• 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:
    Multi-phase plate heat exchanger for 2 air media, wherein the active surfaces (13a) for heat transfer of liquids (3,4) are wetted, so that evaporation or condensation occur, and where the primary medium (1) is the hot and humid fresh air (15a) and the secondary medium (2) is the cool dry exhaust air (16a) of an inhabited space flowing in countercurrent to the gaseous primary medium (1), the inner surfaces of the slats (1a) for the primary medium (1) being filled with hygroscopic solution (17a) and the inner surfaces of the plate columns (2a) for the secondary medium (2) are wetted with water (18a), and where the regeneration of this hygroscopic solution (17b) takes place in a similar or the same heat exchanger (14), the inner surfaces of the plate columns ( la) for the primary medium (1) are wetted with preheated dilute hygroscopic solution (17b), and where the secondary medium (2) is in countercurrent to the primary (1) flows the same air (15c), which is heated after the primary passage through the heat exchanger (14) and saturated with steam, so that on the inner surfaces of the plate columns (la) for the secondary medium (2) as it cools Evaporation heat is recycled by condensation.
    公开号:AT518082A4
    申请号:T167/2016
    申请日:2016-03-31
    公开日:2017-07-15
    发明作者:Gerhard Kunze Dr
    申请人:Gerhard Kunze Dr；
    IPC主号:
    专利说明:

    introduction
    Room air conditioning consumes a large proportion of the global electricity supply and thus also contributes to the C02 balance of the earth. Energy savings can be made by heat recovery, in particular via heat exchangers. However, heat is stored or transported not only in the heat capacity of the substances concerned but also in the enthalpy of the steam involved. Heat recovery can only take place efficiently if cooling and heating, condensation and evaporation take place simultaneously and at the same location. This requires a redesign of the heat exchanger principle, which will be described here.
    State of the art
    Air conditioning is preferably carried out by electrically operated chillers. To achieve a comfortable climate, water vapor from the air usually has to be eliminated by condensation. The energy required for this is in extreme cases a multiple of what would be necessary for the mere cooling of the steam-free air over the same temperature interval. The condensation water is discarded instead of being used for evaporative cooling.
    So-called regulated ventilation is designed to help save energy by using air / air heat exchangers. However, since the enthalpy difference between moist hot outside air and cool dry inside air is much larger than the enthalpy difference between dry inside air and the same air outside temperature, such a heat exchange can only be made a very small contribution to the reduction of the required cooling capacity.
    In the patent document A192 / 2015, therefore, an air / air heat exchanger is described, where the condensate formed from the cooling air is supplied from the fresh air to the exhaust air to evaporate into it and thereby compensate for the heat of condensation liberated as heat of vaporization.
    However, a real cooling of the air below the temperature that prevails in the room to be air conditioned, which would be necessary to eliminate other heat inputs such as solar radiation or computer heat, can not take place. Therefore, this concept still requires the use of an active second cooling system, which typically has to handle more than half of the total cooling load.
    An additional problem arises from the fact that a constant humidification of the heat exchanger surfaces to bacteria or other
    Microbial growth, which could subsequently lead to constipation or even transmission of disease.
    task
    In principle, by a suitable heat exchanger, the total cooling capacity should be achieved by evaporative cooling, because the enthalpy difference between dry indoor air and steam-saturated air on the outside temperature must always be greater than the enthalpy difference between moist hot outside air and cool dry indoor air. In practice, however, this comparison is not entirely true for entropy reasons.
    After all, in many climatic situations, such as in the Austrian summer climate, a pure evaporative cooling is possible, if only the heat exchanger enough water on the exhaust air side feeds.
    The objects of the invention are therefore the following: air-conditioning of rooms by pure evaporative cooling, hygienic conditions in the heat exchanger limiting of the humidity in the rooms to be conditioned by a hygroscopic solution regeneration of the hygroscopic solution after it has taken up water, possibly crystallization processes can come, which must not disturb the entire process, by the same device - A compact design as possible for the whole device solution of the tasks and sub-tasks and the expected results
    The task to accomplish air conditioning of rooms by pure evaporative cooling is accomplished according to the invention by a novel multi-phase plate heat exchanger.
    A multi-phase heat and plate heat exchanger is a plate heat exchanger for two different temperature and vapor content gaseous media moved in countercurrent or parallel flow by a respective adjustable fan, the active heat transfer surface between the affected media on one or both surfaces of one or two two different slow-flowing liquids are wetted, which are in direct interaction with the respective media, so that evaporation or condensation and because of the resulting changes in concentration in the liquids also crystallization or dissolution of crystals can take place, these liquids from the outside to their specific entry positions be pumped between the heat exchanger plates and from there the forces of capillary action, air flow, turbulence, gravity or the constraining forces of special Plattenausf Following ormungen move as more or less thick liquid film through the plate heat exchanger, so that associated media and liquids usually do not flow in parallel.
    To operate such a multi-phase heat exchanger successfully results in the additional task of dropping the said liquids in the columns of the heat exchanger, but the amount introduced per gap should not vary greatly. In order to solve this problem, there are two methods: to allow the supply of liquid from a storage tank to the entry positions between the heat exchanger plates so that the supply line after the pump fills up into a bundle of capillary tubes or hoses, which at the corresponding destinations in the Open heat exchanger. to effect the supply of liquid from a storage tank to the entry positions between the heat exchanger plates so that the supply line to the pump leads to a common connection channel between the heat exchanger plates formed by congruently corresponding apertures through these plates, in each case
    Plate gap, is to be introduced into the liquid, a throttle for the dropwise passage of liquid from the connecting channel is provided in the gap.
    Experiments have shown that the liquid supply by capillaries, although much more complicated and expensive from the effort, as the alternative of a common connection channel across all plates, but the uniform distribution of the liquid over all plates is much more accurate, whereby the efficiency of the system essential getting better.
    Once the said liquids have been guided in the correct amount to the plate surfaces, the next task, namely to evenly wet these plate surfaces.
    This object is achieved in that the surfaces of the active heat transfer surfaces uniform distribution of the liquid film or the local retention of crystals or their further transport by grooves,
    Grinding marks, scratches and / or fiber coating, as well as by hydrophilic materials and coatings or even by a combination of several such measures favor.
    To solve the problem of limiting the humidity in the rooms to be conditioned by a hygroscopic Lösuna an additional Kühluncr the heat exchanger by well water can be helpful. And to solve the task of regenerating the hygroscopic solution after it has absorbed water, heating is needed.
    Both tasks together can be solved simultaneously, if in the described multi-phase plate heat exchanger, the inflows for media or liquids or individual sections of the heat exchanger itself with separate
    Temperierungsmedien or an electric heater in heat conductive contact that can heat or cool these areas.
    The establishment of an external Temperierungsmöglichkeit and their space requirements emphasize the importance of the above task of a compact design as possible to find the whole device. This object is achieved by a combination of a multi-phase heat exchanger with two or more of the plate heat exchangers for heating or cooling purposes, this combination consists of a single plate pack and the individual partial heat exchangers each form congruent areas on the plates of this package.
    The task to guarantee hygienic conditions in the heat exchanger and the task to limit the humidity in the rooms to be conditioned by a hygroscopic solution is jointly solved so that the liquids with which the active
    Surfaces wetted in the multiphase plate heat exchanger may contain water or other solvents as well as hygroscopic salts, refrigerants, disinfectants or wetting agents.
    In summary, the task of air conditioning rooms by pure evaporative cooling and thereby limit the humidity in the rooms to be air conditioned by a hygroscopic solution so that in a multi-phase plate heat exchanger, the primary medium is the hot and humid outside air of an inhabited room and the secondary medium but consumed is relatively dry and cool air of the inhabited space flowing in countercurrent to the primary medium, and that the inner surfaces of the plate columns for the primary medium are wetted with hygroscopic solution, this liquid and the air flow in opposite directions while the inner surfaces of the Plate columns for the secondary medium are wetted with water that can flow in any direction.
    The task of regeneration of the hygroscopic solution by the same device after this solution has absorbed water and thereby diluted and rendered ineffective, is solved by a multi-phase plate heat exchanger where the primary medium is the hot and humid outside air of an inhabited room and where the interior Surfaces of the plate columns for the primary medium preheated dilute and slightly hygroscopic solution are wetted in countercurrent to the primary medium, and where the secondary medium which flows in countercurrent to the primary medium is the same air which is heated after the primary passage through the heat exchanger and nearly saturated with steam, and that condensate water forms on the inner surfaces of the plate columns for the secondary medium as it cools, leaving the heat exchanger cooled in cocurrent with the secondary medium.
    Since it can not be ruled out that in the described drying process to regenerate the hygroscopic solution salt crystals form, which, if they are removed from the heat exchanger by the flow could possibly lead to blockages of the system, it is desirable as an additional task that such crystals on Where they occur, where they then in the next cooling phase, provided that it takes place in the same device, are again dissolved by condensation. This can be achieved if the multiphase plate heat exchanger is such that its plates are horizontal and there are grooves or waves transverse to the flow direction in which these crystals are deposited by gravity.
    List of illustrations and the meaning of the numbers
    Fig la shows a schematic representation of a refrigerator with multi-phase plate heat exchanger and hygroscopic air drying and
    Fig.lb shows the solution regeneration with the same device
    Figure 2 shows a section across the plates with the guide of primary and secondary medium and the liquid wetted layers wetting the plates
    FIG. 2a shows a heat exchanger with vertical plates and a liquid feed through capillaries, and FIG. 2b shows a liquid feed through distribution channels transversely through horizontal plates.
    The numbers in the figures mean: 1 .. gaseous primary medium la ... plate gaps for the primary medium 2 .. .gaseous secondary medium 2a ... plate gap for the secondary medium 3 .. .fluid for wetting the inner walls of the primary medium heat exchanger columns 4... Liquid for wetting the inner walls of the secondary medium heat exchanger columns 5 .. .Capillary for the supply of primary medium liquid 6 .. .Tube for the removal of primary medium liquid 7 ... Capillary for the supply of secondary medium liquid 8 .. .Pipe for the removal of secondary medium liquid 9 .. .Connection channel for supply from liquid to the primary medium 9a ... very small opening in the connecting channel (9) or at the end of a capillary (5) with throttling action 10 .. connecting channel for supplying liquid to the secondary medium 10a ... very small opening in the connecting channel (10) or at the end of a capillary (7) with throttle effect 11 ... Solution pump for the primary side 12 ... Solvent pump for the secondary side 13 ... Heat exchanger plates 13a ... active surface of the heat exchanger, (= separating wall between primary medium and secondary medium) 14 ... Multi-phase plate heat exchanger 14a ... Primary side of the multi-phase plate heat exchanger 14b ... Secondary side of the multi-phase plate heat exchanger 15a ... Hot moist fresh air in the vicinity of a room to be cooled 15b, .. Cooled dried fresh air 15c ... heated saturated with steam Fresh air 16a ... cool dry exhaust air from a cooled room 16b ... heated moist exhaust air 17a ... concentrated hygroscopic solution 17b ... diluted hygroscopic solution 17c ... heated dilute hygroscopic solution 18a ... cool water 18b .. slightly heated water 19 ... condensing water
    Description of the pictures
    Fig.la shows how the multiphase plate heat exchanger according to the invention is used for a ventilation system with cooling function in hot humid climates. The multiphase plate heat exchanger -14- is represented by two adjoining chambers -14a, 14b-with the upper of the two -14a symbolizing the heat exchanger plate columns of the primary side and the lower -14b- the heat exchanger plate columns of the secondary side. Solid lines represent the air flows, dashed lines represent the wetting liquids. On the primary side -14a-hot moist fresh air -15a- in the heat exchanger comes into contact with hygroscopic solution -17a, 17b-. In the process, water vapor condenses in the solution -17a- and the resulting heat is released to the secondary side -14b- of the heat exchanger. The on one
    Room air temperature cooled and dehumidified fresh air -15b-is directed into the room to be cooled. The hygroscopic solution -17b diluted by water condensation leaves the heat exchanger -14- and is then fed to the regeneration which is described in FIG. 1b. On the secondary side -14b-, cool dry exhaust air -16a- from the room to be cooled is brought into contact with cool water -18a-, with at the same time from the primary side -14a-forth heat from the condensation and heat from the cooling of the fresh air -15a -) are available for the evaporation of part of the water -18a-. This heat is thereby removed from the primary side -14a, which is why, in total, a cooling effect occurs in the fresh air. The remaining water -18b- is heated only slightly and runs back into a storage tank.
    FIG. 1b shows, as a further example of application of the multiphase plate heat exchanger -14-, the regeneration of the hygroscopic solution -17b- diluted by the cooling process in FIG. 1a and thus unusable. This corresponds to a particularly energetic form of desalination of water, for which there are also a large number of applications. On the primary side -14a, moist hot fresh air -15a is brought into contact with heated dilute hygroscopic solution -17c - whereby the heating is not shown - the temperature of which must be so high that its vapor pressure is above the vapor pressure of the fresh air -15a - lies. Then the fresh air takes -15a-additional water vapor up to its saturation.
    But as this air flows against the heated solution -17c, it becomes even warmer and can absorb additional water vapor, becoming a hot, almost vapor-saturated air. Through this process, the solution -17b- cools while at the same time its concentration increases, leaving it as a concentrated cool solution -17a-the heat exchanger -14- and can be used again for a cooling process. However, this cooling is limited because at the same time from the secondary side -14b- condensation heat is supplied because the hot, saturated with steam -15c-air is passed to the secondary side of the heat exchanger -14b, where it is deprived of heat from the primary side, whereby it cools and the resulting excess vapor condenses on the dividing wall between the primary side -14a and the secondary side -14b-and thus provides the heat of condensation for the dissolution of the water on the primary side -14a.
    Fig. 2a shows a schematic cross-section of the plates of a multiphase plate heat exchanger with liquid supply by the pumps -11, 12- and the throttling capillaries -5,7- in a case where the liquid path is determined mainly by gravity, a situation that is, where vertical plates recommend, as in each heat exchanger plate gap -la, lb- both adjacent surfaces can be wetted easily with liquids -3,4-, the leadership of primary -1- and secondary medium -2- and the the plates -13- wetting liquid layers -3,4 is drawn. In addition, one recognizes the capillaries -5,7- similar designed pipe system -6,8-but which should have a low flow resistance, since it is intended to return the liquids used to their starting point.
    Fig. 2a shows a schematic section across the plates of a horizontal multiphase plate heat exchanger with liquid supply through the pumps -11, 12- and connecting channels -9, 10-transverse through the heat exchanger plates -13- being at the openings through the gaps of the corresponding respectively Medium -1,2- each small openings -9a, 10a- throttle function a dropwise supply of the liquid layers -3, 4- allow.
    权利要求:
    Claims (10)
    [1]
    Claims:
    1. Multiphase plate heat exchanger (14) for 2 or more gaseous media (1,2), which are moved in countercurrent or parallel flow by a respective adjustable blower, with different temperature and with different steam content, characterized in that the active surface (13a ) for heat transfer between the affected media (1, 2) on one or both surfaces are wetted by one or two different slow flowing liquids (3, 4) which interact directly with the respective media (1, 2), so that evaporation or condensation and because of the resulting changes in concentration in the liquids also crystallization or dissolution of crystals can take place, these liquids (3,4) are pumped from the outside to their specific entry positions (9a, 10a) between the heat exchanger plates (13) and from there as wetting liquid film along the active surfaces (13a) through the plate move entwärmetauscher (14), wherein associated media (1,2) and liquids (3,4) usually do not flow parallel to each other.
    [2]
    2. Multi-phase plate heat exchanger according to claim 1, characterized in that the liquid supply from a storage tank to the small openings (9 a, 10 a), which serve as entry positions between the heat exchanger plates (13), takes place such that the supply line to the pump ( 11, 12) fills into a bundle of capillaries (5, 7) in tubular or tubular form which open at the corresponding small openings (9a, 10a) in the heat exchanger.
    [3]
    3. Multi-phase plate heat exchanger according to claim 1, characterized in that the liquid supply from a storage tank to the small openings (9a, 10a) which serve as liquid inlet between the heat exchanger plates (13), takes place such that the supply line to the pump (11, 12) leads to a common connecting channel (9,10) between the heat exchanger plates (13), which is formed by congruent corresponding openings through these plates (13), wherein in each plate gap (la, lb) to be introduced into the liquid, a throttle (9a, 10a) for the dropwise passage of liquid from the connecting channel (9,10) in the gap (la, 2a) is provided.
    [4]
    4. Multi-phase plate heat exchanger according to one of the above claims, characterized in that the inflows for media (1,2) or liquids (3,4) or individual sections of the heat exchanger (14) even with separate Temperierungsmedien or electrical heating in heat conductive Contact those who can heat or cool those areas.
    [5]
    5. Combination of two or more of the multi-phase plate heat exchangers with other plate heat exchangers according to any one of the preceding claims, characterized in that this combination consists of a single plate package and the individual partial heat exchangers each form congruent areas on the plates of this package.
    [6]
    6. Multi-phase heat exchanger or combination of heat exchangers according to one of the above claims, characterized in that said liquids (3,4) may contain water or other solvents as well as hygroscopic salts, refrigerants, disinfectants or wetting agents.
    [7]
    7. Heat exchanger or combination of heat exchangers according to one of the preceding claims, characterized in that the surfaces (3,4) of the active surfaces (13a) for heat transfer, the uniform distribution of the liquid film (3,4) or the local retention of crystals or their Further transport mechanically by grooves, sanding marks, scratches and / or fiber coating, as well as by hydrophilic materials and coatings or even by a combination of several such measures favor.
    [8]
    8. Multiphase plate heat exchanger according to one of the above claims, characterized in that the primary medium (1) is the hot and moist fresh air (15a) of the environment of a space to be cooled and the secondary medium (2) the spent dry and cool exhaust air (16a) this cooled space, which flows in countercurrent to the primary medium (1), and that the inner surfaces of the plate columns (la) for the primary medium are wetted with hygroscopic solution (17a), wherein liquid (3) and primary medium (l) in opposite directions flow while the inner surfaces of the plate columns (2a) for the secondary medium (2) with water (18a) are wetted, which can flow in any direction.
    [9]
    9. Multiphase plate heat exchanger according to one of the above claims, characterized in that the primary medium (1) is the hot and moist fresh air (15a) of the environment of a space to be cooled and that the inner surfaces of the plate columns (la) for the primary medium (1 ) with in accordance with claim 4 additionally preheated dilute hygroscopic solution (17c) in countercurrent to the primary medium (1) are wetted, and that the secondary medium (2) which in countercurrent to the primary medium (1) flows the same but heated fresh air (15c), the after the primary passage through the multiphase heat exchanger (14) is heated and nearly saturated with steam, and that forms on the inner surfaces of the plate columns (2a) for the secondary medium (2) as it cools condensed water, which in cocurrent with the secondary medium ( 2) is cooled leaving the multiphase heat exchanger (14).
    [10]
    10. The multi-phase plate heat exchanger according to one of the preceding claims, characterized in that the multi-phase plate heat exchanger is such that its plates are horizontal and there are grooves or waves transverse to the flow direction.
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