• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    Device (50) for the thermal processing of plastics, comprising an air dehumidification system (20) and a thermally heated tool (52) which is surrounded by a tool room (54), characterized in that the air outlet (14) of the air dehumidification system (20) and the air inlet (12) of the air dehumidification system (20) are each connected to the tool room (54), the air dehumidification system (20) having at least two heat exchangers (1, 2, 3, 4) which have a common coolant circuit (10) the first heat exchanger (1) and the second heat exchanger (3) are arranged one behind the other, so that the air inlet (12) is arranged on the first heat exchanger (1) and the air outlet (14) is arranged after the second heat exchanger (3), wherein the first Heat exchanger (1) has an evaporative heat exchanger and the second heat exchanger (3) has a condensation heat exchanger, wherein the coolant circuit (10) is such, d the coolant outlet (1.2) of the first heat exchanger (1) opens into an inlet (6.1) of a compressor (6), the outlet (6.2) of the compressor (6) discharging into the coolant inlet (3.1) of the second heat exchanger (3), wherein the coolant outlet (3.2) of the second heat exchanger (3) opens into the coolant inlet (1.1) of the first heat exchanger (1).
    公开号:AT517761A1
    申请号:T50869/2015
    申请日:2015-10-13
    公开日:2017-04-15
    发明作者:
    申请人:Blue Air Systems Gmbh；
    IPC主号:
    专利说明:

    description
    The invention relates to a device for the thermal processing of plastics, comprising an air dehumidification system and a thermally heated tool, which is surrounded by a tool room, wherein the air outlet of the dehumidifying system is connected to the tool room. Furthermore, the invention relates to a dehumidifying system.
    In the thermal processing of thermoplastics such as in injection molding, extrusion blow molding, extrusion or deep drawing, there is the fundamental technical problem that the finished plastic parts and the corresponding tools have very high temperatures and then must be quickly cooled again. In the case of production of polyethylene terephthalate (PET) bottles, temperatures of around 220 ° C occur. If the surface temperature falls below the dew point of the ambient temperature during cooling, condensate forms on the plastic product and on the tool of the device for the thermal processing of plastics.
    In the prior art ambient air is sucked in by a dehumidifying system, filtered in a filter, cooled, then reheated and finally blown into the tool room as dry process air. The ambient air cleaned by the filter is cooled by heat exchangers. The accumulating condensation is collected and removed. For dehumidification mainly adsorption (equipped with silica gel or dry-wheel dryer principle) are used.
    To avoid the condensate, among other things, the cooling water temperature is raised in the prior art. However, this lengthens the cooling time and reduces productivity in production. Increasing the cooling water temperature by 1 ° C causes a reduction of approx. 1% in production. Since such plastic products are produced in very large quantities, the committee and the economic failure in this approach, therefore, are very large.
    It is therefore known from the prior art to supply the tool room with dry process air, which lowers the dew point and thus increases the productivity of plastic processing machines due to significantly shorter cooling times. For this purpose, a cover is placed over the tool room to keep the dry air in the plastic processing machine.
    A disadvantage of the prior art is the fact that the energy consumption for such cooling devices is very high.
    Object of the present invention is therefore to provide a device and an air dehumidification system of the type mentioned, in which the energy required for cooling is reduced.
    This object is achieved by a device for the thermal processing of plastics, comprising a Luftentfeuchtungsanlage and a thermally heated tool, which is surrounded by a tool room, characterized in that the air outlet of the dehumidifying system and the air inlet of the dehumidifying system are each connected to the tool room, said the dehumidifying system has at least two heat exchangers, which have a common coolant circuit, wherein the first heat exchanger and the second heat exchanger are arranged one behind the other, so that the air inlet is arranged on the first heat exchanger and the air outlet is arranged after the second heat exchanger, wherein the first heat exchanger has an evaporating heat exchanger and the second heat exchanger has a condensation heat exchanger, wherein the coolant circuit is such that the coolant outlet of the first heat exchanger into an inlet s of a compressor, wherein the outlet of the compressor opens into the coolant inlet of the second heat exchanger, wherein the coolant outlet of the second heat exchanger opens into the coolant inlet of the first heat exchanger.
    Due to the special nature and arrangement of the heat exchangers as well as the closed loop, i. Recycling the cooling air via the fluid lines significantly reduces the energy consumption for the same degree of cooling of the tool and plastic part, or it can reduce condensate formation and plastic scrap.
    For example, the apparatus for the thermal processing of plastics may be selected from the group of injection molding machine, (co) extrusion device, plastic plasticizing unit, extrusion blower, plastic machine or draw-down iron.
    The object is also achieved by an air dehumidification system, comprising at least two heat exchangers, which have a common coolant circuit, wherein the first heat exchanger and the second heat exchanger are arranged one behind the other, so that the air inlet is arranged on the first heat exchanger and the air outlet is arranged after the second heat exchanger , wherein the first heat exchanger a
    Evaporating heat exchanger and the second heat exchanger having a condensation heat exchanger, wherein the coolant circuit is such that the coolant outlet of the first heat exchanger opens into an inlet of a compressor, wherein the outlet of the compressor opens into the coolant inlet of the second heat exchanger, wherein the coolant outlet of the second heat exchanger in the coolant inlet of the first heat exchanger opens.
    Hereinafter, advantageous embodiments are described, which apply both to the device for the thermal processing of plastics and for the dehumidifying system.
    Particularly preferably, a third heat exchanger is provided, which is arranged between the first heat exchanger and the second heat exchanger, so that air entering through the air inlet flows through the first heat exchanger, the third heat exchanger and then through the second heat exchanger, or so first heat exchanger, third heat exchanger and the second heat exchanger are each arranged one behind the other, wherein the third heat exchanger has an evaporation heat exchanger, wherein the coolant circuit is such that the coolant outlet of the third heat exchanger also opens into the inlet of the compressor. All three heat exchangers thus have a common coolant circuit. This variant is to operate particularly low energy.
    Furthermore, in one embodiment, a fourth heat exchanger may be provided, wherein the coolant circuit is such that the outlet of the compressor opens into the coolant inlet of the fourth heat exchanger, wherein the coolant outlet of the fourth heat exchanger opens into the coolant inlet of the second heat exchanger, wherein the coolant outlet of the second heat exchanger into the coolant inlet of the first heat exchanger and, if a third heat exchanger is present, opens into the coolant inlet of the second heat exchanger. Also in this Lall a common coolant circuit is provided for all heat exchangers. Energy consumption can thus be reduced to a minimum.
    The fourth heat exchanger can be designed differently. For example, it can be provided that the fourth heat exchanger is a condensation heat exchanger. Alternatively, e.g. be provided that the fourth heat exchanger has a water-cooled condenser.
    Furthermore, it can be provided that a fan is arranged in front of the second heat exchanger. In the case of a third heat exchanger, the fan is preferably arranged after the third heat exchanger but before the second heat exchanger. This makes it possible to divert cooling air for other consumers.
    Suitable coolants are conventional coolants. One possible coolant for the coolant circuit is e.g. R404A. R404A is a mixture of 1,1,1-trifluoroethane, pentafluoroethane and 1,1,1,2-tetrafluoroethane.
    In all embodiments, it is preferably provided that the first heat exchanger and the third heat exchanger are evaporative heat exchangers and the second heat exchanger is a condensation heat exchanger.
    The device according to the invention (and the dehumidifying system) can be operated without cooling water. This reduces the considerable energy consumption for such systems to up to 1/10 of conventional systems. This goal is achieved by recycling the produced dry air with a dew point of + 3 ° C and returning it to the dehumidifying unit. The drying of these recirculated air consumes significantly less energy than would supply moist outside air of the system. The new dehumidification system is to be operated via a refrigeration cycle with a compressor. The main advantage is that the compressor power is stepless and can be reduced by up to 90%, which was not possible until now. The energy requirement of the system in combination with this compressor system leads to an extreme energy saving potential. For a smooth production process, it is necessary to achieve a constant dew point of the air. The recycled cooling air can reach the dehumidifying system with a strongly fluctuating moisture content. The dehumidifying system must react quickly to these fluctuations and bring in different intensity output. The refrigeration cycle must react and work differently. In the plant, this is realized by the fact that the evaporator pressure, which is responsible for the condensation at the heat exchanger, permanently adapts to the moisture content or the temperature of the process air. This is realized with the help of an evaporator pressure sensor, an electrical regulator and a solenoid valve in the digital scroll compressor.
    In order to save energy, a control of the process fan can additionally be installed, which decimates the process air when there is no need and additionally improves the energy-saving potential. The air in the foreclosed area of the system is circulated. If the air is not supplied from the outside but recycled, a filter in the process air circuit is integrated, which filters out or neutralizes potentially harmful vapors and gases from the tool room for the dehumidifier. Mixing plastic vapors from production with condensate or moisture can produce hydrofluoric acid which can attack the metals of the plant. In addition to a dust filter, an additional so-called electrostatic filter can be remedied and installed here.
    The result of the developments is a smaller, more efficient plant, with much lower energy consumption than commercially available today.
    Further details and advantages of the invention are illustrated below with reference to the figures.
    Fig. 1 shows a device for the thermal processing of plastics, comprising an air dehumidifying plant according to the prior art.
    Fig. 2 shows a device for the thermal processing of plastics, comprising an air dehumidification system according to the invention.
    Fig. 3a, 3b shows another device for the thermal processing of plastics, comprising an air dehumidification system according to the invention.
    Fig. 4-7 shows embodiments of inventive dehumidifying.
    Fig. 1 shows a device 50 for the thermal processing of plastics in the form of an injection molding machine according to the prior art. The injection molding machine 50 comprises an air dehumidification system 20 and a thermally heated tool 52, which is surrounded by a tool space 54. The dehumidification system 20 has an air inlet 12 which draws in fresh air. The air outlet 14 is connected to the tool room 54 and cools the tool 52 there. The energy requirement of such a device 50 for cooling and dehumidifying the fresh air is very high.
    As can be seen from Table 1 below, a power of approximately 20 kW is necessary for the treatment of the cold water in the air / water heat exchanger. The dehumidifier according to the invention can dispense with this heat exchanger and thus drastically save energy.
    Fig. 2 shows a device 50 for the thermal processing of plastics in the form of an injection molding machine according to the invention. The injection molding machine 50 comprises an air dehumidification system 20 and a thermally heated tool 52, which is surrounded by a tool space 54. The dehumidifying system 20 has an air inlet 12 and an air outlet 14. Both the air inlet 12 and the air outlet is fluidly connected to the tool room 54 for dehumidifying the tool 52. The cooling air is thereby recycled after cooling. The arrows indicate the course of the air.
    3a and 3b show two views of another device 50 according to the invention for the thermal treatment of plastics in the form of an injection molding machine. In contrast to the previously mentioned example in FIG. 2, this embodiment variant also has a discharge line 19, with which other parts on the device 50 can be cooled.
    FIGS. 4 to 7 show air dehumidification systems 20 according to the invention. The same reference numerals are used equally in all figures, so that Figs. 4 to 7 are described together with reference to FIG. 3 and only the differences in Figs. 4 to 7 are worked out.
    The dehumidifier 20 includes the preferred embodiment with four heat exchangers 1, 2, 3, 4, which have a common coolant circuit 10. The first heat exchanger 1, the third heat exchanger 2 and the second heat exchanger 3 are each arranged (linearly) one behind the other, so that air can flow through the heat exchangers 1, 2, 3 in a linear manner. The air inlet 12 is arranged on the first heat exchanger 1 and the air outlet 14 is arranged after the second heat exchanger 3. Cooling air therefore flows first through the first heat exchanger 1, then through the third heat exchanger 2 and then through the second heat exchanger 3. The first heat exchanger 1 and the third heat exchanger 2 are formed as evaporation heat exchanger, the second heat exchanger 3 is designed as a condensation heat exchanger. The coolant circuit 10 is designed such that the coolant outlet 1.2 of the first heat exchanger 1 and the coolant outlet 2.2 of the third heat exchanger 2 open into an inlet 6.1 of a compressor 6.
    The outlet 6.2 of the compressor 6 opens into the coolant inlet 4.1 of the fourth heat exchanger 4. The coolant outlet 4.2 of the fourth heat exchanger 4 opens into the coolant inlet 3.1 of the second heat exchanger 3. The coolant outlet 3.2 of the second heat exchanger 3 opens into the coolant inlet 1.1 of the first heat exchanger 1 and in the coolant inlet 2.1 of the third heat exchanger 2. Thus, a closed coolant circuit is formed. After the air outlet 14, a process air fan 18 is provided, from where the cooling air flows into the tool space 54 of the device 50 (see FIGS. 2, 3a, 3b). The coolant for the coolant circuit is R404A.
    In the examples of Figs. 4 and 5, the fourth heat exchanger 4 is a condensation heat exchanger with two fans. In Figs. 6 and 7, the fourth heat exchanger 4 is a water-cooled condenser. The examples of FIGS. 4 and 5 or 6 and 7 differ by the additional process fan 16.
    The electrically operated compressor 6 compresses the gaseous, cool refrigerant (R404A) from low pressure level (about 5 bar) to high pressure level (about 15 bar). The hot, gaseous refrigerant is pre-cooled at the fourth heat exchanger 4. This air-refrigerant heat exchanger is cooled in Fig. 4 by two speed-controlled fans. The regulation of the condenser fan is done by a high pressure sensor. Depending on the high pressure, they turn faster or slower. The precondensator is mainly used only in the first few minutes until the foreclosure of the production machine is dehumidified. Thereafter, the second heat exchanger 3 is sufficient to handle the load. In addition, the outlet air can be regulated or cooled via the fourth heat exchanger 4. This has an advantageous effect on the energy reduction.
    The refrigerant R404A then flows in the coils of the second heat exchanger 3 (condenser) against the air direction, removes a large part of the heat contained in the air. (From an energy point of view, condensation releases energy that is supplied to the cool air coming from the evaporator.) In plain language: the air is heated up. The now liquid refrigerant flows to the expansion valve 5, which injects this into the heat exchanger (evaporator) 1, 2. These two similar heat exchangers (evaporators) 1, 2 are used for the air cooling in the second cooling stage. Here, refrigerant (R404a) is used instead of cold water for air cooling. In the evaporators 1, 2, the refrigerant changes from the liquid to the gaseous state (condensation). This requires energy, which is extracted from the process air in the form of temperature (in plain language: the air is cooled). Through the two evaporators 1, 2, the air is cooled in two stages. To realize this, evaporator 1 is kept at a somewhat warmer temperature level by a mechanical valve.
    Condensation rises from the air as a result of air cooling in all two stages and accumulates in a condensate tank. Through a hose, the condensate from the dehumidifier 20 is guided and fed into the sewer system.
    The now cool and brought to a low pressure level refrigerant is now sucked by the compressor, recompressed and heated and brought to a higher pressure level, thus closing the circuit again. A high and low pressure switch monitors the operating pressures of the refrigerant and turns off the compressor when the refrigeration unit is moving out of normal operating range. A low pressure gauge and a high pressure gauge indicate the operating pressures. After the third cooling stage 2, the process air is passed to the condenser at a temperature of approx. 3 ° C. There, the process air extracts heat from the refrigerant. With a strong blower 18, the process air is sucked in and transported through an air duct system to the tool room 52. A temperature measuring device can be installed to indicate the temperature of the process air and the refrigerant. Signal lamps are provided next to the temperature measuring device to facilitate the adjustment of the control elements and the monitoring of the operating state.
    The unit is fitted with a condensate pump. The float switch monitors the water level in the condensate tray and switches on the condensate pump if necessary. A condensate filter can protect the pump from dirt particles.
    Instead of designing the fourth heat exchanger 4 as a precondensator, a refrigerant-water heat exchanger may be used (FIGS. 6 and 7). This is controlled by a water valve and has the same positive characteristics as the air heat exchanger (process air temperature control). The size of the dehumidifier 20 may incidentally also be much smaller. The cooling water can be many times warmer than the cooling water used to cool the mold and is therefore much cheaper for the customer (tower water instead of chiller water or evaporation towers instead of cold water aggregate).
    In Fig. 7, an additional, smaller process fan 16 is provided, with which about 10 -30% of the cold air is diverted directly after the evaporator and for cooling the cabinet of the production machine or the conveyor belt, which are the products produced by the production machine be post-cooled or cooled on a conveyor belt or the like. For this purpose, if necessary for temperature control and to avoid condensation of the delivery line or other components warm fresh air via a flap (electronically controlled if necessary) added. As a result, the additionally generated process air temperature can also be controlled here and can be made substantially cooler than the main process air.
    Table 1: Comparison adsorption dryer plant with inventive
    Luftentfeuchtungsanlage
    权利要求:
    Claims (9)
    [1]
    claims
    1. Apparatus (50) for the thermal processing of plastics, comprising an air dehumidification system (20) and a thermally heated tool (52), which is surrounded by a tool room (54), characterized in that the air outlet (14) of the air dehumidification system (20 ) and the air inlet (12) of the air dehumidification system (20) are each connected to the tool room (54), the air dehumidification system (20) having at least two heat exchangers (1, 2, 3, 4) which have a common coolant circuit (10) in that the first heat exchanger (1) and the second heat exchanger (3) are arranged one behind the other, so that the air inlet (12) is arranged on the first heat exchanger (1) and the air outlet (14) is arranged after the second heat exchanger (3) the first heat exchanger (1) has an evaporation heat exchanger and the second heat exchanger (3) has a condensation heat exchanger, wherein the coolant circuit (10) is such in that the coolant outlet (1.2) of the first heat exchanger (1) opens into an inlet (6.1) of a compressor (6), the outlet (6.2) of the compressor (6) opening into the coolant inlet (3.1) of the second heat exchanger (3) wherein the coolant outlet (3.2) of the second heat exchanger (3) opens into the coolant inlet (1.1) of the first heat exchanger (1).
    [2]
    2. Apparatus according to claim 1, characterized in that the device (50) for the thermal processing of plastics is selected from the group of injection molding machine, (co) extrusion device, Kunststoffplastifiziereinheit, Extrusionsblasvorrichtung, plastic machine or thermoforming machine.
    [3]
    3. dehumidifying system (20) comprising at least two heat exchangers (1, 2, 3, 4) which have a common coolant circuit (10), wherein the first heat exchanger (1) and the second heat exchanger (3) are arranged one behind the other, so that the Air inlet (12) on the first heat exchanger (1) is arranged and the air outlet (14) after the second heat exchanger (3) is arranged, wherein the first heat exchanger (1) comprises an evaporative heat exchanger and the second heat exchanger (3) has a condensation heat exchanger, wherein the coolant circuit (10) is such that the coolant outlet (1.2) of the first heat exchanger (1) opens into an inlet (6.1) of a compressor (6), the outlet (6.2) of the compressor (6) into the coolant inlet (3.1) of the second heat exchanger (3) opens, wherein the coolant outlet (3.2) of the second heat exchanger (3) opens into the coolant inlet (1.1) of the first heat exchanger (1).
    [4]
    4. Apparatus according to claim 1 or claim 2 or dehumidifying system according to claim 3, characterized by a third heat exchanger (2) which is arranged between the first heat exchanger (1) and the second heat exchanger (3), wherein the third heat exchanger (2) has an evaporation heat exchanger wherein the coolant circuit (10) is such that the coolant outlet (2.2) of the third heat exchanger (2) also opens into the inlet (6.1) of the compressor (6).
    [5]
    5. Apparatus according to claim 1, 2 or 4 or dehumidifying system according to claim 3 or claim 4, characterized by a fourth heat exchanger (4), wherein the coolant circuit (10) is such that the outlet (6.2) of the compressor (6) in the Coolant inlet (4.1) of the fourth heat exchanger (4) opens, wherein the coolant outlet (4.2) of the fourth heat exchanger (4) opens into the coolant inlet (3.1) of the second heat exchanger (3), wherein the coolant outlet (3.2) of the second heat exchanger (3) into the coolant inlet (1.1) of the first heat exchanger (1) and, if a third heat exchanger (2) is present, into the coolant inlet (2.1) of the third heat exchanger (2).
    [6]
    6. Apparatus according to claim 5 or dehumidifying system according to claim 5, characterized in that the fourth heat exchanger (4) has a condensation heat exchanger.
    [7]
    7. Apparatus according to claim 5 or dehumidifying system according to claim 5, characterized in that the fourth heat exchanger (4) comprises a water-cooled condenser.
    [8]
    8. Device according to one of claims 1, 2 or 4 to 7 or dehumidifying system according to one of claims 3 to 7, characterized in that a fan (16) is arranged in front of the second heat exchanger (3).
    [9]
    9. Device according to one of claims 1, 2 or 4 to 8 or air dehumidification system according to one of claims 3 to 8, characterized in that after the second heat exchanger (3) a process air fan (18) is arranged.
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    同族专利:
    公开号 | 公开日
    AT517761B1|2018-03-15|
    EP3156735A1|2017-04-19|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    EP0689921A1|1994-06-30|1996-01-03|N.V. Resilux|Method for drying a mould|
    EP1676623A1|2004-12-28|2006-07-05|Dagobert Girardelli|Apparatus and method for dehumidifying air|
    EP2116353A1|2007-02-26|2009-11-11|Toyo Seikan Kaisya, Ltd.|Blow molding machine with air conditioning|
    JP2001090990A|1999-09-20|2001-04-03|Chikayoshi Sato|Dehumidifier|IT201800001787A1|2018-01-24|2019-07-24|Selene Spa|Method and device for controlling the temperature of refrigerated components of a blown extrusion apparatus and apparatus comprising said device|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    ATA50869/2015A|AT517761B1|2015-10-13|2015-10-13|Device for the thermal processing of plastics|ATA50869/2015A| AT517761B1|2015-10-13|2015-10-13|Device for the thermal processing of plastics|
    EP16193769.3A| EP3156735A1|2015-10-13|2016-10-13|Air dehumidification system|
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