with reference to fig1 and 2 , a food refrigeration system 10 in accordance with the present invention is illustrated . food processing system 10 is utilized in the freezing of food 12 and is provided with three cooling stages formed by a hydrocooler 14 , a liquid nitrogen immersion freezer 16 , and a mechanical freezer 18 . food refrigeration system 10 is designed to be used in a seafood processing plant and food 10 comprises clams to be frozen for preservation purposes . the food is first loaded onto a conveyor belt 20 located within hydrocooler 14 . hydrocooler 14 is of tank - like construction and contains cooling water 22 that is supplied by a delivery - pipe 24 and is drained from a drain 26 . cooling water 22 has a temperature lower than that of food 12 to produce a temperature difference by which heat is transferred from food 12 to cooling water 22 . after such heat transfer , food 12 is carried from hydrocooler 14 by conveyor 20 and deposited on central , horizontal conveyor 27 . food is next deposited on inclined conveyor 28 which deposits food 12 on an inlet conveyor 30 of liquid nitrogen immersion freezer 16 . as illustrated , liquid nitrogen immersion freezer 16 consists of a trough 32 for receiving liquid nitrogen 34 . liquid nitrogen 34 is supplied via an inlet pipe 36 having an opening 37 . trough 34 is covered by an insulated cover 38 having a vent 40 . food 12 is immersed in liquid nitrogen 34 via a conveyor 42 and is expelled by an outlet conveyor 43 onto a shake table 44 . during immersion of food 12 . heat is transferred from food 12 to liquid nitrogen 34 . such heat transfer causes liquid nitrogen 34 to boil off into a cryogenic vapor of about 77k . it is to be noted that immersion freezer 16 can be a cif - 300 series liquid nitrogen immersion freezer manufactured by koach engineering mfg , inc . of 8950 glenoaks blvd ., sun valley , calif ., 91352 - 2059 . shake table 44 conducts food 12 to mechanical freezer 18 which can be a fluidized bed freezer , specifically a lewis iqf freezer series or a flo - freeze series freezer , manufactured by frigoscandia contracting , ab of rushhallsgatan 21 , s - 251 09 helsingborg , sweden . in food processing system 10 , hydrocooler 14 functions to pre - chill and clean food 12 before being crust frozen in liquid nitrogen immersion freezer 16 . after being crust frozen in liquid nitrogen immersion freezer 16 , freezing is completed , that is food 12 is frozen throughout , in mechanical freezer 18 . in food processing system 10 , the amount of heat required to be transferred from food 12 in the crust freezing of food 12 is distributed between hydrocooler 14 and liquid nitrogen immersion freezer 16 . in other words , a portion of the heat required to be transferred from food 12 is transferred to cooling water 14 and a remaining portion of the heat required to be transferred to liquid nitrogen 34 . as may be appreciated , the greater the amount of heat transferred between food 12 and cooling water 14 , the less heat transfer will be required between food 12 and liquid nitrogen 34 . the lower this latter heat transfer , the less quantity of liquid nitrogen 34 that will boil off into a vapor and hence the lower the rate that liquid nitrogen 34 will be required to be supplied to liquid nitrogen immersion freezer 16 . in the prior art , the temperature of cooling water 22 , as supplied by ground water or municipal water supply , is lower than that of food 12 and hence , there is some degree of heat transfer between food 12 and cooling water 22 . in accordance with the present invention , the cryogen , in this case liquid nitrogen , is further conserved by recovering the cooling potential of the nitrogen vapor in cooling water 22 . the cooling potential of the nitrogen vapor is recovered by transferring further heat from cooling water 22 to the nitrogen vapor prior to the reception of cooling water 22 in hydrocooler 14 . as a result of such further heat transfer between cooling water 22 and the nitrogen vapor , the temperature of cooling water 22 is lowered and thus , there exists a greater degree of heat transfer between cooling water 22 and food 12 over the prior art . consequently , cryogen requirements are further reduced over hydrocooler and cryogenic freezer arrangements of the prior art . a major problem in recovering the cooling potential of the nitrogen vapor , is that the nitrogen vapor venting from liquid nitrogen immersion freezer 16 , can have a temperature as low as 77k , or in other words , low enough to freeze water . this problem is solved in the present invention by accomplishing the heat transfer between cooling water 22 and boiled off nitrogen vapor in eductor 50 . as will be discussed , eductor 50 is connected to a phase separation tank 52 in which cooling water 22 accumulates . accumulated cooling water 22 is preferably gravity fed from an outlet 54 of phase separation tank 52 to hydrocooler 14 via delivery line 24 connected to outlet 54 . after having had heat transferred from food 12 to cooling water 22 , cooling water 22 drains through drain 26 of hydrocooler 14 and is recycled to phase separation tank 52 via a recycle line 56 having an in - line recycle pump 58 and an optional filter 60 , used when cooling water 22 is also used in cleaning food 12 . cooling water 22 is pumped through eductor 50 by a pump 62 , powered by an electric motor 64 . pump 62 has an inlet 66 and an outlet 68 . a transfer pipe 69 communicates between inlet 66 of pump 62 and the bottom of phase separation tank 52 . an outlet pipe 70 communicates between outlet 68 of pump 62 and eductor 50 . additionally , eductor 50 is connected to vent 40 of liquid nitrogen immersion freezer 16 by a vent duct 72 . pump 62 pumps cooling water 22 through eductor 50 , which in turn , draws the boiled off nitrogen vapor into a mixture with cooling water 22 . as a result of such mixing , heat is directly transferred from cooling water 22 to the nitrogen vapor . although cooling water 22 may freeze to some degree at or near the center of the central passageway 76 , the constant flow of cooling water 22 prevents freezing from occurring throughout th entire cross - section of central passageway 76 . any such frozen water would subsequently thaw in phase separation tank 52 . with reference to fig3 a preferred embodiment of eductor 50 is illustrated . eductor 50 includes a body portion 74 having a central passageway 76 . in one end of central passageway 76 , an internal nozzle 78 is connected to body portion 74 . internal nozzle 78 is in turn connected , at one end , to outlet pipe 70 . the other end of internal nozzle 78 defines nozzle orifice 80 within central passageway 76 . beyond nozzle orifice 80 , central passageway 76 gradually reduces in transverse cross - sectional area to a central region 82 and then gradually increases to form a discharge opening 84 . body portion 74 is also provided with a gas inlet section 86 connected to vent duct 72 . gas inlet opening section 86 is provided with an inlet passage 88 in communication with central passageway 76 near restriction orifice 80 . as may be appreciated , cooling water 22 undergoes a drop in pressure when passing through restriction orifice 80 . the drop in pressure in turn produces a low pressure region in central passageway 76 of eductor 50 which draws the nitrogen vapor through vent duct 72 and into a mixture with pumped cooling water 22 . the mixing of the nitrogen vapor and cooling water 22 occurs within central passageway 76 , beyond nozzle orifice 80 . maximum mixing occurs in central region 82 . thereafter , a mixture of cooling water 22 and nitrogen vapor is discharged from eductor 50 through its discharge orifice 84 . discharge opening 84 of eductor 50 can be mounted on a suitable mounting ( not illustrated ) to directly deliver the cooling water from eductor 50 to hydrocooler 14 . however , since the flow of discharge cooling water 22 is violently erratic , it is preferable to first separate the nitrogen vapor from cooling water 22 before delivering cooling water 22 to hydrocooler 14 . it is also preferable to separate the nitrogen vapor from cooling water 22 so that the nitrogen vapor is conducted some distance from the work area surrounding food refrigeration system 10 in order to safeguard the health of workers . in addition to the foregoing , it is important that no flow restriction be placed in the path of cooling water and nitrogen vapor discharge from eductor 34 . such a flow restriction could cause eductor 34 to overflow . in the present invention , the nitrogen vapor is separated from cooling water 22 and the mixture of nitrogen vapor and cooling water 22 is discharged from eductor 50 without flow restriction by discharging cooling water 22 from eductor 50 into phase separation tank 52 . although phase separation tank can be constructed so as to be open at the top thereof , preferably it is provided with a top wall 90 having two openings 92 and 94 . eductor 50 is connected to top wall 90 with its discharge opening 84 aligned with opening 92 . a vent 96 is also connected to top wall 90 in alignment with the other opening 94 . cooling water 22 discharged from eductor 50 is thus , discharged into phase separation tank 52 . at the same time , nitrogen vapor separates from cooling water 22 and is vented through nitrogen conduit 96 at some distance from the work area surrounding food refrigeration system 10 . as mentioned previously , cooling water 22 accumulated in phase separation tank 52 , gradually feeds to hydrocooler 14 by provision of a delivery pipe 24 connected to outlet 54 . it is to be noted that although cooling water 22 may be recycled through recycle pipe 56 , this is entirely optional and instead , cooling water may be drained simply into the municipal sewer system , with of course , the greater concomitant expense of continually supplying cooling water . a nitrogen exhaust outlet 98 having a butterfly damper 100 can be connected to vent 96 . as may be appreciated by those skilled in the art , the degree to which nitrogen vapor is suctioned by eductor 50 is dependent upon a difference in pressure of the cryogenic vapor as measured between inlet passage 88 and discharge opening 84 . the greater this difference in pressure , the greater the rate at which nitrogen vapor is suctioned by eductor 50 . butterfly damper 100 is operable to change the area of exhaust outlet 98 by rotating between positions in which exhaust outlet 98 is open and closed . as exhaust outlet 98 is closed by damper 100 , the back pressure within eductor 50 increases , that is the pressure at discharge opening 84 . this results in nitrogen vapor being suctioned into eductor 50 to a lesser extent and thus , lowering the temperature of cooling water 22 to a lesser degree . in the illustrated preferred embodiment , electric motor 64 is rated at about 15 . 0 horsepower . eductor 50 is designed to draw nitrogen vapor at about 2 , 000 . 0 kg / hr ., and at a temperature of about 200 . 0k . cooling water 22 is pumped through eductor 50 at about 227 . 0 liters / minute . recycle pump 58 is identical to pump 62 and is powered by an electric motor also rated at about 15 . 0 horsepower so as to pump recycle cooling water 22 at about 113 . 0 liters / minute . the entry pressure of cooling water 22 in eductor 50 is about 4 . 05 × 10 5 pascals and the mixture of cooling water and nitrogen vapor is discharged at about atmospheric pressure . eductor 50 is designed with restriction orifice 80 having a diameter of about 1 . 50 cm . ; gas inlet section 86 having an internal diameter of about 25 . 4 cm . ; central region 82 having a diameter of about 10 . 16 cm . ; and discharge opening 84 having a diameter of about 25 . 4 cm . hydrocooler is designed to hold about 400 . 0 liters and phase separation tank 52 is designed to accumulate 340 . 0 liters of cooling water 22 . the food refrigeration system , described above , is designed to freeze clams at a rate of about 2200 . 0 kg / hr . with liquid nitrogen being supplied at about 2 , 000 . 0 kg / hr . in the prior art , the cooling water supplied to hydrocooler 14 is either municipal water or well water having a temperature of 290k . in accordance with the present invention , the cooling water can be reduced in temperature to about 275 . 0k . the increased temperature spread between the clams and cooling water 22 results in a savings of liquid nitrogen of as much as 20 . 0 %. the percentage reduction in the nitrogen consumption will of course decrease with increasing system thermal inefficiencies . conversely , it will increase with decreasing temperature of the nitrogen vapor vented from the immersion freezer . although the preferred embodiment has been illustrated with reference to a food refrigeration system 10 having three cooling stages , the present invention would have equal applicability to other food refrigeration systems having two or greater number of cooling stages . for instance , if it were desired for a food article to simply be frozen without first being crust frozen , the food refrigeration system might comprise a hydrocooler and a liquid nitrogen immersion freezer . the conveyor belt associated with such liquid nitrogen immersion freezers would be set to run at a rate such that the resident time of articles of food in the immersion freezer were sufficient to completely freeze food articles . in a like embodiment , it would also be possible to replace the immersion freezer with a carbon dioxide spiral belt freezer . in such an embodiment , carbon dioxide vapor venting from such a freezer would be drawn into an eductor for mixture with the cooling water flowing to the hydrocooler . in addition to the foregoing , the present invention could be adapted for use in a food processing system in which a liquid nitrogen immersion freezer were utilized as a chiller . in such a system , a hydrocooler and eductor arrangement would have to be added . eductor 50 and pump 62 form an invention in their own right . such invention in its broadest aspects comprises an apparatus and method for cooling an article with a motive fluid . in food refrigeration system 10 , the motive fluid is cooling water 22 which is pumped through eductor 50 to draw cryogenic vapor into a mixture with the cooling water and thereby lower the temperature of cooling water 22 . cooling water 22 having had its temperature lowered is then supplied to a heat transfer device , hydrocooler 14 , to effect an enhanced heat transfer from the article , which comprises food 12 , to cooling water 22 . as may be appreciated , such invention has broader applications that lie beyond food refrigeration system 10 . for instance , a motive fluid , such as water , could be pumped through an eductor connected to any source of cryogenic vapor and the discharge of water could be directed against an article to be cooled with an enhanced heat transfer rate . although preferred embodiments have been shown and described in detail , it would be readily understood and appreciated by those skilled in the art , that numerous omissions , changes , and additions may be made without departing from the spirit and scope of the invention .
the present invention provides a food processing system and method for refrigerating articles of food . the food processing system includes at least two cooling stages formed by a cryogenic freezer and a hydrocooler . the cryogenic freezer receives the articles of food and transfers heat from the articles of food to the cryogen so that the articles of food are refrigerated . after the transfer of heat from the articles of food to the cryogen , the cryogen boils off to form cryogenic vapor . the hydrocooler receives the articles of food prior to the cryogenic freezer and transfers heat from the articles of food to supplied cooling water . such heat transfer reduces the quantity of cryogen required to refrigerate the articles of food . additionally , an eductor is connected to a pump and to vent line from the cryogenic freezer . the cooling water is pumped through the eductor to suction cryogenic vapor from the cryogenic freezer and to mix the cryogenic vapor and the cooling water prior to reception of the cooling water in the hydrocooler . such mixing transfers heat from the cooling water to the cryogenic vapor to increase the heat transfer between the articles and the cooling water in the hydrocooler . as a result of such increased heat transfer , the amount of cryogen required in refrigerating the articles is further reduced the eductor and pump combination has general application to the cooling of articles .