U.S. patent application number 11/364009 was filed with the patent office on 2006-07-06 for fracturing fluids containing borate esters as crosslinking agents.
This patent application is currently assigned to B.J. Services Company Canada. Invention is credited to D.V. Satyanarayana Gupta, Anita Colleen Jerat, Nicole Deanne Litt, Ron Pierce.
Application Number | 20060148659 11/364009 |
Document ID | / |
Family ID | 29734680 |
Filed Date | 2006-07-06 |
United States Patent
Application |
20060148659 |
Kind Code |
A1 |
Gupta; D.V. Satyanarayana ;
et al. |
July 6, 2006 |
Fracturing fluids containing borate esters as crosslinking
agents
Abstract
A formation treating fluid comprises one or more borate esters,
a liquid carrier and, one or more cross linkable polymer wherein
the formation treating fluid has an alkaline pH when the formation
treating fluid is positioned in a formation. The formation treating
fluid is useful in high temperature operations such as hydraulic
fracturing.
Inventors: |
Gupta; D.V. Satyanarayana;
(Tomball, TX) ; Pierce; Ron; (Calgary, CA)
; Litt; Nicole Deanne; (Edmonton, CA) ; Jerat;
Anita Colleen; (Calgary, CA) |
Correspondence
Address: |
BERESKIN AND PARR
40 KING STREET WEST
BOX 401
TORONTO
ON
M5H 3Y2
CA
|
Assignee: |
B.J. Services Company
Canada
Calgary
CA
|
Family ID: |
29734680 |
Appl. No.: |
11/364009 |
Filed: |
March 1, 2006 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
10178410 |
Jun 25, 2002 |
7007757 |
|
|
11364009 |
Mar 1, 2006 |
|
|
|
Current U.S.
Class: |
507/260 ;
507/273 |
Current CPC
Class: |
C09K 8/685 20130101 |
Class at
Publication: |
507/260 ;
507/273 |
International
Class: |
E21B 43/00 20060101
E21B043/00 |
Claims
1. A formation treating fluid including a cross linkable polymer
and comprises, prior to the cross linkable polymer being cross
linked: a) a borate ester comprising a triester or a cyclic ester;
b) an organic solvent for the borate ester; c) a liquid carrier;
and, d) the cross linkable polymer wherein the formation treating
fluid has an alkaline pH when the formation treating fluid is
positioned in a formation.
2. The formation treating fluid as claimed in claim 1 further
comprising a proppant.
3. The formation treating fluid as claimed in claim 1 further
comprising a pH adjustment agent to raise the pH of the formation
treating fluid to about 8 or higher.
4. The formation treating fluid as claimed in claim 3 wherein the
pH is sufficiently low to prevent significant hydrolysis of the
cross linkable polymer.
5. The formation treating fluid as claimed in claim 4 wherein the
pH adjustment agent is an alkali or alkaline salt.
6. The formation treating fluid as claimed in claim 5 wherein the
alkali or alkaline salt is one or more of an hydroxide, a
carbonate, a bicarbonate and a silicate.
7. The formation treating fluid as claimed in claim 1 wherein the
formation treating fluid has a pH from about 8 to about 13.
8. The formation treating fluid as claimed in claim 1 wherein the
formation treating fluid has a pH from about 9.5 to about 11.5.
9. The formation treating fluid as claimed in claim 1 wherein the
organic solvent is a cyclic organic compound.
10. The formation treating fluid as claimed in claim 1 wherein the
borate ester comprises from about 0.001 to about 1 vol. % of the
formation treating fluid.
11. The formation treating fluid as claimed in claim 1 wherein the
borate ester comprises from about 0.005 to about 0.5 vol. % of the
formation treating fluid.
12. The formation treating fluid as claimed in claim 1 wherein the
borate ester comprises from about 0.01 to about 0.1 vol. % of the
formation treating fluid.
13. The formation treating fluid as claimed in claim 1 wherein the
liquid carrier comprises water, methanol or a mixture thereof.
14. A formation treating fluid including a cross linkable polymer
and comprises at the point of addition: a) a borate ester in a
cyclic organic solvent; b) a liquid carrier; and, c) the cross
linkable polymer wherein the formation treating fluid has an
alkaline pH when the formation treating fluid is positioned in a
formation.
15. The formation treating fluid as claimed in claim 14 further
comprising a proppant.
16. The formation treating fluid as claimed in claim 14 further
comprising a pH adjustment agent to raise the pH of the formation
treating fluid to about 8 or higher.
17. The formation treating fluid as claimed in claim 16 wherein the
pH is sufficiently low to prevent significant hydrolysis of the
cross linkable polymer.
18. The formation treating fluid as claimed in claim 17 wherein the
pH adjustment agent is an alkali or alkaline salt.
19. The formation treating fluid as claimed in claim 18 wherein the
alkali or alkaline salt is one or more of an hydroxide, a
carbonate, a bicarbonate and a silicate.
20. The formation treating fluid as claimed in claim 14 wherein the
formation treating fluid has a pH from about 8 to about 13.
21. The formation treating fluid as claimed in claim 14 wherein the
formation treating fluid has a pH from about 9.5 to about 11.5.
22. The formation treating fluid as claimed in claim 14 wherein the
borate ester is one or more of a triester and a cyclic ester.
23. The formation treating fluid as claimed in claim 14 wherein the
borate ester comprises from about 0.001 to about 1 vol. % of the
formation treating fluid.
24. The formation treating fluid as claimed in claim 14 wherein the
borate ester comprises from about 0.005 to about 0.5 vol. % of the
formation treating fluid.
25. The formation treating fluid as claimed in claim 14 wherein the
borate ester comprises from about 0.01 to about 0.1 vol. % of the
formation treating fluid.
26. The formation treating fluid as claimed in claim 14 wherein the
liquid carrier comprises water, methanol or a mixture thereof.
Description
[0001] This application is a division of U.S. patent application
Ser. No. 10/178,410 filed on Jun. 25, 2002, which is allowed and is
to issue as U.S. Pat. No. 7,007,757
FIELD OF THE INVENTION
[0002] This invention relates to fluids that may be utilized in
fracturing a formation. The fluid may be used in gravel packing,
hydraulic fracturing and fracpacking operations.
BACKGROUND OF THE INVENTION
[0003] Fracturing fluids typically require good shear stability and
low pumping pressures. Shear stability is required to ensure that
the viscosity is maintained while the fluid is loaded into the
borehole. Low pumping pressures are required to ensure that the
fluid may be economically pumped into a borehole. If the viscosity
for fracturing fluid is too high, then difficulties will be
encountered in pumping the fracturing fluid into a borehole. These
include premature pump failure due to excessive pumping pressures,
increased shear on the fracturing fluid and difficulty in ensuring
that all of a borehole is filled with the fracturing fluid.
[0004] Due to its reactivity, borate ions have been utilized in
fracturing fluids. For example, as disclosed in U.S. Pat. No.
4,619,776 [Mondshine], organic polyhydroxy compounds having
hydroxyl groups positioned in the cis-form on adjacent carbon atoms
or on carbon atoms in a 1,3-relationship react with borates to form
5 or 6 member ring complexes. Accordingly, borate ions, when
combined with polymers having the requisite hydroxyl groups in a
cis-relationship, are useful thickeners for preparing fracturing
fluids. Borate cross-linked systems are useful in fracturing
fluids. At a pH of above 8, borate ions will complex with many
compounds such as polysaccharides, guar and locust bean gum as well
as polyvinyl alcohol to provide an effective thickening agent.
[0005] The temperature at the bottom of a borehole can vary. In
deeper boreholes, the temperature at the bottom of the borehole can
be upwards of 150.degree. C. (300.degree. F.). If such a borehole
requires fracturing, then the fracturing fluid preferably has a
stable viscosity at those temperatures. If the viscosity decreases
too much, then the effectiveness of the fluid for retaining a good
dispersion of proppant during the loading of the borehole, and the
subsequent fracturing operation, will be detrimentally affected.
Accordingly, it is preferred that fracturing fluids which are used
under high temperature conditions require thermal stability, in
addition to the other requirements of a fracturing fluid including
shear stability and low pumping pressures.
[0006] Typically, the source of borate ions has been boric acid,
borax or inorganic borates. The use of boric acid as a source of
borate ions has two disadvantages under high temperature
operations. If the sole cross linking agent is borate ions obtained
from boric acid, then the viscosity of the fluid starts to degrade
as soon as elevated temperatures are reached (e.g. 100.degree. F.
and higher) resulting in a system which is very sensitive to any
breaker addition.
[0007] In order to overcome this problem, different approaches have
been developed. For example, Mondshine teaches the use of a
sparingly soluble borate. U.S. Pat. No. 5,165,479 [Harris et al],
discloses a fracturing fluid with delayed cross linking action
wherein the fluid includes a cross linking agent comprising a
source of borate ions and a delayed cross linker comprising a
source of Ti [+4] or Zr [+4] ions. The delayed cross-linking
provides a means by which the viscosity may be further enhanced at
elevated temperatures. U.S. Pat. No. 5,217,632 [Sharif] discloses a
process for preparing boron zirconium chelate solutions that are
stable and useful as a fracturing fluid for treating underground
oil and gas bearing strata.
[0008] In order to address the thermal instability of borate
complexed thickener systems at higher temperatures, these patents
teach the use of additives [which increase the complexity of the
thickener system] or utilize a form of borate ions which are
obtained from alkaline earth metal borates, alkali metal alkaline
earth metal borates and mixtures thereof which are sparingly
soluble and thus complicate the preparation of the fracturing
fluid.
SUMMARY OF THE INVENTION
[0009] It has surprisingly been determined that the use of borate
esters are beneficial in the production of formation treating
fluids (e.g. fracturing fluids) and, preferably, high temperature
formation treating fluids. Borate esters will increase the
viscosity of a fracturing fluid upon addition (i.e. the initial or
start up viscosity). However, several minutes are required from the
addition of a borate ester to result in the solution achieving its
final or ultimate viscosity. The initial viscosity is sufficiently
high to provide good proppant transport characteristics to the
fluid yet sufficiently low to permit the fluid to be pumped into a
borehole. Further, the final viscosity is stable at elevated
temperatures (up to 130.degree. C./265.degree. F. or more) once the
fluid is in the borehole and has achieved its final viscosity.
[0010] These fracturing fluids are particularly advantageous in
high temperature applications. In particular, as the temperature of
the fracturing fluid increases, e.g. over 40-60.degree. C.
(100-140.degree. F.), the rate of cross-linking increases thus
significantly accelerating the rate of viscosity increase. Further,
once the maximum temperature of the fracturing fluid is reached in
a borehole, the viscosity is stable.
[0011] In accordance with one embodiment of the instant invention,
there is provided formation treating fluid comprising: [0012] (a) a
borate ester; [0013] (b) a liquid carrier; and, [0014] (c) a cross
linkable polymer wherein the formation treating fluid has an
alkaline pH when the formation treating fluid is positioned in a
formation.
[0015] In one embodiment, the formation treating fluid further
comprises a proppant (e.g. sand).
[0016] In another embodiment, the formation treating fluid further
comprises a pH adjustment agent to raise the pH of the formation
treating fluid to about 8 or higher. Preferably, the pH is
sufficiently low to prevent significant hydrolysis of the cross
linkable polymer. Preferably, the pH adjustment agent is an alkali
or alkaline salt. The alkali or alkaline salt is preferably an
hydroxide, a carbonate, a bicarbonate a silicate and mixtures
thereof.
[0017] In another embodiment, the formation treating fluid has a pH
from about 8 to about 13.
[0018] In another embodiment, the formation treating fluid has a pH
from about 9.5 to about 11.5.
[0019] In another embodiment, the borate ester is one or more of a
triester and a cyclic ester.
[0020] In another embodiment, the borate ester comprises from about
0.001 to about 1 vol. % of the formation treating fluid, preferably
from about 0.005 to about 0.5 vol. % of the formation treating
fluid and more preferably from about 0.01 to about 0.1 vol. % of
the formation treating fluid.
[0021] In another embodiment, the liquid carrier comprises water,
methanol or a mixture thereof.
[0022] In accordance with the instant invention, there is also
provided a method of fracturing a formation comprising: [0023] (a)
providing an alkaline formation treating fluid comprising a borate
ester, a liquid carrier and, a cross linkable polymer; and, [0024]
(b) pumping the formation treating fluid into the formation.
[0025] In one embodiment, the method further comprises adding a pH
adjusting agent to increase the pH of the formation treating fluid
to about 8 or higher prior to pumping the formation treating fluid
into the formation.
[0026] In another embodiment the method further comprises selecting
the liquid carrier from the group consisting of water, methanol and
mixtures thereof.
[0027] In another embodiment, the method further comprises
selecting one or more of a triester and a cyclic ester as the
borate ester.
[0028] In another embodiment, the method further comprises
adjusting the pH of the formation treating fluid to be sufficiently
low to prevent significant hydrolysis of the cross linkable
polymer.
[0029] In another embodiment, the method further comprises
adjusting the pH of the formation treating fluid to be less than
about 13, and preferably from about 9.5 to about 11.5.
[0030] In accordance with the instant invention, there is also
provided the use of a borate ester in a formation treating fluid as
a cross linking agent for a cross linkable polymer.
DETAILED DESCRIPTION OF THE INVENTION
[0031] In accordance with the instant invention, a formation
treating fluid comprises at least one borate ester, a liquid
carrier and a cross linkable polymer. The liquid carrier is a fluid
that forms the base of the fracturing fluid and provides the medium
for the borate ester and the cross linkable polymer to react to
form a cross linked polymer. The cross linked polymer thickens the
liquid carrier so that the liquid carrier may transport a proppant
to the formation to be treated.
[0032] As used herein, the term "formation treating fluid" refers
to a fluid which is used in pressure treating a formation such as
gravel packing, hydraulic fracturing and fracpacking operations.
Hydraulic fracturing operations may be conducted by pumping a fluid
into a borehole in the formation and subjecting the fluid (and
therefore the formation) to elevated pressures. The following
description is provided in conjunction with the use of the fluid as
a fracturing fluid. However, it will be appreciated that the fluid
may be used in any formation treating operation known in the art
that requires a thickened fluid.
[0033] The liquid carrier may be any liquid that can be thickened
by a borate cross linked polymer. In generally, the liquid carrier
may be any liquid in which the polymer, once added to the liquid,
may be hydrated. The liquid carrier is preferably an aqueous based
solution or an alcohol. The aqueous based solution is preferably
water. The alcohol is preferably methanol. Typically, the preferred
liquid carrier is water. However, in some applications, such as gas
wells, the formation to be fractured may be undersaturated. In
order to prevent swelling of the formation, a non-hydrating
fracturing fluid is utilized. In such applications, an alcohol, may
be used as the liquid carrier. If an alcohol is used as the liquid
carrier, then an agent such as fumaric acid may be added to aid in
the hydration of the polymer.
[0034] The cross linkable polymer may be any polymer that may be
cross linked by reaction of the polymer with borate ions. In
general, any polymer which is soluble in the liquid carrier so as
to produce a stable gel may be utilized. If the liquid carrier is
water, then the cross linkable polymer is preferably guar or a guar
derivative (such as hydroxypropyl guar, carboxymethylhydroxypropyl
guar), or a cellulose derivative (such as carboxymethylhydroxyethyl
methyl cellulose), a polyvinyl alcohol or mixtures thereof.
Preferably, the polymer is one or more of guar or guar derivatives.
If the liquid carrier is methanol, then the cross linkable polymer
may be one or more of guar derivatives and cellulose derivatives.
Preferably, the polymer is a guar derivative. More preferably, the
polymer a hydroxypropyl guar derivative.
[0035] The cross linkable polymer may be added at a rate to provide
the desired viscosity in the thickened fracturing fluid. The cross
linkable polymer may be added at a rate of about 1 to about 10 (8
to 80) preferably from about 2 to about 8 (16 to 65) and, most
preferably, from about 2.5 to about 6 (20 to 50) Kg m.sup.3
(lbs/1,000 gallons) of the fracturing fluid.
[0036] In accordance with the instant invention, the borate ester
acts as a cross linking agent in the fracturing fluid. Any source
of borate ester may be utilized. For example, the borate ester may
be formed in situ. Preferably, the borate ester is preformed (e.g.
it may be purchased from a third party supplier and added preformed
to the liquid carrier). Without being limited by theory, the borate
ester produces borate ions when introduced to the liquid carrier.
For example, if the liquid carrier is water, then the borate ester
hydrolyzes. The borate ions, which are so liberated, combine with
hydroxy and/or carboxyl groups in the polymer, such as by hydrogen
bonding, so as to cross link the polymer. One or more borate esters
may be utilized in a fracturing fluid in accordance to the instant
invention. The borate ester may be one or more of a triester (such
as trimethyl borate, triisopropyl borate, triethyl borate) and a
cyclic ester (such as trimethoxy boroxin).
[0037] An advantage of the use of triesters and cyclic esters is
that the cross linking efficiency of these esters is greater as
compared to boric acid. Thus, improved proppant support will be
provided due to the increased density of cross linking which is
available. Alternately, to obtain the same degree of cross linking
(and therefore the same degree of viscosity) a reduced amount of
borate ester may be utilized on a molar basis.
[0038] Preferably, the fracturing fluid comprises from about 0.001
to about 1, more preferably from about 0.005 to about 0.5 and, most
preferably from about 0.01 to about 0.1 vol. % of borate ester,
based upon the total volume of the fracturing fluid without any
proppant.
[0039] The pH of the fracturing fluid is basic. If the pH of the
fracturing fluid is too high, then the cross linkable polymer will
tend to hydrolize. This reduces the molecular weight of the polymer
and, accordingly, the fracturing fluid will have a reduced
viscosity. Preferably, the pH is maintained below the level at
which significant hydrolysis of the cross linkable polymer occurs.
The upper limit of the pH range will vary depending upon several
factors including the degree to which hydrolysis of the cross
linkable polymer is tolerable in the fracturing fluid and the
actual cross linkable polymer, which is utilized. Preferably, the
pH is maintained at about 13 or less, more preferably at about 12
or less and, most preferably at about 11.5 or less.
[0040] If the pH of the fracturing fluid is too low, then a stable
viscosity will not be obtained. Without being limited by theory, it
is understood that if the pH is too low, then the borate ion will
not form the requisite hydrogen bond with the cross linkable
polymer so as to cross link the polymer. At a pH of about 8 or
higher, preferably about 8.5 or higher, the requisite cross linked
complex is formed. The lower pH limit is preferably about 9.5 or
higher. Accordingly, an acceptable pH range may be obtained by
combining any of the upper and lower pH levels set out previously.
Preferably, the pH is from about 8 to about 13, more preferably
from about 8.5 to about 12 and most preferably from about 8.5 to
about 11.5.
[0041] In order for the formation treating fluid to have the
requisite alkaline viscosity, a pH adjustment agent may be
required. However, this may not be necessary. For example, if the
water is highly alkaline, or if the borate ester is provided in an
alkaline solution, then, upon combining the liquid carrier, the
polymer and the borate ester, a fluid having a sufficiently
alkaline pH may be obtained. If the pH is outside the requisite
range, then a pH adjustment agent may be added. The pH adjustment
agent may be any of those known in the art. For example, the pH
adjustment agent may be an alkali or alkaline salt such as any
hydroxide (such as sodium, potassium, magnesium and/or ammonium
hydroxide), any carbonate or bicarbonate (such as sodium, potassium
and/or ammonium carbonate or bicarbonate) and silicates (such as
sodium and/or potassium silicates). Preferably, the pH adjustment
agent is salt an alkali or alkaline and, more preferably, the pH
adjustment agent is an hydroxide, a carbonate, a bicarbonate and/or
a silicate. The amount that is added will vary depending on the pH
of the fluid without the pH adjustment agent and the desired pH
range. A plurality of salts may be provided so as to act as a
buffer in the fluid.
[0042] The fracturing fluid may include any other additive known in
the art. In particular, the fracturing fluid may include a proppant
(preferably sand). In addition, the fracturing fluid may include
such typical additives as biocides, surfactants breakers and salts
or cationic materials used to prevent formation damage.
[0043] Subsequent to a fracturing operation, the viscosity of the
fracturing fluid may be reduced and the fracturing fluid recovered
from a borehole by any means known in the art. In particular,
oxidizers and enzymes as well as a pH lowering agent (to reduce the
pH of the solution to less than about 8) may be used as
breakers.
[0044] An advantage of the instant invention is that the liquid
carrier, the polymer and the borate ester may be combined in any
order and the pH adjusted to greater than about 8.0 at any time
during the combination of the constituent elements. Accordingly,
the fluid is well suited for being manufactured on a continuous
basis as it is pumped into a borehole. For example, the liquid
carrier may be provided (such as in a storage tank). The liquid
carrier may be combined with the cross linkable polymer in the
storage tank. For example, if the cross linkable polymer is guar,
the guar may be added to an aqueous liquid carrier so as to hydrate
the guar prior to the preparation of the fracturing fluid.
Alternately, a hydrated guar may be added as the liquid carrier is
pumped towards a borehole. As the liquid carrier is pumped towards
the borehole, the borate ester (the polymer if not previously
added) and the optional proppant and other standard industry
additives may be added. Preferably, the borate ester is added
upstream of the proppant so that the viscosity of the liquid
carrier has increased by the time the proppant is introduced into
the fracturing fluid. The completed fracturing fluid is then
introduced into the borehole.
[0045] Preferably, the borate ester is added to the fracturing
fluid shortly before or as the fracturing fluid is pumped into a
borehole so that the viscosity increase is limited at the time the
fluid enters the formation.
[0046] The following are non-limiting examples showing a preferred
embodiment of the instant invention. It will be appreciated by one
skilled in the art that various additions and modifications may be
made to the formation treating fluid disclosed herein and each is
within the scope of this invention.
EXAMPLE 1
[0047] A gel was prepared with 4.5 kg/m.sup.3 (40 lbs/1,000
gallons) loading of guar (WG-15.TM. which is available from BJ
Services Company Canada) in fresh water. (GW-4.TM., which is a guar
that is available from BJ Services Company, U.S.A., could also be
used). After hydration of the guar, the pH was adjusted to the
range of 11.7-11.8 with caustic or a suitable buffer such as Buffer
16X.TM. (which is a silicate buffer and is available from BJ
Services Company Canada). (Buffer-6L.TM., which is a silicate
buffer that is available from BJ Services Company, U.S.A., could
also be used). 250 ml of the hydrated gel was then placed in a
Waring.TM. blender and the speed of the blender increased until a
vortex was formed from the top of the blender blade nut. A gel
stabilizer (GS-1 .mu.m which is an anti-oxidant and is available
from BJ Services Company Canada and B.J. Services Company, U.S.A.)
was added at a loading rate of 1.5 kg/m.sup.3 (12.5 lbs/1,000
gallons). An amount of a cross linking formulation was then added
to the vortex. The time taken for the vortex to close (the "cross
link time") was noted. The cross linkers that were added were
trimethoxy boroxin (TMBX) in xylene, trimethyl borate (TMB) in
hexane and boric acid. The results are set out in Table 1.
TABLE-US-00001 Loading L/m.sup.3 Boron Content Crosslinker
(gallons/1,000 Crosslinker Kg/m.sup.3 (lbs/ Formulation gallons)
Time (sec.) 1,000 gallons) 10% TMBX in xylene 1 110 0.09 (0.75) 10%
TMBX in xylene 2 65 0.18 (1.5) 10% TMBX in xylene 3 50 0.27 (2.25)
10% TMBX in xylene 4 46 0.36 (3.0) Loading L/m.sup.3 Boron Content
Crosslinker (gallons/1,000 Crosslinker Kg/m.sup.3 (lbs/ Formulation
gallons) Time (sec.) 1,000 gallons) 10% TMB in Hexane 2 171 0.14
(1.17) 10% TMB in Hexane 3 100 0.21 (1.75) 10% TMB in Hexane 4 80
0.28 (2.33) 10% TMB in Hexane 5 62 0.35 (3.0) Loading Boron Content
Crosslinker Kg/m.sup.3 (lbs/ Crosslinker Kg/m.sup.3 (lbs/
Formulation 1,000 gallons) Time (sec.) 1,000 gallons) Boric Acid in
Gel 0.15 (1.25) Instantaneous 0.15 (1.25) Boric Acid in Gel 0.2
(1.67) Instantaneous 0.20 (1.67) Boric Acid in Gel 0.25 (2)
Instantaneous 0.25 (2) Boric Acid in Gel 0.3 (2.5) Instantaneous
0.30 (2.5)
[0048] As set out in the above table, the addition of boric acid as
a cross linker resulted in instantaneous closing of the vortex
demonstrating that the viscosity of the fluid increased
instantaneously. However, the use of borate esters required about 1
to about 3 minutes to increase the viscosity sufficiently to close
the vortex. Thus, the addition of borate esters provided a slow
increase in the viscosity of the fluid. Borate esters provide
sufficient viscosity shortly upon addition to provide proppant
transport yet have a viscosity which is sufficiently low to
facilitate being pumping into a borehole.
EXAMPLE 2
[0049] Various cross linked gels were prepared as in Example 1. The
cross linked gels were then loaded into the pressurized Fann.TM. 50
rheometer, which was preheated to a selected temperature
(80.degree. C. (176.degree. F.), 100.degree. C. (212.degree. F.)
and 130.degree. C. (266.degree. F.)). The gels were then sheared at
100 sec-1 and the viscosity monitored. The initial time (0 minutes)
was when the fluid was first loaded into the rheometer after vortex
closure in the blender. The results are set out in Tables 2.1, 2.2
and 2.3. TABLE-US-00002 TABLE 2.1 Viscosity, cP Viscosity, cP
Viscosity, cP @ 100 sec.sup.-1 @ 100 sec.sup.-1 @ 100 sec.sup.-1
10% TMBX in 10% TMB in Boric Acid xylene @ 2 Hexane @ 0.2
kg/m.sup.3 Temperature L/m.sup.3 (2 gal/ @ 3 L/m.sup.3 (1.7 lbs/
Time (.degree. C./(.degree. F.)) 1,000 gal) (3 gal/1,000 gal) 1,000
gal) (min.) of Fluid 180 100 1120 0 22 (72) 310 200 1060 1 29 (84)
840 640 1000 2 40 (104) 540 480 920 3 53 (127) 1100 1040 860 4 62
(144) 1020 990 840 5 72 (162) 990 980 810 10 80 (176) 970 970 780
15 80 (176) 960 970 770 20 80 (176) 960 970 760 30 80 (176) 960 970
760 40 80 (176) 960 970 760 50 80 (176) 960 970 760 60 80 (176) 960
970 750 120 80 (176)
[0050] TABLE-US-00003 TABLE 2.2 Viscosity @ Viscosity @ Viscosity @
100 sec.sup.-1 100 sec.sup.-1 100 sec.sup.-1 10% TMBX in 10% TMB in
Boric Acid xylene @ 2.5 Hexane @ @ 0.25 kg/m.sup.3 Temperature
L/m.sup.3 (2.5 gal/ 4.0 L/m.sup.3 (4 (2 lbs/ Time (.degree.
C./(.degree. F.)) 1,000 gal) gal/1,000 gal) 1,000 gal) (min.) of
Fluid 220 160 1160 0 22 (72) 380 240 1080 1 30 (86) 880 710 940 2
43 (109) 570 520 860 3 57 (135) 1040 940 810 4 68 (155) 1000 900
740 5 79 (174) 940 880 460 10 94 (201) 900 870 370 15 100 (212) 880
860 320 20 100 (212) 880 860 300 30 100 (212) 880 860 290 40 100
(212) 880 860 280 50 100 (212) 880 860 270 60 100 (212) 880 860 200
120 100 (212)
[0051] TABLE-US-00004 TABLE 2.3 Viscosity @ Viscosity @ Viscosity @
100 sec.sup.-1 100 sec.sup.-1 100 sec.sup.-1 10% TMBX in 10% TMB in
Boric Acid xylene @ 3.0 Hexane @ @ 0.3 kg/m.sup.3 Temperature
L/m.sup.3 (3.0 gal/ 5.0 L/m.sup.3 (5.0 gal/ (2.5 lbs/ Time
(.degree. C./(.degree. F.)) 1,000 gal) 1,000 gal) 1,000 gal) (min.)
of Fluid 260 200 1160 0 22 (72) 410 310 1080 1 31 (88) 880 760 940
2 46 (115) 600 560 860 3 62 (144) 910 880 810 4 74 (165) 720 700
740 5 88 (190) 540 520 460 10 121 (250) 520 500 370 15 130 (266)
500 490 320 20 130 (266) 500 480 290 30 130 (266) 500 480 260 40
130 (266) 500 480 240 50 130 (266) 500 480 210 60 130 (266) 500 480
40 120 130 (266)
[0052] As shown in Tables 2.1 to 2.3, even after vortex closure,
the viscosity of fluids made in accordance with the instant
invention is between 100-400 cP which is low enough to minimize
friction and high enough to provide proppant transport
characteristics. As the fluid heats up to over 40-60.degree. C.
(100-140.degree. F.), the viscosity increases due to cross linking.
Once the fluid reaches the maximum temperature, the viscosity is
stable.
[0053] In contrast, the Tables also demonstrate the results using
boric acid in a non-delayed system using conventional technology.
As set out in Tables 2.1-2.3, the initial viscosity was between
1100-1200 cP. Thus, the initial set up viscosity was substantially
higher and would require substantial additional horsepower to pump
the fluid into a borehole. Further, while the ultimate viscosity
was relatively stable at 80.degree. C. (176.degree. F.) (about 750
cP as shown in Table 2.1), the viscosity decreased at elevated
temperatures. For example, at 100.degree. C. (212.degree. F.), the
viscosity decreased to about 200 cP (Table 2.2) while at even
higher temperatures, 130.degree. C. (266.degree. F.), the viscosity
decreased below that level (Table 2.3). Accordingly, the
non-delayed boric acid based system commences degradation as soon
as an elevated temperature is reached.
EXAMPLE 3
[0054] This Example demonstrates a gel prepared utilizing methanol
as the liquid carrier. The cross linkable polymer was a methanol
soluble guar (hydroxypropyl guar), which is available from BJ
Services Company Canada and B.J. Services Company, U.S.A., under
the trade mark GM-55. The cross linkable polymer was added to
technical grade 100% methanol at various loading rates. 0.08
kg/m.sup.3 (0.67 lbs/1,000 gallons) of fumaric acid added to aid in
the hydration of the polymer in the non-aqueous alcohol. After
hydration of the polymer, a carbonate buffer (Buffer 15.TM.
available from BJ Services Company Canada) was added at various
loading rates and the cross linking agent was then added at various
loadings. (BF-9L.TM., which is a carbonate buffer that is available
from BJ Services Company, U.S.A., could also be used). The cross
linked gels were then loaded into a pressurized Brookfield.TM. HPHT
rheometer which was preheated to various preset temperatures and
sheared at 100 sec-1. The viscosity and temperature of the gel was
monitored. The results are set out in tables 3.1-3.8.
TABLE-US-00005 TABLE 3.1 The polymer was added at a rate of 5
Kg/m.sup.3 (42 lbs/1,000 gallons) and Buffer 15 was added at a rate
of 2.0 L/m.sup.3 (2 gallons/1,000 gallons). The cross linking agent
was triethyl borate which was provided in a solution comprising 10
vol. % triethyl borate in hexane. The cross linking agent was
loaded at a rate of 2.0 L/m.sup.3 (2 gallons/1,000 gallons). Time
(min) Temperature (.degree. C./(.degree. F.)) Viscosity, cP at 100
sec-1 0 22 (72) 56 5 41 (106) 191 10 47 (117) 246 15 50 (122) 263
30 50 (122) 260 60 60 (140) 247 75 60 (140) 251 90 65 (149) 225 105
70 (158) 222 120 70 (158) 300 135 70 (158) 500 150 70 (158) 462 165
70 (158) 351 180 70 (158) 365 210 80 (176) 332 240 85 (185) 276 270
90 (194) 233 300 95 (203) 167 330 100 (212) 133 360 120 (248)
55
[0055] TABLE-US-00006 TABLE 3.2 The polymer was added at a rate of
5 Kg/m.sup.3 (42 lbs/1,000 gallonsft.sup.3) and Buffer 15 was added
at a rate of 2.0 L/m.sup.3 (2 gallons/1,000 gallons). The cross
linking agent was triethyl borate which was provided in a solution
comprising 10 vol. % triethyl borate in hexane. The cross linking
agent was loaded at a rate of 3.0 L/m.sup.3 (3 gallons/1,000
gallons). Time (min) Temperature (.degree. C./(.degree. F.))
Viscosity, cP at 100 sec-1 0 22 (72) 81 5 41 (106) 245 10 47 (117)
292 15 50 (122) 293 30 50 (122) 293 60 50 (122) 276 75 50 (122) 252
90 55 (131) 222 105 60 (140) 224 120 70 (158) 230 135 70 (158) 270
150 70 (158) 286 165 75 (167) 275 180 80 (176) 257 210 80 (176) 240
240 90 (194) 169 270 90 (194) 156 300 100 (212) 71 330 110 (230) 31
360 110 (230) 15
[0056] TABLE-US-00007 TABLE 3.3 The polymer was added at a rate of
5 Kg/m.sup.3 (42 lbs/1,000 gallonsft.sup.3) and Buffer 15 was added
at a rate of 2.0 L/m.sup.3 (2 gallons/1,000 gallons). The cross
linking agent was triethyl borate which was provided in a solution
comprising 10 vol. % triethyl borate in hexane. The cross linking
agent was loaded at a rate of 4.0 L/m.sup.3 (4 gallons/1,000
gallons). Time (min) Temperature (.degree. C./(.degree. F.))
Viscosity, cP at 100 sec-1 0 22 (72) 374 5 41 (106) 353 10 47 (117)
316 15 50 (122) 304 30 50 (122) 285 60 60 (140) 392 75 60 (140) 447
90 65 (149) 396 105 70 (158) 330 120 75 (167) 270 135 80 (176) 225
150 80 (176) 180 165 80 (176) 165 180 90 (194) 116 210 90 (194) 63
240 90 (194) 52 270 100 (212) 25
[0057] TABLE-US-00008 TABLE 3.4 The polymer was added at a rate of
5 Kg/m.sup.3 (42 lbs/1,000 gallons) and Buffer 15 was added at a
rate of 2.0 L/m.sup.3 (2 gallons/1,000 gallons). The cross linking
agent was triethyl borate which was provided in a solution
comprising 10 vol. % triethyl borate in hexane. The cross linking
agent was loaded at a rate of 5.0 L/m.sup.3 (5 gallons/1,000
gallons). Time (min) Temperature (.degree. C./(.degree. F.))
Viscosity, cP at 100 sec-1 0 22 (72) 560 5 41 (106) 402 10 47 (117)
360 15 50 (122) 340 30 60 (140) 507 60 60 (140) 421 75 60 (140) 416
90 65 (149) 323 105 70 (158) 287 120 70 (158) 251 135 75 (167) 228
150 80 (176) 205 165 80 (176) 145 180 80 (176) 124 210 90 (194) 90
240 90 (194) 65 270 95 (203) 56 300 100 (212) 32
[0058] TABLE-US-00009 TABLE 3.5 The polymer was added at a rate of
6 Kg/m.sup.3 (50 lbs/1,000 gallonsft.sup.3) and Buffer 15 was added
at a rate of 3.0 L/m.sup.3 (3 gallons/1,000 gallons). The cross
linking agent was triethyl borate which was provided in a solution
comprising 10 vol. % triethyl borate in hexane. The cross linking
agent was loaded at a rate of 2.0 L/m.sup.3 (2 gallons/1,000
gallons). Time (min) Temperature (.degree. C./(.degree. F.))
Viscosity, cP at 100 sec-1 0 22 (72) -- 5 41 (106) 82 10 47 (117)
123 15 50 (122) 151 30 50 (122) 207 60 60 (140) 240 75 60 (140) 260
90 60 (140) 260 105 70 (158) 282 120 70 (158) 291 135 80 (176) 280
150 80 (176) 291 165 85 (185) 330 180 90 (194) 388 210 95 (203) 402
240 100 (212) 350 270 110 (230) 185 300 120 (248). 90
[0059] TABLE-US-00010 TABLE 3.6 The polymer was added at a rate of
6 Kg/m.sup.3 (50 lbs/1,000 gallons) and Buffer 15 was added at a
rate of 3.0 L/m.sup.3 (3 gallons/1,000 gallons). The cross linking
agent was triethyl borate which was provided in a solution
comprising 10 vol. % triethyl borate in hexane. The cross linking
agent was loaded at a rate of 3.0 L/m.sup.3 (3 gallons/1,000
gallons). Time (min) Temperature (.degree. C./(.degree. F.))
Viscosity, cP at 100 sec-1 0 22 (72) 50 5 41 (106) 94 10 47 (117)
203 15 50 (122) 271 30 50 (122) 337 60 60 (140) 331 75 60 (140) 337
90 70 (158) 275 105 70 (158) 275 120 80 (176) 272 135 80 (176) 361
150 80 (176) 433 165 80 (176) 458 180 85 (185) 415 210 90 (194) 385
240 90 (194) 360 270 100 (212) 251 300 105 (221) 165 330 110 (230)
124 360 120 (248) 34
[0060] TABLE-US-00011 TABLE 3.7 The polymer was added at a rate of
6 Kg/m.sup.3 (50 lbs/1,000 gallons) and Buffer 15 was added at a
rate of 3.0 L/m.sup.3 (3 gallons/1,000 gallons). The cross linking
agent was triethyl borate which was provided in a solution
comprising 10 vol. % triethyl borate in hexane. The cross linking
agent was loaded at a rate of 4.0 L/m.sup.3 (4 gallons/1,000
gallons). Time (min) Temperature (.degree. C./(.degree. F.))
Viscosity, cP at 100 sec-1 0 22 (72) 51 5 41 (106) 192 10 47 (117)
317 15 50 (122) 364 30 50 (122) 394 60 60 (140) 306 75 60 (140) 294
90 70 (158) 203 105 70 (158) 192 150 80 (176) 291 165 85 (185) 330
180 90 (194) 388 210 95 (203) 402 240 100 (212) 350 270 110 (230)
185 300 120 (248) 90
[0061] TABLE-US-00012 TABLE 3.8 The polymer was added at a rate of
5 Kg/m.sup.3 (42 lbs/1,000 gallons) and Buffer 15 was added at a
rate of 2.0 L/m.sup.3 (2 gallons/1,000 gallons). The cross linking
agent was triisopropyl borate which was provided in a solution
comprising 10 vol. % triisopropyl borate in hexane. The cross
linking agent was loaded at a rate of 2.0 L/m.sup.3 (2
gallons/1,000 gallons). Time (min) Temperature (.degree.
C./(.degree. F.)) Viscosity, cP at 100 sec-1 0 22 (72) 27 5 41
(106) 76 10 47 (117) 149 15 50 (122) 181 30 50 (122) 194 60 60
(140) 192 75 60 (140) 182 90 70 (158) 158 105 70 (158) 157 120 80
(176) 147 135 80 (176) 150 150 80 (176) 143 165 90 (194) 126 180 90
(194) 103 210 100 (212) 84 240 110 (230) 63 270 120 (248) 43
* * * * *