one aspect of this invention are the polyoxyalkylene random copolymers having the general formula the polyoxyalkylene copolymers must be random in structure as it relates to the components --( ch 2 ch 2 o )--, and --{ ch 2 ( ch 3 ) cho }--, as it has been reported to the inventor herein that block copolymers will not give the benefits in the end use application . as indicated above , one end of the molecules of this polyoxyalkylene copolymer is capped with an unsaturated moiety , such as vinyloxy or allyloxy , allyloxy being preferred . the other end of the molecule contains a polyoxyalkylene segment which is capped with a carbinol , and without this invention , the amount of polyoxyalkylene end groups that contain primary carbinols is limited to generally less than about 10 mole percent . the polyoxyalkylene random copolymers of this invention have a average molecular weight of about 160 to 4130 g / mole . it should be understood by those skilled in the art that the number of primary hydroxyl groups present in the random copolymer must be such that at least 40 mole percent of the molecules have carbinols bonded directly to primary carbon atoms in the polyoxyethylene units in the molecule . the majority of the primary hydroxyl groups are those derived from the ethylene oxide residues but certain of the hydroxyl groups derived from propylene oxide can also be primary depending upon the manner in which the oxirane ring of the propylene oxide opens up in the formation of the copolymer . in this invention , the polyoxyalkylene random copolymer which is &# 34 ; enriched &# 34 ;, contains at least forty mole percent of end groups having primary carbinols before it is endcapped . the primary carbinols are reacted with various acylates in order to cap the carbinols with an acyloxy group . for purposes of this invention , the formula , r &# 34 ; is the alkyl radical of an acyloxy endblocking or endcapping material and these materials are selected from a group consisting of alkyl radicals having from 1 to 6 carbon atoms . preferred for this invention are the methyl , ethyl , propyl and butyl radicals . most preferred is the methyl radical . the molecular weight of the polyoxyalkylene random copolymer is made up primarily of the ethylene oxide and the propylene segments , and such molecular weight is indicated by the subscripts w and z , respectively . the subscript z has a value of 1 to 50 , and w has a value of 1 to 50 ; wherein the ratio of z to w is in the range of 0 . 1 to 10 : 1 . such copolymers include for example : ch 2 ═ chch 2 o ( ch 2 chch 3 o ) 18 ( ch 2 ch 2 o ) 18 c ( o ) ch 3 , and the like . as indicated above , this invention also deals with polysiloxane - polyoxyalkylene copolymers , which are prepared by utilizing the polyoxyalkylene random copolymers described above . the materials are prepared by the well - known hydrosilylation in which the polysiloxanes containing hydrogen attached to silicon atoms , for example , ( ch 3 ) 3 sio { sio ( ch 3 ) h } 1 si ( ch 3 ) 3 ; ( ch 3 ) 3 sio { sio ( ch 3 ) 2 } 1 --{ sio ( ch 3 ) h } 1 si ( ch 3 ) 3 ; ( ch 3 ) 3 sio { sio ( ch 3 ) 2 } 3 . 7 { sio ( ch 3 ) h } 9 . 5 -- si ( ch 3 ) 3 ; ( ch 3 ) 3 sio { sio ( ch 3 ) 2 } 1 . 9 { sio ( ch 3 ) h } 13 . 3 si ( ch 3 ) 3 ; ( ch 3 ) 3 sio { sio ( ch 3 ) 2 } 2 . 1 { sio ( ch 3 ) h } 22 . 8 si ( ch 3 ) 3 ; ( ch 3 ) 3 sio --{ sio ( ch 3 ) 2 } 3 . 3 { sio ( ch 3 ) h } 73 si ( ch 3 ) 3 ; ( ch 3 ) 3 sio { sio ( ch 3 ) 2 } 8 . 0 --{ sio ( ch 3 ) h } 87 si ( ch 3 ) 3 , and ( ch 3 ) 3 sio { sio ( ch 3 ) 2 } 19 -{ sio ( ch 3 ) h } 139 si ( ch 3 ) 3 , are used herein . the silicon bound hydrogen is reacted with the unsaturated terminal of the polyoxyalkylene random copolymers under the catalytic influence of platinum , rhodium , or the like . these reactions are well known in the art and a detailed description of the reaction will not be set forth herein . the polysiloxane portion of the copolymer is comprised of trialkylsilyl endblocking units , and for purposes of this invention , the body of the siloxane chain is comprised of polydimethylsiloxane units and methylhydrogenpolysiloxane units having the general formula : ## str5 ## wherein x has an average value of 1 to 500 , and y has an average value of 1 to 500 . further , the ratio of x to y is in the range of 0 . 1 to 10 : 1 . the polyxiloxane - polyoxyalkylene copolymers are useful as surfactants in the preparation of polyurethane foams . all of the surfactants used in the examples were prepared by hydrosilylation of the allyloxy , or vinyloxy endblocked polyethers , using platinum as the catalyst , according to standard procedures known in the art . a set of samples were subjected to an accelerated hydrolysis test to show the hydrolytic stability of the materials of this invention . a material , ch 2 ═ chch 2 o ( ch 2 chch 3 o ) 18 ( ch 2 ch 2 o ) 18 c ( o ) ch 3 was prepared . samples of this material were placed in a 92 ° c . oven and the acid content was measured periodically over a period of time with the following results . ______________________________________ acid no . totaltime mg . koh / acidmin . gram sample ppm______________________________________ 0 . 0136 14 . 5 17 . 0136 14 . 5 55 . 0194 20 . 7 97 . 0360 38 . 5120 . 0160 17 . 3182 . 0564 60 . 0245 . 0344 36 . 8328 . 0814 86 . 9360 . 0702 75 . 01260 . 0570 61 . 02747 . 0496 53 . 04190 . 07197 77 . 0______________________________________ these results show that the rate was 11 . 2 ppm / hr . and it plateaued around 80 ppm , while a like sample , not falling within the scope of this invention had an initial rate of 37 ppm / hr . and a plateau at about 500 ppm . it was speculated that the erratic acid values were caused by the use of glass vials having plastic tops which may have leaked acetic acid through the caps as they were heated in this accelerated test . however , the data shows the desired trend leading to the conclusions regarding the benefits recited herein . hydrolysis rates were measured on the material of example 1 and it was compared with other similar materials with varying amounts of ethylene oxide groups containing acetoxy groups . ______________________________________ hydrolysissample rate______________________________________a 11 . 2 ppm / hr . b 37 . 3 ppm / hr . c 15 . 2 ppm / hr . d 12 . 3 ppm / hr . ______________________________________ sample b is a material of the prior art . sample a is the inventive material of example 1 . sample c is a material of this invention having 80 % ethylene oxide ends covered with acetoxy groups , and sample d is a material of this invention having 60 % ethylene oxides ends covered with acetoxy groups . in spite of the fact that the hydrolysis rate does not line up with very well with the percentage of ethylene oxide ended polymers , it is clear that the hydrolysis rates of the materials of the instant invention are lower than those of the prior art material . preparation of a flexible polyurethane foam using ( ch 3 ) 3 sio {( ch 3 ) 2 sio } 103 ( ch 3 rsio ) 10 si ( ch 3 ) 3 wherein r is --( ch 2 ) 3 o ( ch 2 chch 3 o ) 18 ( ch 2 ch 2 o ) 18 c ( o ) ch 3 . the polyether was reacted with a polydimethylsiloxane substituted with 0 . 117 weight percent hydrogen attached to silicon atoms and having a viscosity of 155 centistokes . the resulting polysiloxane - polyoxyalkylene copolymer was used in a test for flexible polyurethane foam as follows : 92 . 7 weight percent of polyol 235 - 048 , a product of dow chemical , midland mich . 0 . 1 weight percent of dabco bl11 , an amine catalyst product of air products & amp ; chemicals . 3 . 0 . 4 g of t - 10 catalyst , a tin catalyst product of air products & amp ; chemicals . the components 1 to 4 were thoroughly mixed and a flexible polyurethane foam was produced having a foam height of 233 . 7 mm . the average for production lots having the same formulation , but made with acyloxy polyethers not of this invention is 233 . 2 mm . this shows that the ability of the surfactant to perform in a polyurethane formulation is essentially unaffected .