in the practice of this invention , sand , preferably gravel packing sand , is directed into a washed out area adjacent to a wellbore that penetrates a hydrocarbonaceous fluid producing zone . the washed out area extends circumferentially from the wellbore into the formation which causes an increased possibility that the wellbore will collapse . gravel is placed into the washed out area by directing sand through perforations in a casing until the washed out area is filled with the sand . a method which can be used for gravel packing a well is discussed in u . s . pat . no . 4 , 945 , 991 which issued to jones on aug . 7 , 1990 . this patent is hereby incorporated by reference herein . after the washed - out area has been packed by sand , sand is consolidated by forming a silica cement in - situ while a desired permeability is retained in the sand within the consolidated washed out area . a silica cement is formed and binds sand within the washed out area which is sufficient to preclude formation fines or sand from being produced to the surface along with hydrocarbonaceous fluids . as is known by those skilled in the art , core samples taken from the formation containing the washed - out area can be used to determine the extent to which the agent must be applied . a method for determining the saturation characteristics of a porous material is disclosed in u . s . pat . no . 4 , 381 , 665 which issued to levine et al . on may 3 , 1983 . this patent is hereby incorporated by reference herein . in order to form the silica cement , as shown in the drawing , an aqueous hydroxide slug is injected into well 10 where it enters formation 12 via perforations 14 . as the aqueous hydroxide slug proceeds through formation 12 , it saturates the sand - packed area and near wellbore area of the formation . after saturating the sand - packed area with the aqueous hydroxide solution selected from a member of the group consisting of an organoammonium hydroxide , ammonium hydroxide or alkali metal hydroxide , a spacer volume of a water - immiscible hydrocarbonaceous liquid 16 is next injected into the sand - packed area . hydrocarbonaceous liquids for use herein comprise paraffinic and aromatic liquids . paraffinic liquids are preferred . this spacer volume of water - immiscible hydrocarbonaceous liquid is selected from a member of the group consisting of mineral oils , naphthas , c 5 - c 40 alkanes , and mixtures thereof . the water - immiscible hydrocarbonaceous fluid used as a spacer volume may be of an industrial grade . utilization of the spacer volume should be kept to a minimum in order to keep as much of the organoammonium hydroxide , alkali metal or ammonium hydroxide as possible in spaces between the sand grains in the formation . by keeping the maximum amount of said hydroxide between sand grains , a stronger and more imperious silica cement will be formed . a spacer volume of the hydrocarbonaceous liquid is used to remove excess hydroxide from between the sand grains while allowing a thin hydroxide film to remain on the surface to obtain a subsequent cementing reaction with an injected alkylpolysilicate solution . afterwards , a slug containing a water - miscible organic solvent with an alkylpolysilicate 18 mixed therein is injected into the formation whereupon it displaces any spacer volume of solution remaining therein . the water - miscible organic solvent is selected from a member of the group consisting of methanol , ethanol , higher alcohols , glycols , ketones , tetrahydrofuran , and dimethyl sulfoxide . this organic solvent can be of an industrial grade . as the aqueous hydroxide solution and the alkylpolysilicate meet , they react simultaneously to form a silica cement between the sand grains . the cementing reaction takes place so as to bind sand grains in the formation thereby forming a consolidated porous zone 22 . although the sand grains are consolidated , a porous cement is formed which results in a substantially high retention of the formation &# 39 ; s permeability . retention of the formation &# 39 ; s permeability allows alkylpolysilicate slug 18 to move continually through the formation while cement is being formed between sand grains . injection of the alkali metal hydroxide slug , spacer volume 16 and alkylpolysilicate slug 18 containing alkylpolysilicate can be continued until enough cement has been formed to exclude formation fines and sand . as will be understood by those skilled in the art , this amount of cement is formation dependent and may vary from formation to formation . core samples obtained from the interval to be treated can be tested to determine the required amount of cement . u . s . pat . no . 4 , 549 , 608 which issued to stowe et al . teaches a method of sand control where clay particles are stabilized along the face of a fracture . this patent is incorporated by reference herein . in order to increase the cement &# 39 ; s consolidation strength , the concentration of the organoammonium hydroxide , alkali metal hydroxide or ammonium hydroxide contained in an aqueous solution slug or the alkylpolysilicate contained in the solvent slug can be increased . similarly , the flow rates of each of these slugs through the higher permeability zone can be decreased to obtain better consolidation strength . a decreased flow rate is particularly beneficial for increasing the consolidation strength when the alkylpolysilicate slug &# 39 ; s flow rate is decreased . as will be understood by those skilled in the art , optimal concentrations and flow rates are formation dependent . therefore , optimal concentrations and flow rates should be geared to field conditions and requirements . organoammonium hydroxides which can be used in an aqueous solution include those having c 1 through c 10 alkyl or aryl groups , including those with other hetero atoms . tetramethylammonium hydroxide is preferred . the alkali metal hydroxide which is utilized herein comprises sodium , potassium , or lithium . sodium and potassium are the preferred alkali metal hydroxides for use herein . sodium hydroxide is most preferred . the concentration of the alkali metal hydroxide solution , organoammonium hydroxide , or ammonium hydroxide is about 20 to about 60 wt . percent , preferably about 30 wt . percent . as will be understood by those skilled in the art , the exact concentration should be determined for each application . in general , concentrated hydroxide solutions result in greater permeability reduction due to higher contents of solids which form in the consolidated washed - out area . alkylpolysilicate ( eps ) contained in the organic solvent solution is the hydrolysis - condensation product of alkylorthosilicate according to the reaction equation below : ## str1 ## where n ≦ 2 r = c 1 - c 10 r should be ≦ 10 carbons for good solubility and high sio 2 content . tetramethyl ( tms ) or tetraethylorthosilicates ( teos ) are preferred . mixed alkylorthosilicate can also be used . it is desirable to obtain an alkylpolysilicate with n & gt ; 0 . 5 , preferably n greater than 1 . as n increases , the sio 2 content increases , resulting in stronger consolidation . it is desirable to use an alkylpolysilicate with a silica content of 30 % or more , preferably about 50 wt . %. eps which is used herein is placed into one of the water - miscible organic solvents mentioned above . the preferred solvent is ethanol . of course , other alcohols can be used . eps , tms , teos , or other alkylpolysilicates are contained in the solvent in an amount of from about 10 to about 100 weight percent sufficient to react with the hydroxide contained in the aqueous solution . twenty ( 20 ) to about eighty ( 80 ) wt . percent is preferred . although alcohol is the solvent preferred because of its versatility and availability , other water - miscible organic solvents can be utilized . these solvents , as previously mentioned , include methanol and higher alcohols , glycols , ketones , tetrahydrofuran , and dimethyl sulfoxide . the viscosity of the silicate in the solvent can also determine the extent to which it will enter a higher permeability zone . in those cases where it is not possible to control the viscosity of the silicate contained in the solvent and preclude entry into a lower permeability zone , a mechanical packer may be used . the silica cement which is formed can withstand ph &# 39 ; s less than about 7 and temperatures up to and in excess of about 1 , 000 ° c . ( 1 , 832 ° f .). once enough cement has been formed to exclude formation fines , hydrocarbonaceous fluids can be produced from formation 12 into well 10 . alternatively , an enhanced oil recovery ( eor ) process can be instituted in formation 12 via well 10 . eor processes which can be utilized include steam - flooding , water - flooding , carbon dioxide stimulation and fire - flooding . steam - flooding processes which can be utilized when employing this cemented gravel - pack described herein are detailed in u . s . pat . nos . 4 , 489 , 783 and 3 , 918 , 521 which issued to shu and snavely , respectively . u . s . pat . no . 4 , 479 , 894 that issued to chen et al . describes a water - flooding process which may be used herein . fire - flooding processes which can be utilized herein are disclosed in u . s . pat . nos . 4 , 440 , 227 and 4 , 669 , 542 which issued to holmes and venkatesan , respectively . these patents are hereby incorporated by reference herein . a carbon dioxide eor process which can be used after forming the gravel pack is disclosed in u . s . pat . no . 4 , 513 , 821 which issued to w . r . shu on apr . 30 , 1985 . this patent is hereby incorporated by reference herein . although the present invention has been described with preferred embodiments , it is to be understood that variations and modifications may be resorted to without departing from the spirit and scope of this invention , as those skilled in the art readily understand . such variations and modifications are considered to be within the purview and scope of the appended claims .