METHOD AND ARRANGEMENT FOR MEMBRANE FILTRATION OF MILK IN CONNECTION WITH MILKING

Abstract: When membrane filtrating milk in connection with the milking the milk after the milking is transported to a container, a so-called end unit (1). From this the milk is led by way of a balance tank (6) to a circulation path, in which the membrane filter (10) is a part. After the milking permeate obtained during the membrane filtration is returned to the end unit (1) and is used to press milk from the same and from equipment between this container (1) and the circulation path.

Description: METHOD AND ARRANGEMENT FOR MEMBRANE FILTRATION OF MILK IN CONNECTION WITH MILKING The present invention relates to a method and an arrangement for membrane filtration of milk in connection with milking. When cows are milked by means of milking machines the flow varies very strongly. The variation is caused parcly by the construction of the milking plant and partly by the physiological properties of the cows. Milking plants work with vacuum and the milk is transported through a pipe line system, which has a vacuum which is fairly equal y to a container usually called an end unit. From this container the milk is pumped, under atmospheric pressure, through a pipe line to a cooling tank or some other storage vessel. When milk is membrane filtrated in connection to the milking, a membrane filter is connected to the milking plant by way of a balance tank. From this the milk is pumped to a circu¬ lation path comprising the membrane filter, in which the milk is divided into two fractions, a concentrate and a permeate. Depending on the choice of filter media these fractions have a different composition. If the milk is to be concentrated by way of ultrafiltration, the permeate consists of water, milk sugar and low molecular salts. If the concentration takes place by way of reverse osmosis the permeate consists of water obtained from the milk. The membrane filtration usually takes place in direct connection to the milking. After the milking the milk has a temperature of about 35°C and considering the shelf life it is important that the time the milk is kept at this temperature is kept as short as possible. The milk is transported from the end unit by way of a milk filter, in which coarser contaminations are separated off, to the balance tank and is from there pumped to the circulation path of.the membrane filter. When the level in the balance tank has fallen to a certain pre- determined value, the pump which transports the milk to the cir¬ culation path stops. At this time there are consequently rests of milk in the end unit, in the pipe lines between this unit and the balance tank and in this tank. The milking plant as well as the components which are included in the membrane filtration equipment must be cleaned after each milking. The milk which is left in the plant will if no measures are taken be lost during the washing and consequently represents a loss to the milk producer. According to the invention it is therefore proposed that permeate obtained during the membrane filtration is used to press forward milk from the end unit in the milking plant and from the pipe lines between the same and the membrane filter, when the milking is ended. An arrangement for membrane filtration of milk in connection with milking comprises a so called end unit, a balance tank and pumps to transport the milk from these units and a circulation path comprising a circulation pump and a membrane filter and pipes for transport of concentrate and permeate. The arrangement according to the invention also comprises a pipe line to return permeate to the end unit. According to the invention there is obtained an increased yield of milk concentrate. By pressing forward the milk by means of permeate, that is a product which has been obtained from the milk, no oppositions could be made from a food technical point of view, the more since the permeate (used for pressing forward the milk) according to the invention is produced in direct connection with the pressing forward of the milk and is not stored during the production phase. If ordinary tap water is used there is always a risk for contamination, especially in such an exposed environment as a stall. The method and the arrangement according to the invention are described further with reference to the attached drawing which shows an example of how a membrane filtration equipment is connected to the end unit in a milking plant. In the drawing there is shown an end unit 1 to which milk is transported under vacuum by way of a pipe line 2. From the end unit 1 the milk is transported by a pump 3 through a milk filter 4 in a pipe line 5 to a balance tank 6 provided with a level guard. From the balance tank 6 the milk is transported by a pump to a circulation path comprising a pump 9 and an ultra filter 10. From the circulation path there is removed a concentrate flow by way of a pipe 11 which flow is heat treated in a heat exchanger 12 and from this is transported to a cooling tank not shown in the drawing. The permeate is obtained from the ultra filter by way of a pipe line 13, which during the time the mil¬ king takes place, is connected to a pipe line 14 for transport of permeate. The pipe line 14, which e.g. may be connected to a system for distribution of liquid to the cows and at that may be used as a liquid for these, is with advantage provided with a transparent section 15 arranged within sight of the person who milks the cows. With such an arrangement this person may easily see that the filter works in a correct way. If a leakage should occur the permeate will no longer be clear but become muddy with milk fat and proteins. Between the pipe line 13 and the balance tank 1 there is a pipe line 16, through which permeate may be returned to the balance tank 1. This transparent section may of course be located at some other place in the permeate pipe line. In the pipe line 16 there is a valve 17 and in the pipe line 14 a valve 18. The method according to the invention is with advantage carried through in the following way. When the last group of cows is milked the milker activates the programme for emptying the milk from the milking- and membrane filtration equipment. The milk which is obtained from the balance tank 6 is treated in the ultra filter until the level in the balance tank falls under a certain position. This means that the programme for emptying starts. The first step in this programme is that the end unit 1 is emptied of milk, by keeping the pump 3 in operation for about 15 seconds. The second step is that the milk is ultrafiltrated as earlier and the concentrate is heat treated while on the other hand permeate is returned to the end unit 1 by way of the pipe line 16. When permeate has been transported to the end unit for 1-2 minutes, the pump 3 starts and during 10-15 seconds the rest of the milk left in the milk filter 4 and the pipe line 5 is pressed forward by permeate. In the meantime the ultra filter works with the milk transported to the same. When the balance tank 6 has been emptied of milk there is about 20 liters permeate in the end unit 1 and about 10 liters milk concentrate in the ultra filter 10 and its circulation path. The circulation pump is then stopped and the pump 3 of the end unit transports permeate to the balance tank 6. The pump 7 which is arranged after the balance tank 6 now transports permeate further to the ultrafilter and its circulation path in such a way that the milk concentrate is pressed out through the heat exchanger 12 to the cooling tank. When the pump 7 has transported about 10 liters permeate it stops and the circulation pump 9 starts. This works during about 2 minutes and rinses the filter surfaces with permeate. After this time period the circulation pump 9 stops and the pump 7 starts and presses forward the diluted milk now present in the ultra filter by means of the permeate volume which is left in the balance tank. The emptying method described above concerns an ultrafiltration equipment where the milk concentrate is heat treated. The method will anyhow be the same, although the times and volumes are different, if the heat treatment unit 12 is dismissed or is located prior to the filter immediately after the pump 7. The same is thecase if the membrane filter consists of a membrane module for reversed osmosis. During some parts of the emptying phase the normal control of the level in the balance tank 6 carried through by the pump 7 is out of function. The pump 7 is then controlled by the control equipment of the ultra filter.

Claims: Claims 1. Metnod for membrane filtration of milk in connection with milking, at which the milk after the milking is transported to a container, a so called end unit and from this by way of a balance tank to a circulation path in which the membrane filter is a part, c h a r a c t e r i z e d i n that permeate obtained during the membrane filtration is returned to the end unit and is used for pressing forward milk from the same and from equipment arranged between this container and the circulation path when the milking is ended. 2. Arrangement for membrane filtration of milk in connection with milking, which comprises a so called end unit (1), a balance tank (6) and pumps (3, 7) to transport the milk from these units (1, 6) and a circulation path comprising a circulation pump (9) and a membrane filter (10) and pipe lines (11, 14) for transport of concentrate and permeate, c h a r a c t e r i z e d b y a pipe line (16) for returning permeate to the end unit (1) and means for controlling the pumps (3, 7, 9).

Inventors: LIDMAN MAGNUS, LIDMAN, MAGNUS
Applicants: ALFA LAVAL AGRI INT, ALFA-LAVAL AGRICULTURE INTERNATIONAL AB
Application year: 1988
Main classification: A01J7
IPC codes: A23C9