• 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:
    1473074 Heating and cooling systems O SCHAFER 21 May 1975 [27 May 1974] 21919/75 Heading F4U A heating and cooling system for a heat exchanger, e.g. a press 7 or a reaction vessel, comprises a pump 8, a boiler 5 and a cooler 9 and includes a reservoir 12 which can be connected in a closed circuit including only the pump 8 and heat exchanger 7 or in a closed cooling circuit including the cooler 9. Similarly, a second reservoir 13 is provided and may be connected in a closed circuit including only the pump and heat exchanger or in a closed heating circuit including the boiler 5. The circuit arrangement is such that the reservoir 13 serves for the preliminary heating of the heat exchanger at the beginning of the warm-up phase and the reservoir 12 serves for the preliminary cooling of the heat exchanger at the beginning of the cool-down phase. Upon changing from heating to cooling, liquid in the reservoir having the higher temperature is delivered to the heat exchanger for preliminary cooling. The amounts of liquid in each warm-up or cool-down phase are circulated exclusively in closed circuits, first between the heat exchanger and one reservoir and, at a later stage in the same phase, between the heat exchanger and the other reservoir, the entire amount of liquid stored during the warm-up or cool-down phase being included in the cool-down or warmup process which follows. In a further embodiment, Fig. 8 (not shown), an additional reservoir is provided.
    公开号:SU843783A3
    申请号:SU752142374
    申请日:1975-05-27
    公开日:1981-06-30
    发明作者:Шефер Отмар
    申请人:Schaefer Otmar；
    IPC主号:
    专利说明:

    one. .. ;. This invention relates to heat engineering. There are known methods for operating a heating and cooling unit by heating and cooling the fluid circulating through a heat exchanger, heater, cooler and battery zones, and having a temperature in the latter above the temperature at the cooler and lower than the temperature at the outlet of the heater. the final stage of heating forms a closed fluid circuit through the heater and heat exchanger, c. at the last two cooling stages, they form a closed fluid circulation circuit through the heat exchanger and the IlJ refrigerator. Disadvantages of the known method, impossibility of their realization when using a liquid with boiling point at normal pressure below the required maximum operating temperature. “The purpose of the invention is to increase operational reliability when using a fluid with a boiling point below the required maximum operating temperature. The goal is achieved by forming a closed circulation loop between the heat exchanger and the accumulator zone with the temperature of the fluid exceeding the temperature in the heat exchanger. , at the second stage, a closed circulation circuit between the heat exchanger, the battery zone, which has a temperature higher than in the previous stage and the heater And the first cooling stage to form a closed loop circulation between the heat exchanger and the secondary battery area with the liquid temperature below the temperature in the heat exchanger. FIG. 1 shows a heating cooling unit with two. battery zones; in fig. 2 shows schematically the stages of the heating and (Cooling. Installation for the implementation of the method with two battery zones) contains heater 1, heat exchanger 2, cooler 3, battery zones 4. and 5 / pump B. Battery zone 4 using switching valves 7 and 8 and connecting
    The pipes are either connected to the heat exchanger 2, or connected to the cooling circuit, and the battery zone 5 is switched to the heat exchanger by the switching valve 9 or connected to the heating circuit.
    In FIG. 2 thin lines indicate temperatures close to the maximum operating temperature, dotted lines indicate temperatures close to the minimum operating temperature, dash-and-dot lines indicate average operating temperatures.
    In the first heating stage of the heat exchanger, water is supplied with an average temperature to the battery zone 5, and high temperature is supplied to the battery zone 4. Then, 1x is closed (an fluid circuit in which water from zone 5, with an average temperature is pumped into heat exchanger 2, and cold water from the heat exchanger is forced out into accumulator zone 5, while heat exchanger 2 is heated with water of average temperature. The accumulator The torus zone 5 should be about three times the volume of the heat exchanger. The first heating stage ends when the front front of cold water from the heat exchanger 2 passes through the battery zone 5 and reaches the exit from the zone. In this case, the heat exchanger increases by about a third the difference between maximum and minimum temperatures, the second stage heating fla fla the heated heat exchanger is connected to the heater 1 and, together with hot water, the average temperature return water from the heat exchanger 2 is pumped into the battery zone 4, which contains hot water from the previous cooling stages. This water is pumped back to heater 1, Battery zones 4 and 5 have the same volume. When the entire water of the battery zone 4 enters the heater 1, the battery zone 4 exits the heating circuit and a third heating stage begins, during which the heat exchanger is heated further to achieve a maximum temperature that is maintained for a predetermined period of time.
    In the first cooling stage, the heat exchanger 2 is connected to a storage zone 4 containing medium-temperature water, as a result of which the heat exchanger is cooled to an average temperature, and hot water heat exchanger enters the storage battery 4. When the water front of the heat exchanger passes through the battery zone 4 to its outlet, a second cooling stage begins, at which the water is of medium temperature.
    It is injected from the heat exchanger 2 into the battery zone 5, and cold water flows from it again into the refrigerator 3..
    After all the cold water from the battery zone 5 enters the refrigerator, the battery zone 5 is turned off from the circuit. The third cooling stage forms a closed circulation loop between the cooler and the heat exchanger to achieve the minimum temperature that is maintained for a predetermined time, after which the heating cycle repeats.
    For the implementation of the method, installations can be applied, - containing more than two battery zones, then the stepwise distribution of preheating and cooling is more EXACT. In this case, during the transition from cooling to heating, the low temperature storage zone for heating is connected to the heat exchanger and the contents of the next zone are pumped into the heater. During the transition from heating to cooling, precooling is performed stepwise, first the battery zone with the highest temperature, then the next with the lowest temperature, and the contents of the battery zone with the lowest temperature is injected into the refrigerator.
    When using a heating and cooling unit that implements the proposed method, liquids with a boiling point below the required maximum operating temperature can be used, and, in addition, the heat exchanger is not subjected to unacceptable heat stresses as the difference between the maximum and minimum temperatures increases.
    权利要求:
    Claims (1)
    [1]
    1. US Patent No. 3556201, cl. 165-2, published. 1972.
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    同族专利:
    公开号 | 公开日
    DE2425589B2|1979-05-10|
    JPS512051A|1976-01-09|
    FR2273243A1|1975-12-26|
    JPS5413009B2|1979-05-28|
    BR7503332A|1976-04-20|
    DE2425589A1|1975-12-11|
    GB1473074A|1977-05-11|
    US4026347A|1977-05-31|
    FR2273243B1|1979-03-30|
    DE2425589C3|1980-01-10|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    DE1013062B|1956-03-24|1957-08-01|Krantz H Fa|Method and device for alternating heating and cooling of presses or the like.|
    US3262493A|1963-05-20|1966-07-26|Ind Institution International|Means for heating and cooling a structure|
    US3548923A|1967-12-11|1970-12-22|Matsushita Electric Ind Co Ltd|Cooling and heating apparatus of heat storage type|
    DE1778068B2|1968-03-25|1976-05-06|Konus-Kessel Gesellschaft für Wärmetechnik mbH & Co KG, 6832 Hockenheim|DEVICE FOR SUCCESSIVE HEATING AND COOLING OF A PROCESSING DEVICE|
    US3603379A|1969-04-08|1971-09-07|Carrier Corp|Heating and cooling system|
    US3605873A|1970-03-30|1971-09-20|Carrier Corp|Heating and cooling system|
    US3738899A|1971-08-02|1973-06-12|Mc Farlan A Co Inc|Air conditioning system and method|
    US3931806A|1974-05-06|1976-01-13|Johnson Service Company|Method and apparatus for storing a medium heated by solar energy|CA1070669A|1976-05-26|1980-01-29|Richard E. Hinkle|Process and apparatus for the cyclic heating and cooling of processing equipment|
    US4146084A|1976-06-14|1979-03-27|American Hydrotherm Corp.|Process and apparatus for the cyclic heating and cooling of processing equipment|
    US4188995A|1977-05-26|1980-02-19|American Hydrotherm Corporation|Apparatus for the cyclic heating and cooling of processing equipment|
    DE2943797C2|1979-10-30|1984-05-17|Otmar Dipl.-Ing. 8000 München Schäfer|Method and device for alternating heating and cooling of a heat exchanger|
    DE3225403C2|1982-07-07|1986-02-06|Otmar Dipl.-Ing. 8000 München Schäfer|Process for the step-by-step heating of an item in a treatment device and subsequent cooling|
    AT506978A1|2008-07-02|2010-01-15|Engel Austria Gmbh|INJECTION MOLDING MACHINE WITH ENERGY RECOVERY|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE2425589A|DE2425589C3|1974-05-27|1974-05-27|Method and device for alternating heating and cooling of a heat exchanger of a heating-cooling system|
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