Classifications

• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
  • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
  • F04B43/00—Machines, pumps, or pumping installations having flexible working members
  • F04B43/0009—Special features
  • F04B43/0081—Special features systems, control, safety measures
  • F04B43/009—Special features systems, control, safety measures leakage control; pump systems with two flexible members; between the actuating element and the pumped fluid
• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
  • F04B—POSITIVE-DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS
  • F04B43/00—Machines, pumps, or pumping installations having flexible working members
  • F04B43/02—Machines, pumps, or pumping installations having flexible working members having plate-like flexible members, e.g. diaphragms
  • F04B43/06—Pumps having fluid drive
  • F04B43/067—Pumps having fluid drive the fluid being actuated directly by a piston

Definitions

• a MEMBRANE ARRANGEMENT A PISTON PUMP ARRANGEMENT HAVING SUCH A MEMBRANE ARRANGEMENT. AND A PROCESSING
• the invention relates to a membrane arrangement, a piston pump arrangement having such a membrane arrangement, and a processing line for hygienic processing applications.
• homogenizers within the food processing industry. For instance, within the dairy industry homogenizers are used for dividing fat globules into minor parts in order to obtain a stable fat emulsion against gravity separation. In other words, by homogenizing milk one can avoid that a cream layer is formed on top of the milk product. Other reasons for homogenizing food products are to achieve a more appetizing colour, reduced sensitivity of fat oxidation, more full bodied flavor, improved mouthfeel and better stability of cultured milk products.
• a homogenizer can be divided in two main parts, a high pressure pump forming a high pressure and a homogenizing device providing a gap through which the product is forced.
• the high pressure pump is a piston pump with three to five pistons.
• piston seals are used.
• a common approach is to have at least two piston seals placed apart from each other such that a barrier can be formed between the product, placed on a so-called hygienic side, and non-hygienic parts of the homogenizer, such as crankcase and crankshaft using hydraulic oil, placed on a so-called non- hygienic side.
• non-aseptic homogenizers i.e. homogenizers placed upstream a heat treatment station
• a common approach is to have double piston seals with water provided between the seals to lubricate the piston seals.
• aseptic homogenizers i.e. homogenizers placed downstream a heat treatment station
• a mixture of hot condensate and steam may be supplied between the seals in order to prevent re-infection.
• the technical solution should require a reasonable investment cost for the food producer and when running the technical solution the need for utilities should be kept at a low level, and providing service should be possible without increasing operational costs significantly.
• the life length of the piston seals would increase by using oil instead of water as a lubricant. To be able to use oil, however, a solution is required that will ensure that the oil is separated from the product in a secure manner.
• the present invention preferably seeks to mitigate, alleviate or eliminate one or more of the above-identified deficiencies in the art and disadvantages singly or in any combination and solves at least the above mentioned problems.
• a membrane arrangement comprising a first membrane, a second membrane, a membrane interior space formed between said first membrane and said second membrane, said membrane interior space housing a fluid, and a sensor configured to register at least one property of said fluid.
• the sensor is configured to measure a capacitance level of said fluid.
• the senor may comprise at least one electrode at least partly housed in a ceramic body and the fluid may be chosen from water or deionized water.
• the membrane arrangement may further comprise a membrane ring connecting said first membrane and said second membrane to each other such that said membrane interior space is formed, wherein said membrane interior space is configured to hold said fluid. Additionally, the membrane arrangement may further comprise a sampling opening in said membrane ring.
• the sensor may be placed in said membrane interior space, which is advantageous in that a sample of the fluid easily may be obtained.
• the second membrane may comprise a main body having a first side and a second side, wherein said main body is made of an elastic material, wherein said second side may be provided with a plastic coating.
• the elastic material may be ethylenepropylenedienemonomer (EPDM) or fluoropren rubber (XP41 ) and the plastic coating may be polytetrafluoroethylene (PTFE).
• a piston pump arrangement comprising a membrane arrangement according to the first aspect.
• The, membrane arrangement may be arranged to separate a hydraulic oil chamber and a product chamber.
• the piston pump arrangement may further comprise a pressure relief valve connected to a hydraulic oil chamber.
• a processing line comprising a piston pump arrangement according to the second aspect.
• the processing line may be a food processing line.
• Fig. 1 schematically illustrates a homogenizer.
• Fig. 2 schematically illustrates a so-called wet end of the homogenizer of Fig. 1 .
• Fig. 3 schematically illustrates a wet end in a membrane equipped homogenizer.
• Fig. 4 illustrates a number of different perspective views on a
• Fig. 5a and 5b illustrate a membrane in a first mode and a second mode.
• Fig. 6a, 6b and 6c illustrate a membrane module.
• Fig. 7a and 7b illustrate an example of a capacitance sensor.
• Fig. 8 schematically illustrates a sampling sensor system.
• Fig. 9a, 9b and 9c illustrates an example set up of a sampling sensor system.
• Fig. 10 schematically illustrates a food processing system with a membrane equipped homogenizer provided with a pressure relief valve.
• Fig 1 generally illustrates a homogenizer 100, more particularly a homogenizer sold under the name Tetra Pak ® Homogenizer by Tetra Pak.
• the homogenizer 100 comprises two main parts, a high pressure pump and a homgenising device.
• the high pressure pump forms a high pressure and the homogenising device provides one or several gaps through which the product is forced with the effect that smaller fat globules are formed. Further effects of homogenization is more appetizing colour, reduced sensitivity to fat oxidation, more full-bodied flavour and better stability of cultured milk products.
• the high pressure pump is a piston pump driven by a main drive motor 101 connected via a belt transmission 102 and a gearbox 103 to a crankshaft placed in a crankcase 104.
• a crankshaft placed in a crankcase 104.
• the crankshaft By using the crankshaft the rotary motion is converted to a reciprocating motion driving pump pistons 105 back and forth.
• the pump pistons 105 run in cavities formed in a pump block 106 made to withstand the high pressure created by the pump pistons.
• homogenizing device 108 As described above, by forcing the product through one or several gaps the properties of the product can be changed.
• Fig 2 illustrates a so-called wet end of the homogenizer in greater detail.
• the piston 105 is moving back and forth such that a high pressure is formed in a product chamber 200 in the pump block 106.
• One or several seals 202 are used for keeping a tight fitting between the piston 105 and a piston receiving element 204.
• the one or several seals 202 also keep the product in the product chamber 200 apart from the crankcase and other non-hygienic parts of the homogenizer. In order to further make sure that unwanted microorganisms do not end up in the product it is a common approach today to use steam barriers or the like in combination with the piston seals 202.
• a wet end 300 of a membrane equipped homogenizer is illustrated.
• the homogenizer illustrated in fig 1 and 2 the homogenizer is provided with a piston 302, or more correctly a number of pistons, although only one of them is illustrated in this cross sectional view. Further, the piston 302 is forming a high pressure in a pump block 304.
• the wet end 300 is provided with a first membrane 306 and a second membrane 308.
• the first membrane 306 can be arranged such that a hydraulic oil chamber 310 and a membrane interior space 312, that is, a space formed between the first membrane 306 and the second membrane 308, are kept apart.
• the second membrane 308 can be arranged such that the membrane interior space 312 and a product chamber 314 are kept apart.
• a high pressure relief valve 31 6 can be connected to the hydraulic oil chamber 310 such that a pressure in the hydraulic oil chamber can be lowered by opening this valve.
• hydraulic oil may be fed into a tank.
• This tank may also be connected to an inlet in the hydraulic oil chamber via an inlet valve such that hydraulic oil can be fed into the hydraulic oil chamber at a later stage.
• a positive effect of this set up is that the hydraulic oil released via the high pressure relief valve 31 6 can be re-used.
• An example set up is illustrated in fig 3.
• the reason for having hydraulic oil is that this is used for forwarding the pressure formed by the piston 302 via the first membrane 306 and the second membrane 308 to the product chamber 314, but also for lubricating the seals and in that way extend the life time of the seals.
• the piston is indirectly forming a pressure in the product chamber 314.
• a risk with membrane equipped homogenizers is that the membranes break and that hydraulic oil enters the product chamber. This may be a food safety hazard depending on the hydraulic oil being used, but it will with a high likelihood result in product losses.
• a fluid may be present in the membrane interior space 312, that is, the space formed between the first membrane 306 and the second membrane 308, .
• the aim of the fluid is to make it possible to detect a membrane rupture in a reliable, fast and cost efficient way.
• a further aim of the fluid is to provide a pressure between the membranes without establishing any friction between the same.
• the fluid can be a gel, but it can also be a water solution or any other material capable of forwarding a pressure and changing properties, such as capacitance, when mixed with a hydraulic oil or a product.
• One way of detecting a membrane rupture is to have a capactive solution, as fluid and to have a capacitance sensor continuously measuring capacitance of the fluid. If the first membrane 306 breaks, hydraulic oil will enter the membrane interior space 312 and mix with the fluid with the result that the capacitance is changed, provided of course that a hydraulic oil with different capacitance than the capacitance of the fluid has been chosen. On the other hand, if the second membrane 308 breaks product will enter the membrane interior space 312 and mix with the fluid. Provided that the product has a different capacitance than the fluid the capacitance will be altered. Hence, by having a fluid with a capacitance in the membrane interior space 312 it can be detected if any of the two membranes 306, 308 should break.
• a solution not having a capacitance can be used, or a solution with low capacitance. If having the solution without capacitance, such as deionized water, the capacitance will increase if the first membrane 306 or the second membrane 308 break, provided of course that the product and the hydraulic oil both have a higher capacitance than the solution without capacitance.
• a sample channel 318 By having the sample channel 318 a sample from the membrane interior space 312 may be taken and analyzed by a capacitance sensor placed outside the membrane interior space 312.
• a capacitance sensor placed outside the membrane interior space 312.
• One reason for not placing a capacitance sensor in the membrane interior space 312 is the high pressure. However, if having a capacitance sensor withstanding the high pressure the capacitance sensor may be placed in the membrane interior space.
• turbidity instead of measuring capacitance, or as a complement thereto, other parameters may be used, for instance turbidity.
• turbidity By having for instance a fluid with a turbidity different from a turbidity of the hydraulic oil and the product, turbidity will change in case of leakage due to membrane rupture. This turbidity change can be detected by a turbidity sensor.
• Yet another example is to have a fluid with light transmitting properties different from both the hydraulic oil and the product.
• a light registering sensor possibly combined with a light emitting device, such that absorbed light or reflected light can be measured, it can be detected whether any of the membranes has broken and hydraulic oil or product have entered the membrane interior space.
• Fig 4 illustrates a number of different perspective views of a membrane 400 that can be used as the first membrane 306 or the second membrane 308 in the wet end illustrated in fig 3.
• the membrane 400 may be provided with a raised section 402 placed between a periphery 404 of the membrane and a mid section 406 making sure that the membrane can flex between a first mode, illustrated in fig 5a, and a second mode, illustrated in fig 5b, without wearing out the material of the membrane. Further, an advantage of having the raised section may also be greater volume difference between the first mode and the second mode.
• the mid section 406 may be strengthened by a strengthening portion 408, e.g. a metal portion incorporated in the membrane, in order to avoid so- called “coining", i.e. the membrane breaks such that a small portion of the mid section in the shape of a coin is torn from the membrane.
• a strengthening portion 408 e.g. a metal portion incorporated in the membrane, in order to avoid so- called “coining", i.e. the membrane breaks such that a small portion of the mid section in the shape of a coin is torn from the membrane.
• fig 5a the membrane is in the first mode in which no force is exerted on the membrane, neither on a product chamber side (left side in fig 5a and 5b), nor on a hydraulic oil chamber side (right side in fig 5a and 5b).
• the membrane In fig 5b the membrane is in the second mode in which a force is exerted on the hydraulic oil chamber side such that the mid section of the membrane is pushed towards the product chamber side.
• the product chamber side of the membrane is preferably provided with properties such that food residues can be easily removed. Further, the product chamber side should also be able to withstand chemicals used when cleaning, e.g. lye and acid.
• the hydraulic oil chamber side should on the other hand preferably have properties suited to work well with the hydraulic oil.
• the membrane as a whole should be elastic such that the pressure formed by the piston can be forwarded to the product chamber without wearing out the membrane. Further, the membrane should also be elastic such that the membrane can be small, e.g. a diameter of 10-30 cm. A small membrane namely has the effect that the pump block can be made small, in turn implying that less material, e.g. stainless steel, is needed, which directly affect the investment cost for the food producer.
• a membrane 500 comprising a main body 502 made of a rubber material.
• a rubber material In one particular example fluoropren rubber (XP41 ) has been chosen, but since the choice of material depends on the hydraulic oil used other material can be chosen as well.
• a rubber material such as an elastomer, for the main body, makes it possible to reduce the size of the membrane to about 10-30 cm or lower while still being able to forward the pressure from the piston satisfactorily.
• a coating 504 may be provided on this side.
• the coating 504 may be made of polytetrafluoroethylene (PTFE), but other material suitable for food processing can be used as well. Further, the coating can also protect the elastic material against the cleaning agents used during cleaning and also against abrasive products.
• PTFE polytetrafluoroethylene
• the coating 504 is preferably made thin, e.g. 0,5 mm. However, since different material have different properties the thickness of the coating may differ for different material.
• fig 5a and 5b are mainly for illustrative purposes. In real applications, a difference between the first mode and the second mode may be less or more significant.
• Fig 6a, 6b illustrate a membrane module 600 comprising a first membrane 602, a second membrane 604, a membrane ring 606 and a sensor 608 in an exploded view from two different perspectives.
• Fig 6c illustrates the membrane module when the first and second membrane are attached to the membrane ring 606. As illustrated, both membranes may be of the kind illustrated in fig 4, 5a and 5b.
• a closed space is formed, herein referred to as the membrane interior space.
• the fluid can be held, thereby making it possible to easily replace one membrane module by another.
• the sensor 608, that may be a capacitance sensor as explained above, can be placed in the membrane interior space.
• sensor connection elements may be provided on an outer side of the membrane ring such that data collected by the sensor 608 can be captured and transmitted to a control device or the like configured for analyzing data in order to detect if one or more properties of the fluid has been changed, e.g. due to that the first membrane has ruptured and that hydraulic oil has entered the membrane interior space.
• Fig 7a illustrates an example of a capacitance sensor withstanding a high pressure such that it can be placed in the membrane interior space.
• the capacitance sensor 700 is further illustrated in fig 7b.
• a body 702 can be arranged for holding an electrode 704.
• the fluid can be placed such that a capacitance can be measured by using the electrode 704.
• the body 702 is preferably made of a ceramic material to withstand the harsh environment in the membrane interior space.
• a challenge with having the sensor placed in the membrane interior space is the high pressure.
• a homogenizer of today it is common to increase the pressure from 300 kPa (3 bar) to 10-25 MPa (100-250 bar).
• Fig 8 illustrates a so-called sampling sensor system 900 that can be used as an alternative to an in-line sensor illustrated in fig 7a and 7b. Further, if measuring more than one property of the fluid, it is possible to detect one of the measure by using an in-line sensor and another measure by the sampling sensor system. Still an option is to use the sensor in the membrane interior space as the first sensor registering data continuously and to use the sampling sensor system as a back-up sensor system or for making additional measurements.
• the sampling sensor system 900 can comprise a membrane module 902 provided with a channel leading to a low pressure sampling chamber 904. In order to make sure that the high pressure in the membrane module 902 can be kept a valve 906 may be provided on the channel.
• a sensor 908 can be arranged for registering one or more properties of the fluid fed from the membrane module 902 via the channel.
• the sensor 908 may be connected to a control device 910, such as a computer, for analyzing the sensor output.
• Fig 9a, 9b and 9c illustrate different perspective views of an example set up of a sampling sensor system 1000.
• a valve 1004 and a conduit 1006 a low pressure sampling chamber 1008 is provided.
• an accumulator 1010 can be used for soaking up part of the fluid, which in this particular example has been chosen to be a gel. After having made a measurement the fluid can be pushed down into the membrane interior space again.
• Fig 10 illustrates a schematic view of an example set up of a part of a food processing system 1 100.
• a separator 1 102 is placed upstream a piston pump arrangement 1 104 and a spray dryer 1 106 is placed downstream said piston pump arrangement 1 104.
• a heat treatment station 1 108, a dearator 1 1 10 or other pieces of equipment may be part of the system as well.
• the piston pump arrangement 1 104 can be provided with a membrane 1 1 12 providing for that product is kept separated from hydraulic oil placed in a hydraulic oil chamber 1 1 14. By having the hydraulic oil the pressure formed by a piston 1 1 1 6, or several pistons, can be forwarded to the membrane 1 1 12 as described above.
• a sudden pressure increase enter the product chamber of the piston pump arrangement 1 104 e.g. when the separator 1 102 discharges or when a blockage occur in the spray dryer 1 106, this pressure increase will be spread to the hydraulic oil chamber 1 1 14 via the membrane 1 1 12.
• a pressure relief valve 1 1 18 By opening a pressure relief valve 1 1 18 the pressure increase may be reduced by releasing hydraulic oil from the hydraulic oil chamber 1 1 14 to a container 1 120. In this way the pressure increase, or pressure peak, may be eliminated without product losses, which would be the case if a line pressure relief valve was used, i.e. a pressure relief valve placed, for instance, on a pipe between the piston pump arrangement 1 104 and the spray dryer 1 106.
• pressure relief valve 1 1 18 as described will also improve safety in food processing plants. As soon as the pressure in the hydraulic chamber is above a set threshold, e.g. due to a blocked nozzle in the spray dryer, the pressure in the hydraulic oil chamber is reduced and the pistons will thereby not increase the pressure additionally.

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• Engineering & Computer Science (AREA)
• Mechanical Engineering (AREA)
• General Engineering & Computer Science (AREA)
• Reciprocating Pumps (AREA)

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• 2016
  • 2016-06-03 EP EP16728279.7A patent/EP3303841A1/en not_active Withdrawn
  • 2016-06-03 AR ARP160101667A patent/AR104910A1/es unknown
  • 2016-06-03 CN CN201680031795.XA patent/CN107709777A/zh active Pending
  • 2016-06-03 WO PCT/EP2016/062608 patent/WO2016193410A1/en active Application Filing

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