奥地利专利AT512536A4 mixing device

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专利摘要:
Mixing device for mixing at least two liquids, comprising at least two containers, in each of which a liquid is located, and at least two pumps for conveying the liquids, which pumps are each arranged on a container, wherein the pumps (4) are screw pumps, the pumps (4) are connected to a follower plate (6) and the follower plate (6) is adjustable in height, wherein the follower plate (6) rests on the liquid surface and seals with the container.
公开号:AT512536A4
申请号:T1097/2012
申请日:2012-10-10
公开日:2013-09-15
发明作者:
申请人:Waizenauer；
IPC主号:

专利说明:

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The invention relates to a mixing device for mixing at least two liquids and to a method for mixing at least two liquids.
State of the art
The emptying of containers containing a liquid is a routine process in the industry. Many chemicals and other raw materials, e.g. Oils, sealants, adhesives, are supplied as liquids to the processing industry. In order to be used in the production process, the liquids must be taken from the containers and fed into the production process.
The systems on the market are working together
Schopfkolbenpumpen as a conveyor unit. These are driven pneumatically, hydraulically or electrically depending on the manufacturer. Piston pumps need to be driven linearly and promote a pulsating flow of material as they have a dead center and the change in direction of movement can not be accomplished infinitely fast.
Ladle pumps pump the material only partially volumetrically, i. it can not be precisely defined, which flow rate is promoted in a particular way, as these pumps promote Undefined material when switching the direction of movement. The built-in check valves open and close differently depending on the viscosity. A scoop pump therefore brings systemic disadvantages, which must be avoided during daily work. Since the piston pump pump systematically under the follower plate or pump housing 1 ··· «•« ♦ »· ··· • ♦ • ·· # ·" scoop " a large amount of residue remains in the barrel or in the inlet funnel of the follower plate,
Furthermore, a device for emptying containers can also be used for mixing liquids from two different containers. Basically, there are conveyor systems with a fixed mixing ratio and with a variable mixing ratio.
Constant mixing ratio 1: 1
The scoop pumps are mechanically / hydraulically or electrically coupled so that they have the same position and therefore the same switchover time at all times.
Since the viscosity of component A and component B can differ greatly depending on the manufacturer, there is the possibility that the volumetric mixing ratio deviates. In addition, unequal filled packages of material can be left unaffected and large amounts of material left over from one component.
Variable mixing ratio
The mixing ratio can be freely adjusted. The feed pumps operate independently of each other and mix the media in the set mixing ratio and a specified tolerance. With variable mixing ratios, it is also possible that the level of the barrels affects the flow rate per component, so that the containers are emptied evenly. To set a variable mixing ratio, the feed units of component A and component B are not 2 99 99 • t · t · 9 · 9 9 · 9 · 9 · 999 · § · · · · · ··· * 9 • 9 · • 99 • 99 9 coupled together. Depending on the manufacturer, volumetric measuring devices are installed in the hose lines for control purposes. The delivery pressure in current systems is about 150-200 bar depending on the viscosity and hose length. For a constant discharge pressure, a pressure reducing valve is installed at the end of the hose line, which reduces the system pressure to a constantly set pressure to compensate for fluctuations in the feed pumps. EP 1 331 072 B1 describes a method for the control of a device for the removal of liquid materials by means of a piston pump. The scoop pumps are controlled with different pulse frequencies. DE 20 2011 108 222 LJl describes a device for dispensing liquid components of a
A multi-component formulation comprising conveyors comprising a pump operated by an electric drive, wherein sensors indicate the fill level and are connected to a controller controlling the application of the components. As an example of a pump, a scoop pump is mentioned, which is arranged on a follower plate.
The aim of the invention is therefore to provide a device for mixing at least two liquids, which allows a complete emptying and delivers a pulsation-free material flow and promotes volumetrically.
According to the invention this is achieved by providing a mixing device, wherein the pumps are screw pumps, the pumps are connected to a follower plate 3 and the follower plate is adjustable in height, wherein the follower plate rests on the liquid surface and sealingly seals with the container.
Such a mixing device ensures a pulsation-free and volumetric delivery rate. The mixing ratio, if at least two containers are provided, is freely selectable. Volumetric measuring devices are not required due to volumetric conveyors. Furthermore, this mixing device is energy efficient, since volumetric measuring devices, which cause a very high pressure drop, omitted. For very small dosing volumes volumetric measuring devices can not capture the quantity or require a minimum flow rate. This can lead to incorrect mixing ratios. Optionally volumetric measuring devices can additionally be used to carry out a parallel measurement, so that a higher measuring reliability can be achieved or additionally verified.
The energy saving is achieved by measuring the system pressure of each component at the hose ends immediately before the processing unit and speed controlling the associated conveyor. The feed pumps only have to generate the necessary pressure, which arises due to the pressure drop in the hose line. It eliminates the pressure reducing valve, which reduces the system pressure at the processing unit. It is believed that when two materials are mixed at a constant pressure and the feed volume of the feed pumps is adjusted, a very accurate mixing ratio is achieved regardless of the different viscosity of the materials.
Advantages of the screw spindle purape:
An essential advantage of the screw pump is that it has a constant delivery pressure or a constant delivery volume. The exact mixing ratio is ensured at all times. Previously used scoop pumps promote a non-constant flow, so it comes in the switching of the direction of movement to a brief change in the mixing ratio.
Another advantage of the screw pump is the monitoring of the volume flow. With the aid of a pressure sensor and the speed of the pump, characteristics of the medium to be pumped are determined. If these values deviate from those determined during production, an alarm can be output or the system can react accordingly to the change. For example, a container can be completely emptied, since, when completely emptied, the negative pressure on the suction side becomes too large and the delivery pressure deviates from the rotational speed.
Basically, the delivery is done volumetrisch with a screw pump. However, with very high viscosity fluids, it is possible that one revolution of the screw pump will not deliver the same volume as a low viscosity fluid. However, such a deviation, which is only slight, can easily be determined by calibration curves, which can sometimes also be created by oneself.
The screw pump requires a very small inlet funnel on the follower plate and sits directly on the lower edge of the follower plate. This state has this advantage that the containers can be almost completely emptied and that in a drum change, the amount of mixed with air material is much lower than with a previously used pump piston pump. There is less material to be rinsed. One has a material and time saving. It must be disposed of less rinsed material.
Another advantage of the screw pump is the large viscosity range in which the pump can be operated. This can promote from water (viscosity 1 mPa.s) to highly viscous media (3,000,000 mPa.s). Previously used scoop pumps have a limited delivery range usually up to 1,500,000 mPa.s.
In one embodiment of the present invention may be provided after the pump - in the conveying direction - a hose having a valve for the addition of additives. The addition of an additive to the pumped liquid is often a requirement in the production process. For example, color, a reaction accelerator, a diluent, a dye or the like may be added. The admixture can be done for example by means of additive valves, wherein a certain amount of additive is added to the volume flow in intervals. The volume, which is added in time, depends on the respective metering and the Dosierkolbendurchmesser. The mixing can be discontinuous or continuous.
In another embodiment of the invention, the liquid may have a viscosity in the range from 1 mPa.s to 3,000. 000 mPa.s have. That the device is for a liquid having a viscosity in the range of 1 mPa.s to 3,000. 000 mPa.s suitable. Both low-viscosity and high-viscosity liquids can be mixed with this mixing device. The liquids to be mixed may have the same viscosity or may have different viscosities.
In yet another embodiment of the invention, the liquid may have a viscosity in the range of 100,000 mPa.s to 3,000,000 mPa.s. That the device is suitable for a liquid having a viscosity in the range from 100,000 mPa.s to 3,000,000 mPa.s. Such liquids are particularly preferred for industrial applications.
In an embodiment of the invention, the mixing device may comprise a curling device for easy transport of the container to the point of emptying. Such a curling device is for example a plate on which the container can be placed and which can be moved to the desired location in the device. This eliminates a tedious maneuvering the container to the right place.
In another embodiment of the present invention, the mixing device may comprise transport rollers. If the device is to be moved, it can be moved on the transport rollers. The transport rollers can be fixable and / or foldable. If the mixing device at the desired place, the transport rollers can be fixed and / or folded. Thus, the mixing device can no longer slip.
In one embodiment of the invention, the follower plate may include an automated vent valve. About the vent valve, the container can be vented. Inevitably, the container contains after placing the follower plate air, which must be removed before the beginning of material removal, since the trapped air may not be supplied to the production process and subsequently falsifies the measurements. The removal of air is ideally done via a vent valve.
In another embodiment of the invention, a pressure transducer may be provided at the pump outlet. With this pressure transducer, the measurement of the pressure after the pump is possible, which allows conclusions about the possibly still contained amount of air and / or on the conveyed amount of liquid. A pressure transducer may be, for example, a pressure gauge.
In another embodiment, a control unit may be provided which controls the automated vent valve by measuring the delivery pressure at the pressure transducer, wherein the discharge pressure is compared with the target value of an air-free liquid with the vent valve closed and the vent valve is opened as often and until the delivery pressure with the vent valve closed is the same as the target value, whereupon the vent valve remains closed. This control unit provides the ► »* ·· ···· ··«. It is possible to vent the container automatically. An air-free liquid has a specific delivery pressure that changes when air is trapped. The pressure transducer measures the delivery pressure and the control unit compares this control pressure with the target value of the air-free fluid. If the values do not match, the control unit opens the vent valve. Before the next comparison, the vent valve is closed again and the values are compared again. If the measured value and the target value agree, the bleeding valve remains closed and the mixing operation can be performed.
In another embodiment of the invention, the control unit can evaluate the revolutions or rotational angle position of the pump shaft or of the pump drive. In this way, an efficient check of the air content in the liquid takes place.
In yet another embodiment, sensors may be arranged on the lifting cylinder, which measure the filling level of the container and are connected to a control unit, which in turn is connected to the pump and via which control unit the pumps for uniform emptying of at least two containers are controllable. The even emptying of e.g. Two containers are of exceptional importance in batch mode, as each container has its own lot number and there may be little difference between batches. For this reason, a container that has not been completely emptied can not be used for mixing with another new container; the remaining content must be disposed of for a fee. By this arrangement with a sensor which measures the filling level of the container and has a length of 9 ·······················································. * * * * * * * «*« «* Ftft • • • ft • * * * * * ft * * * *« * *
Control unit regulates the emptying, the remaining of residual liquid is avoided in a container; both containers are completely emptied. It may also be that, in terms of production technology, the two containers used are not filled to the same level (this can also be caused, among other things, by different viscosities of the liquids in the containers); In this case, a compensation of the filling heights is also necessary.
In another aspect, the invention relates to a method for mixing at least two liquids, wherein in a mixing device as described above, at least two containers are arranged, a follower plate which seals with the container is placed on the liquid surface, the air between the liquid surface and Follower plate is removed and the liquids are conveyed out of the at least two containers by a respective screw pump and the material flows are subsequently combined, whereby the mixing takes place. This method has the advantage of pulsation-free promotion and subsequently mixture of at least two liquids.
In one embodiment of the invention, the air between the liquid surface and follower plate can be removed by a control unit by measuring the delivery pressure on the pressure transducer controls an automated vent valve, the discharge pressure is compared with the vent valve closed with the target value of an air-free liquid and the vent valve so often and is opened until the delivery pressure with the vent valve is closed coincides with the desired value, whereupon the vent valve remains closed. By this control unit is the 10 * ··· φφ φφφφ φφφφ φ · φ φ φ φ φ φ φ · · · φ φ φ φ φ φ φ φ φ φ φ φφφφφφφ φ φ φ φφφ φ φ φφφφ automated venting of the container possible. An air-free liquid has a specific delivery pressure that changes when air is trapped. The pressure transducer measures the delivery pressure and the control unit compares this control pressure with the target value of the air-free fluid. If the values do not match, the control unit opens the vent valve. Before the next comparison, the vent valve is closed again and the values are compared again. If the measured value and the setpoint value agree, the venting valve remains closed.
In another embodiment of the invention, the control unit can evaluate the revolutions or rotational angle position of the pump shaft or of the pump drive. In this way, an efficient check of the air content in the liquid takes place. ,
In one embodiment of the invention, sensors disposed on the lift cylinder may measure the level of the container, the sensors being connected to a control unit, which in turn is connected to the pump, the control unit controlling the pumps for uniform discharge of at least two containers , The even emptying of e.g. Two containers are of exceptional importance in batch mode, as each container has its own lot number and there may be little difference between batches. For this reason, a container that has not been completely emptied can not be used for mixing with another new container; the remaining content must be disposed of for a fee. By this arrangement with sensor which measures the filling height of the container, and »♦ * · · · ····························································································································································································· both containers are completely emptied. It may also be that, in terms of production technology, the two containers used are not filled to the same level (this can also be caused, among other things, by different viscosities of the liquids in the containers); In this case, a compensation of the filling heights is also necessary.
In another aspect, the invention relates to the use of a mixing device as described above for mixing at least two liquids. By this use, at least two liquids can be mixed without pulsation.
In yet another aspect, the invention relates to the use of a mixing device as described above in a method as described above. Through this use in such a process, at least two liquids can be mixed pulsation-free.
Brief description of the drawings
The following reference numerals are used in the figures: 1 lifting cylinder for follower plate 2 servo drive unit with gearbox 3 connecting flange drive - pump body 4 pump body 5 follower plate breather 6 follower plate 7 curl device for moving the containers 8 panel operating unit 12 • * ft ········· Μ · · ft ft ft 9 9 9 9 9 9 9 9 · · · · · · · · · 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 9 Coding of follower plate size 12 Transport rollers fixable 13 Drawbar 14 Follower plate seal 15 Containers
Fig. 1. shows a schematic representation of a device according to the invention.
Fig. 2 shows a detail of a device according to the invention.
Fig. 3 shows a schematic representation of a device according to the invention, in which a container is arranged.
EXAMPLES
example 1
An example of a device according to the invention is constructed as follows.
A lifting cylinder 1 for the follower plate 6 can move the follower plate 6 up and down. The follower plate 6 may have different diameters and is adapted to the container 15 to be emptied. The follower plate 6 has a.
Follower plate breather 5. When placing the follower plate 6 on the container 15 air must be able to escape; this is done via the follower plate breather 5. A servo. 13 ··· ** · «* · ♦ • ·« «· · · · · · · · ·« ··································································· Drive unit 2 with a transmission is connected via a connecting flange 3 with the pump body 4. The drive movement is rotational. The pump body 4 is a screw pump. This screw pump or screw pump is a constant current pump. A curling device 7 for moving the container may be provided. With this curling device 7, the container 15 can be moved without great effort to the right place under the pump 4. The device may be clad with a panel 8 to hide sharp edges and increase the reliability. A slide 9 may be provided to switch between the venting position and operating position. A pressure sensor 10 at the pump outlet serves for pressure regulation or overpressure protection on the pump. A pressure sensor in the area of the processing unit is used to control the system pressure. The follower plate 6 is connectable with a connector 11 for encoding the follower plate size with the conveyor system. Transport rollers 12 which are fixable and / or foldable are also provided. A pull rod 13 serves to attach the various parts. Exemptions in the base plate serve as a means of transporting the dosing system by means of a lift truck or forklift truck.
The container 15 is usually a keg. The seal is a static seal. An inflatable seal can be used for 20-1 and 200-1 drums. This makes it possible to process slightly damaged barrels. As advantages, the variable sealing adjustable for the viscosity of the material to be conveyed, a lighter change of the container 15, since the seal in the extension of the 14 "······························································" ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦ ♦
Follower plates is not present and the container 15 does not need to be lifted, are listed. The follower plates 6 can be lightweight (weight less than 15 kg, change for operators lt. Occupational safety possible).
The device may be embodied on rollers 12, wherein a detent may be integrated in the rollers 12. This prevents rolling during operation.
The hose guide can be made with swivel joints, which allows a very short hose length in the area of the movable plates. This results in a lower pressure drop, which reduces energy consumption.
Screw pumps generate a constant volume flow. The pressure in front of the processing unit is precisely controlled. This can be recalculated to the flow rate. Since the material in the fluid hoses is highly compressible and the hoses expand and act as a reservoir, the control loop must include all confounding factors.
The liquid in the container is, for example, liquid silicone rubber (LSR), adhesives, resins, food, etc.
At least two of these devices are coupled together to form a mixing device according to the invention. These at least two devices or removal devices can be combined with one another, so that the at least two liquids are removed in the desired mixing ratio and present in the correct mixing ratio in the discharging tube. That the tubing from each device is combined to form a tube, which is then connected to the tube. The tubing is then filled * * · * · ♦ ♦ »·············································································································································································································· It can also be provided more than two devices or removal devices, as desired, the desired, to be mixed liquids.
Example 2: Injection molding
The most common form of LSR processing (LSR stands for "liquid silicone rubber", ie liquid silicone rubber) is the application in the conventional injection molding in conjunction with an injection molding machine. Here, the material is dosed in the mixing ratio 1: 1 in the screw conveyor of the injection molding machine. This injects the material into the hot mold.
Example 3: Direct encapsulation
Further fields of application of these conveying and mixing systems can be found in the direct casting in which the material is conveyed directly into a tool without the aid of an injection molding machine. Of course, other materials can also be promoted, such as Resins and adhesives.
Example 4
In a device as set forth in Example 2, the mixing block may be equipped with one check valve each to prevent the backflow of one component into the supply of the other component. It may be necessary to measure the material pressure of the already mixed material after the shut-off unit to make the regulator more stable. 16
Optionally, the volumetric flow can be measured, since the exact current volume flow must be known for the exact additive admixture.
Example 5
When adding an additive, e.g. of a color, the volumetric flow can be calculated from the current speed and pressure. The injection unit of additive addition injects the additive in proportion to the volume flow.
Example 6
When adding an additive, e.g. of a paint, the volumetric flow can be measured using volumetric measuring equipment. The injection unit of additive addition injects the additive in proportion to the volume flow.
Example 7
When direct injection in molds can be necessary for large-volume parts, which are produced in the casting process, often very high amounts of material. Injection takes place directly from the feed pump to the tool. On the user interface you can set the spray profile (quantity, time). Optionally, the use of in-mold pressure sensors can regulate the injection.
Example 8: Automatic deaeration 17
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After the change of container air is introduced into the conveyor system. This must be removed from the system. If air remains in the system, the downstream process is severely affected and production downtime can occur. When the air reaches the mostly longer fluid hoses, a large amount of material has to be flushed through the entire system. This manual process relies on the visual and audible perception of the operators. It can not be said with certainty if all the air in the system has been vented. Most of the time, therefore, more material is drained than is necessary because it must be removed bubble-free for a certain time.
To remove the air, in the device according to Example 1 in the follower plate 6, an automated vent valve 5 is integrated or constructed on the follower plate 6, which can be opened and closed by the controller. The pressure transducer 10 mounted at the pump outlet measures the delivery pressure. The revolutions or rotational angle position of the pump shaft or of the pump drive are evaluated.
The operator operates the controls for lowering the follower plate 6 in the material container. The conveyor recognizes that the follower plate 6 rests on the liquid or air cushion in the drum 15 (no change in follower plate position) and opens the follower plate breather 5. The trapped air at the pump inlet and the amount of X material from the follower plate 6 can escape. The vent valve 5 closes after a predetermined time. Subsequently, the pump 4 starts the measurement sequence against the closed hydraulic system. If the pressure transducer 10 does not measure the setpoint value (ie the value of the liquid without 18 • fr * φ * φφφφ φφφφ ···•••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••••) fr · fr fr · for ··· · fr ···
Air), the vent valve 5 is opened again so that air can escape. If the next measurement yields the setpoint value, the venting valve 5 remains closed and the system goes into automatic mode.
Optionally, a second automatic valve 9 can be mounted at the pump outlet, which reduces the pump pressure, so that a new measurement of the air is possible.
If necessary, the pump pressure can also be reduced by reversing the direction of pump flow (change of direction of rotation), so that a new measurement of the air is possible.
Optionally, the vent slide 5 can also be operated manually (there is a request from the controller to the operator in dialogue form).
The evaluation principle is defined such that the pump 4 starts to rotate, the information of the pressure transducer 10 at the pump outlet being compared with the rotation angle of the pump 4. If air is in the system or pending at the pump input, this is evaluated by the relationship between pressure and angle of rotation. This information is compared to default values (if there is no air in the system). Based on the pressure increase for the rotation of the pump 4 can be back-calculated on the trapped air (compressibility of the material) "An evaluation of the pulsation of the pressure is also possible. If the system detects air in the system, the built-up pump pressure is reduced and the vent valve 5 is opened on the follower plate 6 and discharged a certain amount of material or air. Subsequently, the vent valve 5 is closed again and measured whether φφ φφ φφ φφφφφφφφ φφ φφφφφφφ φφφ φ · φ φ φ φ φφφ φ φ φφφφφφφ · φ φ φφφφ φ φφφφ still air is in the system. This process is repeated until the pressure rise curve is stable or has approached the standard values.
Example 9: Compensation of different filling heights
Due to the possibility that the materials to be mixed may differ in viscosity, it is possible that this may result in an unequal emptying of the material container in systems with a volumetric displacement and a mixture of 1: 1. Often, in practice, the container supplied by the manufacturer is not equally high {components A and B are different in volume). Since the containers A and B must be emptied simultaneously (batch production process) and these can not be replaced optionally, it comes with a fixed mixing ratio to an unequal emptying and a residual material content in a container, the second container has been completely emptied. Thus, it can occur that 10% residual material is contained in a container, which can not be further processed and thus must be disposed of as hazardous waste. This means an increased environmental impact and for the user in addition a financial burden.
Depending on the manufacturer, the silicones can be mixed with a slight deviation of + -5% (depending on the manufacturer's data sheet of the silicone). This allows an adjustment of the mixing ratio, so that the containers can be emptied simultaneously (if the filling level does not exceed +5% of the maximum deviation). 20
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The material containers are loaded at the same time, and after the deaeration process, the drum filling height is determined with a sensor which is arranged on the lifting cylinder 1. From the deviation, the necessary mixing ratio is calculated; the control unit then controls the pumps 4 to the extent that both containers are emptied evenly and completely. The necessary mixing ratio is recalculated during production to compensate for any viscosity differences in the container. 21

权利要求:
Claims (17)
[1]
Tf ♦ »I ** · · · · · · · · · · · · · · · · · · · ·» »» »» »» »» »» »» »» » 1. A mixing device for mixing at least two liquids, comprising at least two containers (15), each containing a liquid, and at least two pumps (4) for conveying the liquids, which pumps (4) are each arranged on a container (15), characterized in that the pumps (4) are screw pumps, the pumps (4) are connected to a follower plate (6) and the follower plate (6) is adjustable in height, wherein the follower plate (6) rests on the liquid surface and sealing with the container (15) closes.
[2]
2. Device according to claim 1, characterized in that after the pump (4) - seen in the conveying direction - a hose is provided which has a valve for the addition of additives.
[3]
3. Mixing device according to claim 1 or 2, characterized in that the liquid has a viscosity in the range of 1 mPa.s to 3,000,000 mPa.s.
[4]
4. Mixing device according to one of claims 1, 2 or 3, characterized in that the liquid has a viscosity in the range of 100,000 mPa.s to 3,000,000 mPa.s.
[5]
5. Mixing device according to one of the preceding claims, characterized in that the mixing device comprises a curling device (7) for easy conveying of the container (15) to the point of emptying. 23 • 4 »4M 4 4 4 4 4 4 4 4 4 * ·» ······ * «*« »« ·· * 4 * »« · «· 4 4 4 4 4
[6]
6. Mixing device according to one of the preceding claims, characterized in that the mixing device has transport rollers (12).
[7]
7. Mixing device according to one of the preceding claims, characterized in that the follower plate (6) has an automated vent valve (5).
[8]
8. Mixing device according to one of the preceding claims, characterized in that a pressure sensor (10) is provided at the pump outlet.
[9]
9. Mixing device according to claim 8, characterized in that a control unit is provided which controls the automatic venting valve (5) by measuring the delivery pressure at the pressure transducer (10), wherein the delivery pressure when the venting valve (5) is closed with the desired value of an air-free Liquid is compared and the vent valve (5) is opened as often and until the delivery pressure with the vent valve (5) is closed with the target value, whereupon the vent valve (5) remains closed.
[10]
10. Mixing device according to claim 9, characterized in that the control unit evaluates the revolutions or angular position of the pump shaft or the pump drive.
[11]
11. Mixing device according to one of the preceding claims, characterized in that sensors on the lifting cylinder (1) are arranged, which measure the filling level of the container (15) and are connected to a control unit, which in turn is connected to the pump (4) and via which control unit the 24 »♦ Μ Μ ·· ♦ · ································································································. It is possible to control pumps (4) for uniform emptying of at least two containers (15).
[12]
12. A method for mixing at least two liquids, characterized in that in a mixing device according to any one of claims 1-11 at least two containers (15) are arranged, a follower plate (6) which seals with the container, placed on the liquid surface is, the air between the liquid surface and the follower plate (6) is removed and the liquids from the at least two containers (15) by a respective screw pump (4) are promoted and the material streams are subsequently combined, whereby the mixing takes place.
[13]
13. The method according to claim 12, characterized in that the air between the liquid surface and follower plate (6) is removed by a control unit by measuring the delivery pressure at the pressure transducer (10) controls an automated vent valve (5), wherein the discharge pressure with the vent valve closed ( 5) is compared with the target value of an air-free liquid and the vent valve (5) is opened as often and until the delivery pressure with the vent valve (5) is closed with the target value, whereupon the vent valve (5) remains closed ,
[14]
14. The method according to claim 13, characterized in that the control unit evaluates the revolutions or angular position of the pump shaft and the pump drive. 25

[15]
15. The method according to any one of claims 12 to 14, characterized in that sensors which are arranged on the lifting cylinder (1), measure the filling level of the container (15), wherein the sensors are connected to a control unit, which in turn with the pump ( 4), wherein the control unit controls the pumps (4) for uniform emptying of at least two containers (15).
[16]
16. Use of a mixing device according to one of claims 1 to 11 for mixing at least two liquids.
[17]
17. Use of a mixing device according to one of claims 1 to 11 in a method according to one of claims 12 to 15. Vienna, 10 October 2012 Dietmar WAIZENAUER BSc. Kematen an der Krems (AT) Bernhard WAIZENAUER BSc.

Patent Attorney 26

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同族专利:

公开号 | 公开日

WO2014056011A3|2014-07-17|

AT512536B1|2013-09-15|

US20150375185A1|2015-12-31|

EP2906333B1|2017-01-04|

WO2014056011A2|2014-04-17|

EP2906333A2|2015-08-19|

引用文献:

公开号 | 申请日 | 公开日 | 申请人 | 专利标题

EP1331072B1|2002-01-28|2004-09-22|ELAST Kunststofftechnik GmbH & Co. KEG|Process and apparatus for the controlled removal of fluent materials from several receptacles|

DE102004030654A1|2004-06-24|2006-01-19|Sca Schucker Gmbh & Co. Kg|Device for conveying viscous material|

DE102005037118B3|2005-08-03|2007-01-18|Leistritz Ag|Double-flow screw pump with manifold bearings for supplying single/multi-phase mixtures has a drive spindle and a main arbor each with a central arrangement of bearings and screw-shaped workings|

DE202011108222U1|2011-11-24|2012-02-14|Reinhardt-Technik Gmbh & Co.|Device for dispensing liquids from containers|EP2801462A1|2013-05-07|2014-11-12|ELAST Kunststoffverarbeitungs-GmbH & Co. KG|Method and device for the controlled removal of liquid materials from several containers|

CN110902636A|2019-12-18|2020-03-24|佛山市金银河智能装备股份有限公司|Sealant pressing machine|

DE102020127440A1|2020-08-06|2022-02-10|Atlas Copco Ias Gmbh|Device for conveying viscous material|US4090640A|1975-07-24|1978-05-23|Smith Ray V|Hot melt adhesive pumping apparatus having pressure-sensitive feedback control|

US4651897A|1984-10-22|1987-03-24|Sashco, Inc.|Portable progressive cavity pump|

IL131011A|1997-02-17|2002-07-25|Bayer Ag|Method and mixing head for producing a reaction mixture from an isocyanate and a higher-viscous polyol formulation|

US6220747B1|1997-08-14|2001-04-24|Michael Gosselin|Proportional pump system for viscous fluids|

JP4292264B2|2003-10-31|2009-07-08|兵神装備株式会社|Discharger|

DE102005049805B4|2005-08-19|2007-06-14|Erich Scheugenpflug|emptying|

DE102007003972B4|2007-01-26|2012-01-19|Viscotec Pumpen- Und Dosiertechnik Gmbh|Device for air-free removal and improved ventilation with porous dividing plates|US9539552B2|2013-03-08|2017-01-10|Rex DeWald|Device for enhancing the mobility of a standard mixer|

EP3296075B1|2016-09-20|2021-11-10|Wagner International Ag|Feeding apparatus for feeding a viscous material from a container and method for operating the feeding apparatus|

AT17329U1|2019-10-16|2021-12-15|Nexus Elastomer Systems Gmbh|Integrated sensor system|

CN111644095B|2020-06-15|2022-02-01|多立克科技新材料集团有限公司|Hierarchical thick liquids agitating unit|

法律状态:
2018-04-15| PC| Change of the owner|Owner name: NEXUS AUTOMATION GMBH, AT Effective date: 20180226 |

优先权:

申请号 | 申请日 | 专利标题

ATA1097/2012A|AT512536B1|2012-10-10|2012-10-10|mixing device|ATA1097/2012A| AT512536B1|2012-10-10|2012-10-10|mixing device|

US14/434,918| US20150375185A1|2012-10-10|2013-09-04|Mixing device|

EP13795407.9A| EP2906333B1|2012-10-10|2013-09-04|Mixing device and mixing method|

PCT/AT2013/050171| WO2014056011A2|2012-10-10|2013-09-04|Mixing device|

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