in the following description of the invention , the same reference numeral will be used to identify the same or similar elements in the each of the figures . fig1 through 5 , and 7 illustrate a waste milk treatment system 20 in accordance with the present invention , including : a controller 22 ; a milk pump 24 ; an inlet conduit 26 ; an outlet conduit 28 ; a pump inlet conduit 29 ; an ultraviolet milk treatment device 30 ( referred to herein as “ uv reactor ”); and an outlet conduit 32 . a storage vat 34 and a mobile platform 36 ( fig5 ) are used in connection with the milk treatment system 20 . generally , the depicted milk treatment system 20 uses the milk pump 24 to pump milk through the inlet conduit 26 , and into the uv reactor 30 . while being treated in the uv reactor 30 , the milk is heated or cooled in a heat exchanger to be in a temperature range that minimizes the growth of bacteria without destroying the immunoglobulins that are important for calf health . the treated milk moves through the outlet conduit 28 to be temperature adjusted and stored in the storage vat 34 . the milk storage vat 34 may be supported on the mobile platform 36 for transporting the milk to calves before the treated milk falls out of a predetermined temperature range . the mobile platform 36 may also include a milk distribution pump 39 to pump milk through a feed tube 41 to calves . more specifically , the controller 22 activates the pump 24 to circulate milk to the uv reactor 30 which is preferably surrounded by a heat exchanger 38 to raise milk temperature to between 85 ° f . and 120 ° f . and then circulates the warmed milk through the uv reactor 30 at an appropriate rate and frequency to kill harmful bacteria . the milk can then be chilled and stored or fed directly to calves . by raising the milk temperature to only the range of 85 ° f . to 120 ° f ., there is much less destruction of immunoglobulins and the milk is still safely pasteurized by the uv light from the uv reactor 30 . unlike batch pasteurizers , uv reactors do not rely on the temperature of the milk to kill bacteria . instead , the uv light alone in the range of 200 to 280 nanometers , uvc range ( germicidal range ), kills the bacteria . nonetheless , milk temperature is important because cold milk is churned by the pump and piping system and butter flakes can form that are less likely to be adequately treated by the uv light . raising milk temperature to 85 ° f . or higher is sufficient to melt or reduce the size of butter flakes that form so that the milk is adequately treated by the uv reactors . preferably , the milk temperature is raised to above 95 ° f ., and more preferably to above 100 ° f . on the other hand , heating the milk to too high of a temperature can destroy beneficial immunoglobulins . an upper end of the temperature range to minimize destruction of the immunoglobulins is 120 ° f . a temperature range of about 85 ° f . to about 120 ° f . includes a feeding temperature range of between about 100 ° f . and about 110 ° f . if the milk is to be fed directly to calves , then heating to the feeding temperature range of between about 100 ° f . to 110 ° f . for pasteurizing is appropriate . if the milk is to be chilled and stored after pasteurization , a milk temperature in the lower end of the range of 85 ° f . to 120 ° f . will produce adequate results in the present invention . it is noted that treated waste milk may need to be transported to the calves where they are kept in the dairy facility . in this situation , heating the milk to above the feeding temperature range can compensate for milk cooling as it is being transported . heat loss is a function of ambient conditions , the time between pasteurization and feeding , and other factors . thus , using the present invention , milk temperature can be adjusted to compensate for these and other factors in any particular dairy situation . a preferred heat exchanger 38 for use with the present invention is disposed around the uv reactor 30 . the heat exchanger 38 is depicted in fig7 and includes an inlet 62 , a water jacket 64 , and an outlet 66 . the water jacket 64 surrounds and is substantially coaxial with the uv reactor 30 to define an annular space through which water , air or other heat exchanger fluid can flow to adjust the temperature of the uv reactor 30 and the milk being pasteurized therein . preferably , the water jacket 64 is made of stainless steel , but other materials can be used . the inlet 62 is in communication with a source of water or other fluid , and the fluid source can be a hot water heater , for example . preferably , the hot water heater is a dedicated unit for the heat exchanger 38 , in a closed loop configuration with the heat exchanger 38 . other types of heat exchangers can be used with the present invention , and be positioned at any point in the milk flow path . a temperature sensor 44 is used to determine milk temperature throughout the pasteurizing process . preferably , the temperature sensor 44 is a precision fahrenheit temperature sensor model lm34 , available from national semiconductor . if the pasteurization process has been completed and the desired milk temperature has not been reached , milk will continue to be circulated until the desired temperature is reached . further , the controller 22 is preferably in communication with a milk quantity sensor 43 , which is preferably an integrated silicon pressure sensor ( mpx5010gp , case 867b - 04 ) available from freescale semiconductor ( www . freescale . com ) that uses a long stand tube 42 that traps air when the liquid level of the vat 34 increases . as the milk level in the vat 34 rises , pressure in the long stand tube 42 increases . the milk quantity sensor 43 generates a voltage readout signal that is communicated to the controller 22 to automatically determine run time for any batch size of milk . preferably , the controller 22 is set initially by a skilled installer or technician . adjustments can be made by any dairy operator at an operator interface 45 to adjust temperature , flow rates , treatment time or any other condition in the pasteurizing process . the controller 22 also provides a display 42 indicating how long it has been since the pasteurizing process has been completed and the milk &# 39 ; s current temperature so that re - circulation through the heat exchanger 38 can bring milk temperature back within a desired range . the display 42 can provide a dairy operator with any relevant information , including operating times , flow rates , milk temperature , component failure , maintenance requirements , and so on . finally , after pasteurized milk has been distributed to calves or the mobile platform 36 , the milk treatment system 20 can be coupled to a wash system ( not illustrated ) for automatic cleaning and preparation for the next pasteurizing cycle . the milk treatment system 20 can include one or more uv milk pasteurizer reactors 30 . three uv reactors 30 are used in the illustrated embodiment . uv milk pasteurizers for use in the present invention can be those of the type disclosed in rix et al ., u . s . pat . no . 6 , 916 , 452 ( incorporated herein by reference ). the uv reactors 30 as depicted in fig7 include an inlet 50 , an outlet 60 , a quartz tube 52 , a uv light bulb 56 disposed inside the quartz tube 52 to prevent milk from contacting the light bulb 56 . other types of tubes can be used to protect the light bulb 56 from being damaged by milk . surrounding the quartz tube 52 is an outer tube 58 ( preferably made of stainless steel ) that defines with the quartz tube 52 , an annular milk flow channel . the heat exchanger 38 surrounds the outer tube 58 . milk flows through the inlet 50 , the annular flow channel 58 where it is pasteurized by uv light , and out the outlet 60 . the uv light bulb 56 is preferably a gia972t5lca / 2s07 / pt - 18 ″/ 4w / n / cb - 061 ( uv pure ) available from first light technologies , inc ., p . o . box 191 , 212 ideal way , poultney , vt . 05764 . ballasts for use in the uv reactor 30 preferably are electronic ballasts , evg 100 . . . 200w / 230v ac , available from zed — ziegler electronic devices gmbh . the quartz tube 52 is about one inch in outside diameter and the inside diameter of the outer tube 58 is about 1 . 37 inches . further , the outside diameter of the outer tube 58 is about 1 . 50 inches in diameter and the inside diameter of the water jacket 64 is about 2 . 37 inches , but other dimensions of the water jacket 64 are possible . other combinations of bulbs and ballasts are possible , and it is desirable that the combination be ul rated . the uv reactors 30 can be used in series or parallel to reduce the number of times milk is circulated through the uv reactors . preferably , the controller 22 of the present invention is in monitoring communication to monitor uv reactor 30 components and adjust treatment time to accommodate defective uv light bulbs 56 , ballasts or related components . one way to monitor such components is to monitor electrical current flow through a light bulb , for example . if the bulb is not working no current will be flowing through the bulb . the pump 24 pumps milk through the uv reactor 30 at a rate that ensures optimal sterilization of milk and / or colostrum and prevents stagnation in the uv reactor 30 related piping , connections , and control systems . preferably , the flow rate is about 17 gallons per minute , but other flow rates may be used as other system components are changed in size or type . preferably , the controller 22 is programmed to operate the milk pump 24 at about seventeen gallons per minute flow rate . using one uv reactor 30 alone , this flow rate will result in pasteurized milk after about 40 “ passes ” through the uv reactor 30 . using two uv reactors 30 in series will require about 20 passes , and using three uv reactors in series will require about 13 . 4 passes through the reactors 30 . for fifty gallons of waste milk at 2 . 9 minutes per pass , the uv pasteurizing process will take about 59 minutes . this is an improvement over batch pasteurizing heating , treatment , and cooling times . further , the present invention saves time and energy primarily because the milk does not require heating to such high temperatures . tests have shown 30 % to 70 % time savings for the present invention over the batch pasteurizing process . further , the present invention promotes efficiencies in dairies because a milk vat 34 can be filled hours before milk is needed , and the pasteurizing process can be initiated automatically by the controller 22 at an appropriate time to warm , pump , pasteurize and store the milk on a mobile platform 36 for transport to calves . this function is preferably set by a pasteurization start timer accessible at the operator interface 45 . as depicted in fig6 , the present invention also can include a stand pipe 42 with milk volume detector 38 for determining the amount of milk in the vat 34 . the controller 22 calculates and controls treatment time based on the milk quantity in the vat 34 . for example , a 100 gallon vat 34 can be filled or partially filled with 100 gallons or 5 gallons of milk , and the present invention will automatically set the approximate treatment time . apparatus of the present invention can also include a mobile platform 36 ( fig5 ) or storage vat 34 for transporting the milk from the pasteurizer to the calves at remote locations . the mobile vat 36 can be insulated and include a spray ball or device for cleaning the mobile vat 36 . a mobile platform 36 may simply be a frame and wheels to transport the vat 34 in which the milk was stored during pasteurization . comparisons between the present invention and the prior art batch pasteurizers illustrate the efficacy of the present invention for use with waste milk and colostrum . in this example a , the standard batch pasteurizer is more effective than the uv pasteurizer for all the organisms tested in killing harmful bacteria , but when milk is used , the invention is effective for all three organisms tested ( 99 . 98 % for e . coli , 100 % for b . cereus and 99 . 992 % for salmonella ). however , when colostrum is used the invention is certainly less effective for all three to the point where it may not be effective enough . more research may be needed to determine the maximum effectiveness , in terms of increasing treatment time , for effective bactericidal action on microorganisms when present in colostrum . further , single radial immunodiffusion assays were also run for these samples for bovine igg . the batch pasteurizer samples displayed a significant reduction in igg ( around 43 %) whereas the uv samples had no reduction in igg at all . thus , the present invention as shown in example a results in healthier waste milk , but possibly not healthier colostrum . b substrate ( milk or colostrum ) right after getting up to the pasteurization temperature ( time = 0 ). this takes about one - half an hour . for this example , the uv pasteurizer trial for the milk was repeated , with the addition of another time at 22 minutes exposure of the milk to uv light . these results are very similar to example a with a satisfactory level of kill after 15 minutes exposure for 10 gallons of milk with all three bacteria tested . the second part of the study utilized colostrum which example a had an ineffective level of kill after 15 minutes for the organisms tested . example b utilized exposure levels of 30 and 45 minutes . these results indicated better efficacy in two of the three organisms at 15 minutes versus example a . example a shows the efficacy at 15 minutes to be marginal for two organisms and unacceptable for the third ( bacillus ). at both 30 and 45 minutes exposure , however , the efficacy of the pasteurizer of the present invention for all three organisms was adequate to very good . further , single radial immunodiffusion assays were also run for these samples for bovine igg . the results indicated no reduction in immunoglobulin ( igg ) after 15 minutes and a relatively minimal reduction in immunoglobulin ( igg ) after 30 and 45 minutes . thus , the present invention as reflected in example b results in healthier milk and colostrum than the prior art batch pasteurizer . this example utilized colostrum at the same exposure levels of 15 , 30 and 45 minutes as example b . these results indicated that the uv pasteurizer of the present invention overall is still effective at 30 and 45 minutes , especially the latter time . the only possible exception is possibly the bacillus where only the 45 minute exposure time showed solid results . the results generally showed less percent kill then the previous test at the same exposure times , but the time 0 concentrations were also higher , which probably accounts for this reduction in kill . in real field use , the concentration of these pathogens is very unlikely to be anywhere near what is being tested in this example . it can therefore be concluded that the kill rates are satisfactory at both 30 and 45 minutes . further , single radial immunodiffusion assays were also run for these samples for bovine igg . the results indicated minimal or no reduction in immunoglobulin ( igg ) after 15 , 30 and 45 minutes . this is therefore , a distinct improvement over batch pasteurizing . the above examples illustrate the effectiveness of the present invention in killing three types of pathogens while preserving essentially all of the immunoglobulins in milk and colostrum . the previous detailed description of the preferred embodiments of the invention are presented for clearness of understanding , and are not intended to limit the scope of the following claims . further , the term “ milk ” as used in the claims is intended to be broad enough to include milk , waste milk , non - saleable milk , colostrum or any other calf feed supplement that would benefit from pasteurizing prior to feeding to calves .
the present invention is directed to a system for treating milk and colostrum . the system includes a circulation pump and piping system , a heat exchanger for adjusting and / or maintaining milk temperature , and an ultraviolet light treatment device that treats the milk .