particulate material ( which can be one material or a combination of materials ) useful in the present invention is substantially insoluble in aqueous liquid and organic liquid such as water and ethyl acetate and in the elution liquid . not more than 1 . 0 gram of particulate will dissolve in 100 g . of aqueous or organic liquid or elution solvent into which particulate is mixed at 20 ° c . the particulate material can be at least one of an organic polymer such as polydivinylbenzene , or a copolymer , preferably a copolymer of styrene and divinylbenzene ( 75 - 25 to 99 . 99 - 0 . 01 ), or poly ( meth ) acrylic acid esters , and derivatives thereof , particularly those containing ion - exchange groups such as sulfonated or aminated groups . suitable optional particles for the purposes of this invention include any particle which can be coated with aqueous - or organic - insoluble , non - swellable sorbent material or the surface ( external and / or internal ) of which can be derivatized to provide a coating of insoluble , non - swellable sorbent material . optional particles include inorganic oxide particles such as silica , alumina , titania , zirconia , and other ceramics to which are covalently bonded organic groups . preferred inorganic oxide particulate materials are silica and zirconia because they are commercially available , with silica being particularly preferred because of the ease in bonding a variety of hydrophobic and hydrophilic ligands and coatings onto its surface . the insoluble , aqueous non - swellable sorbent coatings generally have a thickness in the range of one molecular monolayer to about 100 nanometers . such particles having coated surfaces are well known in the art , see , for example , snyder and kirkland , &# 34 ; introduction to modern liquid chromatography &# 34 ;, 2d ed ., john wiley & amp ; sons , inc . ( 1979 ) and h . figge et al ., &# 34 ; journal of chromatography &# 34 ; 351 ( 1986 ) 393 - 408 and include modified silica particulate , silica particles having covalently bonded thereto organic groups , preferably cyanopropyl , cyclohexyl , phenyl , c 2 ( ethyl ), c 4 ( butyl ), c 8 ( octyl ), and c 18 ( octadecyl ) groups . coatings which can be applied to inorganic particulate can be either thin mechanical coatings of insoluble , non - swellable polymers such as crosslinked silicones , polybutadienes , etc . or covalently bonded organic groups such as aliphatic groups of varying chain length ( e . g ., c 2 , c 4 , c 8 , and c 18 ) and organic groups including aliphatic and aromatic groups . preferred groups include amino , cyano , hdyroxyl , phenyl , cyclohexyl , chiral , and other groups which alter the polarity of the coating . the silica , or other support particle , in this case acts primarily as a carrier for the organic coatings and the particles are non - swellable . many such coated particles are commercially available ( e . g ., c 18 bonded phase silica , alltech , deerfield , ill ., or varian sample preparation products , harbor city , calif .). variation in chemical composition of the coatings can provide selectivity in molecular separations and polarity . __________________________________________________________________________particularly preferred particulate for use in the present inventioninclude : material particle size trademark available from__________________________________________________________________________highly crosslinked 50 - 100 micrometers amberchrom ™ cg - 161m supelco , inc ., styrene and divinyl - bellefonte , pabenzene copolymers , high performancematerial * highly crosslinked 50 - 100 micrometers amberchrom ™ cg - 71m supelco , inc ., methacrylic resin , bellefonte , pahigh performancematerial * highly crosslinked 220 - 830 micrometers amberlite ™ xad - 2 supelco , inc ., styrene and divinyl - ( ground to average bellefonte , pabenzene copolymer * size about 50 micro - meters ) highly crosslinked 220 - 830 micrometers amberlite ™ xad - 7 supelco , inc ., methacrylic copolymer * ( ground to average bellefonte , pa size about 50 micro - meters ) octadecyl - bonded 8 micrometers c . sub . 18 ™ varian samplesilica preparation products , harbor city , ca__________________________________________________________________________ * disclosed in one or more of u . s . pat . nos . 4 , 501 , 826 ; 4 , 382 , 124 ; 4 , 297 , 220 ; 4 , 256 , 840 ; 4 , 224 , 415 any of the particulate material may have a spherical shape , a regular shape or an irregular shape . particulate material which has been found useful in the invention has an apparent size within the range of 0 . 1 to about 150 micrometers , preferably in the range of 0 . 1 to 100 micrometers , more preferably 1 to 100 micrometers . it has been found advantageous in some instances to employ particulate materials in two or more particle size ranges falling within the broad range . as an example , particles having an average size in the range of 0 . 1 - 30 micrometers having chromatographic activity may be employed in combination with particles having an average size in the range 1 to 150 micrometers acting as a property modifier . some particle size reduction may take place during high shear mixing and calendering operations , depending upon the friability of the particulate material . thus , while the particulate material initially may be rather large , it may ultimately be reduced to a finer size in the final product . in some instances , particle size reduction may be necessary before mixing . particles useful in the present invention have water sorptive capacity less than 25 % by weight , preferably less than 5 % by weight , compared to particle weight . as noted above , particles which undergo dimensional changes due to water swellability are less desirable because they can cause dimensional changes , such as wrinkling , in the article . more than one type of active sorbent particles useful in the present invention can be pre - mixed in any proportion , the total sorptive particules being present in the range of more than 30 up to 100 weight percent of at least one of organic polymeric particles , preferably 35 to 100 weight percent , more preferably 50 to 100 weight percent organic polymeric particles , and 0 to 70 weight percent of total particulate of porous organic - coated or uncoated inorganic particles , preferably 0 to 65 weight percent , and more preferably 0 to 50 weight percent porous organic - coated or uncoated inorganic particles . other non water - swellable property modifiers may be advantageously added to the mixture of the ptfe aqueous dispersion and the primary particulate material to provide further improvement in or modification of the composite articles of the invention . for example , modifier particulate can include chromatographically inactive materials such as low surface area glass beads to act as property modifiers and processing aids . coloring or fluorescing particulate can be added at low levels ( up to 10 weight percent of particulate ) to aid in visualizing sample components to be separated . chemically active particulate which indicate ph or acidity of the component bands can be useful for diagnostic purposes . a limited amount of water - swellable property modifiers ( i . e ., up to 30 weight percent , preferably less than 25 weight percent , more preferably less than 10 weight percent , and most preferably less than 1 weight percent , of total particulate ) can be useful as a processing aid . representative swellable property modifiers include starch , chitosan , modified starches such as sephadex ™ and sepharose ™ ( pharmacia , sweden ), agarose , polyacrylamides , cellulosics , and coated particles ( e . g ., silica coated with a polyacrylamide ). water - swellable but insoluble materials may be used as a thin coating on non - swellable particulate . when the particulate is hydrophobic , the preferred method of manufacture of the article of the invention utilizes an emulsion of ptfe with a masking agent added to modify the hydrophobic particle surface / water interaction and to allow rapid wetting of the surface of the hydrophobic particulate . preferred masking agents are polar organic compounds such as alcohols , amines , acids , etc . with the preferred agent being alcohols due to their efficacious removability as by solvent extraction or drying after formation of the article . specifically , the ptfe composite sheet material of the invention is prepared by blending the particulate or combination of particulates employed with a ptfe emulsion until a uniform dispersion is obtained and adding a volume of process lubricant up to approximately one half the volume of the blended particulate . blending takes place along with sufficient process lubricant to exceed sorptive capacity of the particles in order to generate the desired porosity level of the resultant article . preferred process lubricant amounts are in the range of 3 to 200 percent by weight in excess of that required to saturate the particulate , as is disclosed in u . s . pat . no . 5 , 071 , 610 . the aqueous ptfe dispersion is then blended with the particulate / masking agent mixture to form a mass having a putty - like or dough - like consistency . the sorptive capacity of the solids of the mixture is noted to have been exceeded when small amounts of water can no longer be incorporated into the mass without separation . care should be taken to ensure that the ratio of water to masking agent does not exceed 3 : 1 . this condition should be maintained throughout the entire mixing operation . the putty - like mass is then subjected to intensive mixing at a temperature and for a time sufficient to cause initial fibrillation of the ptfe particles . preferably , the temperature of intensive mixing is up to 90 ° c ., preferably it is in the range of 0 ° to 90 ° c ., more preferably 20 ° to 60 ° c . minimizing the mixing at the specified temperature is essential in obtaining extraction media and chromatographic transport properties . mixing times will typically vary from 0 . 2 to 2 minutes to obtain the necessary initial fibrillation of the ptfe particles . initial mixing causes partial disoriented fibrillation of a substantial portion of the ptfe particles . initial fibrillation generally will be noted to be at an optimum within 60 seconds after the point when all components have been fully incorporated into a putty - like ( dough like ) consistency . mixing beyond this point will produce a composite sheet of inferior extraction medium and chromatographic properties . devices employed for obtaining the necessary intensive mixing are commercially available intensive mixing devices which are sometimes referred to as internal mixers , kneading mixers , double - blade batch mixers as well as intensive mixers and twin screw compounding mixers . the most popular mixer of this type is the sigma - blade or sigma - arm mixer . some commercially available mixers of this type are those sold under the common designations banbury mixer , mogul mixer , c . w . brabender prep mixer and c . w . brabender sigma blade mixer . other suitable intensive mixing devices may also be used . the soft putty - like mass is then transferred to a calendering device where the mass is calendered between gaps in calendering rolls preferably maintained at a temperature up to 125 ° c ., preferably in the range of 0 ° to about 100 ° c ., more preferably in the range of 20 ° to 60 ° c ., to cause additional fibrillation of the ptfe particles of the mass , and consolidation while maintaining the water level of the mass at least at a level of near the sorptive capacity of the solids , until sufficient fibrillation occurs to produce the desired extraction medium . preferably the calendering rolls are made of a rigid material such as steel . a useful calendering device has a pair of rotatable opposed calendering rolls each of which may be heated and one of which may be adjusted toward the other to reduce the gap or nip between the two . typically , the gap is adjusted to a setting of 10 millimeters for the initial pass of the mass and , as calendering operations progress , the gap is reduced until adequate consolidation occurs . at the end of the initial calendering operation , the resultant sheet is folded and then rotated 90 ° to obtain biaxial fibrillation of the ptfe particles . smaller rotational angles ( e . g ., 20 ° to less than 90 °) may be preferred in some extraction and chromatographic applications to reduce calender biasing , i . e ., unidirectional fibrillation and orientation . excessive calendering ( generally more than two times ) reduces the porosity which in turn reduces the solvent wicking rate in tlc and the flow - through rate in the filtration mode . during calendering , the lubricant level of the mass is maintained at least at a level of exceeding the absorptive capacity of the solids by at least 3 percent by weight , until sufficient fibrillation occurs and to produce porosity or void volume of at least 30 % and preferably 40 to 70 % of total volume . the preferred amount of lubricant is determined by measuring the pore size of the article using a coulter porometer as described in the examples below . increased lubricant results in increased pore size and increased total pore volume as is disclosed in u . s . pat . no . 5 , 071 , 610 . the calendered sheet is then dried under conditions which promote rapid drying yet will not cause damage to the composite sheet or any constituent therein . preferably drying is carried out at a temperature below 200 ° c . the preferred means of drying is by use of a forced air oven . the preferred drying temperature range is from 20 ° c . to about 70 ° c . the most convenient drying method involves suspending the composite sheet at room temperature for at least 24 hours . the time for drying may vary depending upon the particular composition , some particulate materials having a tendency to retain water more than others . the resultant composite sheet preferably has a tensile strength when measured by a suitable tensile testing device such as an instron ( canton , mass .) tensile testing device of at least 0 . 5 mpa . the resulting composite sheet has uniform porosity and a void volume of at least 30 % of total volume . the ptfe aqueous dispersion employed in producing the ptfe composite sheet of the invention is a milky - white aqueous suspension of minute ptfe particles . typically , the ptfe aqueous dispersion will contain about 30 % to about 70 % by weight solids , the major portion of such solids being ptfe particles having a particle size in the range of about 0 . 05 to about 0 . 5 micrometers . the commercially available ptfe aqueous dispersion may contain other ingredients , for example , surfactant materials and stabilizers which promote continued suspension of the ptfe particles . such ptfe aqueous dispersions are presently commercially available from dupont de nemours chemical corp ., for example , under the trade names teflon ™ 30 , teflon ™ 30b or teflon ™ 42 . teflon ™ 30 and teflon ™ 30b contain about 59 % to about 61 % solids by weight which are for the most part 0 . 05 to 0 . 5 micrometer ptfe particles and from about 5 . 5 % to about 6 . 5 % by weight ( based on weight of ptfe resin ) of non - ionic wetting agent , typically octylphenol polyoxyethylene or nonylphenol polyoxyethylene . teflon ™ 42 contains about 32 to 35 % by weight solids and no wetting agent but has a surface layer of organic solvent to prevent evaporation . it is generally desirable to remove , by organic solvent extraction , any residual surfactant or wetting agent after formation of the article . silica is available from aldrich chemical co . ( milwaukee , wis .). zirconia is available from z . tech corporation ( bow , n . h .). other inorganic oxides are commercially available ( aldrich chemical co .). the present invention provides a novel composite structure and method therefore , the composite structure preferably being a uniformly porous , composite sheet comprised of non water - swellable sorptive particles distributed uniformly throughout a matrix formed of interentangled , fibrillated ptfe fibrils . in such a structure almost all of the particles are separate one from another and each is isolated in a cage that restrains the particle on all sides by a fibrillated mesh of ptfe microfibers . the preferred novel sheet of the invention has a thickness in the range of 125 to 10 , 000 micrometers and preferably has a tensile strength of at least 0 . 5 mpa and even as high as 13 . 6 mpa . the article is substantially uniformly porous , making it suited for use in separation science . more particularly , it can be used in solid phase extraction , and as a chromatographic composite article which can be used as a single self - supporting sheet or a combination of sheets to form a stack or as a composite film adhered to a support such as glass , paper , metals , or polymers . the ptfe - particulate media technology can be useful in a first mode wherein the composite article of the invention is used for preconcentration and isolation of certain materials for further analysis by high resolution column chromatography . in this mode , which is well known in the art and commonly called solid phase extraction , solvent and sample flow are introduced at an angle of 90 degrees to the surface of the sheet . this is a conventional configuration and the separation path length is equal to the thickness of the sheet . the path length can be increased by stacking additional layers ( media ) which may be the same or of different composition but the individual layers are not intimately bound together . this mode is effective for one step or multi step adsorption - desorption separations . this mode is effective using reactive particulate such as non - swellable ion exchange materials or sorptive particulate in the direct or reverse phase modes . the article strongly adsorbs the component of interest onto the active ( non - swellable ) particulate in the composite and undesirable components are washed out with a first solvent . a more effective eluting solvent is then used to displace the desired component from the particulate allowing it to be recovered in a more concentrated and unified form . the composite extraction and chromatographic articles of the invention can be of a variety of sizes and shapes . preferably the articles can be sheet - like materials which , for example , can be in disk or strip form . the composite articles have utility in a wide variety of separations wherein the choice of the particulate material is useful for size controlled filtration or steric exclusion , for simple one step or multistep adsorption - desorption separations of specific components , for immobilization of particulate to perform ion - exchange conversion and isolation of cations and anions , for purification of materials , and for chromatographic separations and analyses in both passive and forced flow modes , for hydrophobic reverse phase and direct phase chromatography . this invention discloses the discovery of a solid phase extraction ( spe ) disk / sheet composite material and a method which is effective , for example , in removing relatively polar compounds such as certain pollutants from liquid and gas samples . solid phase extraction is a technique wherein solid particulate such as polymeric materials , silica , alumina , or zirconia , etc ., coated with insoluble polymeric phases or covalently bonded organic ligands are used to preferentially adsorb organic compounds from liquids or gases for isolation purposes . representative polar and semi - polar compounds described in the examples below are an explosive ( 1 , 3 , 5 , 7 - tetranitro ,- 1 , 3 , 5 , 7 - tetraazacyclooctane ) ( hmx ), an explosive impurity ( dinitrotoluene ), and a series of phenolic compounds such as phenol , o - cresol , 2 - nitrophenol , 4 , 6 - dinitro - o - cresol , 2 , 4 - dichlorophenol , 2 , 4 , 5 - trichlorophenol , and 2 , 4 , 6 - trichlorophenol , which are pollutants in water and which are of environmental concern . representative pesticides , generally considered semi - polar compounds , which can be recovered from aqueous liquids include atrazine , alachlor , and diazinon . these compounds are commonly extracted from water using liquid / liquid ( lle ) extractions , described in epa method 608 , 625 , etc . it is highly desirable to replace liquid - liquid extraction ( lle ) methods with solid phase extraction ( spe ) materials and methodology to reduce or eliminate extraction solvent usage , extraction time , and environmental hazards . this invention discloses using a hybrid of column particle and membrane technologies to provide a means of overcoming the deficiencies of conventional methods with substantial savings in time and cost . the extraction medium of the present invention is also useful to extract certain polar contaminants such as phenols from a nonpolar liquid such as hexane . solid phase extractions of polar compounds from water samples are known to result in low recoveries because of the unfavorable partition coefficients of the compounds between water and the conventional non - polar stationary solid phases such as c 18 - bonded silica . this is particularly true when large volumes of water are used , where the volume of sample is larger than the breakthrough volume of the specific compound . breakthrough volume is defined as that volume in which the capacity of the sorbent particle bed for a particular contaminant is exceeded allowing passage of the extractant without efficient sorption . more specifically , it is the volume at which the contaminant ( extracted material ) can be detected in the exit stream from the extraction medium . prior art methods of overcoming the problem of inadequate recovery are : ( 1 ) to use smaller sample volumes of less than the breakthrough volume , ( 2 ) accept low recovery data , and designate the results as &# 34 ; semi - quantitative &# 34 ;, or ( 3 ) include an additive in the water sample , such as sodium chloride , to shift the partition coefficient in favor of the solid phase . none of these solutions are particularly attactive . ideally , polar compounds can be isolated using the same conditions as those used for the less polar pollutants , thus providing a universal spe method and spe media for many pollutants including the less polar pesticides , polychlorinated biphenyls ( pcbs ) and polynuclear aromatic hydrocarbons ( pahs ) as well as the more polar pesticides , phenolics , and explosive residues . it has been found advantageous where combinations of contaminants are to be extracted to use a stack of disks ( e . g ., 2 to 5 or more ) with one or more types of particulate chosen , each having optimum extraction efficiency for individual contaminants . choice of elution solvents depends on contaminants and extraction particulate . in fig1 stack of disks 10 contains disks 12 and 14 which can be identical or they can contain different particulate so as to have different selectivities for different contaminants . in fig2 similarly , stack of disks 20 , made of disks 22 , 24 , 26 , 28 , and 30 , each of which can be the same or can contain different particulate so as to provide an effective separations medium . extraction media of the present invention are particularly useful to isolate polar , semi - polar , and nonpolar organic contaminants from fluids ( gases and liquids ). in particular , residues of explosives , phenolic compounds , and organic acids are common contaminants of soil , air , water , and can be efficiently removed , concentrated , or isolated using the teachings of the present invention . the isolations can be performed on an analytical scale or in large scale applications . objects and advantages of this invention are further illustrated by the following examples , but the particular materials and amounts thereof recited in these examples , as well as other conditions and details , should not be construed to unduly limit this invention . data of this example show increased recoveries of contaminants in a solid phase extraction application using articles ( disks ) of the present invention compared to disks comprising conventional bonded silica particulates enmeshed in a ptfe matrix . a . ( comparative ) a disk was prepared as follows : ten grams of c 18 bonded silica ( analytichem int ., harbor city , calif .) was placed in a 100 ml beaker . this particle has a lubricant sorptive capacity approximately 75 percent of particle weight . 1 . 6 grams of polytetrafluoroethylene ( ptfe ) resin emulsion ( teflon ™ 30b , e . i . dupont , inc ., wilmington , del .) was added stepwise in three portions with intermittent vigorous stirring . this provided a c 8 bonded silica to ptfe ratio of 90 / 10 . the temperature can be up to 90 ° c ., preferably in the range of 0 ° to 90 ° c ., more preferably about 23 ° c . lubricant was added ( 10 . 5 grams ) stepwise in three portions with intermittent vigorous stirring . after these ingredients have been thoroughly mixed , a semi - coherent material was formed with enough physical integrity to allow the entire contents of the beaker to be removed as a single mass . the above mass was passed between two rollers kept at 50 ° c . it is also possible to maintain the rollers up to 125 ° c ., preferably 0 ° to 100 ° c ., more preferably 20 ° to 60 ° c ., and spaced about 0 . 5 cm apart to give a strip of cohesive material . the resulting strip was folded to three thicknesses and then passed through the rollers after a 90 degree rotation from the previous pass . the cyclic process of folding and re - rolling in a direction 90 ° from the direction of the previous pass was repeated multiple times to give a tough , strong , flat piece of material . the material was then calendered along the long axis via a series of roller passes with roller spacing adjusted to successively smaller distances apart to give a continuous ribbon . the ribbon was folded to give a multi - layer piece which was then calendered as before along the axis 90 ° from the calendering direction used previously . the calendered sheet of material was then allowed to dry in air for 48 hours . one hundred ml portions of reagent water were fortified individually with a set of compounds at concentations of from 0 . 5 to 20 mg / l ( ppm ), passed through the disks , which were then eluted with acetonitrile ( to recover the concentrated contaminant compounds extracted from the water ), and subsequently analyzed by high pressure liquid chromatography ( hplc ). data are shown in table i , below . these results on disks of c 18 - bonded silica particulate enmeshed in ptfe were the best obtained from several particulates , including cyano , cyclohexyl , and c 8 - bonded silica ( c 18 - bonded and c 8 - bonded silicas were available from varian sample preparation products , harbor city , calif .). the first column ( a ) shows the data obtained using no additives in the water , except the usual 0 . 5 % ( vol / vol ) methanol / water used to promote &# 34 ; wetting &# 34 ; of the c 18 - bonded silica disks . second column ( b ) shows the data using the same disk , but with 3 . 5 % ( wt / vol ) sodium chloride added to the water . column c shows the data without sodium chloride but with the ph of the water adjusted to 2 , and the data in column d show the effect of a ph of 2 and 25 % ( wt / vol ) sodium chloride . data of table i illustrate the positive effect of addition of sodium chloride to shift partitioning of the contaminant from the water to the solid phase sorbent particulate and adjustment of the ph to suppress ionization of the phenolics . recoveries of the explosive hmx and phenol were low from the 100 ml sample of water , even with high concentrations of salt and ph adjustment steps , indicating that breakthrough or incomplete sorption had occurred . b . ( present invention ) sorbent particles obtained from supelco , bellefonte , pa ., were incorporated into the ptfe matrix using the following procedure : to prepare disks the following procedure was used : twenty grams of styrene divinylbenzene copolymer ( amberchrom cg - 161m ) were placed in a 100 ml beaker . ten grams of polytetrafluoroethylene ( ptfe ) resin emulsion ( fluon ™, ici americas , inc ., wilmington , del .) was added stepwise in three portions with intermittent vigorous stirring . this provided a copolymer to ptfe ratio of 90 / 10 . the temperature can be up to 90 ° c ., preferably in the range of 0 ° to 90 ° c ., more preferably about 23 ° c . fifty - five grams of lubricant ( water / isoproanol 70 / 30 ) was added stepwise in three portions with intermittent vigorous stirring . after these ingredients had been thoroughly mixed , a semi - coherent material was formed with enough physical integrity to allow the entire contents of the beaker to be removed as a single mass . the above mass was passed between two rollers kept at 38 ° c . it is also possible to maintain the rollers up to 125 ° c ., preferably 0 ° to 100 ° c ., more preferably 20 ° to 60 ° c ., and spaced about 0 . 5 cm part to give a strip of cohesive material . the resulting strip was folded to three thicknesses and then passed through the rollers after a 90 degree rotation from the previous pass . the cyclic process of folding and re - rolling in a direction 90 ° from the direction of the previous pass was repeated multiple times to give a tough , strong , flat piece of material . the material was then calendered along the long axis via a series of roller passes with roller spacing adjusted to successively smaller distances apart to give a continuous ribbon . the ribbon was folded to give a multi - layer piece which was then calendered as before along the axis 90 ° from the calendering direction used previously . the calendered sheet of material was then allowed to dry in air for 24 hours . the resulting disks , cut to the appropriate size from the sheet , were used for the extraction under the same conditions used for table i , but without any additives to the water except 0 . 5 % methanol . the sorbent particles were amberchrom ™ cg - 161m ( supelco , bellefonte , pa . ), which is a relatively large - particle ( 50 - 100 um ) styrene - divinyl benzene resin . 100 ml of water was extracted as shown above , but without acid or sodium chloride , 0 . 5 % ( vol / vol ) methanol / water was added in all cases . additionally , the usual acetonitrile elution was followed by two - 1 ml ethyl acetate elutions of the disk . ethyl acetate is less polar than acetonitrile and is a more effective eluting solvent than acetonitrile . results of this trial are given in table ii , below . data in column e is from amberchrom cg - 161m resin , 100 ml water samples with no salt or acid , extracted in 24 min . data in column f is the same , but using 1000 ml water samples , extracted in 30 min . data obtained and listed in columns g and h used the same volumes and conditions as e , but the 100 ml samples were passed through the 47 mm disk in 12 and 72 seconds , respectively . in all cases , elution was accomplished by using the normal acetonitrile solvent , following with two - 1 ml portions of ethyl acetate solvent added directly to the disk . data from table ii show that amberchrom cg - 161m resin particles with an elution solvent stronger ( stronger in the sense of being less polar ) than acetonitrile [ relative polarities of solvents are given in l . r . snyder , journal of chromatography , 92 , 223 , ( 1974 ), and l . r . snyder , journal of chromatographic science , 16 , 223 , ( 1978 )] can give quantitative recoveries of the phenols without addition of acid or salt . this is in contrast to data shown in table i , columns b , c , and d , wherein improved recoveries required salt and / or acid added to the sample liquid . in addition , the data show that these recoveries using media of the invention containing styrene - divinyl benzene resin are strongly dependent on flow rate , indicating kinetics that may be somewhat slow compared to those of conventional c 18 silica , in which it is possible to process a liter of water in less than 2 minutes with 100 % recoveries . this flow rate dependence could be either a function of the relatively large particle size of the amberchrom cg - 161m resin , the structure of the relatively loose ( porous ) disk , or perhaps is a basic property of the resin &# 39 ; s pore structure and / or sorptive interaction . data from the one liter sample ( column f ) also show a surprisingly high capacity of the disk for these compounds . when the percent recoveries shown in column f are multiplied by the total weight of these contaminant compounds fortified into the one liter water sample , the resulting number is the total weight of contaminants retained on the disk . approximately 60 mg of contaminants were retained on the 240 mg disk . this weight of contaminants is 25 percent of the disk &# 39 ; s weight , which is much higher than the usual 5 percent by weight capacity often cited for c 18 bonded silica . table i______________________________________ ( comparative ) % recoverycontaminant a b c d______________________________________hmx 5 5 12 9phenol 4 5 7 23o - cresol 20 26 40 942 - nitrophenol 35 33 62 902 , 6 - dinitrotoluene 97 100 99 974 , 6 - dinitro - o - cresol 14 35 96 942 , 4 - dichlorophenol 106 115 95 922 , 4 , 5 - trichlorophenol 108 112 94 922 , 4 , 6 - trichlorophenol 110 116 94 92______________________________________ table ii______________________________________ % recoverycontaminant e f g h______________________________________hmx 122 51 36 55phenol 90 19 28 49o - cresol 120 50 40 622 - nitrophenol 108 85 52 802 , 6 - dinitrotoluene 113 102 66 934 , 6 - dinitro - o - cresol 96 60 47 732 , 4 - dichlorophenol 107 88 56 864 , 6 - dinitro - o - cresol 96 60 47 732 , 4 , 5 - trichlorophenol 95 93 61 872 , 4 , 6 - trichlorophenol 96 95 62 89______________________________________ a similar set of trials ( using disks prepared as in example 1 , a and b ) was run to evaluate recoveries of the set of compound of example 1 using stacked disks of the invention . the trial used 100 ml water samples with no acid or salt , and the disks indicated below were stacked one on top of the other and then put in place on the filtration apparatus . elution was accomplished using two 5 - ml portions of acetonitrile solvent , rinsing the glassware , followed by two 1 - ml portions of ethyl acetate elution solvent directly onto the disk . results are given in table iii , below . column i shows the data using c 18 - covalently bond silica on top of the amberchrom cg - 161m resin - containing disk , and eluted with both solvents . column j is the data from the c 18 - bonded silica disk on top of the amberchrom cg - 161m resin disk , but eluted with only the two 5 ml portions of acetonitrile . column k is the bottom amberchrom cg - 161m resin disk , separated from the top c 18 - bonded silica disk and eluted with both solvents . column l is the top c 18 bonded silica disk , separated from the amberchrom cg - 161m resin disk and eluted with both solvents . the disks from k and l were run stacked together for the extraction step and disks from k and l were then separated for the elution step . data in column m is the sum of the data in columns k and l , which is the total recovery from the separately eluted disks . there are some surprising results from using stacked disks . first , data of column j of table iii show that acetonitrile solvent eluted the hydrophobic compounds from the c 18 disk through the amberchrom cg - 161m resin disk . second , and more importantly , stacking the disks and then separately eluting them individually gave additional information about the types of compounds in each eluting fraction as shown in columns k and l of table iii . if a compound was well retained on the top c 18 - bonded silica disk , it was inferred that it was relatively hydrophobic or nonpolar . if , on the other hand , a compound was unretained on the upper c 18 - bonded silica disk , but quantitatively retained on the lower amberchrom cg - 161m resin disk , it was inferred that the compound was relatively polar or hydrophilic . in a further step a ratio can be made of the recovery from the c 18 disk to the recovery from the amberchrom cg - 161m disk as a qualitative confirmation of the compound &# 39 ; s identity . the ratio for the peak from the unknown compound can be compared to the ratio for a known reference compound . this ratio would provide a useful second piece of evidence relating to a compound &# 39 ; s identity from the chromatographic peak in addition to the retention data and could be used in either gas chromatography ( gc ) or hplc . for this ratio to be effective , the c 18 disk must be used on top of the amberchrom cg - 161m disk , or all of the compounds would be retained on the top amberchrom cg - 161m disk , giving no additional information to the analyst . column n ( comparative ) lists the data from two c 18 disks , stacked one on top of the other , and eluted with acetonitrile solvent only . data shown in column n from the stacked c 18 disks show a recovery of the poorly retained compounds that was about twice the recovery from a single c 18 disk ( table i , column a ). these data illustrate the utility of using stacked disks as a way to increase recovery and breakthrough volume for poorly retained compounds . in addition , stacked disks can double the capacity of a filtration / extraction trial for samples which have high levels of dissolved organics or are heavily polluted . finally , the bottom disk of a set of disks can be used to detect an overloading of or breakthrough from the top disk , thus indicating that the analytical data is suspect ( the latter is quite common in air sampling , where sampling tubes have backup sections to detect breakthrough ). table iii______________________________________ % recoverycontaminant i j k l m n______________________________________hmx 94 109 81 12 93 17phenol 78 94 55 10 65 18o - cresol 91 118 48 34 82 692 - nitrophenol 89 104 35 47 82 772 , 6 - dinitrotoluene 91 112 -- 89 89 994 , 6 - dinitro - o - cresol 41 80 41 21 62 292 , 4 - dichlorophenol 89 101 -- 88 88 992 , 4 , 5 - trichlorophenol 86 99 -- 86 86 982 , 4 , 6 - trichlorophenol 89 97 -- 88 88 96______________________________________ for 4 , 6 - dinitro - o - cresol it would appear a lower ph would provide more efficient extraction . amberchrom ™ cg - 71m resin , an acrylic resin bead ( supelco , bellefonte , pa . ), was evaluated using the contaminants and procedures of example 1b except that the particles were amberchrom cg - 71m and the amount of lubricant was 40 g . also tested were disks in which there was a blend of particles : 20 % amberlite xad - 2 : 80 % c 18 - bonded silica . the particles were homogeneously blended into the disk with about 90 % particles and 10 % ptfe . the 100 ml water samples contained no acid or salt . the elution was accomplished using both acetonitrile and ethyl acetate solvents , as described in example 1 . the results are shown in table iv . data in column p is from amberchrom ™ 71 resin ; data in column q is from the amberlite xad - 2 / c 18 blend . data of table iv show recoveries were good for the amberchrom ™ 71 resin . table iv______________________________________ % recovery p o______________________________________hmx 101 29phenol 85 18o - cresol 125 752 - nitrophenol 108 1022 , 6 - dinitrotoluene 116 1114 , 6 - dinitro - o - cresol 65 312 , 4 - dichlorophenol 103 1032 , 4 , 5 - trichlorophenol 106 1042 , 4 , 6 - trichlorophenol 106 104______________________________________ to conclude the trials on polar compounds , the compounds which worked so well on the c 18 - bonded silica disks ( prepared as in example 1a ), i . e ., pesticides , were tested with the amberchrom cg - 161m particle - containing disks ( prepared as in example 1b ) and amberchrom cg - 71m resin particle - containing disks ( prepared as in example 3 ) to see if amberchrom cg - 161m and amberchrom cg - 71m resin disks could be used for a series of pollutants or organic compounds in water , with a wide range of polarity and functionality . the size of the water sample was one liter which was fortified with about 100 μg / l of the three pesticides shown in table v . the water was filtered / extracted rather slowly , since the kinetics of the separation were assumed to be slow with the large resin particles . one liter was filtered in about 2 hours . the elution was done using two 3 - ml portions of acetonitrile solvent followed by two 1 - ml ethyl acetate solvent on the disk . the only additive in the water was the usual 0 . 5 % methanol for &# 34 ; wetting &# 34 ; purposes . results are shown in table v . column r data are from a production c 18 - bonded silica disk ( varian sample preparation products , harbor city , calif .). column s data are from an amberchrom cg - 71m resin disk , and column t data are from an amberchrom cg - 161m resin disk . data of table v show amberchrom cg - 161m and cg - 171m resin disks work as well as the c 18 - bonded silica disks for the pesticides , which were chosen for their different functionalities . table v______________________________________ % recovery rcontaminant comparative s t______________________________________atrazine 94 88 92alachlor 92 96 135diazinon 99 98 102______________________________________ a 25 mm × 0 . 5 mm diameter disk containing macroporous 3 - 10 micrometer crosslinked styrene - divinylbenzene copolymer ( sarasep , inc ., santa clara , calif .) was placed in a stainless steel holder and used to sample air , as is common practice ( see astm method d 4861 - 88 ). the disks were prepared using the procedure of example 1b except the weight of particulate was 32 g , the weight of ptfe emulsion was 16 g , and the weight of lubricant water / isopropanol 50 : 50 was 40 g . five hundred nanograms each of five common organophosphorus pesticides were placed in a vapor generator and the vapors were drawn through the disk using a positive - pressure nitrogen flow at a sampling rate of one liter per minute for 18 hours and 30 minutes , making a total volume of 1110 liters . the disk was then removed from the 25 mm holder and placed in the bottom of a beaker along with 1 ml of ethyl acetate . after 30 minutes with occasional swirling , the ethyl acetate , which had desorbed the pesticides from the disk , was analyzed by gas chromatography with a nitrogen - phosphorus detector . the sampling efficiency ( percent recovery ) was determined by comparing the peak areas of the sample to those of standards . results are shown in table vi . with the exception of malathion , which is known to degrade under these conditions , the recoveries indicate that the disk with the crosslinked styrene - divinylbenzene copolymer particulate is effective as an air sampling medium . this represents a major advance in the practice of air sampling , since the standard procedure outlined in the astm procedure ( above ) calls for large amounts of solvent to pre - extract impurities from the standard polyurethane foam sorbent , and large amounts of solvent to extract the contaminants from the polyurethane foam sorbent after sampling . by using the disk as described above , which uses only a few ml of solvent to pre - extract impurities and one ml of solvent to extract the contaminants , the amount of solvent , time , and labor used can be reduced . various modifications and alterations of this invention will become apparent to those skilled in the art without departing from the scope and spirit of this invention , and it should be understood that this invention is not to be unduly limited to the illustrative embodiments set forth herein .