the present invention relates to a blend of cellulose acetate and starch acetate and other inventions derived from the novel blend , as well as , a process to prepare this blend . in this application , the term &# 34 ; cellulose acetate &# 34 ; refers to any conventional wood pulp , cotton or any other suitable cellulose material being acetylated by organic acids to a degree of substitution ranging between 1 . 0 to 3 . 0 with an acetyl value of 20 to 62 %. the term &# 34 ; acetyl value &# 34 ; as used herein refers to the weight % of acetic acid per unit measure of starch acetate or cellulose acetate . the term &# 34 ; starch acetate ,&# 34 ; as used herein refers to any conventional corn , potato , grain , or other suitable starch , containing amylose and amylopectin in any ratio deemed acceptable for our process and being acetylated by organic acids to a degree of substitution ranging between 1 . 0 to 3 . 0 with an acetyl value of 20 - 60 %. the term &# 34 ; blend &# 34 ;, as used herein shall refer to combining , by use of a solvent , starch acetate with any cellulose esters with organic or inorganic acids and with mixtures of cellulose esters and other polymers . the term &# 34 ; solvent &# 34 ; shall refer to acetone , methyl ethyl ketone , methylene chloride / methanol , glacial acetic acid or any suitable solvent which is capable of dissolving the forementioned cellulose esters , cellulose acetate , starch acetate or any combination thereof . the present invention also provides a process for making spun yarn from said blend comprising the steps of preparing a mixture of cellulose acetate and starch acetate , solutioning the mixture in a suitable solvent , mixing , filtering , and then spinning the resultant blend in a spinning cabinet . any type of spinning which is routinely used in the preparation of cellulose acetate is contemplated . these include dry spinning , wet spinning and melt spinning . an alternate method to prepare the blend is to co - precipitate a cellulose acetate and starch acetate reaction mixture in water in the proper ratio already in acetate manufacturing and then to follow routine cellulose acetate preparation steps including spinning . the dope temperature should be maintained at about 50 ° to 95 ° c . with a downdraft airflow temperature in the spinning cabinet held at about 50 ° to 100 ° c . to remove the solvent from the spun yarn by evaporation . the preferred solvent in the process of the present invention is acetone . solvents suitable for the process of this invention are any nonaqueous solvents capable of creating an extrudable dope . preferably , the solvent will be chosen such that it is capable of total solubility of cellulose acetate and starch acetate . examples of such solvents include volatile , nonaqueous liquids such as low molecular weight aldehydes and ketones , hydrocarbons and halogenated hydrocarbons , esters and ethers . examples of solvent expressly capable of solubilizing cellulose esters are disclosed in u . s . pat . no . 2 , 362 , 182 , incorporated herein by reference . those solvents include acetone , methyl ethyl ketone , methyl acetate , ethyl acetate , propyl acetate , methyl formate , ethyl formate , propyl formate and combinations thereof . other suitable solvents include acetic acid , methylene chloride , methanol and combinations . one major use of cellulose acetate is in flake to be made into cigarette tow for use in cigarette filters . cellulose acetate is used because it does not impart any unwanted taste to the filters . through sensory testing , it has been found that cigarettes made with filters of the cellulose acetate / starch acetate blend show no significant difference in taste to those made from cellulose acetate alone . the following examples further illustrate various embodiments of the present invention . they are presented solely for illustrative purposes and are not to be construed as limiting the invention disclosed herein . a mixture consisting of 7 . 5 lbs of cellulose acetate ( ca ) ( av = 2 . 55 ) and 2 . 5lbs . of starch acetate ( sa ) ( av & gt ; 2 . 8 ) in 27 . 3 lbs acetone ( 26 . 8 % solids , 25 % sa , 75 % ca ) was fed through a high shear mixer . the resultant stable solution was spun in a conventional ca spinning cabinet and compared to a control of pure ca ( av = 2 . 55 ) dissolved in acetone ( 26 . 8 % solids , 100 % ca ). the yarn was produced with a feed roll speed of 500 m / mn and the dope temperature was kept at 85 ° c . the downdraft airflow in the spinning cabinet had a temperature of 75 ° c . to remove the acetone from the spun yarn by evaporation . the viscosity of the blend was less than 100 , 000 cps as compared to 150 , 000 to 180 , 000 for the control . denier , tenacity and elongation were 179 , 1 . 00 grm / denier and 25 . 27 % in the blend as compared to 170 , 1 . 14 grm / denier and 28 . 50 % in the control . the blend showed improved dyeability . a solution consisting of 7 . 5 lbs of ca ( av = 2 . 55 ) and 2 . 5 lbs of sa ( av = 2 . 59 ) in 18 lbs acetone ( 35 . 7 % solids , 25 % sa , 75 % ca ) was prepared according to the same process as in example 1 . the resultant solution was spun in a conventional ca spinning cabinet and compared to a control of pure ca ( av = 2 . 55 ) dissolved in acetone ( 26 . 8 % solids , 100 % ca ). metier conditions were consistent with those used in example 1 . the viscosity of the blend was 265 , 000 cps as compared to 150 , 000 to 180 , 000 for the control . denier , tenacity and elongation were 175 , 0 . 79 grm / denierand 28 . 36 % in the blend as compared to 155 , 1 . 22 grm / denier and 33 . 49 % in the control . other examples were similarly run with the conditions and results as shown below in table 1 . table 1__________________________________________________________________________the effect of metier conditions and % starch acetateon physical properties of the blend % starch acetate dope temp . ° c . jlat . ° c . * ten . grams / den elong . % ten . x sqrt elong__________________________________________________________________________control 1 0 85 70 1 . 14 28 . 50 6 . 09control 2 0 85 70 1 . 22 33 . 49 7 . 06control 3 0 85 70 1 . 20 32 . 47 6 . 84trial 1a15 75 60 1 . 10 32 . 14 6 . 24trial 1b20 75 60 1 . 03 30 . 77 5 . 71trial 1c25 75 60 1 . 02 34 . 34 5 . 97trial 2a15 85 60 1 . 09 34 . 96 6 . 44trial 2b20 85 60 1 . 00 35 . 22 5 . 93trial 2c25 85 60 1 . 00 36 . 68 6 . 05trial 3a15 95 60 1 . 05 36 . 99 6 . 39trial 3b20 95 60 1 . 01 35 . 43 6 . 01trial 3c25 95 60 0 . 95 36 . 49 5 . 73trial 4a15 95 70 1 . 04 36 . 86 6 . 31trial 4b20 95 70 0 . 97 37 . 19 5 . 92trial 4c25 95 70 0 . 96 37 . 22 5 . 85trial 5a15 85 70 1 . 08 36 . 00 6 . 48trial 5b20 85 70 1 . 00 35 . 45 5 . 95trial 5c25 85 70 1 . 02 36 . 93 6 . 20trial 6a15 75 70 1 . 10 34 . 58 6 . 47trial 6b20 75 70 1 . 03 33 . 99 6 . 01trial 6c25 75 70 1 . 00 34 . 98 5 . 91trial 7a15 75 80 1 . 06 34 . 89 6 . 26trial 7b20 75 80 1 . 00 37 . 13 6 . 09trial 7c25 75 80 0 . 85 34 . 48 4 . 99trial 8a15 85 80 1 . 08 37 . 02 6 . 57trial 8b20 85 80 1 . 00 37 . 02 6 . 08trial 8c25 85 80 0 . 94 34 . 94 5 . 56trial 9a15 95 80 1 . 06 37 . 45 6 . 49trial 9b20 95 80 0 . 98 37 . 42 5 . 99trial 9c25 95 80 0 . 91 36 . 85 5 . 52__________________________________________________________________________ * jet level air t ° c .