the present invention proposes a process for making wet - wipes comprising a lotion composition . wet wipes or wipes or wet - tissues or body wipes is the general term to describe a piece for material , generally nonwoven material , used to cleanse body parts . in particular most of currently available wipes are intended for the cleaning of the peri - anal area after defecation . other wipes are available for the cleansing of the face or other body parts . the present invention focuses on wipes for peri - anal ( or perineal ) area but it not limited to that type of wet wipes . wet - wipes are generally of sufficient dimension to allow for a convenient handling while being small enough to be easily disposed to the sewage system . the material of the wipes ( so called “ substrate ”) is generally soft and flexible , potentially having a structured surface enhancing its cleaning performance . the material is preferably a non - woven material , generally made of synthetic compounds . however , woven materials as well as the use of natural compounds in either woven or nonwoven materials are within the scope of the present invention . in one embodiment of the present invention the substrate comprises a non - woven material comprising fibers selected from the group consisting of polyolefin , polyester , cellulose , rayon , polyamides , polyesteramide , polyvinyl alcohols , and combinations thereof . while in some wet - wipes the texture and material of the wipe are of high relevance to the performance of the wipe , the present invention however focuses on the formation of the composition impregnating the substrate to form the wet - wipes . wipes are generally impregnated with a liquid or semi liquid composition , intended to both enhance the cleaning and to provide for a smooth feeling . other ingredients or actives ( for example cosmetic or pharmaceutical active ) can be part of the composition . generally the composition is of sufficiently low viscosity to impregnate the entire structure of the wipe . in some other instances , the composition can be primarily present at the wipe surface and to a lesser extend in the inner structure of the wipe . in one optional embodiment the composition is releasably carried by the material , that is , the composition is contained either in or on a substrate and is readily releasable from the substrate by applying some force to the substrate , for example , wringing the substrate , or wiping a surface , such as a child &# 39 ; s bottom , with the wet - wipe . the compositions used in the process of the present invention include the concentrated oil - in - water emulsion composition and the diluted composition . diluting the former with water forms the latter . with , the exception of the water concentration the components of the diluted composition are the same as the corresponding concentrated oil - in - water emulsion composition . the diluted composition then impregnates the substrate to form the wet - wipe . the concentrated oil - in - water emulsion composition is interchangeably called lotion , soothing lotion , concentrated composition , soothing composition , cleansing or cleansing lotion or composition , emulsion , or emulsion composition . all those terms are hereby used interchangeably and indicate the , at least - dual basic function of the composition of the present invention : enhancing cleansing and delivering skin soothing effect . in most of its embodiments , the composition of the present invention comprises , but is not limited to : other ingredients may be incorporated into the composition these include , but are not limited to , are rheology modifiers , soothing agents and preservatives . common dictionaries define “ emollient ” as “ something that softens or soothes . their function in a wet - wipe include ( 1 ) to improve the glide of the wipe on the skin , by enhancing the lubrication and thus decreasing the abrasion of the skin , ( 2 ) to hydrate the residues ( for example fecal residues or dried urine residues ), thus enhancing their removal from the skin , ( 3 ) to hydrate the skin , thus reducing its dryness and irritation while improving its flexibility under the wiping movement , ( 4 ) to protect the skin from later irritation ( for example , caused by the friction of the underwear ) as the emollient is deposited onto the skin and remain at its surface as a thin protective layer . preferable emollients used by the process of the present invention are silicon based . silicones based emollients are organo - silicone based polymers with repeating silioxane ( si — o ) units . silicones based emollients of the present invention are hydrophobic and exist in a wide range of possible molecular weights . they include linear , cyclic and cross - linked varieties . silicone oils are generally chemically inert and usually have usually a high flash point . due to their low surface tension , silicone oils are easily spread able and have high surface activity . examples of silicon oil of the present invention include , but are not limited to : cyclomethicones , dimethicones , phenyl - modified silicones , alkyl - modified silicones , silicones resins , silica and combinations thereof . other emollients useful in the present invention include unsaturated esters or fatty esters , such as caprylic capric triglycerides in combination with bis - peg / ppg - 16 / 16peg / ppg - 16 / 16 dimethicone c 12 - c 15 alkylbenzoate . the amount of emollient that can be included in the lotion composition concentrate and in the diluted composition will depend on a variety of factors , including the particular emollient involved , and the lotion - like benefits desired , the other components in the lotion composition . in one embodiment , the concentrated composition comprises from about 75 % to about 99 % of the emollient , more preferably from about 80 % to about 94 %, and even more preferably from about 85 % to about 92 % of the emollient ( all % herein are weight to weight % unless otherwise specified ). also preferably the emollient of the present invention has a solubility parameter between about 5 and about 12 , more preferably between about 5 and about 9 . the concentrated composition and the diluted composition also include an emulsifier such as those are known in the art for forming oil - in - water emulsions . the emulsifier can be a mixture of chemical compounds and include a surfactant . the preferred emulsifiers are those acting as well as a surfactant . both terms , surfactant and emulsifier are used interchangeably in this document . mixtures of emulsifiers may be used . in the present invention , the surfactant is used as a solution of least about 25 % surfactant content ( w / w ). in one embodiment the surfactant is used as a pure form ( 100 % w / w ). the surfactant solutions of the present invention can be aqueous solution or non - aqueous solutions . the terms surfactant , emulsifier , surfactant solution are used herein interchangeably . the emulsifier can be a polymeric emulsifier . in one embodiment of the present invention the emulsifier has a viscosity of less than about 15 , 000 cps at about 25 degrees celsius of a 1 % aqueous solution of the emulsifier as measured by a brookfield apparatus as described in the method part of this document . more preferably the viscosity is less than about 10 , 000 cps under the same conditions . the emulsifier is employed in an amount effective to emulsify the emollient and non - water - soluble oils that are be present in the composition . in one embodiment of the present invention , the amount of emulsifier in the concentrated composition ranges from about 1 % to about 25 %, preferably from about 6 % to about 20 %, more preferably about 8 % to about 15 % ( based on the weight of emollient over the weight of the concentrated composition ). in one embodiment of the present invention , the concentrated composition has ratio between the amount of surfactant and emollient between about 1 : 9 and about 1 : 72 ( on a weight / weight basis ), more preferably between about 1 : 14 to about 1 : 30 ( w / w ). surfactant / emulsifiers having a low surface tension are preferred for the present invention . other characteristics of preferable surfactant / emulsifier include high polarity and a non - ionic nature . the composition of the claimed invention can optionally include an adjunct ingredient . the adjunct ingredient may include a wide range of additional ingredients such as , but not limited to perfumes , soothing agents , fragrances , preservative , rheology modifiers , moisturizers , texturers , colorants , medically active ingredients , in particular healing actives and skin protectants . combinations of adjunct ingredients are also within the scope of the present invention . soothing agent can be added to the composition of the present invention . soothing agents are compound having the ability to reduce the irritation or stinging effect of some chemicals . soothing agents can be of a variety of chemical classes . soothing agents can have a variety of mode of actions to neutralize the effects of the skin irritants especially for paraben based preservative systems . for example antioxidants can be soothing agents for oxidants . buffers can be soothing agents neutralizing the stinging effect on skin of acids or bases . it is to be noted that emollients can also be soothing agents . soothing agent acting against the stinging / irritation effect of some preservatives are preferred . those soothing agents can be emollients or surfactants helping , for example , the solubilization or the micellization of the preservatives . the preferred soothing agents of the present invention are ( a ) ethoxylated surface active compounds , more preferably those having a ethoxylation number below about 60 , and ( b ) polymers , more preferably polyvinylpirrolidone ( pvp ) and / or n - vinylcaprolactam homopolymer ( pvc ), and ( c ) phospholipids , more preferably phospholipids complexed with other functional ingredients as e . g ., fatty acids and organosilicones . optionally , the composition used by the process of the present invention can include a preservative or a mixture of preservatives . the need to control microbiological growth in personal care products is known to be particularly acute in water based products such as non - ionic oil - in - water emulsions and in pre - impregnated wipes such as baby wipes . the process of the present invention can comprises providing a preservative compound or more preferably a combination of preservative compounds acting together as a preservative system . preservative and preservative systems are used interchangeably in the present document to indicate one unique or a multiplicity of preservative compounds . as preservative it is understood a chemical or natural compound or a multiplicity of compounds reducing the growth of microorganisms , thus enabling a longer shelf life for the pack of wipes ( opened or not opened ) as well as creating a environment with reduced growth of microorganisms when transferred to the skin during the wiping process . the preservative of the present invention ( or preservative system ) can comprise one or more of the parabens class of preservatives . preferably the preservative is selected from the list of methylparaben , ethylparaben , propylparaben , butylparaben , isobutylparaben or a combination thereof . the total concentration of paraben preservatives encompassed by the present invention is preferably lower than about 1 %, more preferably lower than about 0 . 5 %, even more preferably lower than about 0 . 3 % ( it is to be noted that legal requirements may restrict those ranges in practice ). the minimum amount of paraben antimicrobial is any amount sufficient to obtain the desired preservation of the composition , in most embodiments of the invention more than 0 . 001 % ( w / w ). rheology modifiers are compounds that increase the viscosity of the composition at lower temperatures as well as at process temperatures . rheology modifiers or suspending agents or stabilizers also provide “ structure ” to the compositions to prevent settling out ( separation ) of insoluble and partially soluble components . other components or additives of the compositions may affect the temperature viscosity / rheology of the compositions . the effect and advantage of rheology modifiers are in particular described in us20020128621a1 entitled “ absorbent articles with simplified compositions having good stability ” published on sep . 12 , 2002 , filed on dec . 21 , 2001 , by kruchoski et al ., and us20020128615a1 entitled “ absorbent articles with non - aqueous compositions containing anionic polymers ” published on sep . 12 , 2002 , filed on dec . 22 , 2001 , by tyrrell et al . in addition to stabilizing the suspension of insoluble and partially soluble components , the rheology modifiers also help to stabilize the composition on the wipe and enhance the transfer of lotion to the skin : the wiping movement increases the shear and pressure therefore decreasing the viscosity of the lotion and enabling a better transfer to the skin as well as a better lubrication effect . additionally , the rheology modifier helps to preserve a homogeneous distribution of the composition within the wipe stack : any fluid composition has a tendency to migrate to the lower part of the wipes stack during prolonged storage . this effect creates an upper zone of the stack having less composition than the bottom part . this is seen as a sign of relatively low quality by the users . preferred rheology modifiers exhibit low initial viscosity and high yield . particularly suited for the present invention are rheology modifiers such as , but not limited to : blends of material as are available from uniqema gmbh & amp ; co . kg , of emmerich , germany under the trade name arlatone . particularly preferred are arlatone v - 175 which is a blend of sucrose palmitate , glyceryl stearate , glyceryl stearate citrate , sucrose , mannan , and xanthan gum , and arlatone v - 100 which is a blend of steareth - 100 , steareth - 2 , glyceryl stearate citrate , sucrose , mannan , and xanthan gum . blends of material as are available from seppic france of paris , france as simulgel . particularly preferred is simulgel ns which comprises blends of hydoxyethylacrylate / sodium acryloyldimethyl taurate copolymer and squalene and polysorbate 60 , sodium acrylate / sodium acryloyldimethyltaurate copolymer and polyisobutene and caprylyl capryl glucoside , acrylate copolymers , such as but not limited to acrylates / acrylamide copolymer , mineral oil , and polysorbate 85 . acrylate homopolymers , acrylate crosspolymers , such as but not limited to acrylate / c 10 - 30 alkyl acrylate crosspolymers , carbomers , such as but not limited to acrylic acid cross linked with one or more allyl ether , such as but not limited to allyl ethers of pentaerythritol , allyl ethers of sucrose , allyl ethers of propylene , and combinations thereof as are available as the carbopol ® 900 series from noveon , inc . of cleveland , ohio ( e . g ., carbopol ® 954 ). naturally occurring polymers such as xantham gum , galactoarabinan and other polysaccharides . combinations of the above rheology modifiers . examples , of commercially available rheology modifiers include but are not limited to , ultrez - 10 , a carbomer , and pemulen tr - 2 , an acrylate crosspolymers , both of which are available from noveon , cleveland ohio , usa , and keltrol , a xanthan gum , available from available from cp kelco san diego calif ., usa . when present rheology modifiers are typically present in the dilute composition at a weight / weight % ( w / w ) of preferably from about 0 . 01 % to about 3 %, more preferably from about 0 . 015 % to about 2 %, even more preferably from about 0 . 02 % to about 1 %. the concentrated composition of the present invention ( also called herein interchangeably concentrate , concentrate composition , concentrated emulsion , emulsion concentrate ) has a water content of less than about 30 % ( w / w ), preferably the water content is less than about 20 % ( w / w ), more preferably less than about 10 % ( w / w ). the minimum amount of water is , in most embodiments of the present invention , more than about 0 . 1 %. in one embodiment of the present invention the average particle size (= emollient droplet size ) is less than about 12 microns , more preferably less than about 10 , even more preferably less than about 5 microns , even more preferably still less than about 1 micron . to this corresponds an average particle size of the diluted composition having the same values , also some variation in the particle size can be observe during / after the dilution step . examples of compositions that can be manufactured by the process of the present invention are described in co - pending u . s . provisional patent application no . 60 / 520 , 031 entitled “ a composition for wet wipes that enhances the efficacy of cleansing while being gentle to the skin ” by george deckner et al ., procter & amp ; gamble attorney docket no . cm2755p2q and filed on nov . 14 , 2003 . in one embodiment of the present invention an article of commerce is provided . the article of commerce of the present invention typically comprises ( a ) a container as described herein , and ( b ) at least wet wipe as described herein . containers useful in the present article include but are not limited , for example , pet tubs , flow wrap pouches , precut sachets for individually packed cleansing mitt , and other packaging known in the art as suitable for a nonwoven article . additionally , the container can also be manufactured to facilitate removal of individual cleansing wet wipes . the container can be made of any suitable material or materials , and can be manufactured in any suitable manner . for example , the container can be made of polystyrene , polypropylene , pet , poet , polyethylene , polyester , polyvinyl alcohol , or the like . the containers may also be made of mixtures of materials . the containers can be manufactured by , for example , a vacuum molding process or an injection molding process , or any suitable process . additional information on containers , as well as additional option components for containers , including but not limited to : container bodies ; lids ; containers features , such as but not limited to , attachments of lids , hinges , zippers , securing means ; and the like , can be found in u . s . pat . nos . des 451 , 279 ; des 437 , 686 ; des 443 , 508 ; des 443 , 451 ; des 421 , 901 ; des 421 , 902 ; des 416 , 794 ; des 414 , 637 ; des 445 , 329 ; 3 , 982 , 659 ; 3 , 967 , 756 ; 3 , 986 , 479 ; 3 , 994 , 417 ; 6 , 269 , 970 ; 5 , 785 , 179 ; 5 , 366 , 104 ; 5 , 322 , 178 ; 5 , 050 , 737 ; 4 , 971 , 220 ; 6 , 296 , 144 ; 6 , 315 , 114 ; 4 , 840 , 270 ; 4 , 471 , 881 ; 5 , 647 , 506 ; 6 , 401 , 968 ; 6 , 269 , 969 ; 6 , 412 , 634 ; 5 , 791 , 465 ; 6 , 092 , 690 ; and 6 , 092 , 690 ; u . s . patent application publication no . 2002 / 0064323 published on may 30 , 2002 , inventor chin ; and wo 00 / 27268 published on may 18 , 2000 , and assigned to the procter & amp ; gamble co . ; wo 02 / 14172 published on feb . 21 , 2002 , and assigned to the procter & amp ; gamble co . ; and wo 99 / 55213 published on nov . 4 , 1999 , and assigned to the procter & amp ; gamble co . on contrary to the conventional emulsification process using very high shear rate , the present invention allows for ( and is best practices when ) using a preferred shear rate below about 10 , 000 s − 1 , more preferably below 1 , 000 s − 1 , and even more preferably below 100 s − 1 ( shear rate is measured according to the method described herein ). in one embodiment of the present invention , the rate of addition of the emollient into the surfactant solution is chosen as such as to not decrease the viscosity of the concentrated composition being formed . the process of the present invention comprises a step of providing a wipe substrate and providing a quantity of the diluted composition onto the substrate . this step is referred as a converting step . any known type of substrate can be used in the converting step , preferably substrate are of synthetic nonwoven nature but can also include ( or be primarily constituted from ) cellulosic fibers . the step of providing the diluted composition onto the wipes substrate can be achieved by any conventional application process , such as ( but not limited to ) spraying , printing , and coating ( for example with the use of a curtain coater or a slot coater ). examples a and b are examples of the first process step of the present invention , where a concentrated emulsion mix is prepared . [ heading - 0095 ] ( the equipment used is described therein for a batch size of 100 kg .) a mix - tank is equipped with a top - entry double - stage agitator , designed such as the ratio z / t with z being the maximum height of liquid in the mix - tank and t being the mix - tank diameter , is comprised between 0 . 80 and 1 . 2 ( for instance , t = 546 mm ), and such as the ratio d / t with d being the impeller diameter and t as described above , is 0 . 66 . the top entry double stage agitator will be a wide blade hydrofoil having 4 blades per stage each having a high angle of attack ( for instance a philadelphia 4hs45 ) and will be positioned such as the ratio c 1 / t with c 1 being the distance between the bottom of the vessel and the middle of the lowest agitator stage ( for instance c 1 = 70 mm ) and t as described above is between 0 . 12 and 0 . 15 , such as the ratio c 2 / t with c 2 being the distance between the bottom of the vessel and the middle of the highest agitator stage and t as described above is between 0 . 5 and 0 . 6 . table a component amount (% by weight ) ( 1 ) plantacare2000up ™* 10 . 5 ( 2 ) dc 1501 ™** 89 . 5 * plantacare2000up ™ comprises about 50 % surfactant ( decylglucoside ) in water , and is commercialized by cognis gmbh , 40551 düsseldorf , germany , www . cognis . com . ** dc 1501 ™** comprises cyclopentasiloxane dimethiconol and is commercialized by dow corning , 65201 wiesbaden , germany www . dowcorning . com . ( a ) add the whole amount of ( 1 ) in the vessel . the lower blade of the agitator reaches the surface of the agitator ( liquid level is ≧ c 1 ). agitation process is started at n = 200 rpm . ( b ) start continuous addition of ( 2 ) into ( 1 ) at flow - rate comprised between 260 and 340 kg / h . the flow - rate must be slow enough to allow good incorporation of ( 2 ) into ( 1 ). the agitator speed is gradually increased up to 300 rpm . when 70 - 80 % of ( 2 ) in weight is added , the addition flow - rate will decrease to a range comprised between 180 and 230 kg / h to ensure good incorporation of the remaining of ( 2 ) in the composition . the agitator speed can be increased to 350 rpm at the end of addition for better incorporation . ( c ) at the end of addition , the composition is stirred for an extra 2 min . the batch can be discharged for further processing . the calculated shear - rate is 88 s − 1 at 350 rpm . [ heading - 0103 ] ( the equipment used is described therein for a batch size of 20 kg ) a mix - tank is equipped with a top - entry double - stage agitator , designed such as the ratio z / t with z being the maximum height of liquid in the mix - tank and t being the mix - tank diameter , is comprised between 0 . 80 and 1 . 2 ( for example t = 300 mm and z = 300 mm ), and such as the ratio d / t with d being the impeller diameter and t as described above , is 0 . 66 ( for example d = 200 mm ). the top entry double stage agitator will be a pitch blade turbine 45 ° having 4 blades per stage and will be positioned such as the ratio c 1 / t with c 1 being the distance between the bottom of the vessel and the middle of the lowest agitator stage and t as described above is between 0 . 12 and 0 . 15 , such as the ratio c 2 / t with c 2 being the distance between the bottom of the vessel and the middle of the highest agitator stage and t as described above is between 0 . 5 and 0 . 6 . table b component amount (% by weight ) ( 1 ) plantacare2000up ™* 10 ( 2 ) abil care 85 ™** 90 * plantacare2000up ™ comprises about 50 % surfactant ( decylglucoside ) in water , and is commercialized by cognis gmbh , 40551 düsseldorf , germany , www . cognis . com . ** abil care 85 ™ comprises bis - peg / ppg - 16 / 16 peg / ppg dimethicone caprylic capric triglyceride and is commercialized by goldschmidt / degussa , goldschmidt ag , 45127 essen , germany www . goldschmidt . com . ( a ) add the whole amount of ( 1 ) in the vessel . the lower blade of the agitator reaches the surface of the agitator ( liquid level is ≧ c 1 ). agitation process is started at 130 rpm . ( b ) start continuous addition of ( 2 ) into ( 1 ) at a flow - rate comprised between 60 and 65 kg / h . the addition flow - rate must be low enough to allow good incorporation of ( 2 ) into ( 1 ). the addition flow - rate is increased gradually . after ⅓ of the amount of ( 2 ) is added , the flow - rate can be increased to 90 kg / h . after ⅔ of the amount of ( 2 ) is added , the flow - rate can be increased to 120 kg / h . ( c ) at the end of addition , the composition is stirred for another extra minute at the same speed ( 130 rpm ). the batch can then be discharged for further processing . the calculated shear rate is 35 s − 1 at 155 rpm . examples c and d are examples of the second process step of the present invention where the concentrated emulsion mix is diluted in water with additional ingredients . ( the equipment used is described therein for a batch size of 750 kg .) a mix - tank is equipped with a top - entry double - stage agitator , designed such as the ratio z / t with z being the maximum height of liquid in the mix - tank and t being the mix - tank diameter , is comprised between 0 . 80 and 1 . 2 , and such as the ratio d / t with d being the impeller diameter and t as described above , is between 0 . 3 and 0 . 4 ( for instance 0 . 33 ). the top entry double stage agitator will be a pitch blade turbine 45 ° having 4 blades per stage and will be positioned such as the ratio c 1 / t with c 1 being the distance between the bottom of the vessel and the middle of the lowest agitator stage and t as described above is between 0 . 25 and 0 . 35 , such as the ratio c 2 / t with c 2 being the distance between the bottom of the vessel and the middle of the highest agitator stage and t as described above is between 0 . 5 and 0 . 6 . table c amount component (% by weight ) ( 1 ) disodium edta 0 . 10 ( 2 ) arlatone - v 175 ™* 0 . 80 ( 3 ) dc 1501 ™** 0 . 45 ( 4 ) plantacare2000up ™*** 0 . 05 ( 5 ) 1 . 2 propylengylcol 1 . 50 ( 6 ) sodium benzoate 0 . 20 ( 7 ) methylparaben 0 . 15 ( 8 ) propylparaben 0 . 05 ( 9 ) ethylparaben 0 . 05 ( 10 ) peg - 40 hydrogenated castor oil 0 . 80 ( 11 ) perfume 0 . 05 ( 12 ) purified water balance total 100 . 00 * dc 1501 ™* comprises cyclopentasiloxane dimethiconol and is commercialized by dow corning , 65201 wiesbaden , germany www . dowcorning . com . ** arlatone - v 175 ™ comprises sucrose palmitate , glyceryl stearate , glyceryl stearate citrate , sucrose , mannan , xanthan gum and is commercialized by uniqema gmbh & amp ; co . kg , 46429 emmerich , germany , www . uniqema . com . ** plantacare2000up ™ comprises about 50 % surfactant ( decylglucoside ) in water , and is commercialized by cognis gmbh , 40551 düsseldorf , germany , www . cognis . com . a mixing time of about 2 min is allowed in between the process steps . a — ingredient ( 12 ) is added into the vessel . agitation is started at 206 rpm and maintained through the whole process . b — ingredients ( 5 ), ( 6 ), ( 7 ), ( 8 ) and ( 9 ) are delivered in a premix form . the amount of ingredient ( 10 ) is added into the weighed out quantity of the above - mentioned premix and stirred for 15 min with a propeller stirrer . c — a triblender ™ f2116 md mbv b40 equipment is connected on a re - circulation loop and a water flow is pumped through at a flow rate of about 5100 kg / h . ingredient ( 2 ) is added via the funnel of the triblender at a speed sufficient for suction . an extra stirring time of 10 min is allowed for homogeneous dispersion . d — ingredients ( 3 ) and ( 4 ) were mixed together as described in example a . the resulting composition of example a is added into the vessel while stirring is increased at 220 rpm . an extra 5 min of stirring time is allowed for good dispersion . e — the premix prepared in step b — is added into the vessel . an extra 3 min of stirring time is allowed . f — ingredient ( 11 ) is added into the vessel . an extra 2 min of stirring time is allowed for good dispersion . g — ingredient ( 1 ) is added into the vessel . an extra stirring time of 5 min is allowed before end of batch . h — the composition can be discharged for further processing . table d amount component (% by weight ) ( 1 ) disodium edta 0 . 10 ( 2 ) arlatone - v 175 ™* 0 . 80 ( 3 ) abil care 85 ™** 0 . 45 ( 4 ) plantacare2000up ™*** 0 . 05 ( 5 ) 1 . 2 propylengylcol 1 . 50 ( 6 ) sodium benzoate 0 . 20 ( 7 ) methylparaben 0 . 15 ( 8 ) propylparaben 0 . 05 ( 9 ) ethylparaben 0 . 05 ( 10 ) peg - 40 hydrogenated castor oil 0 . 80 ( 11 ) perfume 0 . 05 ( 12 ) purified water balance total 100 . 00 * arlatone - v 175 ™ comprises sucrose palmitate , glyceryl stearate , glyceryl stearate citrate , sucrose , mannan , xanthan gum and is commercialized by uniqema gmbh & amp ; co . kg , 46429 emmerich , germany , www . uniqema . com . ** abil care 85 ™ comprises bis - peg / ppg - 16 / 16 peg / ppg dimethicone caprylic capric triglyceride and is commercialized by goldschmidt / degussa , goldschmdit ag , 45127 essen , germany www . goldschmidt . com . *** plantacare2000up ™ comprises about 50 % surfactant ( decylglucoside ) in water , and is commercialized by cognis gmbh , 40551 düsseldorf , germany , www . cognis . com . a mixing time of about 2 min is allowed in between each process steps . a — ingredient ( 12 ) is added into the vessel . agitation is started at 206 rpm and maintained through the whole process . b — ingredients ( 5 ), ( 6 ), ( 7 ), ( 8 ) and ( 9 ) are delivered in a premix form . the amount of ingredient ( 10 ) is added into the weighed out quantity of the above - mentioned premix and stirred for 15 min with a propeller stirrer . c — a triblender ™ f2116 md mbv b40 equipment is connected on a re - circulation loop and a water flow is pumped through at a flow rate of about 5100 kg / h . ingredient ( 2 ) is added via the funnel of the triblender at a speed sufficient for suction . an extra stirring time of 5 min is allowed for homogeneous dispersion . d — ingredients ( 3 ) and ( 4 ) were mixed together as described in example b . the resulting composition of example b is added into the vessel . an extra 5 min of stirring time is allowed for good dispersion . e — the premix prepared in step b — is added into the vessel . f — ingredient ( 11 ) is added into the vessel . an extra 2 min of stirring time is allowed for good dispersion . g — ingredient ( 1 ) is added into the vessel . an extra stirring time of 5 min is allowed before end of batch . h — the composition can be discharged for further processing . example e is an example of the third process step of the present invention , where the diluted composition is applied to a wipe substrate material . the substrate is a nonwoven substrate comprising 60 % ( w / w ) polypropylene fibers and 40 % ( w / w ) viscose fibers and having a average fiber lengths being about 38mm to 40 mm ( available for example from pgi , usa ). the wipe substrate material is unwinded at a constant speed from the mother roll to a folding plate . on the unwind path , the substrate material moves against a slot coater with a slot size of 200 microns . the diluted composition as prepared in example c or d is pumped through the slot coder at a flow rate designed such as to ensure a lotion load of 3 . 0 g of lotion per gram of substrate . the wetted substrate material is folded on the folding board and cut to the size of the wipes . the water used in the examples of this invention as well as in its description , methods and teaching is water of cosmetic grade or pharmaceutical grade , preferably deionized water , interchangeably referred to as “ purified water ” or “ water ”. [ heading - 0139 ] generation of viscosity curve to calculate the k value and shear rate index ( n ): the samples are run on a ta instruments ar2000 series rheometer ( new castle , del ., usa , www . tainst . com ), with a cone / plate geometry , tooling : 40 mm , 2 ° cone . the software used for analysis is ta rheology advantage , version 4 . 1 . 2 . the flow curve method used is a continuous , shear rate controlled ramp from 1 to 1000 sec − 1 for 5 min at 25 ° c . the yield stress method used is a continuous shear stress controlled ramp from 200 to 400 pa for 5 min at 24 ° c . the viscosity curve is generated as follows : approximately 3 ml of sample is placed on a temperature controlled peltier plate and the cone tooling compresses the sample to its truncating gap . the sample is forced to flow by applying a shear stress controlled by the method . the applied stress is divided by the corresponding shear rate ( determined by the rpm and the geometry of the tooling ) to generate the viscosity curve . the k and n values were generated via power - law model from 2 to 50 sec − 1 . the process described therein describes the mixing of the components of the composition at a low shear rate versus commonly used process . the shear rate is calculated as follows : given the impeller configuration and dimensions and the mixing vessel dimensions described as z being the maximum height of liquid in the vessel , t being the diameter of the vessel , d being the diameter of the impeller , c 1 being the distance between the bottom of the vessel and the middle of the lowest agitator stage , c 2 being the distance between the bottom of the vessel and the middle of the highest agitator stage , given the composition properties ( specific gravity , k and shear index n determined with the viscosity curve ), given the agitation speed n in rpm , the shear rate is calculated based on the metzner & amp ; otto concept for non - newtonian fluids . (“ mixing in the process industries ” second edition by n . harnby , m . f . edwards and a . w . nienow . chapter 8 , pg 140 - 145 , 1992 ). the used method to measure the particle size distribution of lotions is the horiba la - 910 . this analyzer measures the particle size distribution by scattering technique . when light goes into a spherical particle of r diameter , three types of light will be emitted . light which reflects at the outer surface of the particle . light which passes through the inside of the particle and then reflects at the inner surface of the particle . light which passes through the inside of the particle and then reflects when it goes out . device : horiba la - 910 standard measure agitation speed 2 conditions : circulation speed 1 ultra sonic speed 1 min 0 sonic works during measuring no waiting time after ultra sonic 0 sec sampling times 15 form of distribution standard type of dispersant deionized water form of distribution standard relative refractive index 1 . 14 - 0 . 00i address : horiba europe gmbh 65843 sulzbach / ts ., germany www . horiba . com all documents cited in the detailed description of the invention are , in relevant part , incorporated herein by reference ; the citation of any document is not to be construed as an admission that it is prior art with respect to the present invention . while particular embodiments of the present invention have been illustrated and described , it would be obvious to those skilled in the art that various other changes and modifications can be made without departing from the spirit and scope of the invention . it is therefore intended to cover in the appended claims all such changes and modifications that are within the scope of this invention .