EP2194774A2 - Equipment for transferring milk from a milking machine to a storage tank - Google Patents
Equipment for transferring milk from a milking machine to a storage tankInfo
- Publication number
- EP2194774A2 EP2194774A2 EP08829572A EP08829572A EP2194774A2 EP 2194774 A2 EP2194774 A2 EP 2194774A2 EP 08829572 A EP08829572 A EP 08829572A EP 08829572 A EP08829572 A EP 08829572A EP 2194774 A2 EP2194774 A2 EP 2194774A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- milk
- heat exchanger
- storage tank
- transfer
- upstream
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
Classifications
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01J—MANUFACTURE OF DAIRY PRODUCTS
- A01J5/00—Milking machines or devices
- A01J5/04—Milking machines or devices with pneumatic manipulation of teats
- A01J5/044—Milk lines or coupling devices for milk conduits
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01J—MANUFACTURE OF DAIRY PRODUCTS
- A01J9/00—Milk receptacles
- A01J9/04—Milk receptacles with cooling arrangements
Definitions
- the present invention relates to installations for transferring milk from a milking machine to a storage tank, and in particular to the installations comprising a milk collection tank associated with a transfer pump, followed by a piping system ( s) equipped with a heat exchanger for cooling or at least pre-cooling the milk transferred.
- facilities for milk collection include, from upstream to downstream along the direction of milk flow, the following main functional elements:
- a facility for the transfer of milk consisting of a milk collection tank (or milk chamber) associated with its transfer pump, followed by a piping system (s), and - a tank or tank, serving storage of milk pending recovery by the dairy.
- the transfer pump ensures the flow of the milk along the transfer lines to the storage tank; for this purpose, it is controlled, during milking, from the information provided by a milk level sensor disposed in the harvesting tank.
- This pump can also be used to inject pressurized water into the transfer lines, for their cleaning; it works in this case continuously.
- the transfer pump preferably has a high flow rate (for example of the order of 200 L / minute).
- this transfer pump runs for a short time (a few minutes) and in successive short cycles (often of a few seconds) for the transfer of the milk, this with regard to the total duration of the treats (which is usually of the order of 1 hour).
- the preservation of the organoleptic and physico-chemical qualities of the milk requires, in particular, its rapid cooling after harvest.
- GB-1 465 516 concerns in this case a facility for the collection of milk, the pipe system (s) is equipped with a heat exchanger for cooling the milk passing through.
- This installation also comprises a recirculation pump arranged, on the one hand, to collect the milk within the storage tank, and on the other hand, to transfer this milk within the pipeline system (s), upstream of the aforementioned heat exchanger.
- This installation thus ensures the cooling of the milk during two successive operations: a first cooling, during the first passage of the milk within the pipeline system (s), from the harvesting tank to the storage tank,
- the recirculation pump reinjects the milk from the storage tank into the pipe system (s), in order to reach and maintain the desired temperature. More traditionally, the collected milk is cooled within the storage tank which is refrigerated.
- the piping system (s) of the transfer installation may comprise a heat exchanger ensuring the cooling of the milk during its transfer, or at least its pre-cooling, even before reaching the storage tank.
- the action time of the heat exchanger is very short compared to the overall milking time (about 1/10 of the milking time); and efficiency cooling or pre-cooling on the milk before it flows into the storage tank is thus relatively limited.
- the Applicant has developed a new transfer installation structure to optimize the action of the heat exchanger on the milk during its transfer, and therefore before it flows into the storage tank.
- This new structure also makes it possible to improve the energy balance of the installation, in particular by limiting the energy consumption of the storage tank.
- the transfer installation comprises a pipe system (s) provided with a heat exchanger, and means that allow a loop circulation of at least a portion of the milk to the breast / through said heat exchanger, this upstream of the storage tank.
- This recycling of the milk during transfer allows its passage several times within the heat exchanger, and thus increases its circulation time or passage in this exchanger. This provides an effective and optimal heat exchange between the milk being transferred and the coolant, throughout the milking period if necessary and before its final flow into the storage tank.
- the cooling of the milk at the level of the heat exchanger is obtained with a lower energy consumption compared to that required at the milk tank, thus improving the energy balance of the installation.
- the means which allow the loop circulation of the milk in the exchanger are in the form of at least one circulator, suitable for withdrawing the milk downstream and transferring it upstream.
- upstream and downstream refer to the meaning of milk flow within the pipeline system (s), from the transfer pump to the storage tank.
- the circulator (s) ensure a loop circulation of the milk over the entire surface of the exchanger. This uses all the cooling capacity of the exchanger.
- the volume capacity of the heat exchanger is at least equal to the volume of milk transferred during a cycle of the milk pump.
- the heat exchanger is of the tubular type. It advantageously comprises at least one module consisting of at least one rectilinear central tube for the circulation of milk, housed concentrically within a rectilinear peripheral tube for the countercurrent flow of a refrigerant fluid.
- the central and peripheral tubes are advantageously inclined downwards, from upstream to downstream.
- This particular structure allows a natural flow of milk and refrigerant by gravity, useful especially for emptying and cleaning operations.
- the module or at least one of the modules (see all the modules), consists of two central tubes each housed in a peripheral tube and connected by a junction elbow, the first top tube starting from the side of the circulator and the second lower return tube returning from the side of the same circulator.
- These forward and return sections are inclined downwards, from upstream to downstream, thus forming a Ve of substantially horizontal axis.
- This particular structure of V-module (s) has the advantage of combining a compact appearance, with cooling efficiency and ease of cleaning.
- the peripheral tubes advantageously terminate at the junction bend, and they are connected to this side by an external pipe. This structure makes it possible in particular to reduce the costs of production and to facilitate its dismantling.
- the heat exchanger comprises several modules, arranged in parallel and / or in series.
- at least some of the successive modules are provided with their own means for loop circulation and are powered by separate coolants; the temperature of the refrigerant circulating within a module is then advantageously greater than the temperature of the refrigerant circulating in the module located downstream.
- the present invention also relates to the heat exchanger for the piping system (s) of the milk transfer installation, this heat exchanger comprising at least one circulator adapted to collect and transfer the milk from the downstream to the upstream, with respect to the direction of travel of the latter, to generate its loop circulation.
- the milk is taken at the outlet of the exchanger, to be transferred at its inlet.
- the invention also relates to the method of operation of the transfer installation presented above, this method consisting in ensuring the loop circulation of the milk in the heat exchanger by putting into operation the circulator or circulators at least between some of the cycles of the transfer pump and during at least part of this inter-cycle time, or even during the entire milking period.
- FIG. 1 is a schematic view of a dairy plant part, comprising a milk transfer facility connecting a harvest tank and a storage tank, and whose heat exchanger comprises a single Vee module;
- FIG. 2 is a schematic sectional view of the tubes forming the heat exchanger
- FIG. 3 shows, seen from above and very schematically, a particularly advantageous structure of heat exchanger composed of three V e exchanger modules, mounted in parallel, and intended to equip a transfer facility of the type of Figure 1;
- FIG. 4 is a diagrammatic view of a milk installation part constituting a variant of FIG. 1, the milk transfer installation of which comprises a heat exchanger here formed of two series-connected V e modules, each equipped with his own circulator;
- FIG. 5 is a schematic view of a dairy installation part of the type of Figure 4, the pair of modules in series Vee is here equipped with a single and common circulator.
- the transfer facility 1 connects - a tank 2 (also called “receiver” or “milk chamber”) for the collection of milk from a milking machine (not shown), and - A refrigerated storage tank 3 (still commonly called “milk tank”).
- This transfer installation 1 comprises a pipe system 5, adapted for the circulation of milk, which is associated along its length with different functional elements detailed below.
- the pipe 5 Upstream, the pipe 5 consists of a rectilinear vertical section 5a, called a "milk cane", connected to the tank 2 by means of a transfer pump 6 associated with at least one maximum level sensor (not shown) disposed in said harvesting tank; as developed subsequently, the information provided by this sensor ensures operation in successive cycles of the transfer pump 6, during milking.
- the upstream end of this milk can 5a is connected to the transfer pump 6 via a non-return valve 7; its downstream end is connected to the rest of the pipe 5, through an air intake 8 for purging these pipes.
- the pipe system 5 continues with an intermediate section 5b forming part of a heat exchanger.
- This intermediate section 5b can be set up in the milking parlor, above the working pit.
- the advantage of the heat exchanger 10 will be to ensure cooling (or at least pre-cooling) of the milk transferred before it flows into the storage tank 3.
- the pipe system 5 terminates in a downstream section 5c_, extending to the milk tank 3.
- the heat exchanger is of the tubular type.
- It comprises a set of tubes which form here a single exchanger module 1 1 consisting of the intermediate pipe section 5b, associated along its length with peripheral tubes 12 adapted for the flow against a refrigerant or refrigerating fluid.
- the intermediate section 5b of this exchanger module 1 1 here consists of two straight stainless steel tubes, one upper 5b 'and the other lower 5b "connected to each other by a connecting bend 5b'" of semicircular general shape.
- the rectilinear aspect of the stainless steel tubes 5b 'and 5b "facilitates in particular the cleaning and the control of the phenomena of expansion.
- the stainless steel tubes 5b may have a generally helical shape; they can also consist of a plurality of tubings longitudinal, extending parallel to each other within the peripheral tubes 12.
- the upper tube 5b ' forming the forward tube of the module 11, extends from the downstream end of the milk can 5a to the connecting bend 5b 1 ".
- the second tube 5b corresponding to the lower return tube, extends from the junction bend 5b '"and ends at the terminal section 5c_.
- These stainless tubes go 5b 'and 5b "return are each inclined downwardly, from upstream to downstream, according to inverted slopes with respect to each other.They together form a kind of inclined V on the side, and substantially horizontal axis or plane of symmetry (this axis or plane still corresponds to the bisector of the Vé module).
- This particular Vee shape has the advantage of optimizing the compactness of the exchanger and its emptying.
- the stainless steel tubes 5b 'and 5b " are each housed, concentrically and for a significant portion of their respective length, within one of the tubes rectilinear peripheral 12, respectively 12 'and 12 ".
- peripheral tubes 12 stop just at the ends of the associated stainless tubes 5b 'and 5b' and they do not cover the joining bend 5b '".
- peripheral tubes 12 are advantageously made of PVC material, for reasons of cost, insulation and pressure drop.
- the annular space 13 delimited between the outer surface of the stainless steel tube 5b and the inner surface of the associated peripheral tube 12 is adapted to allow the flow of the liquid or refrigerant fluid.
- This annular space 13 is advantageously narrow relative to the diameter of the central stainless steel tube 5b, so as to ensure its self-cleaning and to limit its thermal inertia due to fouling.
- the inner diameter of the central tube 5b is between 23 and 38 mm.
- the thickness of the annular space 13 is of the order of 1 to 5 mm.
- Bosses 14, forming spacers are prominently formed and regularly around the periphery of the stainless steel tube 5b so as to maintain its concentric position relative to the associated peripheral tube 12 ( Figure 2).
- the spacers can also be in the form of welded stainless rods longitudinally to the surface of the stainless steel tubes 5b 'and 5b ", these rods bearing against the inner surface of the associated PVC 12 peripheral tube.
- the counter-flow of the cooling fluid within the peripheral spaces 13 is obtained by a connection adapted to fluid input and output channels.
- the channel 15a of cooling fluid supply "cold" is connected to one of the ends of the peripheral tube 12 "associated with the stainless steel tube back
- a connecting channel 15b is provided between the opposite ends of the peripheral tubes 12' and 12 "on the side of the elbow 5b ''.
- the outlet channel 15c extends from the other end of the peripheral tube 12 'associated with the first stainless steel tube 5b', that is to say the end opposite the elbow 5b '".
- the cooling fluid may be water or any other suitable refrigerant fluid.
- its path is implemented by a suitable water pump system, suitable for operation, or by its own pressure if the fluid comes from a distribution network.
- means 16 are provided to allow circulation in a loop (in other words, recycling or recirculation), at least part of the milk in the breast (or in other words "through ”) Of the heat exchanger 10.
- the means 16 in question are in the form of a circulator connected to the inlet and the outlet of the heat exchanger 10, that is to say respectively on the side of the upstream end of the first stainless steel tube 5b 'and the side of the downstream end of the second stainless steel tube 5b ".
- the upstream end of the first stainless steel tube 5b 'and the downstream end of the second stainless steel tube 5b are located on the circulator side 16, the elbow 5b' 'is arranged at a distance from this same circulator 16.
- This circulator 16 is well known to those skilled in the art, and advantageously consists of a similar material to that conventionally used in central heating installations.
- This pump is oriented and configured to ensure a withdrawal of the milk at the outlet of the heat exchanger 10 and upstream of the storage tank 3; the return of the sampled milk is effected upstream, at the inlet, of this same heat exchanger 10.
- the flow rate and the power of the circulator 16 are lower than those of the transfer pump 6.
- the flow rate of this circulator 16 may be of the order of 1500 to 3000 l / h, while the flow rate of the transfer pump is of the order of 8000 to 14000 l / h. This flow rate is such that the speed of the milk is advantageously less than 2.5 m / s.
- the power of the circulator is for example of the order of 70 to 120 W, compared to that of the transfer pump of the order of 736 to 1100 W; the power of this circulator advantageously corresponds to that of a small agitator tank milk.
- the volume capacity of the heat exchanger 10, and more precisely of its intermediate stainless steel section 5b is equal to, or at least approximately equal to, the volume of milk transferred during a cycle of the transfer pump. 6 (usually 10 I to 30 I). This characteristic ensures the recycling in the exchanger of the total volume of milk transferred by a pump cycle, and its heat treatment during the period between two cycles.
- the volume of milk transferred by a cycle of the transfer pump 6 is in particular a function of the average rate of milking.
- the transfer pump 6 and the circulator 16 are controlled in operation by suitable control means. These control means are for example electronic and / or computer means, in particular of the industrial programmable logic controller type or electrical circuit.
- This transfer pump 6 and this circulator 16 will preferably operate in cycles, the duration of which is controlled.
- the duration of the operating cycles of the circulator 16 is advantageously adjusted according to the desired cooling rate for the milk (that is to say still the desired temperature for the milk before it flows into the storage tank); this duration is advantageously independent with respect to the duration of the operating cycles of the transfer pump 6.
- the milk collected by the milking machine is recovered continuously in the tank 2.
- the transfer pump 6 will operate for a predetermined time, for the discharge of a suitable volume of milk, in particular that of the associated exchanger 10.
- This operating time is for example obtained by means of an adjustable delay device (for example between 2 and 10 seconds) associated with an activation / deactivation switch of the pump 6.
- the circulator 16 is turned on; and the coolant is circulated within the exchanger 10.
- the circulator 16 is advantageously also associated with an adjustable delay device (for example between 10 and 60 seconds), associated with an activation / deactivation switch of the circulator 16.
- the operating time of the circulator 16, in particular determining the active heat exchange rate, is advantageously distinct / independent from that of the transfer pump 6.
- This heat exchange time is adapted as a function of the characteristics of the exchanger 10 (in particular the flow rate of cooling liquid), and the final temperature of the milk to be released into the storage tank.
- the sensor of the collector 2 is reactivated. A new milk transfer and pre-cooling cycle can then restart.
- this transfer pump 6 operates in a succession of "short cycles", and ultimately for a “short” overall period; "short” means a significantly lower time than the overall milking period.
- the average duration of milking is about one hour; the operation of the transfer pump generally consists of 90 to 120 successive cycles of the order of 3 to 4 seconds each, ie 5 to 6 minutes of activity.
- the circulator 16 operates according to its own cycle.
- the milk present in the exchanger 10 then circulates in a loop, and travels, continuously and repeatedly, within the upper stainless steel tube 5b 'and then the lower stainless steel tube 5b "(that is to say also within or through the exchanger 10, and upstream of the storage tank), for some applications, these stainless steel tubes 5b are kept under vacuum during recycling.
- the refrigerant fluid also continues to circulate within the heat exchanger 10 and ensures a gradual cooling of the recycled milk.
- the action of the coolant is optimized because of its path in the opposite direction to that of the milk, that is to say from the lower peripheral tube 12 "to the upper peripheral tube 12 '.
- the continuous flow of refrigerant throughout the milking also has the advantage of reducing its flow in the exchanger, and adapt accordingly the section of PVC peripheral tubes.
- the milk cooled in the exchanger is pushed to the storage tank 3, and it is replaced by an equivalent volume of new milk, the latter being intended to undergo in turn the desired cooling.
- an increase in the flow rate of coolant allows a decrease in the operating time of the circulator 16; the volume of the exchanger 10 can then be reduced, and the time between two cycles of operation of the transfer pump 6 shortened.
- the draining of the transfer lines 5 is obtained by virtue of a simple gravity flow, in particular following the opening - of the air intake 8 for the milk and - of a three-way valve 15a ' equipping the inlet channel 15a for the refrigerant. Due to this continuous flow of milk between two cycles of operation of the transfer pump 6, the heat exchange is implemented over a significant and optimal period, independent of the operating time of this transfer pump.
- the milk output of the heat exchanger 10 thus has an optimum temperature, corresponding to that sought by the operator (or at least close to it). This removes most of the disadvantages due to current heat exchangers, operating only concomitantly with the transfer pump 6.
- the circulator 16 can also operate continuously when the washing operations of the transfer lines 5 are implemented, so as to ensure a complete cleaning of the transfer facility.
- FIG. 3 represents an embodiment deriving from the heat exchanger equipping the transfer installation of FIG. 1, and which is distinguished by the presence of several heat exchanger modules V e 1 1, connected in parallel.
- the peripheral tubes 12 are not shown to simplify the description.
- line 5 for the circulation of milk is found: an upstream section 5a and a terminal section 5c, between which extends the intermediate section 5b forming part of the heat exchanger 10.
- the heat exchanger 10 consists here of three exchanger modules 1 1, connected in parallel to a common circulator 16 and the upstream sections 5a and 5c downstream.
- Each module 1 1 is of the type described above in connection with FIG.
- the total volume capacity of the exchangers 1 1 advantageously corresponds to the volume of milk delivered by a cycle of the transfer pump 6.
- the operation of the circulator 16 causes a recycling of the milk within the three exchanger modules 11, this in a manner as described above in relation to Figure 1.
- This heat exchanger structure 10 is particularly interesting for the treatment of milk volumes from a transfer pump having a high flow rate; this configuration also makes it possible to optimize the efficiency of the thermal cooling by distributing the volume of milk to be treated in three juxtaposed modules.
- the transfer facility shown in FIG. 4 still consists of a variant of that described previously with reference to FIG.
- This transfer installation is distinguished by the fact that it comprises a heat exchanger 10 provided with a set of two V e exchanger modules 11 connected in series, one upstream 11a and the other downstream 1 1b.
- each heat exchanger module 1 1 comprises two stainless steel tubes 5b 'and 5b', arranged according to a V e horizontal axis, each associated with a peripheral tube 12 in which circulates the coolant.
- the downstream end of the second stainless steel tube 5b "of the first module 1 1a is thus connected, via an intermediate bend 17, to the upstream end of the first stainless steel tube 5b 'of the second module 1 1b.
- Each module 11 is associated with its own circulator 16, which takes the milk at the outlet of the same module 1 1 (upstream of the storage tank 3) and to reinject it at its input; the milk circulates in a loop within its own heat exchanger module 1 1 (upstream of the storage tank 3).
- heat exchanger modules 11 are each associated with their own refrigerant circuit.
- the refrigerant circulating within the upstream heat exchanger module 1 1 has then a temperature greater than that of the refrigerant circulating within the heat exchanger module downstream 1 1 b .
- the water circulating within the upstream exchanger module 11a is cold (for example water supply network or a well), that is to say between 10 and 15 0 C; the water circulating in the downstream heat exchanger module 1 1 b is for its part frozen (from for example a refrigeration plant), with a temperature between 1 and 2 0 C.
- each heat exchanger module 11 is here equal to the volume of milk transferred during a cycle of the transfer pump 6. This structural feature allows a residence and a heat treatment of the milk, successively and for an identical time within of each of the two modules, before its transfer to the milk tank. The final temperature of the milk is then particularly close to that of the milk already stored in the tank (ie generally about 40).
- the refrigerant fluid at the level of the downstream exchanger module 11b can be used to supply an ice-water plant used for the refrigeration of the tank. milk and / or for the refrigerant supply of the same downstream module 1 1b.
- FIG. 5 represents, schematically, an alternative embodiment of the transfer installation described with reference to FIG. 4.
- This transfer installation is similar to that described above in that it comprises a heat exchanger 10 having two heat exchanger modules 1 1, connected in series.
- This heat exchanger 10 is distinguished only by the fact that the circulator 16 and the refrigerant circuit are common to the two heat exchanger modules 11a and 11b.
- the refrigerant enters the exchanger 10 at a channel 15a on the side of the downstream module 1 1b, flows to the upstream module 1 1 a via a central connecting channel 15d, to stand out at the level of the lane 15c on the side of said upstream module 11a.
- this circulator 16 will take the milk at the outlet of the downstream exchanger module January 1 (upstream of the storage tank 3) to transfer it to the input of the upstream exchanger module 11a.
- the loop circulation phenomenon thus generated is common to the two chiller modules and is carried out upstream of the storage tank 3.
- the heat exchanger 10 of the transfer systems shown in FIGS. 4 and 5 may consist of pairs of heat exchanger modules 11 which are connected in parallel, as described previously with reference to FIG.
- the structure of the heat exchanger (number of modules mounted in series and / or in parallel) has the advantage of being able to be easily adapted, in particular according to the general structure of the dairy plant, the flow rate of the pump of transfer, the volume of milk transferred by each cycle of the transfer pump and the desired final temperature for the milk.
- the overall section of the milk pipes 5b of the heat exchanger 10 is at least equal to the section of the discharge pipe of the transfer pump.
- This particular size allows the transfer pump 6 to operate optimally without applying excessive pressure on the transferred milk. This also makes it possible to limit the pressure losses and to keep the flow rate of the transfer pump during the washing phases of the installation.
- the tubes of the transfer system are advantageously oriented and arranged so that the liquids can flow naturally, by simple gravity phenomenon, at the end of the milk harvest but also during operations. of cleaning.
- the circulator (s) may each be associated with a thermal sensor (differential thermostat) of the bi-probe type: one at the level of the milk at the outlet of the heat exchanger (or module) and the other at the level of the refrigerant fluid. This type of sensor will allow a shutdown of the circulator and the coolant between two cycles of the transfer pump, when the temperature differential between the transferred milk and the coolant is zero or reaches a predefined value; it also allows their restarts after a pump cycle.
- peripheral tubes of the exchanger can be associated with a system of multiple input / output channels in refrigerant fluid, to create a circuit in the wrong direction specific to each peripheral tube or several separate circuits along the length of the same tube.
- the circuit of the cooling fluid in the heat exchanger is adapted to optimize the progressive cooling of the milk throughout its recycling.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Animal Husbandry (AREA)
- Environmental Sciences (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Dairy Products (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0706053A FR2920268B1 (en) | 2007-08-29 | 2007-08-29 | MILK TRANSFER FACILITY FROM A TRAINING MACHINE UNTIL A STORAGE TANK |
PCT/FR2008/051537 WO2009030860A2 (en) | 2007-08-29 | 2008-08-28 | Equipment for transferring milk from a milking machine to a storage tank |
Publications (1)
Publication Number | Publication Date |
---|---|
EP2194774A2 true EP2194774A2 (en) | 2010-06-16 |
Family
ID=39402634
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08829572A Withdrawn EP2194774A2 (en) | 2007-08-29 | 2008-08-28 | Equipment for transferring milk from a milking machine to a storage tank |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP2194774A2 (en) |
FR (1) | FR2920268B1 (en) |
WO (1) | WO2009030860A2 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2955851B1 (en) * | 2010-01-29 | 2012-03-23 | J & Y Charriau Ets | MILK TRANSFER FACILITY FROM A MILKING MACHINE UNTIL A STORAGE TANK EQUIPPED WITH AT LEAST ONE HEAT EXCHANGER |
GB2509515B (en) * | 2013-01-04 | 2018-10-17 | Drilling And Pumping Supplies Ltd | Milk cooling system |
FR3002828B1 (en) * | 2013-03-06 | 2015-03-13 | Ets J & Y Charriau | INSTALLATION FOR THE HARVEST OF MILK, EQUIPPED WITH AT LEAST ONE HEAT EXCHANGER |
EP3179847B1 (en) | 2014-08-11 | 2018-07-11 | DeLaval Holding AB | Cooling system for cooling a flow of milk, milk storage facility, milking system, and method for reconfiguring a cooling system |
FR3049161B1 (en) * | 2016-03-25 | 2018-03-16 | Ets J. & Y. Charriau | MILK TRANSFER FACILITY EQUIPPED WITH AT LEAST ONE THERMAL EXCHANGER FOR PARTIAL COOLING OF TRANSFERRED MILK |
FR3066358B1 (en) * | 2017-05-16 | 2019-07-05 | Ets J. & Y. Charriau | MILK TRANSFER FACILITY EQUIPPED WITH AT LEAST ONE THERMAL EXCHANGER FOR PARTIAL COOLING OF TRANSFERRED MILK |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IT1017099B (en) * | 1973-07-14 | 1977-07-20 | Alfa Laval Bergedorfer Eisen | PROCEDURE AND DEVICE FOR COOLING APPE NA MUNTO MILK |
DE29723985U1 (en) * | 1996-03-29 | 1999-07-08 | Maasland N.V., Maasland | Device for milking animals |
DE69908177T2 (en) * | 1998-12-16 | 2004-01-29 | Prolion Bv | DEVICE AND METHOD FOR MILKING ANIMALS |
SE9904647D0 (en) * | 1999-12-16 | 1999-12-16 | Alfa Laval Agri Ab | A method for cooling milk and a milking arrangement with cooling means |
-
2007
- 2007-08-29 FR FR0706053A patent/FR2920268B1/en not_active Expired - Fee Related
-
2008
- 2008-08-28 EP EP08829572A patent/EP2194774A2/en not_active Withdrawn
- 2008-08-28 WO PCT/FR2008/051537 patent/WO2009030860A2/en active Application Filing
Non-Patent Citations (1)
Title |
---|
See references of WO2009030860A3 * |
Also Published As
Publication number | Publication date |
---|---|
WO2009030860A3 (en) | 2009-04-30 |
WO2009030860A2 (en) | 2009-03-12 |
FR2920268B1 (en) | 2012-10-19 |
FR2920268A1 (en) | 2009-03-06 |
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