Set retarded cement compositions and well cementing methods
CROSS-REFERENCE TO RELATED APPLICATION 
     This application is a continuation-in-part of application Ser. No. 540,742, filed Oct. 11, 1983, now U.S. Pat. No. 4,524,828. 
    
    
     BACKGROUND OF THE INVENTION 
     1. Field of the Invention 
     This invention relates generally to set retarded cement compositions and methods of cementing across zones in wells, and more particularly, but not by way of limitation, to set retarded cement compositions having enhanced compressive strength development after placement and methods of cementing across zones in wells using such compositions. 
     2. Description of the Prior Art 
     In cementing operations carried out in oil, gas and water wells, a hydraulic cement is normally mixed with sufficient water to form a pumpable slurry and the slurry is pumped across a subterranean zone or zones to be cemented by way of the wellbore penetrating such zone. After placement across the zone or zones, the cement slurry sets into a hard mass. 
     While cement compositions are utilized in carrying out a variety of operations in wells to accomplish a variety of purposes, cement compositions are most commonly used in primary cementing whereby casing and/or liners are bonded within the wellbore to the formations penetrated thereby. Cementing is accomplished by introducing a cement composition into the annular space between the casing or liner and the wellbore, generally by pumping the cement composition downwardly within the casing or liner to the bottom thereof and then upwardly into the annulus, and then allowing the cement composition to set into a hard mass therein. 
     One or more of the formations or zones adjacent the cemented annulus can contain fluids under pressure which enter and flow through the cement-containing annulus when the cementing procedure carried out therein is faulty or inadequate. The most common problem of this nature is the flow or migration of gas in the cemented annulus. Such gas can flow to the surface, create communication between producing or other subterranean formations or zones and can, when in high enough volume, create blowouts during the cementing operation between when the cement composition is placed and before the cement composition has set into a hard mass. Minor interzonal gas flow problems can lower production. When the magnitude of leakage requires remedial action, expensive secondary cementing procedures must be carried out. 
     The occurrence of annular gas flow in a cemented casing-wellbore annulus is believed to relate to the inability of the cement slurry to transmit hydrostatic pressure during the transition of the slurry from a true fluid to a hard, set mass. During this transition phase, initial hydration has begun and the slurry starts to develop static gel strength. Although the system has no compressive strength at this point, the cement column becomes partially self-supporting. This is a very critical period as far as potential gas entry into the cement column is concerned. That is, although the original hydrostatic pressure is trapped within the gelled cement matrix, any volume reductions of the aqueous phase at this point result in rapid decreases in the hydrostatic pressure due to the low compressibility of the fluid phase. Such volume reductions usually occur due to the ongoing hydration reactions and due to the loss of part of the fluid phase to the formation (fluid loss). In this situation, it is possible for the pressure within the cement matrix to fall below the gas entry limit and for gas migration to occur. 
     Static gel strength is the development of some internal rigidity in the matrix of the cement that will resist a force placed upon it. The development of static gel strength will start to occur immediately after pumping has stopped and will continue to increase until the cement is set. At some time before actual set, the cement will develop a static gel strength high enough to prevent a fluid from moving through it. Tests have indicated that a gel strength of 500 pounds per 100 square feet is sufficient to prevent any movement, although at certain conditions such gel strength can be considerably lower. When the cement has developed a static gel strength high enough to prevent formation fluids from moving through it, the cement is said to have completed its transition phase. 
     Volume reduction in the cement column can occur as a result of fluids lost from the cement slurry to the formation. Even when fluid loss is very low, small amounts of fluid are still lost from the slurry which can result in a pressure drop in the cement column during the transition phase thereof. Additionally, as the cement in the cement slurry hydrates, a volume reduction caused by such hydration results. Hydration volume reduction can ultimately be as high as three percent. Where the static gel strength development is slow and the volume reduction due to hydration and fluid loss are appreciable, the hydrostatic pressure exerted by the cement column on adjacent formations can drop below the pressure of formation fluids thereby allowing the fluids to enter the cement-filled annulus. If the gel strength of the cement slurry is not high enough to prevent further movement of formation fluids, a fingering or migration phenomena will occur and annular gas leakage and/or interzonal communication will ultimately result. However, where the gel strength is high enough, the flow of formation fluids through the cement column is prevented. 
     Traditionally, the petroleum industry has attempted to prevent annulus formation fluid flow by increasing the cement slurry density, improving mud displacement, controlling mud-cement slurry compatibility, using fluid loss control additives, causing the cement slurry to expand after setting, and multiple stage cementing. Although these techniques are helpful and have shown some measure of success, none have completely solved the problems. New techniques using cement slurries containing gas whereby the cement slurries are compressible have attained a much greater degree of success. Such techniques are the subject matter of U.S. Pat. Nos. 4,304,298 and 4,340,427. 
     Another problem often encountered in cementing relates to the cement slurry developing compressive strength at a slow rate and/or the compressive strength development of the in-place cement column not being uniform. With the drilling of wells for the production of hydrocarbons to increased depths during recent years, extended cementing times are required to mix cement compositions and pump them into the annular space in the wells. In addition, at the greater depths, elevated temperatures are encountered which accelerate the normal setting rates of cement compositions to the point where the pumping times, i.e., the mixing and placement times, exceed the pumpable times of the cement compositions, making it difficult or impossible to place the cement compositions at the desired locations in the wells. In order to increase the pumpable times of cement compositions, various set retarding additives have been utilized in cement compositions. While such additives successfully extend the pumpable times between mixing and the setting of cement compositions, they are temperature sensitive, i.e., the higher the temperature of the cement slurry, the greater the quantity of set retarder additive required. In cementing operations, especially when a long liner is involved, the static temperature of the cement column at the top thereof after placement can be considerably lower than the static temperature of the column at the bottom of the annulus, i.e., at the bottom hole static temperature (BHST). In some cementing applications, the static temperature of the cement column at the top can be as much as 40° F. cooler than the BHST. In these applications, the cement slurries must contain set retarders in quantities to achieve required pumpable times at the highest temperature to which the cement slurry is heated, and consequently, after placement the cooler slurry at the top of the cement column can take an excessive time to set and to develop compressive strength whereby the continuation of well operations is delayed. 
     By the present invention, set retarded cement compositions for cementing across zones in wells are provided which have enhanced gel strength and compressive strength development after placement in the annulus. That is, the cement compositions develop high gel strength in a short period of time after placement followed by rapid compressive strength development. The rapid development of high gel strength in a short time span prevents fluid invasion into the annulus containing the cement composition even though the hydrostatic pressure of the cement column may fall below the pressure of formation fluids during the transition of the slurry to a solid mass. Further, the enhanced and uniform compressive strength development of the cement column in spite of a temperature differential over the length of the column shortens the down time required as a result of carrying out the cementing procedure. 
     SUMMARY OF THE INVENTION 
     A set retarded cement composition for cementing across a zone or zones in a well having enhanced compressive strength development after placement in the annulus is provided. The composition is comprised of hydraulic cement, sufficient water to form a pumpable slurry which will set into a hard mass, one or more set retarders present in the slurry in a quantity sufficient to retard the set of the slurry until after the slurry is placed in the annulus, and a delayed retarder neutralizer present in the slurry in a quantity sufficient to neutralize the one or more retarders and enhance the compressive strength development of the slurry after placement. The delayed retarder neutralizer is comprised of one or more alkanolamine titanium chelates which hydrolize in the cement slurry to bring about the delayed release of alkanolamines therein which in turn neutralize the retarding effect of the one or more set retarders therein. The cement composition can also include one or more titanium crosslinkable materials which provide thixotropic properties and gel strength development when crosslinked by titanium released from the alkanolamine titanium chelates to the composition. Methods of cementing subterranean zones penetrated by wellbores using the cement compositions are also provided. 
     While a principal object of the cement compositions and methods of this invention is to combat the problems mentioned above encountered in cementing operations carried out in wells, it is to be understood that the compositions and methods can be utilized in a variety of secondary and other well cementing operations. 
     DESCRIPTION OF PREFERRED EMBODIMENTS 
     The cement compositions of the present invention are comprised of pumpable aqueous hydraulic cement slurries containing various components which, after placement in an annulus to be cemented, set into hard masses having required compressive strengths. While various hydraulic cements can be utilized in forming the slurries, Portland cement is preferably utilized and can be, for example, one or more of the various types identified as API Classes A-H and J cements. These cements are identified and defined in API Specification for Materials and Testing for Well Cements, API Spec. 10, Second Edition, June 15, 1984, of the American Petroleum Institute which is incorporated herein by reference. 
     The thickening and initial set times of cement compositions are strongly dependent upon temperature and pressure. To obtain optimum results in oil, gas and water well applications, a variety of additives are often included in the cement compositions to vary the cement slurry density, increase or decrease strength, accelerate or retard thickening time, control fluid loss, reduce slurry viscosity, increase resistance to corrosive fluids, etc. Essentially, a cement meeting the specifications of the American Petroleum Institute is mixed with water and other additives to provide a cement slurry appropriate for the conditions existing in each individual well to be cemented. 
     In accordance with the present invention, a set retarded cement composition for cementing across a zone or zones in a well having enhanced and uniform compressive strength development after placement in tne annulus is provided. The composition is comprised of hydraulic cement, sufficient water to form a pumpable slurry which will set into a hard mass, one or more set retarders and a delayed retarder neutralizer. 
     The set retarders which can be utilized in the compositions of this invention are those which when present in the compositions in relatively small quantities retard the setting of the compositions, i.e., increase the time period between mixing and setting whereby required pumping times can be achieved. The particular duration of set retardation brought about by the retarders is dependent upon a variety of factors including the temperature of the cement compositions containing the retarders, the quantities of retarders utilized therein, the reactivity of the retarders with other components in the cement compositions, etc. Examples of particularly suitable such set retarders are salts of lignosulfonates, organic acids and their salts, mixtures of these compounds, and combinations of these compounds in admixture with one or more water soluble borates. Of these, calcium lignosulfonate and potassium pentaborate tetrahydrate in a 1:1 ratio by weight is preferred. All of the above-mentioned set retarders, and possibly all set retarders effective in cement compositions of the type herein contemplated, are neutralized, i.e., the set retardation effect thereof terminated, when contacted or reacted with amines such as triethanolamine. 
     As mentioned above, the cement compositions of the present invention include, in addition to the one or more set retarders described above, a delayed retarder neutralizer present in the composition in a quantity sufficient to neutralize the one or more set retarders and thereby bring about the enhanced and uniform compressive strength development of the composition after the placement thereof in an annulus to be cemented. Such delayed retarder neutralizer is comprised of an alkanolamine titanium chelate or a mixture of such chelates which when added to a hydraulic cement slurry, slowly hydrolize to liberate amines in the slurry. Particularly suitable such chelates include triethanolamine titanium chelate represented by the formula: ##STR1## and modifications of such chelate which include replacement of the --C 3  H 7  group with various other alkyl or aryl groups or replacement of the --OC 3  H 7  groups with hydroxide or halogen atoms, and partially polymerized versions of these chelates. Other ligands useful in this class which may replace one or both of the triethanolamine ligands include (R 1 ) 2  N--R 2  --OH where R 1  is hydrogen, alkyl, and/or hydroxyalkyl and R 2  is ethylene, trimethylene, or isopropylene (--C(CH 3 ) 2  --), R 4  (R 5 )N--R 3  --N(R 6 )(R 7 ) where R 3  is ethylene, trimethylene, or isopropylene (--C(CH 3 ) 2  --) and R 4 , R 5 , R 6 , and R 7  are individually hydrogen, alkyl, hydroxyalkyl, and/or aminoalkyl groups with the limitation that each possible molecule contains at least one hydroxyalkyl group, and various other alkanolamines. The modified complexes can contain in the range of from one to four alkanolamine ligands per titanium atom. 
     The preferred titanium chelate represented by the above formula is prepared by the reaction of titanium isopropoxide with two moles of triethanolamine to yield isopropoxytitanium triethanolamine chelate plus two moles of isopropyl alcohol. The product is a liquid containing about 8.3% titanium. 
     A preferred class of solid titanium chelates are described in U.S. Pat. No. 2,935,522 issued May 3, 1960, which is incorporated herein by reference. These chelates have the following general formula: ##STR2## wherein R is isopropyl (--C 3  H 7 ) and R 1  is ethylene or isopropylene. A particularly preferred chelate of this type for use in accordance with this invention is a chelate of the above formula wherein R is isopropyl and R 1  is ethylene, i.e., isopropoxytitanium triethanolamine chelate. This chelate is a white free-flowing solid which can be readily dry-blended with a hydraulic cement. 
     Modifications of the above chelate include products containing two triethanolamine groups represented by the structural formula: ##STR3## where R 1  is ethylene or isopropylene; and dimers with a structure represented by the following: ##STR4## where R 1  is ethylene or isopropylene. 
     As mentioned above, the particular quantity of the one or more set retarders utilized in the cement compositions depends upon various factors including the time required and the temperature to which the cement composition will be heated during and after placement. Generally, the retarder or retarders are included in the cement compositions in amounts in the range of from about 0.1% to about 5.0% by weight of dry cement utilized therein. When the preferred retarder comprised of calcium lignosulfonate and potassium pentaborate tetrahydrate in a 1:1 ratio by weight is utilized, it is included in the cement compositions in amounts in the range of from about 0.5% to about 3.0% by weight of dry cement utilized. 
     The amounts of delayed retarder neutralizer or mixtures of neutralizers utilized in the cement compositions will vary with the amounts of retarder or retarders present, the amounts of crosslinkable material present, if any, and to some degree, the temperatures to which the cement compositions will be heated during and after placement. The general amount of retarder neutalizer used may vary as much as from 0.05% to about 1.5% by weight of dry cement used. The more usual and preferred range is from about 0.1% to about 0.5% by weight of dry cement. When combined with a cement slurry, the titanium chelate neutralizers slowly hydrolyze to release amines which in turn function in the slurry to neutralize the effects of the retarders. Thus, once the chelates hydrolyze and produce amines, the cement slurry will rapidly set and compressive strength will rapidly be developed. 
     A thixotropic set retarded cement composition of this invention having enhanced gel strength and compressive strength development after placement in the zone to be cemented is comprised of hydraulic cement, water, one or more set retarders, a crosslinkable material, and a crosslinking agent which also neutralizes the influence of retarders, i.e., an alkanolamine titanium chelate or mixture of chelates. 
     The crosslinkable material must be capable of being crosslinked by titanium as well as being water soluble and relatively non-reactive with other components in the cement compositions. Preferably, the material is selected from the group consisting of cellulose ethers exemplified by hydroxyalkylcellulose, carboxyalkylcellulose or carboxyalkylhydroxyalkylcellulose; polyvinyl alcohol; homopolymers, copolymers and terpolymers of AMPS (2-acrylamido-2-methylpropane sulfonic acid), sodium vinylsulfonate, acrylamide, N,N-dimethylacrylamide, acrylic acid and mixtures thereof. Most preferably, the crosslinkable material is selected from the group consisting of carboxymethylhydroxyethylcellulose, hydroxyethylcellulose, a copolymer of 2-acrylamido-2-methylpropane sulfonic acid and N,N-dimethylacrylamide and mixtures of these compounds. 
     The crosslinkable material is generally included in the thixotropic cement compositions of this invention in an amount in the range of from about 0.1% to about 2.0% by weight of dry cement utilized. A more preferred range of crosslinkable material is from about 0.2% to about 0.6% by weight of dry cement. 
     As will be understood, in the thixotropic cement compositions, as the crosslinking-retarder neutralizing agent slowly hydrolyzes, the released titanium crosslinks the crosslinkable material in the composition which brings about the rapid development of gel strength during the transition phase of the cement composition after placement. Simultaneously, the alkanolamines released react with or otherwise function to neutralize the retarding effect of the set retarders which in turn causes the cement composition to set and rapidly develop compressive strength after placement. 
     The quantities of the one or more set retarders and the alkanolamine titanium chelate or chelates utilized in the thixotropic set retarded cement compositions are essentially the same as set forth above for the non-thixotropic set retarded cement compositions. 
     A preferred set retarded cement composition of this invention is comprised of hydraulic cement, sufficient water to form a pumpable slurry which will set into a hard mass, one or more set retarders selected from the group consisting of salts of lignosulfonates, organic acids and their salts, mixtures of the foregoing compounds and one or more of the foregoing compounds in admixture with one or more water soluble borates present in the composition in an amount in the range of from about 0.1% to about 5.0% by weight of dry cement therein, and a delayed retarder neutralizer comprised of one or more of the titanium chelates described above present in the composition in an amount in the range of from about 0.05% to about 1.5% by weight of dry cement. 
     The most preferred such cement composition includes a set retarder comprised of calcium lignosulfonate and potassium pentaborate tetrahydrate in a 1:1 ratio by weight present in the composition in an amount in the range of from about 0.5% to about 1.5% by weight of dry cement, and isopropoxytitanium triethanolamine chelate present in the composition in an amount in the range of from about 0.1% to about 0.5% by weight of dry cement. 
     A preferred thixotropic set retarded cement composition of this invention is comprised of hydraulic cement, sufficient water to form a pumpable slurry which will set into a hard mass, a set retarder for delaying the set of the slurry selected from the group consisting of salts of lignosulfonates, organic acids and their salts, mixtures of the foregoing compounds and one or more of the foregoing compounds in admixture with one or more water soluble borates present in the composition in an amount in the range of from about 0.1% to about 5.0% by weight of dry cement, a crosslinkable material for producing thixotropic properties and gel strength development in said composition when crosslinked with titanium selected from the group consisting of carboxymethylhydroxyethylcellulose, hydroxyethylcellulose, a copolymer of 2-acrylamido-2-methylpropane sulfonic acid and N,N-dimethylacrylamide and mixtures thereof present in the composition in an amount in the range of from about 0.1% to about 2.0% by weight of dry cement, and the titanium chelate or mixture of chelates described above present in the composition in an amount in the range of from about 0.05% to about 1.5% by weight of dry cement therein. 
     The most preferred thixotropic, set retarded cement composition includes a set retarder comprised of calcium lignosulfonate and potassium pentaborate tetrahydrate in a 1:1 ratio by weight present in the composition in an amount in the range of from about 0.5% to about 3.0% by weight of dry cement, a crosslinkable material comprised of carboxymethylhydroxyethylcellulose present in the composition in an amount in the range of from about 0.2% to about 0.6% by weight of dry cement and isopropoxytitanium triethanolamine chelate present in the composition in an amount in the range of from about 0.1% to about 0.5% by weight of dry cement therein. 
     In carrying out the method of the present invention, a set retarded or thixotropic, set retarded cement composition is formed including one or more retarders present in a quantity sufficient to retard the set of the composition until after it is placed across the interval to be cemented. The delayed retarder neutralizer is included in the composition in a quantity sufficient to neutralize the retarder after placement of the composition whereby rapid gel strength and compressive strength development take place. In the case of a thixotropic composition including crosslinkable material, the crosslinker-retarder neutralizer simultaneously crosslinks the crosslinkable material and neutralizes the retarder bringing about the formation of high gel strength during the transition phase as well as the rapid and uniform development of compressive strength thereafter. The set retarded cement compositions are pumped across the interval to be cemented and then allowed to set into a hard mass. 
     The pumping times of the compositions can be extended by the inclusion of retarders therein up to 12 hours at bottom hole circulating temperatures of up to 400° F. As mentioned above, the in situ hydrolysis of the alkanolamine chelates is slow whereby the set retarders are not totally neutralized nor is the crosslinkable material completely crosslinked until after placement of the cement compositions. 
    
    
     In order to facilitate a clear understanding of the methods and compositions of this invention, the following Examples are given. 
     EXAMPLE 1 
     A series of tests are conducted to determine how effective a variety of titanium chelates are in producing thixotropic behavior. The cement slurries tested are prepared by dry blending all the additives with the cement prior to addition to water. If any liquid additives are used, the liquid is added to the mixing water prior to adding cement. The cement slurry is placed in a static gel strength measuring device and a standard thixotropic test is conducted. 
     The static gel strength measuring apparatus consists of three major components, the chamber and lid, the magnetic drive assembly, and the cord pulling assembly. 
     The chamber is a heavy wall, high strength metal vessel equipped with strip heaters attached directly to the outside of the chamber. A thermocouple is inserted into the vessel to allow the temperature of the vessel to be controlled. The lid of the chamber is equipped so that the principal drive shaft of the magnetic drive assembly can be inserted. On the shaft a stirring paddle is fitted over one end of the shaft and secured with a shear pin. On the other end of the principal drive shaft the magnetic drive head is connected. The magnetic drive head is then in turn connected by a belt system to a variable speed magnetic drive power source and torque measuring device. A thermocouple is inserted through the top of the magnetic drive head and down the middle of the hollow principal drive shaft. The lid of the chamber is equipped with two ports. One port is connected to a pressure volume pump used to generate pressure and the other port is equipped with a quick opening safety valve. The bottom of the chamber is equipped with a quick opening valve and used to relieve the pressure and discharge the test slurry at the end of the test period. The cord pulling mechanism consists of a cord pulling capstan or drum arrangement driven by a variable speed gear motor with the cord running through the pulley arrangement to a load cell and then to the top of the magnetic drive head. 
     To determine the gel strength development of cement slurry under down hole conditions, this equipment was specifically designed for measuring static gel strength after a stirring period that simulated slurry placement. The equipment is designed to operate at a maximum temperature of 400° F. at 10,000 psi. The low friction magnetic drive allows the slurry to be stirred while monitoring consistency during the stirring time. After simulating placement time, the motor is shut off and the cord pulling system is attached to the magnetic drive head. Static gel strength is determined by continuously measuring the torque required to rotate the paddle at a very slow speed (0.5° to 2.0° per minute). At such speeds, a magnetic drive has very low friction and very accurate torque measurements can be made. Since the torque measuring system consists of a cord pulling capstan or drum arrangement driven by a variable speed gear motor, accurate continuous rotation and means for continuously recording the torque are provided. The gel strength is then calculated from the torque measurement and the vessel geometry. The slow movement of the paddle allows static gel strength to be measured but does not inhibit gel strength development. Continuous static gel strength values can be measured up to a maximum of 1000 lbs/100 ft 2 . 
     The standard thixotropic test procedure is as follows: 
     1. stir the slurry with the magnetic drive consistometer for one hour while increasing temperature and pressure from ambient conditions to bottom hole circulating temperature (BHCT) and bottom hole pressure (BHP) according to schedule; 
     2. after one hour of stirring, set static for 15 minutes while continually measuring static gel strength; 
     3. after a static period of 15 minutes, stir for 15 minutes while continually measuring consistency; and 
     4. repeat static and stirring times a total of three times. 
     In the data that is developed, one basic slurry composition is tested. This slurry consists of API Class H cement, 0.4% carboxymethylhydroxyethylcellulose by weight of cement, 44% water by weight of cement and retarder as given in Table I. 
     Table I provides the range of temperatures, pressures and retarder amounts used in each simulated well condition. The temperature range varies from 140° F. to 275° F. The amount of retarder utilized is sufficient to provide at least 31/2 hours thickening time at test conditions where thickening time is taken as the definition given in API Specification 10. 
     
                       TABLE I                                                     
______________________________________                                    
Test Conditions and Retarder Amounts                                      
Temperature  Pressure Percent by Weight                                   
(°F.) (psi)    Retarder*                                           
______________________________________                                    
140          6000     0.4                                                 
170          8000     1.2                                                 
180          8000     1.2                                                 
200          8000     1.6                                                 
215          8000     2.0                                                 
245          8000     2.2                                                 
275          8000     2.4                                                 
______________________________________                                    
 *The retarder used is a 1:1 mixture of calcium lignosulfonate and        
 potassium pentaborate tetrahydrate.                                      
 Table II provides the physical and chemical properties of the compounds  
 tested.                                                                  
 
    
     
                                           TABLE II                                
__________________________________________________________________________
Physical and Chemical Properties of Compounds                             
Considered as Thixotropic Cement Additives                                
          Physical                                                        
Compound  Form   Chemical Description                                     
__________________________________________________________________________
Zirconium Solid  Zirconium oxychloride (zirconyl chloride)-               
oxychloride      ZrOCl.sub.2                                              
Zirconium Liquid Zirconium chelate of acetylacetone                       
acetylacetonate                                                           
Titanium  Liquid Titanium oxychloride (TiOCl.sub.2)                       
oxychloride                                                               
Titanium  Liquid Prepared by reaction of titanium                         
triethanol-                                                               
          (non-aqueous)                                                   
                 isopropoxide with two moles of tri-                      
amine            ethanolamine.                                            
                 Ti(OCH(CH.sub.3).sub.2).sub.4 + 2N(CH.sub.2 CH.sub.2     
                 OH).sub.3 →                                       
                 (C.sub.3 H.sub.7 O).sub.2 Ti[OCH.sub.2 CH.sub.2 N(CH.sub.
                 2 CH.sub.2 OH).sub.2 ].sub.2 +                           
                 2C.sub.3 H.sub.7 OH                                      
                 The two moles of isopropyl alcohol are                   
                 left in the reaction mixture. Thus, this                 
                 compound consists of triethanolamine                     
                 titanate plus isopropyl alcohol.                         
Titanium  Solid  Titanium Monotriethanolamine,                            
monotriethanol-  [N(CH.sub.2 CH.sub.2 O--).sub.3 ]Ti[OCH(CH.sub.3).sub.2  
                 ], contains                                              
amine            about 19.0% titanium by weight.                          
Titanium mono-                                                            
          Solid  A mixture of 57% titanium monotriethanol-                
triethanolamine plus                                                      
                 amine and 43% fructose by weight                         
fructose (Blend I)                                                        
Titanium mono-                                                            
          Solid  A mixture of 73% titanium monotriethanol-                
triethanolamine plus                                                      
                 amine and 27% fructose by weight                         
fructose (Blend II)                                                       
Titanium  Solid  Titanium triethanolamine deposited on                    
triethanolamine  diatomaceous earth. Contains about                       
deposited on     4.1% Ti by weight                                        
diatomaceous earth                                                        
Titanium  Liquid Solution of titanium monotriethanolamine                 
monotriethanol-  containing about 7.6% Ti by weight                       
amine solution                                                            
Hydrolyzed,                                                               
          Solid  Organic titanate (chelate) from hydro-                   
partially poly-  lyzed titanium acetylacetonate. Prepared                 
merized titanium by controlled addition of water as                       
acetylacetonate  illustrated below.                                       
                 Ti(Cl).sub.2 [OC(CH.sub.3)═CHCOCH.sub.3 ].sub.2 +    
                 2H.sub.2 O →                                      
                 Ti(OH).sub.2 [OC(CH.sub.3)═CHCOCH.sub.3).sub.2 +     
                 2HCl                                                     
                 Ti(OH).sub.2 (OC(CH.sub.3)═CHCOCH.sub.3).sub.2 +     
                 H.sub.2 O →                                       
                 partially polymerized, solid product.                    
Titanium  Liquid Prepared by the reaction of titanium                     
lactate   (aqueous)                                                       
                 isopropoxide with two moles of lactic                    
                 acid in presence of water.                               
                 Ti(OCH(CH.sub.3).sub.2).sub.4 + 2CH.sub.3 CH(OH)COOH     
                 →                                                 
                 [ Ti(OH).sub.2 (OCH(CH.sub.3)COO.sup.-).sub.2 ][H+].sub.2
                  + 4C.sub.3 H.sub.7 OH                                   
                 The acidic protons are neutralized with                  
                 ammonium hydroxide. This product may be                  
                 described as the ammonium salt of tita-                  
                 nium lactate. However, the structure of                  
                 this product is complicated by polymeri-                 
                 zation of the titanium chelate to some                   
                 degree.                                                  
Polymerized                                                               
          Solid  Polymerized titanium lactate.                            
titanium         Prepared from the titanium lactate.                      
lactate          Extent of polymerization has been                        
                 increased to insolublize the chelate and                 
                 yield a solid containing about 21.4% Ti.                 
Lactic acid                                                               
          Solid  One mole of lactic acid reacted with two                 
reacted with     moles of hydrated TiO.sub.2. Ti content is               
hydrated TiO.sub.2                                                        
                 about 20.8% by weight                                    
Titanium  Liquid Tartaric acid analog of titanium lactate.                
tartrate         Contains about 8.2% Ti by weight                         
Titanium malate                                                           
          Solid  Titanium malate which has been spray                     
                 dried. Contains about 7.9% Ti by weight                  
Titanium  Liquid Prepared by the reaction of titanium                     
acetylacetonate                                                           
          (non-aqueous)                                                   
                 isopropoxide with two moles of acetylace-                
                 tone.                                                    
                 Ti(OCH(CH.sub.3).sub.2).sub.4 + 2(CH.sub.3 COCH.sub.2    
                 COCH.sub.3) →                                     
                 Ti(OC.sub.3 H.sub.7).sub.2 [OC(CH.sub.3)═CHOCH.sub.3 
                 ].sub.2 + 2C.sub.3 H.sub.7 OH                            
                 The two moles of isopropyl alcohol are                   
                 left in the reaction mixture.                            
__________________________________________________________________________
 
    
     Table III provides the actual data obtained. The additive description along with the amount of additive used (by weight of cement), temperatures and actual get strength measurements are shown. The retarder level at each temperature is given in Table I. The gel strengths given are the maximum strength in pounds per 100 feet square reached during each 15 static minute period. 
     
                       TABLE III                                                   
______________________________________                                    
Gel Strength Measurements.sup.a                                           
          Percent           Gel Strength                                  
          Addition                                                        
                 Temperature                                              
                            (lbs/100 ft.sup.2                             
Additive    (bwc)    (°F.)                                         
                                1    2    3                               
______________________________________                                    
None        0        140         12   30   70                             
Zirconium   1.0      140         60   70   60                             
oxychloride 1.0      200         75  100   95                             
Zirconium   0.5      140         75  100  160                             
acetylacetonate                                                           
Titanium    0.5      140        365  --   --                              
oxychloride                                                               
Titanium    0.25     140         30   40   32                             
triethanolamine                                                           
            0.50     140         0    0    30                             
            0.50     200        350  205  212                             
            0.50     275        305  310  225                             
Titanium    0.25     140         50   6    15                             
monotriethanol-                                                           
            0.25     140         40   20   15                             
amine       0.50     140         50   50   50                             
            0.50     140         25   25   25                             
            0.25     180        200  320  270                             
            0.25     215        500  500  500                             
            0.25     275        265  250  220                             
            0.50     275        225  500  500                             
Titanium mono-                                                            
            0.50     140        500  500  500                             
triethanolamine                                                           
            0.50     275         80   90   85                             
plus fructose                                                             
            0.50     275         70  100  100                             
(Blend I)                                                                 
Titanium mono-                                                            
            0.25     140        400  500  --                              
triethanolamine                                                           
            0.50     140        500  500  500                             
plus fructose                                                             
            0.50     180        200  210  --                              
(Blend II)  0.50     215        500  500  500                             
            0.50     275        500  500  500                             
Titanium tri-                                                             
            0.50     140        135  120  100                             
ethanolamine                                                              
deposited on                                                              
diatomaceous earth                                                        
Titanium mono-                                                            
            0.25     180        500  200  250                             
triethanolamine                                                           
            0.50     180        450  500  500                             
solution                                                                  
Hydrolyzed, 0.5      140        205  200  205                             
partially poly-                                                           
merized titanium                                                          
acetylacetonate                                                           
Titanium Lactate                                                          
            0.25     170        160  200  215                             
Polymerized 0.5      275        270  330  235                             
titanium lactate                                                          
Lactic acid 0.5      140        350  400  300                             
reacted with                                                              
            0.5      200        160  160  195                             
hydrated TiO.sub.2                                                        
            0.5      275         40   35   40                             
Titanium tartrate                                                         
            0.5      140        115  150  155                             
            0.5      275        180  390  280                             
Titanium malate                                                           
            0.5      140        500  500  500                             
            0.5      275         20   40   45                             
Titanium    0.5      245        450  500  500                             
acetylacetonate.sup.b                                                     
______________________________________                                    
 .sup.a Slurry composition: Class H Cement, 0.4% CMHEC, 44% H.sub.2 O     
 .sup.b Replacement of CMHEC with HEC in slurry formulation               
 
    
     The foregoing data indicates the operability of alkanolamine titanium chelates in crosslinking CMHEC to impart thixotropic properties to cement compositions. 
     EXAMPLE 2 
     A cement composition of the present invention is used in carrying out a primary cementing job in the field. The well conditions are as follows: 
     Total depth: 12,000 ft. 
     Wellbore size: 61/4 inches, 
     Casing size: 27/8 inch long string, 
     Bottom hole circulating temperature: 239° F., 
     Bottom hole static temperature: 300° F., 
     Well fluid: 15.4 lbs/gal mud, 
     Displacement fluid: 2% KCl water. 
     A slurry having the following composition is first prepared and tested in the laboratory: 
     Class H Cement+30% coarse silica+4% CMHEC+0.5% potassium pentaborate+0.5% calcium lignosulfonate+0.25% titanium triethanolamine 
     Slurry density--16.4 lbs/gal, 
     Slurry volume--1.35 ft 3  /sk, 
     Slurry water--5.2 gal/sk. 
     The laboratory gel strength tests indicate this slurry develops static gel strength of 500 lbs/100 ft 2  in 20 minutes at a bottom hole circulating temperature of 240° F. and a pressure of 8000 psi. The job is run and considered successful by the customer. No gas flow is observed on the well and the casing shoe withstands the pressure test. Adequate compressive strength is developed in good time after placement of the slurry. 
     EXAMPLE 3 
     A cement composition of the present invention is used in carrying out a cementing job in the area of Monahans, Tex. The well conditions are as follows: 
     Total depth: 21,300 ft. 
     Depth of last casing: 10,646 ft. 
     Liner size: 51/2 inches 
     Hole size: 81/2 inches 
     Top of cement: 10,600 ft. 
     Bottom hole static temperature: 320° F. 
     Bottom hole circulating temperature: 294° F. 
     Static temperature at top of cement: 150° F. 
     Mud density: 11.5 lbs/gal (invert emulsion) 
     Cement density: 13.5 lbs/gal 
     Due to the extreme well conditions, conventional cement formulations tested do not achieve initial sets at top of cement conditions even after 72 hours curing time. 
     A cement slurry of the following composition is prepared and tested: 
     [A mixture of 65% by volume Class H cement and 35% by volume fly ash]+17.5%* fine silica+0.5% hydroxyethylcellulose+0.5% carboxymethylhydroxyethylcellulose+0.8% calcium lignosulfonate+0.8% potassium pentaborate+0.5% titanium triethanolamine. 
    
     The above described cement slurry has the following compressive strengths with a thickening time of 5 hours 54 minutes. 
     
         ______________________________________                                    
Compressive Strengths                                                     
Temperature      Hours   PSI                                              
______________________________________                                    
320° F.   24      600                                              
                 48      1000                                             
                 72      1700                                             
150° F.   24      400                                              
                 48      500                                              
                 72      700                                              
______________________________________                                    
 
    
     The job is conducted and hard cement is found 400 feet on top of the liner in 48 hours and the liner tap tests to 5000 psi.