Polysaccharides, methods for preparing such polysaccharides and fluids utilizing such polysaccharides

• US 4,579,942 A
• Filed: 09/26/1984
• Issued: 04/01/1986
• Est. Priority Date: 09/26/1984
• Status: Expired due to Term

• Current Assignee: Union Carbide Corporation (Dow, Inc.)
• Original Assignee: Union Carbide Corporation (Dow, Inc.)
• Inventors: Brode, George L., Partain, Emmett M. III, Stanley, James P.
• Primary Examiner(s): GRIFFIN, RONALD
• Application Number:
  US06/654,595
• Time in Patent Office: 552 Days
• Field of Search: 536/84, 536/90, 536/91, 106/170
• US Class Current: 536/84
• CPC Class Codes: C08B 11/20 Post-etherification treatments of chemical or physical type, e.g. mixed etherification in two steps, including purification
• CPC Class Codes: C08B 15/005 Crosslinking of cellulose derivatives
• CPC Class Codes: C09K 8/685 containing cross-linking agents
• CPC Class Codes: C09K 8/887 containing cross-linking agents
• CPC Class Codes: C09K 8/90 of natural origin, e.g. polysaccharides, cellulose

Abstract

Water-soluble polysaccharides, including cellulose ethers, containing pendent vicinal dihydroxy structure capable of cis geometry, which upon crosslinking with a polyvalent metal, have shear-thermal stability characteristics of at least about 30 at 250° F., are useful in oilfield applications.

Claims

1. A water-soluble cellulose ether containing pendent vic dihydroxy structure having or capable of assuming a cis geometry and having a shear-thermal stability characteristic of at least about 30 at 250°

F. for a 0.6 percent by weight aqueous solution of said cellulose ether crosslinked by a polyvalent metal ion.

2. The water-soluble cellulose ether of claim 1 wherein said cellulose ether has said shear-thermal stability characteristic of at least about 60.

3. The water-soluble cellulose ether of claim 2 wherein said cellulose ether has said shear-thermal stability characteristic of at least about 90.

4. The water-soluble cellulose ether of claim 1 wherein said pendent vic dihydroxy structure is present in an amount to provide a degree of substitution of from about 0.3 to about 1.3.

5. The water-soluble cellulose ether of claim 4 wherein the degree of substitution is in the range of from about 0.5 to about 1.2.

6. The water-soluble cellulose ether of claim 1 wherein said pendent vic dihydroxy structure comprises the residue of glycidol.

7. The water-soluble cellulose ether of claim 1 wherein said cellulose ether is a hydroxyethyl cellulose, a hydroxypropylhydroxyethyl cellulose, a carboxymethyl cellulose or a hydroxypropyl cellulose.

8. The water-soluble cellulose ether of claim 7 wherein said cellulose ether is hydroxyethyl cellulose.

9. The water-soluble hydroxyethyl cellulose of claim 8 wherein said cellulose ether has, as a 1 percent by weight solution in water, a Brookfield viscosity at 20°

C. of at least about 1,200 centipoise.

10. The water-soluble hydroxyethyl cellulose of claim 9 wherein the Brookfield viscosity is at least about 1800.

11. The water-soluble hydroxyethyl cellulose of claim 9 wherein the Brookfield viscosity is at least about 2500.

12. A process for preparing a water-soluble cellulose ether containing pendent vic dihydroxy structure having or capable of assuming a cis geometry which comprises:

(a) charging a cellulose ether starting material to a diluent system including water in an amount sufficient to swell the cellulose ether starting material to provide a slurry in an enclosed reaction vessel,

(b) stirring the slurry while sparging the reaction vessel with an inert gas to remove entrained air,

(c) adding an alkaline material in an amount sufficient to catalyze the reaction of the cellulose ether with a reactant capable of incorporating into said cellulose ether a pendent vic dihydroxy structure,

(d) adding said reactant over a predetermined period of time in an amount sufficient to incorporate in the cellulose ether a predetermined degree of substitution of pendent vic dihydroxy structure,

(e) continuing stirring the slurry while allowing the reaction to be completed, the total reaction time being at least about 2 hours, the temperature being maintained throughout in the range of from about ambient conditions to reflux of the diluent system,

(f) adding acid in an amount sufficient to neutralize the resulting water-soluble cellulose ether product and

(g) recovering same, said cellulose ether having, upon cross-linking, a shear-thermal stability characteristic of at least about 30 at 250°

F. for a 0.6 percent by weight aqueous solution of said cellulose ether crosslinked by a polyvalent metal ion.

13. The process of claim 12 wherein said cellulose ether is hydroxyethyl cellulose.

14. The process of claim 13 wherein said hydroxyethyl cellulose starting material has, as a 1 percent by weight solution in water, a Brookfield viscosity at 20°

C. of at least about 2,500 centipoise.

15. The hydroxyethyl cellulose of claim 14 wherein said Brookfield viscosity is at least about 5,000 centipoise.

16. The process of claim 13 wherein said hydroxyethyl cellulose starting material is the purified product resulting from the etherification of a cellulosic source contained in the diluent system in which said product was prepared.

17. The process of claim 13 wherein the diluent is a member selected from the group consisting of acetone, isopropanol and t-butanol.

18. The process of claim 17 wherein the diluent is acetone.

19. The process of claim 18 wherein the water content of the diluent system is from about 5 to about 20 percent, based upon the total weight of acetone and water.

20. The process of claim 19 wherein the water content is in the range of about 7 to about 13 percent by weight.

21. The process of claim 13 wherein the weight ratio of the diluent to the hydroxyethyl cellulose starting material is in the range of from about 4:

1 to about 25;

1.

22. The process of claim 13 wherein the diluent to hydroxyethyl cellulose starting material weight ratio is in the range of from about 5:

1 to about 10;

1.

23. The process of claim 13 wherein said inert gas is nitrogen.

24. The process of claim 13 wherein said alkaline material is sodium hydroxide.

25. The process of claim 24 wherein the molar ratio of sodium hydroxide to said hydroxyethyl cellulose is in the range of from about 0.4:

1 to about 1;

1.

26. The process of claim 13 wherein said reactant is glycidol.

27. The process of claim 26 wherein said reactant is distilled glycidol.

28. The process of claim 26 wherein said reactant is crude glycidol.

29. The process of claim 13 wherein said reactant is 2,3-epoxy-1,4-butanediol.

30. The process of claim 13 wherein said reactant is added in an amount sufficient to provide a degree of substitution in the hydroxyethyl cellulose starting material in the range of from about 0.3 to about 1.3.

31. The process of claim 30 wherein said reactant is added in an amount sufficient to provide a degree of substitution in the range of from about 0.5 to about 1.2.

32. The process of claim 13 wherein said reactant is added over a period of at least one hour.

33. The process of claim 13 wherein the hydroxyethyl cellulose product recovered is washed to remove impurities and then dried.

34. A viscosified fluid comprising water, an effective viscosifying amount of a crosslinked water-soluble cellulose ether containing pendent vic dihydroxy structure having or capable of assuming a cis geometry, and a polyvalent metal cross-linker, said cellulose ether having a shear-thermal stability characteristic of at least about 30 at 250°

F. for a 0.6 percent by weight aqueous solution of said cellulose ether crosslinked by a polyvalent metal ion.

35. The viscosified fluid of claim 34 wherein said fluid includes a proppant.

36. The viscosified fluid of claim 34 wherein said fluid includes a gravel pack material.

37. The viscosified fluid of claim 34 wherein said fluid includes an acid.

38. The viscosified fluid of claim 34 wherein the shear-thermal stability characteristic of said cellulose ether is at least about 60.

39. The viscosified fluid of claim 38 wherein the shear-thermal stability characteristic of said cellulose ether is at least about 90.

40. The viscosified fluid of claim 34 wherein said pendent vic dihydroxy structure is present in an amount to provide a degree of substitution of from about 0.3 to about 1.3.

41. The viscosified fluid of claim 40 wherein the degree of substitution is in the range of from about 0.5 to about 1.2.

42. The viscosified fluid of claim 34 wherein said pendent vic dihydroxy structure comprises the residue of glycidol.

43. The viscosified fluid of claim 34 which includes a buffer to maintain the pH in the range of from about 6 to about 9.

44. The viscosified fluid of claim 34 wherein said cellulose ether is a hydroxyethyl cellulose, a hydroxypropylhydroxyethyl cellulose, a carboxymethyl cellulose or a hydroxypropyl cellulose.

45. The viscosified fluid of claim 44 wherein said cellulose ether is hydroxyethyl cellulose.

46. The viscosified fluid of claim 45 wherein said water-soluble hydroxyethyl cellulose has, as a 1 percent by weight solution in water, a Brookfield viscosity at 20°

C. of at least about 1,200 centipoise.

47. The viscosified fluid of claim 46 wherein said Brookfield viscosity is at least about 1800.

48. The viscosified fluid of claim 46 wherein said Brookfield viscosity is at least about 2500.