while the present invention has been described with references to preferred embodiments , various changes or substitutions may be made on these embodiments by those ordinarily skilled in the art pertinent to the present invention with out departing from the technical scope of the present invention . therefore , the technical scope of the present invention encompasses not only those embodiments described above , but also all that fall within the scope of the appended claims . approximating language , as used herein throughout the specification and claims , may be applied to modify any quantitative representation that could permissibly vary without resulting in a change in the basic function to which it is related . accordingly , a value modified by a term or terms , such as “ about ”, is not limited to the precise value specified . in at least some instances , the approximating language may correspond to the precision of an instrument for measuring the value . range limitations may be combined and / or interchanged , and such ranges are identified and include all the sub - ranges included herein unless context or language indicates otherwise . other than in the operating examples or where otherwise indicated , all numbers or expressions referring to quantities of ingredients , reaction conditions and the like , used in the specification and the claims , are to be understood as modified in all instances by the term “ about ”. as used herein , the terms “ comprises ,” “ comprising ,” “ includes ,” “ including ,” “ has ,” “ having ” or any other variation thereof , are intended to cover a non - exclusive inclusion . for example , a process , method , article or apparatus that comprises a list of elements is not necessarily limited to only those elements , but may include other elements not expressly listed or inherent to such process , method article or apparatus . one embodiment of the present invention is directed to a process for reducing the fouling of microfiltration systems that is used in water treatment processes . in operation , the water to be treated is collected or obtained from its source , and subjected to treatment by a cationic coagulant prior to its being directed to a raw water pond or holding tank . as shown in fig1 , which is a block diagram of a prior art process , water proceeds from an inlet water source 100 , to a raw water pond 110 or other holding tank . the water is held at the pond , to allow for settling of solids and contaminants . thereafter , the water proceeds from the raw water pond 110 , and is split into two streams , one which proceeds to a microfiltration system 120 , where it is filtered and then on to collection as treated water 130 . the second stream of water that leaves the holding tank 110 , is treated with a coagulant 140 prior to being subjected to the clarifier 150 , and then on to the cooling tower 160 , or other intended use . in an alternate embodiment , the second stream of water is treated with a coagulant 140 and then proceeds directly on to its use , such as a cooling tower , without being subjected to a clarifier . this known process differs from one embodiment of the presently claimed process in that water is obtained form an inlet water source 200 and is immediately treated with a coagulant 210 prior to proceeding on to a raw water pond 220 . the remainder of the process of treatment is similar to that known in the industry . the water in the raw water pond 220 proceeds and is split into two streams , one of which is treating with a second coagulant 250 prior to proceeding onto a functional or point of use , such as in a cooling tower 270 . these stream may be subjected to a clarifier 260 prior to proceeding on to a point of use , such as a cooling tower . the second stream of water from the raw water pond 220 , proceeds to the microfiltration system 230 and then on as treated water 240 . in prior processes , it has not been the general practice to use water - soluble coagulants or flocculants in water treatment processes , except after the water has already passed through a microfiltration system , or as is shown in fig1 , in a stream that does not proceed through the microfiltration system . this is due to the fact that it has been generally understood that the use of such a coagulant actually increases the fouling of microfiltration systems and other membranes , and results in dramatic decreases in membrane or microfiltration system flux . in an alternate embodiment , the filtration system is an ultrafiltration system instead of the microfiltration system . however , we have found that by using cationic coagulants , particularly those which are an organic and inorganic cationic polymer blend , the microfiltration system performs more efficiently and lowers the times required to clean the microfiltration system at levels of up to about 95 %. additional benefits have also been found by introduction of a coagulant at prior to the microfiltration or ultrafiltration system in the process . in particular , there is better color removal from the influent water , improved turbidity removal , low aluminum carryover and low dosage requirements . the input or influent water may come from a multitude of possibilities ; some examples include but are not limited to , rivers , ponds and industrial wastewater . the inlet water is directed to a holding facility or tank , such as but not limited to a raw water pond , wherein it is held for varying amounts of time , depending on the process conditions and the facility . the cationic coagulant can be one of many available coagulants . in particular , cationic polymers have been found to be useful . cationic polymer means a polymer having an overall positive charge . the cationic polymers of this invention include polymers composed of cationic and nonionic monomers . cationic polymers of this invention include , but are not limited to , solution polymers , emulsion polymers , and dispersion polymers . inorganic and organic cationic polymer blends have been found to be useful in one embodiment of the invention , for example klaraid ckp 1348 ™ ( ge betz canada , inc ., mississauga , ontario , canada ). for cationic polymers that are blends of organic and inorganic polymers , the blend comprises from about 10 to about 50 % organic polymers , and in an alternate embodiment , comprises from about 15 to about 25 % organic materials . inorganic polymers include , for example , polyaluminum chloride , and organic polymers include , for example , tannins . the high charge density of this particular product results in outstanding removal of inorganic and organic colloids , oily solids and color - causing contaminants in water treatment systems . in another embodiment the cationic coagulant is a blend of organic polymers . in one embodiment of this invention , the coagulant added prior to the raw water pond or holding tank , the initial coagulant is the same as the second coagulant , which is added subsequent to the raw water pond or holding tank . in some embodiments , this second coagulant is added prior to a clarifier . in an alternate embodiment , the initial coagulant differs from the second coagulant . the initial coagulant is added in an amount of from about 20 to about 120 ppm . as stated above , additional benefits are derived from the use of the initial coagulant in the process . the color of the water to be treated decreases drastically , from about 80 to about 100 % of the color is removed , optimally , from about 94 to about 100 % removal takes place from the addition of the initial cationic coagulant . the addition of the initial cationic coagulant also has a beneficial effect on the turbidity of the input water . addition of the initial cationic coagulant decreases the turbidity levels to from about 2 to about 10 % of the initial values , preferably from about 3 to about 7 % of the initial value . another benefit received from a present embodiment is the limited amount of aluminum carryover , amounts of less than about 0 . 3 ppm to less than about 0 . 1 ppm . the foregoing may be better understood by reference to the following example , which are presented for purposes of illustration and are not intended to limit the scope of this invention . raw water from a river was collected and measured for turbidity , color , total organic carbon ( toc ) and aluminum carryover , as compared to the same water with various dosages of two different cationic coagulants , polyaluminum chloride ( pac ) and klaraid cdp 1348 ™ ( ge betz canada , inc ., mississauga , ontario , canada ). the results are shown in the following tables . klaraid cdp 1348 ™ exhibited the best overall results , including best color removal , and lowest aluminum carryover . as shown , the optimal dosage for this coagulant was at a 30 to 40 % lower level than pac . while the present invention has been described with references to preferred embodiments , various changes or substitutions may be made on these embodiments by those ordinarily skilled in the art pertinent to the present invention with out departing from the technical scope of the present invention . therefore , the technical scope of the present invention encompasses not only those embodiments described above , but also all that fall within the scope of the appended claims .