# Patent

## Title
Method of fracturing using mannanohydrolase enzyme breaker

## Abstract

A thermophilic mannanohydrolase enzyme may be used as an enzyme breaker for fracturing fluids containing hydratable polymers of guar and underivatized guar. The amino acid sequence of the mannanohydrolase is at least 90% homologous to the amino acid sequence of SEQ ID NO:2.

## Background
This application is a continuation-in-part application of U.S. patent application Ser. No. 12/579,771, filed Oct. 15, 2009, now U.S. Pat. No. 8,058,212, herein incorporated by reference.


FIELD OF THE INVENTION
An isolated mannanohydrolase enzyme which hydrolyzes galactomannan substrates at temperatures in excess of 160° F. has particular applicability as an enzyme breaker in fracturing fluids containing guar and derivatized guars.
BACKGROUND OF THE INVENTION
Hydraulic fracturing is used to create subterranean fractures that extend from the borehole into rock formation in order to increase the rate at which fluids can be produced by the formation. Generally, a high viscosity fracturing fluid is pumped into the well at sufficient pressure to fracture the subterranean formation. In order to maintain the increased exposure to the formation, a solid proppant is added to the fracturing fluid which is carried into the fracture by the high pressure applied to the fluid.
Greater than 65% of conventional fracturing fluids are made of guar gum (galactomannans) or guar gum derivatives such as hydroxypropyl guar (HPG), carboxymethyl guar (CMG) and carboxymethylhydroxypropyl guar (CMHPG). These polymers can be crosslinked in order to increase their viscosities and increase their capabilities of proppant transport.
Once the high viscosity fracturing fluid has carried the proppant into the formation, breakers are used to reduce the fluid's viscosity which allows the proppant to settle into the fracture and thereby increase the exposure of the formation to the well. Breakers work by reducing the molecular weight of the polymers, thus ‘breaking’ the polymer. The fracture then becomes a high permeability conduit for fluids and gas to be produced back to the well.
Chemical oxidizers and enzymes are most commonly used as breakers. The oxidizer produces a radical which then degrades the polymer. This reaction is limited by the fact that oxidizers are stoichiometric and they will attack not only the polymer but any molecule that is prone to oxidation. Enzymes, on the other hand, are catalytic and substrate specific and will catalyze the hydrolysis of specific bonds on the polymer. An enzyme will degrade many polymer bonds in the course of its lifetime. Unfortunately, enzymes operate under a narrow temperature range and their functional states are often inactivated at high temperatures.
Conventional enzymes used to degrade galactomannans work well at ambient to moderate temperatures (75° F. to 150° F.). At elevated temperatures, (>150° F.) these enzymes quickly denature and lose activity. The beta-mannanase enzyme used in conventional enzyme formulations has a temperature maximum of approximately 150° F. Activity profiles have indicated that the enzyme retains little to no activity past this point. Because many downhole fracturing operations are conducted at temperatures in excess of 150° F., it would be beneficial to have an enzyme that can degrade guar-based fracturing fluids under these elevated temperatures.
SUMMARY OF THE INVENTION
A mannanohydrolase enzyme effectively hydrolyzes galactomannins and has particular effectiveness in the hydrolysis of guar polymers at elevated temperature ranges. The high temperature mannanohydrolase enzyme may be associated with glutathione S-transferase (GST) or may be unassociated from GST.
The nucleotide sequence encoding the mannanohydrolase enzyme was derived from the β-mannanase gene of Caldocellum saccharolyticum and codon optimized for expression in E. coli. The gene coding for the mannanohydrolase (hereinafter “htβ”) has the nucleotide sequence set forth in FIG. 1A (SEQ ID NO:1) which is codon optimized to increase the expression of the mannanohydrolase in E. coli. The gene htβ (SEQ ID NO:1) may then be cloned into suitable plasmid vectors, such as pUC57, pUC 19, and pGS-21a, or into any other commercially available or custom expression or cloning vector. The mannanohydrolase can be transformed and expressed in commercially available Escherichia coli strains. The translated amino acid sequence of the mannanohydrolase is shown in FIG. 1B (SEQ ID NO:2).
An aqueous fracturing fluid may then be prepared which contains the enzyme, guar polymer and crosslinking agent.
When used in hydraulic fracturing, the mannanohydrolase is effective in degrading guar based polymers at temperatures in excess of 160° F.



BRIEF DESCRIPTION OF THE DRAWINGS
In order to more fully understand the drawings referred to in the detailed description of the present invention, a brief description of each drawing is presented, in which:
FIG. 1A (SEQ ID NO:1) represents the nucleotide sequence that codes for the mannanohydrolase used in the invention. FIG. 1B (SEQ ID NO:2) represents the amino acid sequence of the mannanohydrolase enzyme.
FIG. 2 represents creation of the plasmids pUC57-htβ, pGS-21a-gst-htβ and pGS-21-htβ harboring the mannanohydrolase gene.
FIG. 3 contrasts reduction in viscosity after 18 hours at 180° F. of a 25 ppt borate crosslinked guar suspension containing the mannanohydrolase enzyme versus a suspension not containing the mannanohydrolase enzyme.
FIG. 4 contrasts reduction in viscosity after 18 hours at 160° F. of a 25 ppt borate crosslinked guar suspension containing the mannanohydrolase enzyme versus a suspension not containing the mannanohydrolase enzyme.
FIG. 5 contrasts reduction in viscosity over 10 hours at 180° F. of a borate crosslinked guar suspension containing the mannanohydrolase enzyme versus a suspension not containing the mannanohydrolase enzyme.
FIG. 6 contrasts reduction in viscosity over 3.5 hours at 140° F. of a borate crosslinked guar suspension containing the mannanohydrolase enzyme versus a suspension not containing the mannanohydrolase enzyme.
FIG. 7 contrasts reduction in viscosity over varying temperatures of a guar suspension containing the mannanohydrolase enzyme.
FIG. 8A shows a photomicrograph of a proppant pack made in the absence of the mannanohydrolase enzyme.
FIG. 8B shows a proppant pack made in the presence of the mannanohydrolase enzyme.



DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
The high temperature enzyme used in the fracturing method of the invention is referred to herein as “mannanohydrolase” when it is unassociated with glutathione S-transferase (GST) and “GST-mannanohydrolase” when it is the fusion of β-mannanase and GST.
The mannanohydrolase enzyme described herein originates from the thermophilic and anaerobic Caldocellum saccharolyticum. Isolation of the gene encoding for the β-mannanase enzyme is described in E. Luthi et al, “Cloning, Sequence Analysis, and Expression in Escherichia coli of a Gene Coding for a β-Mannanase From the Extremely Thermophilic Bacterium ‘Caldocellum saccharolyticum’, Applied and Environmental Microbiology, March 1991, pp. 694-700, herein incorporated by reference.
The gene for the mannanohydrolase enzyme was then codon optimized to increase the efficiency of its expression in E. coli. The nucleotide sequence of the htβ gene is set forth in FIG. 1A (SEQ ID NO:1). This nucleotide sequence has a 74% homology to the sequence depicted in FIG. 2 of Luthi et al for the mannanase gene. The nucleotide sequence includes the coding sequence for the mannanohydrolase and the leader sequence on the N-terminus.
As illustrated in FIG. 2 (a), the htβ gene may be cloned into cloning vector pUC57 to create the plasmid pUC57-htβ. In (b) and (c), the gene may be cloned into expression vector pGS-21a which contains a coding region for GST protein. In (b), the resultant gene codes for a GST-mannanohydrolase fusion product. In (c), the resultant gene codes for an enzyme without the GST fusion tag. Expression using the pGS-21a-gst-htβ and pGS-21a-htβ plasmid of (b) and (c) respectively produces mannanohydrolase fused to the N-terminal GST protein and mannanohydrolase without the associated GST protein, respectively.
In each of FIGS. 2 (a), (b) and (c), Ampr regulates the expression of β-lactamase, rep(pMB1) and f1 ori represents the origin in pUC57 and pGS-21a, respectively, responsible for the replication of the plasmid, lacI codes for the lactose repressor, T7 represents the T7 RNA polymerase promoter and MCS represents the Multiple Cloning Site. The 5′ end of the optimized sequence contains a BamHI restriction endonuclease site and the 3′ end contains a HindIII restriction endonuclease site for cloning into the pGS-21a expression vector to create the GST-mannanohydrolase fusion protein. Alternatively, the 5′ BamH1 site was replaced with an NdeI restriction endonuclease site to create the mannanohydrolase protein without the associated GST fusion.
The plasmids pGS-21a-htβ, pGS-21a-gst-htβ and pUC57-htβ may be transformed into commercially available E. coli strains and cultured. The cells may then be harvested, lysed, and the resultant solution used as a cell lysate. A cell free extract can be produced by removing the cell debris from the lysate, and the enzyme can then be isolated from the extract. The term “isolated” denotes that the enzyme has been removed from intact cells or cellular debris and, in a condition other than its native environment, is free of other extraneous or unwanted nucleic acids, proteases, and lipids, in a form suitable for use as a breaker for fracturing fluids.
The gene coding for the mannanohydrolase enzyme may further have a nucleotide sequence which is substantially homologous to the nucleotide sequence of FIG. 1A (SEQ ID NO:1). The term “substantially homologous” is used herein to denote nucleotides having at least 75%, more preferably at least 80%, more preferably at least 85%, and even more preferably at least 90%, sequence identity to the sequence shown in FIG. 1A (SEQ ID NO:1).
The translated amino acid sequence of the mannanohydrolase is shown in FIG. 1B (SEQ ID NO:2). Typically, the translated amino acid sequence of the mannanohydrolase enzyme used in the hydraulic fracturing method described herein is at least 60% similar to the translated amino acid sequence set forth in FIG. 1B (SEQ ID NO:2).
In a preferred form, the isolated protein is substantially free of other proteins. It is preferred to provide the protein in a greater than 40% pure form, more preferably greater than 60% pure form. Even more preferably it is preferred to provide the protein in a highly purified form, i.e., greater than 80% pure, more preferably greater than 95% pure, and even more preferably greater than 99% pure, as determined by SDS-PAGE.
The mannanohydrolase effectively hydrolyzes the guar polymer at elevated temperature ranges, such as in excess of 72° F. typically over pH ranges between from about 5.0 to about 11.0. The mannanohydrolase may hydrolyze the guar polymer at temperatures in excess of 160° F. as well as in excess of 180° F. In fact, the mannanohydrolase may hydrolyze the guar polymer at temperatures in excess of 185° F. and even in excess of 195° F. In addition, the mannanohydrolase may be used in combination with other enzymes and/or oxidative breakers to degrade guar gels over broader temperature and pH ranges.
The aqueous fracturing fluid used in the invention may be prepared by blending a hydratable polymer into an aqueous fluid. The aqueous fluid could be, e.g., water, brine, or water-alcohol mixtures. Any suitable mixing apparatus may be used for this procedure. In the case of batch mixing, the hydratable polymer and aqueous fluid are blended for a period of time which is sufficient to form a hydrated sol. The hydratable polymer is added to the aqueous fluid in concentrations ranging from about 0.10% to 5.0% by weight of the aqueous fluid. The most preferred range for the present invention is about 0.20% to 0.80% by weight. The pH of the fracturing fluid may generally range from about 5.0 to about 11.0, typically about 6.0 or higher, more typically about 6.5 or higher. In one embodiment, the pH of the fracturing fluid may be about 7.0 or higher or about 7.5 or higher. In another embodiment, the pH of the fracturing fluid may be about 8.0 or about 8.5 or higher. In a preferred embodiment, the pH of the fracturing fluid is greater than or equal to 9.0 and more preferably greater than or equal to about 9.5.
The hydratable polymer useful in the present invention is underivatized guar as well as derivatized guars. Underivatized guar is preferred. Examples of derivatized guars include hydroxypropyl guar, carboxymethyl hydroxypropyl guar, and carboxymethyl hydroxyethyl cellulose.
In addition to the enzyme breaker and hydratable polymer, the fracturing fluid includes a crosslinking agent. The crosslinking agent can be polymers with metal ions including aluminum, antimony, zirconium and titanium containing compounds including the so-called organotitanates as well as borates and boron releasing compounds. In the case of the borate crosslinkers, the crosslinking agent is any material which supplies borate ions. Suitable borate crosslinkers include organoborates, monoborates, polyborates, mineral borates, boric acid, sodium borate, including anhydrous or any hydrate, borate ores such as colemanite or ulexite as well as any other borate complexed to organic compounds to delay the release of the borate ion. Borate crosslinking agents are preferred.
The crosslinking agent is preferably present in the range from about 0.001% to in excess of 0.5% by weight of the aqueous fluid. Preferably, the concentration of crosslinking agent is in the range from about 0.005% to about 0.25% by weight of the aqueous fluid.
Typically, the enzyme is introduced as an aqueous enzyme solution. The weight percentage of enzyme solution in the treatment fluid is dependent upon the number of units of enzyme activity in the aqueous enzyme solution. For instance, the amount of an aqueous enzyme solution having 30,000 units of enzyme activity in the treatment fluid is generally between from about 0.05 to about 1.3 weight percent, preferably from about 0.103 to about 0.206 weight percent. The weight percentage of an enzyme solution containing a different unit of enzyme activity may be determined using the designated weight percentage for the enzyme solution containing 30,000 units of enzyme activity.
The optimum pH of the aqueous fluid containing the crosslinkable polymer is alkaline and typically is between from about 9.5 to about 11.0.
The fracturing fluids of the invention also may have a pH regulating substance incorporated therein as a companion material to the enzyme breaker. The pH regulating substance is any substance which is initially inert but slowly hydrolyzes in the gelled fracturing fluid to produce a Bronsted acid, thereby gradually lowering the pH of the gelled fluid and activating the enzyme breaker. The preferred pH regulating substances include organic anhydrides, acyl halides, sulfonyl halides, benzylic halides and low molecular weight esters which slowly hydrolyze to produce Bronsted acids. By “low molecular weight” ester is meant that the ester should be soluble in the fracturing fluid in order to accomplish its intended purpose of hydrolyzing with time to produce an acid. Generally, the higher the molecular weight, the less soluble the ester. As a result, lower molecular weight esters are preferred for ease of use. Preferably, the pH regulating substance is a low molecular weight ester selected from the group consisting of ethyl acetate, 2-ethoxyethylacetate, ethylacetoacetate, triethylcitrate, methylbenzoate and dimethylphthalate. Typical molecular weights for the 2-ethoxyethylacetate, ethylacetoacetate and triethylcitrate used in the examples which follow are 132, 130 and 276 respectively. Preferably, the pH regulating substance is present in the range from about 0.01% to about 0.85% by weight of the aqueous fluid.
The well treatment fluid may be prepared on location using a high shear foam generator or may be shipped to the desired location.
The fracturing fluid may further contain a proppant which are normally added to the fluid prior to the addition of the crosslinking agent. Once transported into the formation by the fracturing fluid, a pack of proppant may be formed within the created or enlarged fracture to hold the fracture open during production of fluid from the formation. It is desirable that the proppant pack be capable of forming a partial monolayer of proppant in the fracture to provide increased interconnected interstitial spaces between abutting proppant particulates. Increased fracture conductivity results since the produced fluids typically flow around the widely-spaced proppant particulates rather than through the interstitial spaces in a packed bed.
In an aspect, the amount of proppant in the fracturing fluid may be between about 0.5 to about 12.0, pounds of proppant per gallon of fracturing fluid. Preferably, it may be between from about 0.25 to about 4.0 pounds per gallon of fracturing fluid.
Suitable proppants include those conventionally known in the art including quartz sand grains, glass beads, aluminum pellets, ceramics, plastic beads, including polyamides, and ultra lightweight (ULW) particulates such as ground or crushed shells of nuts like walnut, coconut, pecan, almond, ivory nut, brazil nut, etc.; ground and crushed seed shells (including fruit pits) of seeds of fruits such as plum, olive, peach, cherry, apricot, etc.; ground and crushed seed shells of other plants such as maize (e.g., corn cobs or corn kernels), etc.; processed wood materials such as those derived from woods such as oak, hickory, walnut, poplar, mahogany, etc., including such woods that have been processed by grinding, chipping, or other form of particalization, processing, etc.
Further the proppant may include porous ceramics or organic polymeric particulates. The porous particulate material may be treated with a non-porous penetrating material, coating layer or glazing layer. For instance, the porous particulate material may be a treated particulate material, as defined in U.S. Patent Publication No. 20050028979 wherein (a) the ASG of the treated porous material is less than the ASG of the porous particulate material; (b) the permeability of the treated material is less than the permeability of the porous particulate material; or (c) the porosity of the treated material is less than the porosity of the porous particulate material.
The propping agents are normally used in concentrations between about 1 to 8 pounds per gallon of fracturing fluid composition, but higher or lower concentrations can be used as required.
The fracturing fluid can also contain other conventional additives common to the well service industry such as surfactants, corrosion inhibitors, crosslinking delaying agents and the like.
In a typical fracturing operation, the fracturing fluid of the invention is pumped at sufficiently high pressures to cause the formation or enlargement of fractures and to place proppant into the fracture.
The following examples are illustrative of some of the embodiments of the present invention. All percentages set forth in the Examples are given in terms of weight units except as may otherwise be indicated.
EXAMPLES
Example 1
The htβ gene was cloned into cloning vector pUC57 to create the plasmid pUC57-htβ and into expression vector pGS-21a to create the pGS-21a-htβ plasmid. The plasmids pGS-21a-htβ and pUC57-htβ were then transformed into competent BL21(DE3) or DH5α E. coli strains and cultured in 5 mL LB-Miller nutrient media at 98.6° F. at 200 rpm for 16 hours. The culture broth was supplemented with 100 ug/mL ampicillan which was used as an inoculum for a 100 mL culture of E. coli harboring the plasmids pGS-21a-htβ or pUC57-htβ. These cultures were grown at 98.6° F. and 200 rpm. After 4 hours, isopropyl β-D-1-thiogalactopyranoside (IPTG) was added to the culture to a final concentration of 0.1 mM. After 3 hours of incubation in the presence of IPTG, the cells were chilled to 39° F. and harvested by centrifugation at 3,000 rpm for 20 minutes. The culture medium was then discarded and the cells stored at −4° F. until use. The cells were then thawed and resuspended in 5 mLs chilled 50 mM sodium phosphate buffer. Lysozyme was added to a final concentration of 1 mg/mL and the culture was incubated at room temperature for 30 minutes. Nucleic acids were disrupted by brief pulses of sonication and resultant cell free extract (CFX) was obtained by centrifugation.
Example 2
About 1 gpt of conventional beta-mannanase enzyme, commercially available as GBW-12CD from Baker Hughes Incorporated diluted in a 1:33 volumetric ratio in water, and about 2 mLs of the CFX of Example 1 containing pGS-21a-htβ and pUC57-htβ were added to 100 mL aqueous fluid containing 25 ppt GW3, 2gpt BF-7L and 1 gpt XLW-32 and incubated for 18 hours at 180° F. (GW-3 is a guar suspension agent, XLW-32 is a borate crosslinking agent, and BF-7L is a buffering agent, all of which are commercially available from Baker Hughes Incorporated). The samples were then allowed to cool to room temperature and their viscosities measured using a Fann 35 viscometer. The results are shown in FIG. 3 wherein it is illustrated that the mannanohydrolase provides almost complete reduction in the viscosity of guar after 18 hours at 180° F. while the conventional enzyme product does not appear to be as effective in reducing the viscosity of the cross linked fluid at this temperature and pH. The arrow in FIG. 3 represents an unbroken sample. The initial pH of all samples was 10.5.
Example 3
About 1 gpt of the conventional enzyme of Example 3 and of 2 mLs CFX from samples containing pGS-21a-htβ and pUC57-htβ from Example 1 were added to 100 mL aqueous samples containing 25 ppt GW-3, 2 gpt BF-7L and 1 gpt XLW-32 and incubated for 18 hours at 160° F. Samples of GW-3 were used at pH 6.5 and 10.5. The conventional enzyme, GBW-12, was shown to degrade the GW-3 sample at pH 6.5 but not at 10.5. Samples containing the mannanohydrolase provided partial to complete degradation of the cross-linked GW-3 after 18 hours at 160° F. Viscosities were measured on a Fann 35 and are shown in FIG. 4 wherein FIG. 4 represents the viscosity reduction in borate cross-linked 25 ppt GW-3 by the mannanohydrolase. The arrow represents an unbroken sample.
Example 4
A 100 mL aqueous fluid was prepared containing 25 ppt GW3, 1.5 gpt BF-7L and 1.5 gpt of a borate ore crosslinker slurried in hydrocarbon oil, commercially available from Baker Hughes Incorporated as XLW-30. The pH1 of the solution was 10.8. Two samples were then prepared. One sample, designated (−), had no enzyme added to the fluid. The other sample, designated (+), had 0.75 gpt of a 1/25 dilution of mannanohydrolase CFX solution produced from the pGS21a-htβ expression vector. FIG. 5 represents the reduction in viscosity of the two samples over 10 hours at 180° F. FIG. 6 represents the reduction in viscosity of the two samples over 10 hours at 140° F.
Example 5
A 100 mL aqueous fluid was prepared containing 25 ppt GW3, 1.3 gpt BF-7L and 1.0 gpt XLW-32 crosslinker for tests at 72° F. and 140° F. A second 100 mL aqueous fluid was prepared containing 25 ppt GW3, 2.0 gpt BF-7L and 1.5 gpt XLW-30 crosslinker for tests at 200° F. In all samples, the mannanohydrolase enzyme concentration was 0.5 gpt. The rheology of each sample was measured on a Chandler HTHP 5550 viscometer at 100 sec−1. FIG. 7 represents the rheology profiles of the tests at variable temperatures and demonstrates that mannanohydrolase is effective in reducing the viscosity of the crosslinked galactomannan polymer at a range of temperatures from 72° F. to at least 200° F.
Examples 2, 3, 4 and 5 demonstrate that fluids containing the mannanohydrolase effectively hydrolyze the guar polymer at elevated temperature and pH ranges where the conventional enzyme is not as effective.
Example 6
This example illustrates the regained conductivity of a proppant pack treated with an aqueous fluid which contains the mannanohydrolase enzyme breaker. Two samples of a 100 mL aqueous fluid were prepared containing 25 ppt GW-3, 1.5 gpt BF-7L and 1.3 gpt XLW-30. One sample further contained 1.25 gpt (1/5 dilution) of mannanohydrolase (referenced in Example 6); the other sample did not contain any Enzyme. A 60 mL syringe was equipped with a 30 mesh wire screen cut to the internal diameter of the syringe. The screen supported a piece of filter paper (2.5 μm pore size) which was also cut to the internal diameter of the syringe. 10 grams of 20/40 CarboProp, a proppant of Carbo Ceramics, was then applied to the filter paper. The 100 mL cross linked fluid was then applied to the proppant bed and forced through the proppant pack until the plunger came to rest on the top of the proppant pack. The end of the syringe was capped and the syringe submerged in a 180° F. water bath for 24 hours. The syringe was then removed from the water bath and allowed to cool to room temperature. The syringe was then inverted and the plunger gently removed to minimize disturbance to the proppant pack. The proppant pack was placed in a blue weigh boat and immediately visualized under a compound light microscope with 10× magnification. FIGS. 8A and 8B are photomicrographs of the proppant packs illustrating conductivity between a suspension which does not contain the mannanohydrolase (photomicrograph A) versus the suspension which does contain the mannanohydrolase (photomicrograph B).
As shown in photomicrograph A, the proppant pack had a highly defined structure signifying that the fracturing fluid remained crosslinked. (Remaining fluid from the syringe was also crosslinked.) Photomicrograph B illustrates proppant packs with no structure wherein the pack “fell apart” immediately upon removal from the syringe. The remaining fluid from the syringe was water-like with very low viscosity. Proppant packs from fluids containing the mannanohydrolase showed little to no crosslinked gel remaining. This suggests excellent cleanup and high recovery of proppant pack permeability.
Example 7
This example illustrates the production of then mannanohydrolase enzyme in a 10 liter fermentation process. The htβ gene was cloned into the expression vector pGS21-a with the restriction endonucleases NdeI and HindIII to create a mannanohydrolase without the associated GST fusion. The resultant expression vector was transformed into BL21(DE3) E. coli and plated on LB-Agar plates containing 100 ug/mL ampicillan. The plates were incubated at 98.6° F. overnight. A single colony was picked from the plate and used to inoculate 100 mLs of LB-Miller broth containing 100 ug/mL ampicillan. The culture was incubated at 98.6° F. overnight at 200 RPM.
The 100 mL overnight culture was used as an inoculum into 10 L of Terrific Broth in a Bioflow 3000 Fermentor from New Brunswick Scientific. Ampicillin was added to a final concentration of 100 ug/mL. The fermentation culture was grown for 24 hours at 98.6° F. with maximum agitation and feed with compressed air to maintain the maximum aeration possible. Glycerol was added at a rate of 4 mLs/hour for the full 24 hours. An antifoam solution was added as needed. Once the OD600 reached a value of 0.5, a sterile solution of lactose was added to the mixture so that the final concentration of lactose in the system was 15 mM. After 24 hours, the cell culture was stored at 39° F. until further processing.
The cell culture was then homogenized and the cell debris removed either through centrifugation or filtration through a 0.2 um pore-size polyethersulfone membrane. The resultant solution could then be used as the mannanohydrolase enzyme solution or further concentrated as desired. In this example, the filtrate was concentrated via tangential flow filtration (TFF) using a 30,000 MWCO polyethersulfone filter. The retentate was then used as the mannanohydrolase enzyme solution.
Other embodiments within the scope of the claims herein will be apparent to one skilled in the art from consideration of the description set forth herein. It is intended that the specification, together with the examples, be considered exemplary only, with the scope and spirit of the invention being indicated by the claims which follow.

## Claims

1. A method of hydraulic fracturing a subterranean formation which comprises introducing into the formation at a pressure sufficient to create or enlarge fractures in the formation a fracturing fluid having a pH from 8.5 to 11.0 comprising:
(a) a hydratable polymer selected from the group consisting of underivatized guars and derivatized guars;
(b) a crosslinking agent for crosslinking the hydratable polymer to form a polymer gel; and
(c) an enzyme breaker comprising a mannanohydrolase enzyme that has an amino acid sequence that is at least 90% homologous to the amino acid sequence of SEQ ID NO:2.

2. The method of claim 1, wherein the downhole temperature of the subterranean formation is in excess of 180° F.

3. The method of claim 2, wherein the downhole temperature of the subterranean formation is in excess of 185° F.

4. The method of claim 1, wherein the mannanohydrolase enzyme has an amino acid sequence that is at least 95% homologous to the amino acid sequence of SEQ ID NO:2.

5. The method of claim 1, wherein the crosslinking agent contains boron or is capable of providing boron ions to the fluid.

6. The method of claim 1, wherein the hydratable polymer is underivatized guar.

7. A method of hydraulic fracturing a subterranean formation penetrated by a well comprising:
(a) pumping into the well at a pressure sufficient to create or enlarge fractures in the formation a fracturing fluid having a pH from 8.5 to 11.0 comprising:
(i) a hydratable polymer selected from the group consisting of underivatized guars and derivatized guars;
(ii) a crosslinking agent for crosslinking the hydratable polymer to form a polymer gel;
(iii) an enzyme breaker comprising a mannanohydrolase enzyme that has an amino acid sequence that is at least 90% homologous to the amino acid sequence of SEQ ID NO:2; and
(iv) proppant; and

(b) creating a partial monolayer of proppant in the created or enlarged fracture.

8. The method of claim 7, wherein the downhole temperature of the subterranean formation is in excess of 160° F.

9. The method of claim 7, wherein the hydratable polymer is underivatized guar.

10. The method of claim 7, wherein the mannanohydrolase enzyme has an amino acid sequence that is at least 95% homologous to the amino acid sequence of SEQ ID NO:2.

11. The method of claim 10, wherein the mannanohydrolase enzyme has an amino acid sequence that is at least 99% homologous to the amino acid sequence of SEQ ID NO:2.

12. A method of hydraulic fracturing a subterranean formation which comprises:
(a) introducing into the formation at a pressure sufficient to create or enlarge fractures in the formation a fracturing fluid having a pH from 8.5 to 11.0 comprising:
(i) a hydratable galactomannan gum;
(ii) a crosslinking agent for crosslinking the galactomannan gum to form a polymer gel; and
(iii) an enzyme breaker comprising a mannanohydrolase enzyme that has an amino acid sequence that is at least 90% homologous to the amino acid sequence of SEQ ID NO:2; and

(b) reducing the viscosity of the fracturing fluid at a range of temperatures from 72° F. to at least 200° F.

13. The method of claim 12, wherein the fracturing fluid further comprises a pH regulating substance.

14. The method of claim 13, wherein the viscosity of the fracturing fluid is reduced by activating the enzyme breaker by the in-situ production of a Bronsted acid.

15. The method of claim 14, wherein the pH regulating substance is selected from the group consisting of organic anhydrides, acyl halides, sulfonyl halides, benzylic halides and a low molecular weight ester soluble in the fracturing fluid.

16. The method of claim 12, wherein the crosslinking agent is a borate or a boron releasing compound.

17. The method of claim 16, wherein the crosslinking agent is an organoborate, monoborate, polyborate, mineral borate, boric acid, sodium borate, a borate ore or a borate complexed organic compound.

18. The method of claim 12, wherein the enzyme breaker exhibits activity and has a temperature maximum in excess of 160° F.

19. The method of claim 18, wherein the enzyme breaker exhibits activity and has a temperature maximum in excess of 185° F.

20. The method of claim 19, wherein the enzyme breaker exhibits activity and has a temperature maximum in excess of 195° F.