fig1 and 2 show generally the preferred embodiment of the apparatus of the present invention designated generally by the numeral 10 . starch cooking apparatus 10 includes a vessel 11 having an interior 12 for containing water and dry or liquid starch that is added to the vessel through the open top , for example . the vessel 11 provides an interior 12 surrounded by side wall 13 and bottom wall 14 . vessel 11 may be fabricated of a variety of materials suitable for forming a container however , stainless steel or another corrosion resistant material is preferred . the vessel 11 may also be insulated to conserve heating requirements and to reduce the heat lost to the surrounding laundry area . lid 15 is attached to side wall 13 at hinge 16 so that when the lid 15 is open , starch can be added through the open top portion at the open lid 15 . the lid 15 may be provided with a handle 17 to aid in opening and closing the lid 15 . a water supply line 18 supplies fluid to inlet jet 19 when control valve 20 is opened . preferably , water supply line includes a check valve 21 preventing the back flow of water in the line . heating coil 22 is a steam header ( e . g ., ⅜ ″ copper conduit ) that tracks in a generally circular path approximately adjacent to side wall 13 as shown in fig2 . this heating coil 22 receives steam transmitted to vessel 11 via steam inlet line 23 . steam control valve 24 controls the flow of steam through line 23 to heating coil 22 . a steam return line 25 is provided for exiting steam from heating coil 22 , the return line 25 being provided with steam trap 26 . after a starch solution has been cooked within the interior 12 of vessel 11 , that starch solution can be transmitted to a commercial washer ( not shown ) via flow line 28 . discharge port 27 communicates with discharge flow line 28 so that the starch solution can be drained from the vessel 11 at discharge port 27 . a pump 31 is provided in discharge flow line to assist in the transport of the mixed starch to the commercial washer . in the illustrated embodiment , a dayton model 7p087 pump and motor is utilized , however those skilled in the art recognize that a pump of similar capacity by another manufacturer will suffice . a motor drive 32 is included to power pump 31 during the transfer of the starch mix to the washer . a recirculation line 35 is provided to continuously recirculate the starch and water mixture in vessel 11 , to initially mix the starch and water combination and to heat the starch to bring it to the necessary useful temperature and homogeneity , and thereafter to prevent the starch from developing any clumps or lumps , keeping it continually ready to be discharged into the commercial washer . recirculation line 35 terminates in the vessel 11 in the center of the bottom wall 14 , at outlet 36 , to which is attached filter 30 . filter 30 is a stand of pipe of a noncorosive material , such as stainless steel , which in the preferred embodiment of a cooker having a capacity of 5 gallons the filter is of a diameter of three - quarters of an inch and stands approximately 6 inches above the bottom all 14 of vessel 11 . for the standard size cooker being described , the filter has approximately 30 substantially evenly distributed holes which have a diameter of approximately ⅛th inch in diameter , numbering 30 , though the height of the filter . the number and size of holes 30 ′ in filter 30 may be varied so long as the flow rate through the filter is essentially equal to the flow rate of the mixture out of the outlet 39 . in the described preferred embodiment , pump 37 generates a flow rate of approximately 12 gallons per minute though the system , including through filter 30 , through recirculating line 35 and out of discharge nozzle 39 into vessel 11 . as may be better noted on fig2 nozzle 39 is disposed adjacent the vertical wall 13 of vessel 11 such that the velocity of the starch and water mixture exiting the nozzle 39 facilitates the vortex set up in vessel 11 . nozzle 39 is immediately adjacent heating coil 22 disposed around and adjacent to vessel wall 13 in the lower region of the vessel 11 . by such placement and the vortex assisting action of the discharge of nozzle 39 , the starch and water mixture is evenly heated by the continuing flow of starch and water over the heating coil 22 . providing the volume of starch and water flow through filter 30 , nozzle 39 and over coil 22 is centrifugal pump 37 , disposed in recirculating line 35 immediately below discharge opening 36 . in the preferred embodiment , pump 37 is a dayton model 4 rh 41 centrifugal pump which provides a flow rate of approximately 12 gallons per minute flow through recirculating line 35 which is approximately ¾ inches in diameter . as previously described , pump 37 operating at rated capacity provides the flow in the recirculating line 35 and out of nozzle 39 into vessel 11 , causing the load of the mixture of starch and water to swirl in the direction of flow out of nozzle 39 to a degree that filter 30 , at the center of the vortex created , stands approximately 6 inches above the bottom wall 14 of vessel 11 and is barely covered by the mixture of starch and water . for those smaller sized starch cookers described above , the capacity of recirculating pump 37 and the vortex created out of nozzle 39 causes the swirl of the starch and water mixture to bottom just above of the shorter filter 30 for the reduced capacity cooker 10 . as described earlier , nozzle 39 projects the stream of recirculating starch and water generally tangentially of vessel wall 13 across the heating coil 22 to produce the strong vortex which pulls any lumps or clumps of starch into filter 30 , causing them to break - up and dissolve as the starch and water mixture transits holes 30 ′ and enters into inlet 36 and pump 37 . projection of the stream of starch and water out of nozzle 39 onto the vessel wall 13 establishes the circular , vortex action which injects the continuous mixing action and impacts the lumps and clumps of starch , to the degree that any persist , against filter 30 , forcing them through holes therein . the continuous circular injection of the starch and water mixture tangentially at vessel wall 13 and the extraction of the mixture centrally at filter 30 further inhibits any stagnation of starch in the vicinity of either the steam heating coil 22 or at the bottom of vessel 11 , particularly in the region of the outlet port 27 . the combination of the described actions ensures a well - mixed homogeneous mixture of starch and water at a uniform temperature selected to provide the best action of starching garments in the commercial washer to which the cooker 10 is connected . as indicated above , the description is specific to a vessel 11 with a capacity of about 5 gallons . starch cookers 10 are also commonly constructed with a 14 gallon vessel 11 . other than the size of the vessel 11 , the only other adjustment which is made to establish a vortex of sufficient vigor and depth for the above described degree of mixing and heating is by increasing of the size of the outlet on centrifugal pump 37 to ¾ inches compared to the ½ inch size utilized for the 5 gallon vessel . by increasing the flow capacity out of nozzle 39 , the described vortex is made to bottom out just above the top of filter 30 . thermostat 40 regulates the temperature of the starch solution contained within vessel 11 during the cooking period . thermostat 40 is controlled by control panel 41 illustrated in fig1 and 2 . the control panel 41 has a start switch 42 to begin operation of cooker 10 and a stop switch 43 to cease operation . a direct transfer switch 44 is provided for initiating the transfer of the contents of the starch solution in vessel 11 to the commercial washer , via flow line 28 . light indicator 45 illuminates when the starch solution has reached the requisite temperature ( preferably 180 ° f . to 190 ° f .) and the requisite degree of mixing during the cooking operation . once the operating temperature is reached , timer 48 starts operating and is set to allow mixing for 5 minutes to ensure adequate mixing of the starch and uniformity of temperature in the batch . once the 5 minutes of continued mixing expire , a ready light 45 illuminates showing that the starch mixture is ready for dispensing . in the usual cycle for mixing and dispensing a starch and water mixture to a washing machine , the pressing of start switch 42 will start the flow of water into vessel 11 through line 18 . the volume of water added is preferably enough to reach a quantity of about five gallons in vessel 11 . the fill level is controlled in the preferred embodiment by stand pipe 29 , subsequently described . once vessel 11 is filled to the predetermined level , the user adds from about 8 to about 38 ounces of uncooked ( dry ) starch . once the water level reaches the predetermined level as set in water level switch 47 , solenoid 20 turns off the supply of water and the steam valve 24 begins supplying steam to coil 22 for the heating of the starch and water mixture . concurrently , circulation pump 37 is actuated to begin recirculating the liquid in vessel 11 so that the action of the starch and water mixture keeps the heating coil 22 clear of starch build - up and circulation of the mixture through filter 30 breaks up any lumps or clumps of starch . until the temperature of the starch and water mixture reaches the preselected range , steam solenoid 24 continues the supply of steam to heating coil 22 . in the illustrated embodiment , after the mixture has come to the 180 - 190 ° f . range , and five minutes have elapsed , the starch and water have become properly mixed and the ready light 45 will illuminate signaling that the mixture is ready for discharge to a washer . circulation pump 37 will continue circulating the mixture as described and steam valve 24 continues the supply of steam to coil 22 until the commercial washer signals the supply of starch to the washer . at that point , transfer pump 31 begins the transfer of the mixture to the washer . cleaning of the cooker 10 is affected in a manner similar to the preparation of a mixture of starch and water , with the exception that the starch is not added . water is added to the vessel 11 to the predetermined level and is preferably ( though not necessarily ) heated to the predetermined temperature . the water is circulated as with the mixture since the vortex circulation provides such an effective cleaning action that all of the operative parts are stripped of the previous mixture , and when the cleaning is completed ( as with the time it takes for the water to come to the preset temperature and is circulated for the 5 minute period ), the water is dumped and the vessel is clean . the present invention includes an improved water level control which much more effectively and accurately controls the level of water ( and the starch mixture ) in the vessel 11 . prior versions of cookers have utilized metallic inverted stand pipes 29 within the vessel 11 which operate in conjunction with a pressure switch 47 which senses the level of water in the vessel by means of the pressure exerted on the air trapped within pipe stand 29 . it has been discovered that as the level of starch that accumulates upon the exterior of conventional metallic stand pipes affects the coefficient of heat conductance of the stand pipe , and frequently remains there after conventional cleaning . hence , when a new supply of water is added to the mixer , the rising temperature of the water does not get conducted through the stand pipe 29 and the header of air trapped therein is not heated , as with a clean stand , and therefore the pipe stand gives a level reading ( allows overfilling since the air in the tube is not heated and expanded as with the clean pipe ) inconsistent with a clean stand pipe . the present invention incorporates a stand pipe 29 fabricated of schedule 80 pvc plastic pipe . by using the selected material ( selected because it does not readily conduct heat ), the conductance of the heat of the water in the tank is insufficient to change the temperature of the air contained within the pipe stand 29 and therefore , the readings from batch to batch are consistent from one filling to the next since the temperature of the air is essentially constant ( i . e ., unchanged ) and prompts a reliable , repeatable reading . the following table lists the parts numbers and parts descriptions as used herein and in the drawings attached hereto . the foregoing embodiments are presented by way of example only ; the scope of the present invention is to be limited only by the following claims .