CONTROLLING DEGRADATION RATES OF DIVERTING AGENTS
A treatment to temporarily block highly permeable areas in a wellbore having a temperature of less than 160° F. A diverting agent, a catalyzer, and a viscosifier are mixed together and pumped in the wellbore where the treatment flows in the most highly permeable areas. The diverting agent then begins to block those areas as the well is treated finally causing the fluid to divert to other now more highly permeable areas of the wellbore. After less than 48 the diverting agent degrades sufficiently to restore the permeablility of the wellbore.
1 . A fluid system for treating a well comprising:
a diverting agent,
wherein the diverting agent is a solid urea derivative,
further wherein the diverting agent is present in an amount from about 0.625 percent by weight of the fluid system to about 1.25 percent by weight of the fluid system,
a viscosifier, and
a catalyzing agent.
2 . The system of claim 1 wherein, the fluid system has a downhole temperature of 160° F. or less.
3 . The system of claim 1 wherein, the fluid system has a downhole temperature of 140° F. or less.
4 . The system of claim 1 wherein, the viscosifier is a guar gum.
5 . The system of claim 1 wherein, the viscosifier is a guar derivative.
6 . The system of claim 1 wherein, the viscosifier is a carboxymethylcellulose.
7 . The system of claim 1 wherein, the viscosifier is a cellulose derivative.
8 . The system of claim 1 wherein, the viscosifier is a polyacrylamide polymer.
9 . The system of claim 1 wherein, the viscosifier is a polyacrylamide copolymer.
10 . The system of claim 1 wherein, the diverting agent is a solid isobutylene urea.
11 . The system of claim 1 wherein, the diverting agent is a solid formaldehyde urea.
12 . The system of claim 1 wherein, the catalyzing agent is an organic acid.
13 . The system of claim 12 wherein, the organic acid is citric acid.
14 . The system of claim 12 wherein, the organic acid is acetic acid.
15 . The system of claim 12 wherein, the organic acid is formic acid.
16 . The system of claim 12 wherein, the organic acid is between from about 5% to about 50% by weight of the diverting agent.
17 . The system of claim 12 wherein, the organic acid is between from about 10% to about 30% by weight of the diverting agent.
18 . The system of claim 1 wherein, the catalyzing agent is an inorganic acid.
19 . The system of claim 1 wherein, the diverting agent is between 0.5 and 5.0 pounds per gallon of the fluid system.
20 . The system of claim 1 wherein the diverting agent in solid form has a size particle distribution between 0.04 mm and 4.00 mm.
21 . A method for treating a well comprising:
preparing a fluid by mixing a viscosifier and a diverting agent,
wherein the diverting agent is present in an amount from about 0.625 percent by weight of the fluid system to about 1.25 percent by weight of the fluid system,
adding a catalyzing agent to the fluid,
pumping the fluid into a well,
creating a blockage in a highly permeable area in a wellbore, and
removing the blockage.
22 . The method of claim 21 wherein, the catalyzing agent is added immediately prior to pumping the fluid into the well.
23 . The method of claim 21 wherein, the blockage is removed in less than 24 hours.
24 . The method of claim 21 wherein, the blockage is removed in less than 6 hours.
25 . The method of claim 21 wherein, the fluid has a downhole temperature of less than 160° F.
26 . The method of claim 21 wherein, the fluid has a downhole temperature of less than 140° F.
27 . The method of claim 21 wherein, the viscosifier is a guar gum.
28 . The method of claim 21 wherein, the viscosifier is a guar derivative.
29 . The method of claim 21 wherein, the viscosifier is a carboxymethylcellulose.
30 . The method of claim 21 wherein, the viscosifier is a cellulose derivative.
31 . The method of claim 21 wherein, the viscosifier is a polyacrylamide polymer.
32 . The method of claim 21 wherein, the viscosifier is a polyacrylamide copolymer.
33 . The method of claim 21 wherein, the diverting agent is solid isobutylene urea.
34 . The method of claim 21 wherein, the diverting agent is solid formaldehyde urea.
35 . The method of claim 21 wherein, the catalyzing agent is an organic acid.
36 . The method of claim 35 wherein, the organic acid is citric acid.
37 . The method of claim 35 wherein, the organic acid is acetic acid.
38 . The method of claim 35 wherein, the organic acid is formic acid.
39 . The method of claim 21 wherein, the organic acid is between from about 5% to about 50% by weight of the diverting agent.
40 . The method of claim 21 wherein, the organic acid is between from about 10% to about 30% by weight of the diverting agent.
41 . The method of claim 21 wherein, the catalyzing agent is an inorganic acid.
42 . The method of claim 21 wherein, the diverting agent is between 0.5 and 5.0 pounds per gallon of the fluid.
43 . The method of claim 21 wherein, the diverting agent has a size particle distribution between 0.04 mm and 4.00 mm.
44 . The system of claim 1 wherein, the diverting agent is present in an amount of about 1.0 percent by weight of the fluid system.
45 . The system of claim 21 wherein, the diverting agent is present in an amount of about 1.0 percent by weight of the fluid system.