in an embodiment , a synthetic layered silicate may be synthesized having the following formula : [ si 8 ( mg a li b ) o 20 ( oh ) 4 − y f y ] z − zm + wherein a = 4 . 75 to 5 . 45 ; b = 0 . 25 to 1 . 25 ; y = 0 to & lt ; 4 ; z = 12 - 2a - b ; and m is na + or li + . a water - soluble lithium compound may be added to an amount of water . a water - soluble lithium compound may be any soluble or slightly soluble lithium compound that provides a source of lithium cation when dispersed in an aqueous media . examples of lithium compounds include , but are not limited to , lithium carbonate , lithium chloride , lithium bromide , lithium fluoride , lithium sulfate , or mixtures thereof . an excess of lithium ion content in the reaction mixture may be important in producing a synthetic layered silicate with improved electrolyte tolerances . the lithium compound may be added in amounts such that the lithium content in solution may be from about 100 % to about 300 % above the value of the lithium content required to provide the cation of the layered silicate . the lithium cations may be incorporated into the lattice structure of the produced layered silicate . in one embodiment , the lithium content in the produced synthetic layered silicate may be from about 0 . 3 % to about 2 . 2 %. in an embodiment , the lithium content , in the produced synthetic layered silicate , may be from about 0 . 35 % to about 1 . 0 %. in other embodiments , the lithium content , in the produced synthetic layered silicate , may be from about 0 . 5 % to about 0 . 85 %. various amounts of reactants , expressed as ranges of atomic ratios , may be used to produce a synthetic layered silicate . an atomic ratio relative to lithium , wherein lithium is 1 , may be about 1 - 10 atoms silicon , about 1 - 8 atoms magnesium and about 2 - 16 atoms sodium . in an embodiment , the atomic ratio may be about 2 - 5 atoms silicon , about 1 - 6 atoms magnesium , and about 2 - 14 atoms sodium , all with respect to lithium . in an embodiment , the atomic ratio may be about 3 - 5 atoms silicon , about 1 - 4 atoms magnesium , and about 2 - 7 atoms sodium , all with respect to lithium . experimental results indicate that a synthetic layered silicate produced using atomic ratios in the aforementioned atomic ratios exhibit improved tolerance to electrolytes during use . electrolytic tolerance may be measured by adding the synthetic layered silicate to an electrolytic solution and determining the viscosity of the solution . an improved tolerance to electrolytes is characterized by a viscosity greater than 100 , 000 centipoise ( cps ) in the presence of up to about 10 meqs . of electrolyte per gram of the synthetic layered silicate . the lithium compound may be stirred in the aqueous medium up to about 2 hours at about ambient temperature . the solution may be stirred during the reaction period at rates below about 1000 rpm , however , in other embodiments , the stirring rate may be below about 200 rpm . an additional amount of water may be added to the lithium mixture , followed by the addition of a water - soluble magnesium compound . the magnesium compound may be any water - soluble magnesium compound that may provide a source of magnesium cations when dispersed in an aqueous media . examples of magnesium compounds include , but are not limited to , magnesium sulfate heptahydrate , magnesium chloride , magnesium nitrate , magnesium bromide , or mixtures thereof . the mixture may then be heated to greater than ambient temperature . in a separate container , a solution of a water - soluble carbonate compound may be prepared . the water - soluble carbonate compound may be any carbonate compound that may provide a source of carbonate anions when dispersed in an aqueous media . examples of carbonate compounds include , but are not limited to , sodium carbonate , potassium carbonate , lithium carbonate , or mixtures thereof . the carbonate solution may be added to the aqueous mixture of the magnesium and lithium compounds . the carbonate solution may be added over a period of up to about 1 hour . the temperature may be maintained at greater than about 25 ° c . during addition . a silicate solution may be added to the magnesium , lithium , and carbonate solution . the silicate solution may be added to the above mixture over a period of greater than about 30 minutes , while maintaining the mixture temperature at greater than about 25 ° c . the silicate solution may be any solution which provides sio 2 . the silicate solution may be added to the magnesium , lithium , and carbonate solution such that , in the produced synthetic layered silicate , in an embodiment , the ratio of sio 2 / mgo may be from about 2 . 20 to about 2 . 50 , however , in other embodiments the ratio may be from about 2 . 25 to about 2 . 40 . in some embodiments , the sio 2 / mgo ratio may be from about 2 . 3 to about 2 . 35 . examples of silicate solutions include , but are not limited to , aqueous mixtures of sodium silicate , silicic acid , lithium silicate compounds , potassium silicate compounds , mixtures of silicon dioxide and sodium oxide solutions ( i . e . water glass ), or mixtures thereof . the solution and product may be heated to the point wherein a vapor may be produced , the vapor condensed , and returned to the solution . the heating procedure may continue for longer than about 1 hour . subsequently , the solution may be heated to greater than about 100 ° c . for a period greater than about 2 hours . an autoclave may be used . the resulting hydrous magnesium silicate may be separated by filtration , and subsequently washed and dried . in an embodiment , other orders of addition of reactants or other reactants may be utilized to produce a layered silicate compound . the same types of solutions as in the aforementioned embodiments may be utilized . an aqueous solution of a carbonate compound may be added to an aqueous solution of a magnesium compound . the carbonate compound solution may be added to the magnesium compound solution over a time period greater than about 30 minutes . the reaction solution may be maintained at a temperature greater than about 25 ° c . the solution may be stirred during the reaction period at rates below about 1000 rpm . in other embodiments , the stirring rate may be below about 200 rpm . magnesium carbonate may be subsequently produced . a source of lithium and / or fluoride ions may be added to the stirred suspension of magnesium carbonate . fluoride compounds , as the source of the fluoride ion , include , but are not limited to , lithium fluoride , sodium hexafluorosilicate , hydrofluoric acid , sodium fluoride , potassium fluoride , or mixtures thereof . an excess of lithium ion content in the reaction mixture may be important in producing a synthetic layered silicate with improved electrolyte tolerances . the lithium compound may be added in amounts such that the lithium content in solution may be from about 100 % to about 300 % above the value of the lithium content required to provide the cation of the layered silicate . the lithium cations may be incorporated into the lattice structure of the produced layered silicate . the lithium content , in the produced synthetic layered silicate may , in some embodiments , be from about 0 . 3 % to about 2 . 2 %. in an embodiment , the lithium content , in the produced synthetic layered silicate , may be about 0 . 35 % to about 1 . 0 %, and in other embodiments , the lithium content , in the produced synthetic layered silicate , may be about 0 . 5 % to about 0 . 85 %. a silicate solution , in some embodiments , may be added to the suspension of the precipitated magnesium carbonate such that , in the produced synthetic layered silicate , the ratio of sio 2 / mgo may be from about 2 . 20 to about 2 . 50 . in some embodiments , the sio 2 / mgo ratio may be about 2 . 25 to about 2 . 40 . in other embodiments , the sio 2 / mgo ratio may be about 2 . 3 to about 2 . 35 . examples of silicate solutions include , but are not limited to , aqueous mixtures of sodium silicate , silicic acid , lithium silicate compounds , potassium silicate compounds , mixtures of silicon dioxide and sodium oxide solutions ( i . e ., water glass ), or mixtures thereof . in an embodiment , the entire aqueous suspension from which the precipitate may be formed may be subjected to a hydrothermal treatment . the hydrothermal treatment may be conducted such that the entire aqueous suspension may be heated for a period of greater than about 1 hour at temperatures greater than about 100 ° c . an autoclave may be used . the material may be filtered , washed , and dried . in an embodiment , a carbonate solution may be added to the magnesium solution over a period of greater than about 30 minutes . a silicate solution may be added to the magnesium and carbonate solution , followed by the addition of the lithium and / or fluoride compounds . in an embodiment , the amount of silicate solution added to the suspension of the precipitated magnesium carbonate may be such , that in the produced synthetic layered silicate , the ratio of sio 2 / mgo may be from about 2 . 20 to about 2 . 50 . in an embodiment , the ratio of sio 2 / mgo , in the produced synthetic layered silicate , may be about 2 . 25 to about 2 . 40 . in other embodiments , the sio 2 / mgo ratio , in the produced synthetic layered silicate , may be about 2 . 3 to about 2 . 35 . the lithium compound may be added in amounts such that the lithium content in solution may be from about 100 % to about 300 % above the value of the lithium content required to provide the cation of the layered silicate . the lithium content , in the produced synthetic layered silicate , in some embodiments , may be from about 0 . 3 % to about 2 . 2 %. in an embodiment , the lithium content , in the produced synthetic layered silicate , may be about 0 . 35 % to about 1 . 0 %. in other embodiments , the lithium content , in the produced synthetic layered silicate may be about 0 . 5 % to about 0 . 85 %. the reaction solution may be maintained at a temperature greater than about 25 ° c . the solution may be stirred during the reaction period at rates below about 1000 rpm and , in other embodiments , at rates below about 200 rpm . the entire aqueous suspension in which the precipitate may be formed may be subjected to a hydrothermal treatment . the hydrothermal treatment may be conducted such that the entire aqueous suspension may be heated for a period of greater than about 1 hour at temperatures greater than about 100 ° c . an autoclave may be used . the material produced may be filtered , washed , and dried . a synthetic layered silicate may be prepared using magnesium carbonate as a starting material , rather than generating magnesium carbonate during the manufacturing process . in an embodiment , a water - soluble lithium compound may be added to an amount of water under the same conditions as previously described . the magnesium carbonate may be added to the lithium compound solution . a silicate solution amount may be added such that the sio 2 / mgo ratio , in the produced synthetic layered silicate , may be from about 2 . 20 to about 2 . 50 . in an embodiment , the silicate solution amount may be added such that the sio 2 / mgo ratio , in the produced synthetic layered silicate , may be from about 2 . 25 to about 2 . 40 . in other embodiments , the silicate solution amount may be added such that the sio 2 / mgo ratio , in the produced synthetic layered silicate , may be from about 2 . 3 to about 2 . 35 . the mixture may be processed as described herein . in an embodiment , an acid toilet bowl cleaner may be produced with a synthetic layered silicate as described herein . an acid toilet bowl cleaner formulation may include water , a synthetic layered silicate , a polymer , an acid , and surfactants . surfactants may be provided to wet the surface of the bowl quickly and assist in cleaning performance . non - limiting examples of suitable nonionic surfactants that may be used in an embodiment are as follows : ( 1 ) the polyethylene oxide condensates of alkyl phenols . these compounds include the condensation products of alkyl phenols having an alkyl group with about 6 to 12 carbon atoms in either a straight chain or branched chain configuration with ethylene oxide , the ethylene oxide being present in an amount equal to 5 to 25 moles of ethylene oxide per mole of alkyl phenol . the alkyl substituent in such compounds may be derived , for example , from polymerized propylene , diisobutylene and the like . examples of compounds of this type include nonyl phenol condensed with an average of 9 . 5 moles of ethylene oxide per mole of nonyl phenol ; dodecylphenol condensed with an average of 12 moles of ethylene oxide per mole of phenol ; dinonyl phenol condensed with an average of 15 moles of ethylene oxide per mole of phenol ; and diisooctyl phenol condensed with an average of 15 moles of ethylene oxide per mole of phenol . ( 2 ) the condensation products of aliphatic alcohols with about 1 to about 25 moles of ethylene oxide . the alkyl chain of the aliphatic alcohol may either be straight or branched , primary or secondary , with about 8 to about 22 carbon atoms . a 12 - 15 carbon alcohol may be ethoxylated with an average of 3 - 15 moles of ethylene oxide . examples of such ethoxylated alcohols include , but are not limited to , the condensation product of myristyl alcohol condensed with an average of 10 moles of ethylene oxide per mole of alcohol ; the condensation product of an average of 9 moles of ethylene oxide with coconut alcohol ( a mixture of fatty alcohols with alkyl chains varying in length from about 10 to 14 carbon atoms ); and the condensation product of undecanol with an average of about 7 moles of ethylene oxide . ( 3 ) the condensation products of ethylene oxide with a hydrophobic base formed by the condensation of propylene oxide with propylene glycol . the hydrophobic portion of these compounds may have a molecular weight of from about 1500 to 1800 and exhibit water insolubility . the addition of polyoxyethylene moieties to this hydrophobic portion may increase the water solubility of the molecule as a whole , and the liquid character of the product may be retained up to the point where the polyoxyethylene content may be about 50 % of the total weight of the condensation product , which corresponds to condensation with up to about 40 moles of ethylene oxide . ( 4 ) the condensation of ethylene oxide with the product resulting from the reaction of propylene oxide and ethylenediamine . the hydrophobic moiety of these products include the reaction product of ethylenediamine and excess propylene oxide , the moiety having a molecular weight of from about 2500 to about 3000 . this hydrophobic moiety may be condensed with propylene oxide to the extent that the condensation product contains from about 40 % to about 80 % by weight of polyoxyethylene and has a molecular weight of from about 5 , 000 to about 11 , 000 . ( 5 ) amido amine oxide compounds . examples of amido amine oxides , which may be useful in an embodiment , include , but are not limited to , cocoamidopropyl amine oxide , isostearylamidopropyl amine oxide , isostearylamidopropyl morpholine oxide , lauramidopropyl amine oxide , minkamidopropyl amine oxide , oleoamidopropyl amine oxide , olivamidopropyl amine oxide , sesamidopropyl amine oxide , stearamidopropyl amine oxide , wheat germ amidopropyl amine oxide , or mixtures thereof . the nonionic surfactant may generally be present at a level of about 0 . 05 % to about 50 % by weight . the nonionic surfactant may be a 12 - 15 carbon alcohol , ethoxylated with an average of about 3 - 15 moles of ethylene oxide and may be about 1 % of the cleaner . cationic surfactants may be used in an embodiment . cationic surfactants include , but are not limited to , quaternary ammonium salts of the general formula : wherein the r groups coupled to the nitrogen are long or short hydrocarbon chains , typically alkyl , hydroxyalkyl or ethoxylated alkyl groups , and x is a solubilizing anion . examples include , but are not limited to , coconut trimethyl ammonium chloride or bromide , coconut methyl dihydroxyethyl ammonium chloride or bromide , decyl triethyl ammonium chloride , decyl dimethyl hydroxyethyl ammonium chloride or bromide , c 12 - 15 dimethyl hydroxyethyl ammonium chloride or bromide , coconut dimethyl hydroxyethyl ammonium chloride or bromide , myristyl trimethyl ammonium methyl sulfate , lauryl dimethyl benzyl ammonium chloride or bromide , di - alkyl imidazolines , or mixtures thereof . the cationic surfactant may be present at a level of about 0 . 05 % to about 50 % by weight . anionic surfactants may be used in an embodiment . examples of anionic surfactants include , but are not limited to , alkyl benzene sulfonates , having an alkyl chain length of c 8 - c 15 , primary and secondary alkyl sulfates such as c 8 - c 15 primary alkyl sulfates , alkyl ether sulfates , olefin sulfonates ; alkyl xylene sulfonates ; dialkyl sulfosuccinates ; fatty acid ester sulfonates , primary or secondary alcohol sulfates , wherein the linear or branched primary alcohol sulfates have 10 to 20 carbon atoms , or mixtures thereof . the anionic surfactants may be present at a level of about 0 . 05 % to about 50 % by weight . additional surfactants may be found in u . s . pat . no . 6 , 221 , 831 to emery , et al . and u . s . pat . no . 6 , 204 , 234 to herbots , et al ., both of which are incorporated herein by reference . the acids include , but are not limited to , organic acids such as acetic , citric , lactic , tartaric acid , glycolic acid , or mixtures thereof . other acids include , but are not limited to , hydrochloric acid and sulfamic acid . in an embodiment , a carboxylic acid may be a hydroxy monocarboxylic acid having up to 4 carbon atoms . in an embodiment , the acid content in the cleaner may be from about 1 % to about 50 % by weight of the formulation . a synthetic layered silicate as described herein , may be added to the toilet bowl cleaner to enable the cleaner to cling to the sidewalls of the toilet bowl . having the cleaner cling to the toilet bowl maximizes the time that the cleaner may be in contact with the lime scale and other deposits . if no thickener is used , the cleaner may run down the side of the toilet bowl too quickly , without effectively cleaning the surface . other ingredients such as ph adjusters , stabilizing agents , preservatives , fragrances and / or dyes may be included in the liquid cleaning composition . stabilizing agents may be included to achieve phase stability , ph balance and other desired characteristics . commonly used stabilizing agents include , but are not limited to , monoethanolamine , diethanolamine , triethanolamine , or mixtures thereof . in an embodiment , the ph of the liquid cleaner may be in the range of about 1 to about 4 . agents for controlling the ph may be included . examples include , but are not limited to , carbonates , bicarbonates , mono , di and triethanolamine , alkali metal hydroxides , or mixtures thereof . water may provide the balance of the liquid cleaning composition . in an embodiment , about 50 % to about 99 % water , by weight of the formulation , may be added . fragrance may be added in an amount of up to about 1 %. further information on toilet bowl cleaners may be found in u . s . pat . no . 6 , 153 , 572 to stamm , which is incorporated herein by reference . in an embodiment , a gel cleaner may be formulated with a synthetic layered silicate , as described herein , and with similar materials as in the toilet bowl cleaner . other polymers and co - polymers may be added to increase the viscosity , such that the gel may remain stable when the gel is applied to a surface . u . s . pat . no . 5 , 977 , 050 to faris , which is incorporated herein by reference , provides additional information on gel cleaner formulations . an oven cleaner may be formulated with a synthetic layered silicate as described herein . in an embodiment , water , synthetic layered silicate , polymer , solvent , alkali metal hydroxide , and tetrapotassium pyrophosphate may be mixed to make an oven cleaner . in an embodiment , about 2 % of the synthetic layered silicate may be dispersed in sufficient water to provide a final water content , in the oven cleaner composition , of about 30 % to about 50 %. tetrapotassium pyrophosphate may be added at about 0 . 05 % to about 0 . 15 %, by weight of water , in the oven cleaner composition . alkali metal hydroxide may be added at about 10 % to about 25 %, by weight of water , in the oven cleaner composition . other components may be added , such as , but not limited to , surfactants , solvents , and / or fragrances . further formulations and details may be found in u . s . pat . no . 3 , 779 , 933 to eisen and u . s . pat . no . 5 , 919 , 312 to wierenga et al ., both of which are incorporated herein by reference . the synthetic layered silicate , as described herein , may be formulated into a toothpaste composition . in an embodiment , a toothpaste may be formulated to provide anti - caries and anti - plaque characteristics . sorbitol , at about 25 % to about 35 %, by total weight of the formulation , may be added to water along with about 0 . 1 % to about 0 . 5 % synthetic layered silicate . the final amount of water in the formulation may be about 10 % to about 50 %, by weight of the formulation . silica may be added to the formulation at about 10 % to about 30 % by weight of water , and the remainder of the formulation may include a fluoride compound for anti - caries activity , flavorings , anti - bacterial additives , and / or anti - plaque additives . the fluoride compounds include , but are not limited to , sodium fluoride , potassium fluoride , sodium monofluorophosphate , stannous fluoride , or mixtures thereof . tetrasodium pyrophosphate may be added as an anti - plaque compound . anti - bacterial toothpaste formulations include , but are not limited to , 2 , 4 , 4 ′- trichloro - 2 ′- hydroxydiphenyl ether ( triclosan ) or 2 , 2 ′- dihydroxy - 5 , 5 ′- dibromo - diphenyl ether . additional information on formulations may be found in u . s . pat . no . 5 , 525 , 330 to gaffar , et al ., which is incorporated herein by reference . a drilling fluid may be formulated with a synthetic layered silicate as described herein . in an embodiment , an aqueous calcium chloride solution , a synthetic layered silicate , a weighting agent ( e . g . barium sulfate ), and / or other viscosifiers , fluid loss agents , and / or surfactants may be used in the drilling fluid . additional synthetic layered silicate may be added to the formulation if the drilling fluid contacts a salt formation . if the drilling fluid &# 39 ; s ionic content increases , the additional layered synthetic silicate may be helpful in maintaining viscosity of the drilling fluid . additional formulations and uses for synthetic layered silicates may be found in u . s . pat . no 6 , 025 , 303 to keilhofer , et al . and u . s . pat . no . 6 , 022 , 833 to mueller , et al ., both of which are incorporated herein by reference . a glass cleaner may be formulated with a synthetic layered silicate , as described herein , to produce a non - drip glass cleaner . in an embodiment , about 0 . 5 % to about 1 . 5 % synthetic layered silicate , by weight of the formulation , may be dispersed in water . about 2 % to about 10 % of an alcohol , by weight of the formulation , may be added to the synthetic layered silicate dispersion . examples of an alcohol include , but are not limited to , methanol , ethanol , 1 - propanol , isopropanol , butanol , or mixtures thereof . an oil emulsifier may be added at about 0 . 5 % to about 10 %, by weight of the formulation . examples of oil emulsifiers include , but are not limited to , an ammonia solution , butoxyethanol , propylene glycol , ethylene glycol , ethylene glycol polymers , polyethylene , methoxypolyethylene glycols , or mixtures thereof . a surfactant may be added to the formulation at about 0 . 1 % to about 1 % by weight of the formulation . this formulation may provide a non - drip , streak - free composition for surface and glass cleaning . other formulations may be found in u . s . pat . no . 4 , 315 , 828 to church and u . s . pat . no . 5 , 798 , 324 to svoboda , both of which are incorporated herein by reference . a synthetic layered silicate , as described herein , may be formulated into a paint composition . in an embodiment , about 3 pounds to about 10 pounds of water may be added to about 55 pounds to about 65 pounds of resin . examples of resins include , but are not limited to , ( meth ) acrylic acid , 2 - hydroxyethyl ( meth ) acrylate , ( meth ) acrylic acid amideimides having a hydroxyl group , such as 1 , 1 - dimethyl - 1 -( 2 - hydroxypropyl ) amine ( meth ) acrylimide , 1 , 1 - dimethyl - 1 -( 2 ′- phenyl - 2 ′- hydroxyethyl ) amine ( meth ) acrylimide , 1 , 1 - dimethyl - 1 -( 2 ′- hydroxy - 2 ′- phenoxypropyl ) amine ( meth ) acrylimide , or mixtures thereof . about 2 pounds to about 5 pounds of propylene glycol , about 20 pounds to about 30 pounds of titanium dioxide , about 0 . 1 pounds to about 0 . 5 pounds of synthetic layered silicate may be added to the resin water mixture . in an embodiment , defoamers , dispersants and / or wetting agents may be added . additional paint formulations may be found in u . s . pat . no . 5 , 905 , 109 to shimizu , et al ., which is incorporated herein by reference . a synthetic layered silicate , as described herein , may be formulated into a water - based printing ink composition . in an embodiment , a polymeric resin binder may be added to water , followed by the addition of a water - soluble resin binder to produce a water / binder mixture . a water - soluble rosin salt resin and an aqueous emulsion resin polymer may be added to the water / binder mixture . a rewetting agent , pigment , soybean oil , and the synthetic layered silicate may be added to the ink composition . compositions for printing inks may be found in u . s . pat . no . 6 , 200 , 372 to krishnan , et al ., which is incorporated herein by reference . the following examples serve to illustrate methods of producing a synthetic layered silicate . the examples should not be considered limiting . examples 1 and 2 are for comparative purposes and examples 3 , 4 and 5 are according to an embodiment . the following tests were used in the examples to characterize the synthetic layered silicate material . a 2 . 5 % by weight dispersion of the synthetic layered silicate in demineralized water was prepared and left to stand for 24 hours . the dispersion was then diluted to 2 % by weight synthetic layered silicate concentration with pre - determined aliquots of electrolyte and demineralized water . viscosity measurements were taken after a total of 48 hours since first mixing . the effect of an electrolyte on the dispersion of the synthetic layered silicate may be related to the viscosity measurements . the viscosity measurements were conducted using a brookfield dvii viscometer . the electrolyte tolerance of examples 1 - 5 were determined using sodium sulfate as the electrolyte . the rate of hydration of a 2 % by weight dispersion of the synthetic layered silicate in demineralized water containing tetra - sodium pyrophosphate was assessed by measuring the time taken for the optical density of the dispersion to reduce to a specified value . the hydration rate may be defined as this time expressed in tenths of a minute . if the optical density had not reached the specified value after 20 minutes the hydration rate was expressed as the absorbance value at a wavelength of 550 nm using a 4 cm cell at that time . the optical density of a 2 % by weight dispersion of the synthetic layered silicate in tetra - sodium pyrophosphate solution was measured at 550 nm using a 4 cm cell . the measurement was made 24 hours after the preparation of the dispersion ; it was normally performed on the dispersion retained from the above hydration rate test . table 1 provides the quantities of reactants used in the preparation of examples 1 - 5 . [ 0065 ] table 3 comparison of lithium carbonate added as reactant ( in grams ) and lithium content in final product as % by weight li example example example example example 1 2 3 4 5 lithium 2 . 2 5 . 6 11 . 2 16 . 8 22 . 4 carbonate lithium 0 . 35 0 . 50 0 . 59 0 . 66 0 . 74 [ 0066 ] table 4 hydration rate and clarity of product from examples 2 - 5 example 2 example 3 example 4 example 5 hydration rate 1 . 35 1 0 . 25 1 175 0 . 79 1 clarity 37 . 1 27 . 3 20 . 4 9 . 3 [ 0067 ] table 5 visacosity ( cp ) at 10 meq na / g of synthetic layered silicate example example example example example 1 2 3 4 5 viscosity flocculated 211000 108050 571000 182500 ( cp ) example 1 was prepared following the procedure in u . s . pat . no . 4 , 049 , 780 , example 2 , which is incorporated herein by reference . example 2 was prepared using the following procedure and the quantities of reactants listed in table 1 . the li 2 co 3 , 5 . 6 g , was dispersed in 168 g of water with agitation for 1 hour at ambient temperature . water ( 269 g ) was added to the lithium carbonate solution , followed by addition of 187 g of mgso 4 . 7h 2 o . the magnesium sulfate was allowed to dissolve for a few minutes and then the solution was heated to 60 ° c . in a separate container , 75 g of na 2 co 3 was dissolved in 300 g of water . the sodium carbonate solution was then added to the solution mixture of the lithium carbonate and magnesium sulfate over a period of 30 minutes , maintaining a temperature of 60 ° c . the sodium silicate solution ( 525 g ) was added to the mixture of the magnesium sulfate , sodium carbonate and lithium carbonate over a period of 50 minutes , maintaining the temperature at 60 ° c . the resulting aqueous slurry was then heated to 98 ° c ., and maintained at this temperature for 2 hours , condensing the vapor and returning the condensate to the aqueous slurry . the slurry was heated at 202 ° c . for 6 hours . the resulting hydrous magnesium silicate was separated by filtration , washed and dried . example 2 represents a procedure in which the quantity of lithium compound used was only the stoichiometric amount needed to produce an atomic ratio equivalent to 8 atoms of silicon to 6 atoms of magnesium to 1 atom of lithium in the starting recipe . example 3 was prepared following the procedure in example 2 , except that the reactant quantities were changed example 4 was prepared following the procedure in example 2 , except that the reactant quantities were changed . example 5 was prepared following the procedure in example 2 , except that the reactant quantities were changed . referring to fig1 and corresponding table 5 , examples 3 , 4 and 5 have a much greater tolerance to the presence of an electrolyte when compared to example 1 . example 2 has improved tolerance to the presence of electrolyte , but this product has other disadvantages to examples 3 , 4 and 5 . table 2 is the oxide analysis of examples 1 - 5 . table 3 is a comparison of the amount of lithium carbonate in the reactants compared to the amount of lithium present in example 1 - 5 . table 4 indicates the hydration rate and clarity of the products from examples 2 - 5 . the hydration rate and clarity data for examples 3 - 5 indicate superior performance compared to example 2 . further modifications and alternative embodiments of various aspects of the invention will be apparent to those skilled in the art in view of this description . accordingly , this description is to be construed as illustrative only and is for the purpose of teaching those skilled in the art the general manner of carrying out the invention . it is to be understood that the forms of the invention shown and described herein are to be taken as the presently preferred embodiments . elements and materials may be substituted for those illustrated and described herein , parts and processes may be reversed , and certain features of the invention may be utilized independently , all as would be apparent to one skilled in the art after having the benefit of this description of the invention . changes may be made in the elements described herein without departing from the spirit and scope of the invention as described in the following claims .
a synthetic layered silicate material may be produced which exhibits tolerance to high levels of electrolytes and surfactants as measured by viscosity , hydration rate and clarity . the synthetic layered silicate material may produce similar or improved rheological properties when compared to natural hectorite at comparable or lower addition rates in select aqueous systems .