reel/Frame 026390/0371 →
CORRECTIVE ASSIGNMENT TO CORRECT THE ASSIGNEE'S NAME ON ORIGINAL COVER SHEET AND ORIGINAL ASSIGNMENT DOCUMENT PREVIOUSLY RECORDED ON REEL 013281 FRAME 0566. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Jun 2, 2011
From: MESSIER, PIERRE JEAN
To: TRIOSYN CORP.
Reel/Frame 026380/0558 →
RELEASE OF SECURITY INTEREST Recorded May 31, 2011
From: SOFNOV SOCIETE FINANCIERE D'INNOVATION INC.; BUSINESS DEVELOPMENT BANK OF CANADA; SOCIETE INNOVATECH DU GRAND MONTREAL; MACLEOD, RAY; BERGERON, GILES; SL VENTURES; BRB SPORTS UNLIMITED; MARTIN, JACQUES; DONLAN, DAVID A.; O'BRIEN, JOSEPH W.; O'BRIEN, SHIRLEY; HARNELL, WILLIAM; HARNELL, TERESA; CAPOSELLA, CARMINE; JAGOE, HARVEY
To: TRIOSYN CORP.
Reel/Frame 026362/0496 →
RELEASE Recorded Dec 16, 2010
From: SILICON VALLEY BANK
To: TRIOSYN HOLDING INC.
Reel/Frame 025641/0732 →
RELEASE Recorded Dec 16, 2010
From: SILICON VALLEY BANK
To: TRIOSYN CORP.
Reel/Frame 025641/0727 →
CORRECTIVE ASSIGNMENT TO CORRECT THE IDENTIFICATION OF ASSIGNEE AND ASSIGNOR PREVIOUSLY RECORDED ON REEL 023749 FRAME 0127. ASSIGNOR(S) HEREBY CONFIRMS THE RELEASE OF SECURITY INTEREST. Recorded Jan 13, 2010
From: VANTAGEPOINT CDP ASSOCIATES, L.P.; VANTAGEPOINT CDP ASSOCIATES, L.L.C.
To: TRIOSYN CORP.; SAFE LIFE CORP.
Reel/Frame 023793/0389 →
RELEASE OF SECUITY INTEREST Recorded Jan 7, 2010
From: TRIOSYN CORP.; SAFE LIFE CORP.
To: VANTAGEPOINT CDP ASSOCIATES, L.P.; VANTAGEPOINT CDP ASSOCIATES, L.L.C.
Reel/Frame 023749/0127 →
SECURITY AGREEMENT Recorded Jun 19, 2009
From: TRIOSYN HOLDING INC.
To: SILICON VALLEY BANK
Reel/Frame 022846/0719 →
NOTICE OF GRANT OF SECURITY INTEREST Recorded Apr 8, 2009
From: TRIOSYN CORP.; SAFE LIFE CORP.
To: VANTAGEPOINT CDP ASSOCIATES, L.P.; VANTAGEPOINT CDP ASSOCIATES, L.L.C.
Reel/Frame 022521/0423 →
SECURITY AGREEMENT Recorded Jan 8, 2009
From: TRIOSYN CORP.
To: SILICON VALLEY BANK
Reel/Frame 022078/0275 →
RELEASE OF SECURITY INTEREST AND COLLATERAL Recorded Jun 27, 2007
From: VANTAGEPOINT CDP PARTNERS, L.P.
To: TRIOSYN HOLDING INC.
Reel/Frame 019511/0619 →
RELEASE OF SECURITY INTEREST AND COLLATERAL Recorded Jun 27, 2007
From: VANTAGEPOINTE CDP PARTNER, L.P.
To: TRIOSYN CORP.; HEMO-BIOTECH INC., TRIOSYN HOLDING INC., TRIOSYN RESEARCH INC.
Reel/Frame 019511/0644 →
NOTICE OF GRANT OF SECURITY INTEREST Recorded Jun 15, 2006
From: TRIOSYN CORP.; HENO-BIOTECH INC.; TRIOSYN HOLDING INC.; TRIOSYN RESEARCH INC. (F/K/A HYDRO-BIO TECH INC.)
To: VANTAGEPOINT CDP PARTNERS, L.P.
Reel/Frame 017783/0587 →
NOTICE OF GRANT OF SECURITY INTEREST Recorded Jun 15, 2006
From: TRIOSYN HOLDING INC.
To: VANTAGE POINT CDP PARTNERS, L.P.
Reel/Frame 017783/0778 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 10, 2002
From: MESSIER, PIERRE JEAN
To: TRIOSYN HOLDING INC.
Reel/Frame 013281/0566 →