referring to fig1 a ph modifying apparatus 10 embodying the principles of the invention includes an initial foodstuff supply 11 which feeds an initial foodstuff to two separate streams , labeled a and b in the figure . one stream of foodstuff , stream a , is processed through a ph modifying arrangement 12 and then the two streams a and b are combined in combining arrangement 14 to produce a third stream c in fig2 . the preferred form of the invention includes a ph sensing arrangement 15 for sensing the ph of the ph - modified foodstuff . this sensed ph is then used in determining the proportion at which the two streams a and b are mixed in combining arrangement 14 to produce the desired ph in the third stream c . stream a is carried in a first conduit 18 having an inlet connected to initial foodstuff supply 11 and an outlet connected to combining arrangement 14 . stream b is carried in a second conduit 19 having an inlet end connected to the initial foodstuff supply 11 and an outlet also connected to combining arrangement 14 . a first pump 20 is connected in first conduit 18 for forcing material through the first conduit , while a second pump 21 is connected in second conduit 19 for forcing material through the second conduit . as will be described further below , these first and second pumps 20 and 21 are preferably variable rate pumps and may comprise auger - type pumps , piston - type pumps , or any other pumping device suitable for the particular foodstuff being processed . it will be appreciated that each pump 20 and 21 is driven with a suitable motor with controls for controlling the pumping speed . these motors and controls are within the knowledge of those skilled in the art and are omitted from the figures so as not to obscure the invention in unnecessary detail . other details , such as the specific materials from which conduits 18 and 19 and other components of the system are formed , are likewise omitted from this disclosure since the materials may be any materials suitable for use in handling the desired foodstuffs . although any ph modifying arrangement may be used for the arrangement 12 , the preferred arrangement comprises the arrangement shown in u . s . patent application ser . no . 09 / 286 , 699 , now u . s . pat . no . 6 , 142 , 067 . the entire disclosure of this document is incorporated herein by this reference . as shown in fig1 of the present disclosure , ph modifying arrangement 12 includes a contactor 24 and a mixing device 25 . contactor 24 includes a supply 26 of ph modifying material . the ph modifying material may be any material suitable for use in the particular foodstuff being processed . for example , ammonia gas or aqueous solution of ammonia comprises a suitable ph increasing material for meats and other foodstuffs . carbon dioxide provides a suitable ph reducing material . regardless of the type of ph modifying material or the manner in which it is added to the foodstuff , mixing device 25 functions to distribute the material throughout the foodstuff to produce a generally uniform ph throughout the foodstuff . mixing device 25 preferably comprises a grinder as set out in application ser . no . 09 / 286 , 699 , but may comprise any suitable mixing device . the ph of the ph modified foodstuff exiting mixer 25 is sensed at sensing arrangement 15 . in the preferred form of the invention , sensing arrangement 15 includes a continuous sensing device for providing a continuous ph reading for the ph modified foodstuff exiting mixer 25 . the sensing device may sense material in situ within first conduit 18 or may sense only one or more small portions of the entire stream of material within the conduit . alternatively to the preferred continuous sensing device , the sensing arrangement 15 may include an arrangement for taking discrete samples for manual testing . this manual sensing arrangement is within the scope of the following claims . referring still to fig1 combining arrangement 14 includes a first inlet 31 connected to the outlet end of first conduit 18 , and a second inlet 32 connected to the outlet end of second conduit 19 . combining arrangement 14 also includes a single outlet 33 connected to an outlet conduit 34 . some preferred embodiments of the invention may also include flow control or flow metering devices included in combining arrangement 14 for use in controlling the proportion at which the two foodstuff streams a and b are combined . this control may be in addition to , or an alternative to , any flow rate control provided through pumps 20 and 21 as discussed below . located downstream of combining arrangement 14 , the illustrated form of the invention includes a mixer 36 for thoroughly mixing the combined stream of material exiting the combining arrangement . since the combined stream c includes material from both streams a and b , the material must be mixed in order to provide the desired uniform ph throughout the material . mixer 36 may comprise any suitable foodstuff mixing device . for communicated meats , poultry , and seafood , for example , mixer 36 may comprise a grinder , blender , or bowl chopper . regardless of the type of mixing device used for mixer 36 , an outlet ph sensing arrangement 37 may be operatively connected in the outlet conduit 34 for measuring the ph of the combined stream c . according to the invention , the ph sensed at sensing arrangement 15 may be used in controlling the overall ph modification within apparatus 10 . in the preferred form of the invention , ph modifying arrangement 12 modifies the ph of the foodstuff in stream a over a desired modification amount . this overly modified ph may be brought back to a desired level in the combined stream c by adding under or non - ph modified foodstuff from stream b in the appropriate proportion defined by the respective ph of the two streams . since the initial foodstuff in stream b may be an untreated foodstuff with a generally known ph , while the ph after the ph modifying arrangement 12 may be varied , ph sensed at arrangement 15 comprises a variable which may be used through suitable control devices to control the proportion at which the two streams a and b are combined to produce the combined stream c at the desired ph . the proportions at which the two streams of foodstuff a and b are combined may be controlled by controlling the flow rate of the two streams . fig1 shows that the relative flow rates may be controlled by providing a control signal through line 40 to first pump 20 . the control signal may originate from a controller 39 associated with ph sensing arrangement 15 . fig1 also shows a control line 41 extending from ph sensing arrangement 15 back to second pump 21 . either pump individually , or both pumps together may be controlled to control the proportion at which foodstuff streams a and b are combined in combining arrangement 14 . also , a third control line 42 may provide a control signal to contactor 24 , or the supply 26 of ph modifying material associated with the contactor . this third control signal may be used along with other inputs to control the pressure of ph modifying material applied in contactor 24 , or to control a metering of ph modifying material into the contactor . the method of the invention and operation of apparatus 10 shown in fig1 may be described with reference to fig1 and the flow chart shown in fig2 . the method includes providing a first foodstuff such as stream a , and providing a second foodstuff such as stream b . the method also includes combining the two foodstuffs in a proportion to produce a third foodstuff at a desired ph , stream c . providing the stream of first foodstuff is shown generally at 50 in fig2 and includes a pumping step 51 and ph modifying step 52 . pumping step 51 comprises pumping the initial foodstuff from supply 11 in fig1 to ph modifying arrangement 12 using first pump 20 . ph modifying step 52 comprises contacting the initial foodstuff with ph modifying material as shown at step 53 , and then mixing the initial foodstuff and ph modifying material as shown at step 54 . the method includes sensing the ph of the first foodstuff at step 55 for use in controlling the combination of the two foodstuff streams . providing the second foodstuff includes pumping foodstuff from the initial supply as shown at step 56 in fig2 . this pumping step is performed using second pump 21 shown in fig1 . it will be appreciated that the two streams of foodstuff may not be taken from a common supply as shown in fig1 . the second foodstuff shown as stream b in fig1 may be material which is not ph modified , or which is under modified . in any event , the second foodstuff has a ph which is opposite to a desired or target ph level with respect to the ph of the first foodstuff . where the ph of the first foodstuff is higher than desired , the ph of the second foodstuff is lower than the desired , target ph level , and where the ph of the first foodstuff is lower than desired , the ph of the second foodstuff is higher than the target level . the proportion at which the stream of first foodstuff and stream of second foodstuff is combined at step 58 depends upon the ph of the first and second foodstuffs and the desired fmal ph . fig2 shows a single proportion control step 59 . this control step may include controlling the flow rate of the first foodstuff in stream a in fig1 through first pump 20 . the control step may also or alternatively include controlling the flow rate of the second foodstuff in stream b in fig1 through second pump 21 . fig2 also indicates that the control step may include controlling the addition of ph modifying material through contactor 24 . for example , the control step may include modifying the pressure at which ph modifying material is supplied to contactor 24 , or the flow rate of ph modifying material into the contactor . fig2 also shows mixing step 61 after combining step 58 . this mixing may be performed as a separate step by a separate mixer such as mixing device 36 in fig1 or by a mixing arrangement included in combiner 14 . the purpose of the mixing at step 61 is to thoroughly blend the first and second foodstuffs together to form the third foodstuff having the target uniform ph . the ph of this third foodstuff may be checked at step 62 in fig2 to ensure the desired ph level has been obtained although the invention is described above with reference to a continuous ph modifying process , the method of the invention as defined in the following claims is not limited to a continuous process . the first and second foodstuffs may simply be combined together in a single batch and then mixed to produce a final mixed foodstuff having the target ph . also , the ph modified foodstuff such as the material exiting ph modifying arrangement 12 in fig1 need not be combined immediately with the second foodstuff . rather , the first or ph modified foodstuff may be packaged and shipped to a remote mixing facility where it is combined and mixed with the second foodstuff in the proportion required to produce the target ph . the preferred form of the invention utilizes an over - ammoniated foodstuff as the first foodstuff and an untreated foodstuff as the second foodstuff . the first foodstuff may be over ammoniated to raise the ph of the material over 7 to as much as 10 . 5 , but preferably between 7 . 0 and no more than approximately 9 . 5 . for example , a communicated meat product such as lean finely textured beef “ lftb ” may be over ammoniated to a ph of 9 . 0 and mixed in a 1 to 1 . 3 ratio by weight with ground beef at a ph of 5 . 5 to produce a mixed product ( 43 % lftb and 57 % ground beef ) having a ph of approximately 7 . a lower ph in the lftb would allow a higher percentage of lftb to be used with ground beef in the mixed product to produce a mixed product having the desirable ph of approximately 7 . as another example , lftb over ammoniated to a ph of 8 . 0 may be mixed in a 1 to 7 ratio by weight with ground beef at a ph of 5 . 5 to produce a mixed product ( 59 % lftb and 41 % ground beef ) having a 7 ph . the above described preferred embodiments are intended to illustrate the principles of the invention , but not to limit the scope of the invention . various other embodiments and modifications to these preferred embodiments may be made by those skilled in the art without departing from the scope of the following claims .
a stream of first foodstuff has a first ph and a stream of second foodstuff has second ph . the first ph and second ph are oppositely related to a third or target ph for the foodstuff such that one ph level is above the target level while the other ph level is below the target level . the two streams and are combined in a proportion to produce a combined or third foodstuff at the target ph . the first ph and second ph are sensed or otherwise determined , preferably on a continuous basis , and then these ph values are used to determine the proportion at which the stream of first foodstuff and stream of second foodstuff are combined and mixed . particularly , the ph modification can be loosely controlled to produce an over - modification in the first foodstuff and then the stream of second foodstuff may be combined with the stream first foodstuff to produce a stream of material having the target ph .