CN104024748A - Desiccant-Based Cooling System - Google Patents

Desiccant-Based Cooling System Download PDF

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Publication number
CN104024748A
CN104024748A CN201280041648.2A CN201280041648A CN104024748A CN 104024748 A CN104024748 A CN 104024748A CN 201280041648 A CN201280041648 A CN 201280041648A CN 104024748 A CN104024748 A CN 104024748A
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CN
China
Prior art keywords
air
flow
liquid drier
pond
drier
Prior art date
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Pending
Application number
CN201280041648.2A
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Chinese (zh)
Inventor
丹·福克斯
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Ducool Ltd
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Ducool Ltd
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Publication of CN104024748A publication Critical patent/CN104024748A/en
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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/14Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
    • F24F3/1411Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant
    • F24F3/1417Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification by absorbing or adsorbing water, e.g. using an hygroscopic desiccant with liquid hygroscopic desiccants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1425Regeneration of liquid absorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/26Drying gases or vapours
    • B01D53/263Drying gases or vapours by absorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2252/00Absorbents, i.e. solvents and liquid materials for gas absorption
    • B01D2252/10Inorganic absorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/45Gas separation or purification devices adapted for specific applications
    • B01D2259/4508Gas separation or purification devices adapted for specific applications for cleaning air in buildings
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F3/00Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems
    • F24F3/12Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling
    • F24F3/14Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification
    • F24F2003/1458Air-conditioning systems in which conditioned primary air is supplied from one or more central stations to distributing units in the rooms or spaces where it may receive secondary treatment; Apparatus specially designed for such systems characterised by the treatment of the air otherwise than by heating and cooling by humidification; by dehumidification using regenerators

Abstract

A desiccant-based system and method for conditioning air includes a first unit remotely located from an area whose environment is to be controlled. Additional units are respectively located within areas where air conditioning is desired. Each of the additional units is connected to the first unit such that desiccant can be transferred between each of the additional units and the first unit. Cool, undiluted desiccant can be transferred from the first unit to at least one of the additional units so that ambient air at the location of the additional unit can be dehumidified and cooled. Each of the additional units are separately controllable, such that the respective environments surrounding the additional units can be maintained at different levels of humidity and temperature.

Description

Cooling system based on drier
The cross reference of related application
The application has required the interests of the U.S. Provisional Patent Application that the application number of submission on August 26th, 2011 is 61/527,904, and it is comprised in here by reference.
Technical field
The present invention relates to a kind of system and method for the air conditioning based on drier.
Background technology
Air handling system can be utilized any of heating, cooling, dehumidifying and the several different methods of humidifying air.For example, steam compression system may have and expands and the advantage of compressed refrigerant, think different surrounding spaces provide refrigeration and/heat.The air handling system of another kind of type is used hygroscopic material, and as drier, air-flow is removed or moisturized, and cooling or circumference environment.The example of this system is described in following patent: US6487872, it was registered on December 3rd, 2002, and was comprised in here by reference.
The typical system based on drier is used central location, this central location is used drier to remove moisture from one air-flow, this has diluted drier, and this central location gives moisture another strand of air-flow from drier, thus drier concentrated or that regeneration is diluted.This central location then provides air through regulating to surrounding environment, and this surrounding environment can be, for example, and the one or more rooms in a solitary building.
One of this system based on drier is limited as, and it may not allow the independent of surrounding environment in the not chummery in a solitary building to control.The different piece of long distance positioning desiccant system-for example, by possessing outdoor regenerator and indoor processing section-may require a complicated system for the concentration of the drier between balance regeneration and processing activity.Thereby, there is the demand that the independent air handling system based on drier of controlling is provided for the one or more rooms in a solitary building, this system is not for the too complicated system of drier balance.
Summary of the invention
Embodiments of the present invention provide the system and method for the adjusting air of the system of a kind of use based on drier, and it allows the environment in independent one or more rooms of controlling in a solitary building.
Embodiments of the present invention comprise the system with the first subsystem, and this first subsystem is arranged at the outside that environment is treated controlled building.The second subsystem is positioned at interior of building, in the room that is supposed to control environment.The second subsystem is connected to the first subsystem, and drier is transmitted as requested between the first and second subsystems, so that the environment of the expectation in room to be provided.
Embodiments of the present invention also comprise the air adjustment system based on drier, and it has the first subsystem, or outdoor unit, and a plurality of the second subsystem, or indoor unit.Each indoor unit is connected to outdoor unit, makes drier can flow into independently as requested and flow out each indoor unit, to provide, the independent environment in each room is controlled.This kind of mode that can be implemented is for controlling the flow of the drier that enters indoor unit by use float-controlled valve.Temperature sensor also can be connected to valve, and so that further control to be provided, the flow that consequently enters the drier of indoor unit can be the function of quality and the temperature of drier.Like this, computer algorithm can be employed to control independently the flow that enters and flow out the drier of indoor unit, makes the space separately that is arranged at indoor unit, and varying environment condition can be held.
For object cooling and dehumidifying, indoor unit will receive cold, concentrated drier from outdoor unit, and this drier is then introduced into the air-flow from inner space and contacts.Air-flow can enter a part of indoor unit, and air-flow is given water drier and is cooled simultaneously herein.That be dried, cold air is then discharged in surrounding environment so that the environment of expectation to be provided.
The drier of dilution can be collected in the pond of indoor unit, and is transmitted and gets back to outdoor unit, for example, and by gravity or pumping system.The drier of dilution is regenerated in outdoor unit, and in outdoor unit, the drier of dilution can be exposed in the combination of the air-flow of removing moisture from drier heat and relatively dry.In some embodiments of the present invention, heat can provide by one or more heat exchangers of the part for steam compression system.This steam compression system also comprises at least one evaporimeter, and this can be supplied to the refrigeration source for drier of indoor unit.
Outdoor unit itself can be divided into a plurality of independent chambeies, first of these chambeies, and the first process chamber, receives the drier of dilution, and the drier of regeneration is transferred to indoor unit from indoor unit.The second chamber in outdoor unit is by adding air-flow and/or heat to carry out the regeneration of the drier of dilution to remove moisture from drier.These two chambeies can be connected, for example, by hole, or some other the mechanism that can effectively transmit drier between two chambeies.
Except above-mentioned, embodiments of the present invention also provide the mechanism of the room air of being processed by indoor unit for humidification and heating.This can be implemented, for example, by the drier in outdoor unit, add water, so that is transferred to the moisture that the drier of indoor unit contains relatively high percentage.Thereby when indoor air is processed by one in indoor unit, it obtains moisture and moistening air is expelled back into indoor environment from drier.In the cold climate in winter, when air is conventionally very dry, this mode is particularly useful.By this way, the drier in outdoor unit can be heated, so that except to room air provides moisture, also when processing air by indoor unit, and warm air.
At least some embodiments of the present invention comprise the system that regulates air.This system comprises first module, and it holds regenerator, and it can move to receive the first air-flow, and the first air-flow is contacted with liquid drier, thereby water is transferred to the first air-flow from liquid drier.Described regenerator comprises regenerator pond, and described regenerator pond, for collecting liquid drier at water after the first air-flow is transferred to liquid drier, is connected to the first of the treatment pond in regenerator pond the further containing fluid of described first module.Second unit, it is located away from first module, and is configured to receive the second air-flow and the second air-flow is contacted with liquid drier.Described second unit holds the second portion of collecting the treatment pond of liquid drier after the second air-flow for contacting at liquid drier.Described first module and second unit optionally fluid are communicated with, so that liquid drier can optionally be transmitted between the first and second parts for the treatment of pond, and before liquid drier turns back to second unit, the liquid drier that is transferred to the first for the treatment of pond from the second portion for the treatment of pond can mix with the liquid drier regenerator pond.
At least some embodiments of the present invention comprise the system that regulates air, and it comprises first module, and it is located away from the interior space; And second unit, it is positioned in the interior space, and with first module optionally fluid be communicated with.Described first module comprises regeneration chamber, and the first air-flow is introduced into described regeneration chamber, and contacts that with liquid drier water is transferred to the first air-flow from liquid drier.Described regeneration chamber comprises for collect the regenerator pond of liquid drier after the first air-flow is transferred to liquid drier at water.Described first module further comprises the first process chamber of separating with regeneration chamber, makes the first air-flow be prohibited from entering the first process chamber.Described the first process chamber comprises the first of the treatment pond that is fluidly connected to regenerator pond.Described second unit comprises the second process chamber, and the second air-flow is introduced into described the second process chamber, and contacts with liquid drier with before being discharged into the interior space at the second air-flow, between the second air-flow and liquid drier, transmits water.Described the second process chamber comprises the second portion of collecting the treatment pond of this liquid drier after the second air-flow for contacting at liquid drier.Optionally fluid between Unit first and second is communicated with the optionally transmission that liquid drier between the first and second parts for the treatment of pond is provided.
At least some embodiments of the present invention comprise the method that regulates air, during it is included in the first operational mode, the first air-flow are contacted, so that water is transferred to the first air-flow from liquid drier with the liquid drier in regeneration chamber.After water is transferred to the first air-flow from liquid drier, liquid drier is collected in regenerator pond.Liquid drier in the first of the liquid drier in regenerator pond and treatment pond is mixed, and the first of described treatment pond is arranged in first process chamber in regeneration chamber.Some liquid driers of first from treatment pond are transferred to the second portion for the treatment of pond, the second portion of described treatment pond is arranged in the second process chamber away from the first process chamber location.During the first operational mode, the second air-flow is contacted, so that water is transferred to liquid drier from the second air-flow with the liquid drier in the second process chamber.After the second air-flow has contacted the liquid in the second process chamber, the second air-flow is entered the surrounding environment with air to be conditioned from the second process chamber.
Accompanying drawing explanation
Fig. 1 is schematically illustrating of embodiments of the present invention, and this embodiment has outdoor unit and is arranged in three indoor units in the independent room of building;
Fig. 2 is shown in schematically illustrating of the outdoor unit according to the embodiment of the present invention that can move under the first operational mode;
Fig. 3 A and 3B show respectively front view and the side view of indoor unit according to the embodiment of the present invention; And
Fig. 4 is shown in schematically illustrating of the outdoor unit according to the embodiment of the present invention that can move under the second operational mode.
The specific embodiment
As require, the specific embodiment of the present invention is here described; Yet it should be understood to that disclosed embodiment is only example of the present invention, the present invention can implement with different and interchangeable mode.Accompanying drawing for ratio not necessarily, may be extended or dwindle to show the details of specific components by some features.Therefore, specific 26S Proteasome Structure and Function details disclosed herein should not be understood to restriction, and is appreciated that and is only used for instructing those skilled in the art differently to apply representational foundation of the present invention.
Fig. 1 has shown the air adjustment system 10 based on drier according to the embodiment of the present invention.This system 10 comprises first module, or outdoor unit 12; And three " second units " of locating away from outdoor unit 12, or indoor unit 14,16,18.Each indoor unit 14,16,18 is positioned at the room separately 20,22,24 of building 26.Although at least some in indoor unit 14,16,18 show as the distance relatively long with indoor unit 12 intervals being positioned, but embodiments of the present invention can have Unit first and second of location away from each other, but still in nearer toward each other distance.Conventionally, term " long distance positioning " refers to that Unit first and second are at least roughly arranged in and are operated in different surrounding environment-as, outdoor and indoor environment.
As shown in Figure 1, supply line 28 provides drier from outdoor unit 12 to each indoor unit 14,16,18; Similarly, the line of return 30 receives drier and is sent back to outdoor unit 12 from each indoor unit 14,16,18.Although three indoor units are illustrated in Fig. 1, other embodiments can comprise the indoor unit greater or less than three.As used herein, word " indoor " and " building " be often referred to limit at least a portion enclosure space and by it from the separated any structure of outdoor environment around.For example, " building " can be tent or other interim, local enclosed construction.
Fig. 2 shows schematically illustrating of the outdoor unit 12 shown in Fig. 1.This outdoor unit 12 holds the first process chamber 32, and in this first process chamber, drier 34 is transferred to indoor unit 14,16,18 and transfers out from indoor unit.Any desiccant material that can produce desired effects can be used, and comprises the liquid of following form: neat liquid, solution, the aqueous solution, mixture and their combination.Lithium chloride (LiCl) and calcium chloride (CaCl2) are typical liquid desiccant solutions, but other liquid driers also can be used.Outdoor unit 12 also holds regenerator 35, and it comprises regeneration chamber 36, and drier 34 can be regenerated in this regenerates chamber.In the embodiment shown in Fig. 2, drier 34 is by hole transmission between the first process chamber 32 and regeneration chamber 36, and this hole can be hole 38.In other embodiments, transmission can be controlled by floating and pump machanism or any other method or the system of effectively transmitting as required drier.More specifically, drier 34 is transmission between the first for the treatment of pond 42 and regenerator pond 43, regenerator pond 43 is separated portion 39 separates, and this separating part has the hole 38 being arranged at wherein, and hole 38 allows drier 34 to spread between 42He pond, pond 43 based on concentration gradient.As below more detailed description, each of indoor unit comprises the second portion for the treatment of pond, and the first of each for the treatment of pond second portion and treatment pond 42 optionally fluid is communicated with.
As shown in Figure 2, the first chamber 32 receives from indoor unit 14,16,18 drier 34, as shown in dotted line 40.In this embodiment, drier 34 is maintained at the first of the treatment pond 42 at the place, bottom that is arranged in the first process chamber 32 that is contained in outdoor unit 12.First processes pump 44 is used to through over-heat-exchanger 46, pump drier 34 from the first for the treatment of pond 42, and then drier 34 is pumped into indoor unit, as shown in dotted line 48.In the embodiment shown in Fig. 2, heat exchanger 46 is evaporimeters, and this evaporimeter is a part for the refrigeration system based on steam compression cycle, and this refrigeration system comprises compressor 50, the first condenser 52, the second condensers 54, and thermal expansion valve 55.In other embodiments, drier can be cooled and be heated by other source, as water cooling pond, solar source etc.By-passing valve 57 allows some cooling drier 34 to be reintroduced in the first process chamber 32, as shown in dotted line 59.Effectively make pond 42 keep cooling drier the adding of cooling drier 34 of getting back to the first for the treatment of pond 42, and as cooling liquid storage unit, when one or more indoor units 14,16,18 need when cooling, cooling liquid can be from wherein taking out.
Steam compression system shown in Fig. 2 can be used any fluid, and as cold-producing medium, this fluid can make this steam compression system transmit optionally heating and cooling drier 34 by the heat transmission to cold-producing medium with from the heat of cold-producing medium effectively.Fig. 2 shows the outdoor unit 12 under the first operational mode, and this first operational mode can be effectively used in warm, moist environment.Under this pattern, as shown in dotted line 56, heat is transferred to drier 34 from the first condenser 52.Drier 34 is reproduced pump 58 and pumps through condenser 52.After leaving condenser 52, drier 34 is sprayed on medium 60, and medium 60 can comprise one or more easy penetration materials, and it allows drier 34 to flow through them.The second condenser 54 can have associated fan (not shown), for being transferred to the surrounding environment of outdoor unit 12 outsides from some heats of steam compression system, thus further cooling refrigeration agent before the expansion stage of circulation.Although compressor 50 and condenser 52 are illustrated in regeneration chamber 36, in other embodiments, they can be positioned at the outside in regeneration chamber, and complete in another part of first module, or completely outside in first module.These assemblies are processed additional heat are provided for regeneration in regeneration chamber 36, thereby contribute to deviate from more water from drier 34.
As mentioned above, drier 34 receives the heat of automatic heat-exchanger 52, and this processing contributes to by displacing some moisture drier 34 of regenerating, and these moisture are to be drawn from the air their interior spaces 20,22,24 separately by indoor unit 14,16,18.Except displacing some moistures with heating from drier 34, outdoor unit 12 is also used air-flow further to remove moisture.As shown in Figure 2, the first air-flow 62 enters the second chamber 36 from outdoor environment around through entrance 64.Air-flow 62 is driven in by the fan 66 that drives air to enter the second chamber 36, passes through drier bearing medium 60, and discharges through outlet 68, and at outlet 68 place's air-flows 62, being illustrated as 62 is to represent carrying moisture when it leaves the second chamber 36.Because hole 38 is arranged under the horizontal level of drier in pond 42,43, so the first process chamber 32 is effectively sealed, and there is not any contact with air-flow 62.
Fig. 3 A and 3B show respectively front view and the side view of the indoor unit 14 shown in Fig. 1.As shown in Figure 3A, the drier 34 that valve 70 receives from outdoor unit 12, as shown in dotted line 72, and especially, it receives the drier 34 from the first for the treatment of pond 42.Valve 70 is connected to floating system 74, and this floating system 74 has shown at the horizontal level of drier 34 of second portion for the treatment of pond 76 that is arranged in the bottom of the second process chamber 77 that is contained in indoor unit 14.Thereby in the embodiment with describing shown here, the processing side of system 10 is the slits between outdoor unit 12 and indoor unit 14,16,18.A part that makes to process side has reduced significantly the complexity that the matter and energy about balance drier 34 between dilution process side drier and more concentrated regeneration side drier transmits in this unit of the reproducing unit of containment 10.In addition, the another part that makes to process side is contained in and in indoor unit, allows the independent adjusting of controlling the surrounding air in different spaces.
Except receiving the information about the horizontal level of drier 34, valve 70 also receives the information from temperature sensor 78, and this temperature sensor 78 is measured the temperature of the drier 34 in pond 76.Valve 70 can be the electronically actuated magnetic valve of for example threeway, and the specific input of its response, comprises the input from floating system 74 and temperature sensor 78.The control of valve 70 can be a part for large control system, this large control system also coordinate and control chart 2 shown in the operation of various assemblies of outdoor unit.This control system can comprise the one or more operation programs that allow each indoor unit 14,16,18 to be controlled independently of one another, thus provide they separately in room 20,22,24 the independent of environment control.
When as by floating system 74 shown in drier 34 horizontal level and/or while arriving valve 70 by the input of the temperature of the drier 34 shown in temperature sensor 78, show that this valve 70 should be unlocked, drier 34 from outdoor unit 12 is supplied to indoor unit 14, as shown in dotted line 80.In warm, moist environment, the drier 34 that enters indoor unit 14 from outdoor unit 12 will be cooled and be relatively dried-, by water, do not diluted.As below statement, this makes surrounding air in room 20 dehumidified and be cooled to the level of expectation.
Fig. 3 B shows the side view of indoor unit 14, and has shown how air-flow passes unit 14 and how by unit 14, to be processed.First, the second air-flow 86 enters indoor unit 14 from indoor environment around; Once in inside, when air-flow 86 crosses medium 84, it is introduced into drier 34 and contacts, as shown in arrow 88.Air stream is controlled by fan 90, and after air-flow 86 is cooled and dehumidifies, this fan 90 is discharged the second air-flow 86 to get back in surrounding environment, now by mark 86 ' expression.When the drier 34 at indoor unit 14 is collected moisture constantly, the horizontal level of the drier 34 in pond 76 will promote.In addition, the temperature of the drier in the second portion for the treatment of pond 76 34 will raise.
At certain a bit, some drier 34 will be pumped back to outdoor unit, as shown in the dotted line 94 shown in Fig. 3 A.Drier 34 in indoor unit 14 can be supplied with and be flow to outdoor unit by gravity, or can be pumped.Thereby the equipment 96 schematically illustrating in Fig. 3 A can be valve for example, when drier 34 reaches certain level position, this valve allows drier 34 automatically to flow out indoor unit 14.Selectively, equipment 96 can be electronically actuated valve, and valve 70 as described above.In this case, when specific input signal (temperature of drier 34 and/or horizontal level in as pond 76) occurs, this valve 96 can be unlocked.When turning back to outdoor unit 12, drier 34 is regenerated according to said process.
Because indoor unit 14,16,18 is independently controlled, and as the space may with different requirements, therefore, in some unit, floating system 74 can be activated continually, and in other unit, it is but activated rarely simultaneously.In at least some cases, before floating system 74 activated, air-flow 86,86 ' may be through specific indoor unit recirculation many times.This to be the processing side that makes the air handling system based on drier separate between outdoor unit and independent indoor unit other advantage-, concentration that needn't be based on drier in indoor unit pond from the transmission of the drier of indoor unit (although its can); On the contrary, it can be based on temperature or the volume of the liquid based in tank interior strictly.By this way, the more complicated control of the concentration of balance drier is fully processed in being independent of the outdoor unit of indoor unit.
Above-mentioned air conditioning moves with the surrounding air in cooling and dehumidifying room under the first operational mode.Yet system 10 can also regulate air to make it have reverse effect-, system 10 can be moved with the surrounding air in heating and humidification space under the second operational mode.This kind of mode that can be implemented is to provide the additional water that directly arrives outdoor unit 12.This is represented by dotted line 98 in Fig. 4, dotted line 98 shows directly the adding of water of the first for the treatment of pond, the first of this treatment pond in Fig. 4 by 42 ' indicate, apostrophe (') represents the assembly similar to other accompanying drawings of assembly that are illustrated in the system 10 under the first operational mode.Regenerator 35 ' be closed, and particularly pump 58 ' and fan 66 ' not operation, therefore, to the increase that adds the dilution that has directly caused pond 42 ' middle drier 34 of the water in outdoor unit 12, and regenerator pond 43 ' in, water can not evaporate from drier.
Except add water in drier 34, can also increase heat to drier 34, so that drier warm, dilution can be supplied to indoor unit 14,16,18.Heat can increase by any effective method, to realize the result of expectation, as inverted running steam compression system.As shown in Figure 4, compressor 50 ' existing by refrigerated medium pump to the first condenser 52 ', this first condenser 52 ' be used to by the first processing pump 44 ' from treatment pond 42 ' First wheel cylinder to drier 34 heat-shifts indoor unit 14,16,18.Under this second operational mode, it can be considered to " pattern in winter " in some cases, cold-producing medium by alternatively through second condenser 54 ' pumping, although and not shown in Figure 4, drier 34 can be crossed condenser 52 ' and 54 ' to obtain extra heat by pump.
Selectable, system 10 can be provided with solar collector, and it can, by physically attached or operation at a distance, think that system 10 provides heat and/or electricity.When this processes while being carried out, drier 34 warm, dilution cross medium 84 be situated between referring to Fig. 3 A figure this medium place moisture and heat by the second air-flow 86 collect-referring to Fig. 3 B figure before surrounding environment is got back in this second air-flow discharge.
Although illustrative embodiments is described in the above, this can not be regarded as these embodiments and describe all possibility forms of the present invention.On the contrary, the word using in description is descriptive word rather than restrictive word, and is appreciated that and can makes various changes and not depart from spirit and scope of the invention.In addition, the feature of the different embodiments of implementing can be combined to form other embodiment of the present invention.

Claims (20)

1. a system that regulates air, comprising:
First module, it holds regenerator, it can move to receive the first air-flow, and the first air-flow is contacted with liquid drier, thereby water is transferred to the first air-flow from liquid drier, described regenerator comprises regenerator pond, and for collecting liquid drier at water after the first air-flow is transferred to liquid drier, described first module is also connected to the first of the treatment pond in regenerator pond containing fluid; And
Second unit, it is located away from first module, and be configured to receive the second air-flow and the second air-flow is contacted with liquid drier, described second unit holds the second portion of collecting the treatment pond of liquid drier after the second air-flow for contacting at liquid drier, described first module and second unit optionally fluid are communicated with, so that liquid drier can optionally be transmitted between the first and second parts for the treatment of pond, and before liquid drier turns back to second unit, the liquid drier that is transferred to the first for the treatment of pond from the second portion for the treatment of pond can mix with the liquid drier regenerator pond.
2. system according to claim 1, wherein, the first of described regenerator pond and described treatment pond be separated part every, described separating part has the hole being arranged at wherein, is convenient to liquid drier and spreads between them.
3. system according to claim 1, wherein, described first module is positioned at building outside and is configured to receive from the first air-flow of outdoor environment around and the first air-flow is discharged to outdoor environment around, and described second unit is positioned at interior of building and is configured to reception from the second air-flow of the surrounding environment of interior of building and the surrounding environment that the second air-flow is discharged to interior of building.
4. system according to claim 1, wherein, when the second air-flow is introduced into when liquid drier in second unit contacts, described first module and second unit can move under the first operational mode, so that water is transferred to liquid drier from the second air-flow, and under the second operational mode, can move, so that water is transferred to the second air-flow from liquid drier.
5. system according to claim 4, wherein, described regenerator is configured to close during the second operational mode, to stop the evaporation of water from the liquid drier in regenerator pond.
6. system according to claim 4, wherein, described first module is also held at least a portion of refrigeration system, and described refrigeration system is configured to by conducting optionally heating and cooling liquid drier with the heat of cold-producing medium.
7. system according to claim 6, wherein, described first module is at least held the evaporimeter of refrigeration system, and comprise the first processing pump, described first processes pump is configured to the first's process evaporimeter pumping from treatment pond by liquid drier during the first operational mode, with before being transferred to second unit at liquid drier and being introduced into and contacting with the second air-flow, heat is transmitted to cold-producing medium from liquid drier.
8. system according to claim 7, further comprises by-passing valve, and described by-passing valve was configured to before liquid drier is transferred to second unit, a part of leaving the liquid drier of evaporimeter is turned back to the first for the treatment of pond.
9. system according to claim 6, wherein, described first module comprises regenerative pump, described regenerative pump is configured to during the first operational mode liquid drier condenser pumping through refrigeration system from regenerator pond, with before being introduced into and contacting with the first air-flow, from cold-producing medium, receive heat.
10. system according to claim 9, wherein, described refrigeration system further comprises the second condenser, described the second condenser is configured to further cooling refrigeration agent before the expansion stage of cold-producing medium.
11. 1 kinds of systems that regulate air, comprising:
First module, it is located away from the interior space; And
Second unit, it is positioned in the interior space, and with first module optionally fluid be communicated with,
Described first module comprises regeneration chamber, the first air-flow is introduced into described regeneration chamber, and contacts that with liquid drier water is transferred to the first air-flow from liquid drier, and described regeneration chamber comprises regenerator pond, for collecting liquid drier at water after the first air-flow is transferred to liquid drier
Described first module further comprises first process chamber separated with regeneration chamber, makes the first air-flow be prohibited from entering the first process chamber, and described the first process chamber comprises the first of the treatment pond that is fluidly connected to regenerator pond,
Described second unit comprises the second process chamber, the second air-flow is introduced into described the second process chamber, and contact with liquid drier with before being discharged into the interior space at the second air-flow, between the second air-flow and liquid drier, transmit water, described the second process chamber comprises the second portion of collecting the treatment pond of this liquid drier after the second air-flow for contacting at liquid drier, and the optionally fluid between first module and second unit is communicated with the optionally transmission that liquid drier between the first and second parts for the treatment of pond is provided.
12. systems according to claim 11, further comprise a plurality of second units, and each second unit is arranged in the interior space separately, and each second unit and first module optionally fluid be communicated with.
13. systems according to claim 11, wherein, described regeneration chamber and the first process chamber be separated part every, described separating part has the hole being arranged between regenerator pond and the first for the treatment of pond, is convenient to liquid drier and spreads between them.
14. systems according to claim 11, wherein, when the second air-flow is introduced into when liquid drier in second unit contacts, described first module and second unit can move under the first operational mode, so that water is transferred to liquid drier from the second air-flow, and under the second operational mode, can move, so that water is transferred to the second air-flow from liquid drier.
15. systems according to claim 14, wherein, described first module is further held at least a portion of refrigeration system, and described refrigeration system is configured to by conducting optionally heating and cooling liquid drier with the heat of cold-producing medium.
16. systems according to claim 15, wherein, described first module is at least held the evaporimeter of refrigeration system, described the first process chamber comprises the first processing pump, described first processes pump is configured to the first's process evaporimeter pumping from treatment pond by liquid drier during the first operational mode, with before being transferred to second unit at liquid drier and being introduced into and contacting with the second air-flow, heat is transmitted to cold-producing medium from liquid drier.
17. systems according to claim 16, further comprise by-passing valve, described by-passing valve was configured to before liquid drier is transferred to second unit, a part of leaving the liquid drier of evaporimeter is turned back to the first for the treatment of pond, thereby allow the first for the treatment of pond to keep cooling drier.
18. systems according to claim 17, wherein, described regeneration chamber comprises regenerative pump, described regenerative pump is configured to during the first operational mode liquid drier condenser pumping through refrigeration system from regenerator pond, with before being introduced into and contacting with the first air-flow, from cold-producing medium, receive heat.
19. 1 kinds of methods that regulate air, comprising:
During the first operational mode, the first air-flow is contacted, so that water is transferred to the first air-flow from liquid drier with the liquid drier in regeneration chamber;
After water is transferred to the first air-flow from liquid drier, liquid drier is collected in regenerator pond;
Liquid drier in regenerator pond is mixed with the liquid drier being arranged in abutting connection with in the first for the treatment of pond in first process chamber in regeneration chamber;
Some liquid driers of first from treatment pond are transferred to the second portion being arranged at away from the treatment pond in the second process chamber of the first process chamber location;
During the first operational mode, the second air-flow is contacted, so that water is transferred to liquid drier from the second air-flow with the liquid drier in the second process chamber; And
After the second air-flow has contacted the liquid in the second process chamber, the second air-flow is entered the surrounding environment with air to be conditioned from the second process chamber.
20. methods according to claim 19, during being further included in the second operational mode, stop the liquid drier in the first air-flow contact regeneration chamber; And during the second operational mode, the second air-flow is contacted, so that water is transferred to the second air-flow from liquid drier with the liquid drier in the second process chamber.
CN201280041648.2A 2011-08-26 2012-08-27 Desiccant-Based Cooling System Pending CN104024748A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110785615A (en) * 2017-04-18 2020-02-11 北狄空气应对加拿大公司 Desiccant enhanced evaporative cooling system and method

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103398432B (en) * 2013-07-22 2016-03-30 南京韩威南冷制冷集团有限公司 A kind of solution-type air-conditioner set utilizing compressor air-discharging sensible heat to regenerate
MX2016013587A (en) 2014-04-15 2017-06-07 Mongar Andrew An air conditioning method using a staged process using a liquid desiccant.
US11944934B2 (en) 2021-12-22 2024-04-02 Mojave Energy Systems, Inc. Electrochemically regenerated liquid desiccant dehumidification system using a secondary heat pump

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4635446A (en) * 1981-05-15 1987-01-13 Camp Dresser & Mckee Dehumidification apparatus
CN1149914A (en) * 1994-05-30 1997-05-14 Ff西里·诺明西斯有限公司 Vacuum dewatering of desiccant brines
US20040231512A1 (en) * 2003-02-28 2004-11-25 Slayzak Steven J. Using liquid desiccant as a regenerable filter for capturing and deactivating contaminants
US20090095162A1 (en) * 2007-10-15 2009-04-16 Green Comfort Systems, Inc. Dehumidifier system
EP2306100A1 (en) * 2008-05-27 2011-04-06 Dyna-Air Co., Ltd. Humidity control device

Family Cites Families (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2894376A (en) * 1955-10-20 1959-07-14 Surface Combustion Corp Air conditioning apparatus and method
JPS5163548A (en) * 1974-11-30 1976-06-02 Chugai Ro Kogyo Kaisha Ltd NETSUPUSAISEISHIKIEKITAIJOSHITSUSOCHI
JPS6053822B2 (en) * 1977-09-14 1985-11-27 三菱電機株式会社 air conditioner
AU697594B2 (en) * 1994-05-30 1998-10-08 William Allen Trusts Pty Ltd Vacuum dewatering of desiccant brines
EP1029201A1 (en) 1997-11-16 2000-08-23 Drykor Ltd. Dehumidifier system
JP2001523560A (en) * 1997-11-16 2001-11-27 ドライコー リミテッド Dehumidification system
JP4384699B2 (en) * 2008-05-22 2009-12-16 ダイナエアー株式会社 Humidity control device
JP5349077B2 (en) * 2009-02-26 2013-11-20 ダイナエアー株式会社 Humidity control device

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4635446A (en) * 1981-05-15 1987-01-13 Camp Dresser & Mckee Dehumidification apparatus
CN1149914A (en) * 1994-05-30 1997-05-14 Ff西里·诺明西斯有限公司 Vacuum dewatering of desiccant brines
US20040231512A1 (en) * 2003-02-28 2004-11-25 Slayzak Steven J. Using liquid desiccant as a regenerable filter for capturing and deactivating contaminants
US20090095162A1 (en) * 2007-10-15 2009-04-16 Green Comfort Systems, Inc. Dehumidifier system
EP2306100A1 (en) * 2008-05-27 2011-04-06 Dyna-Air Co., Ltd. Humidity control device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110785615A (en) * 2017-04-18 2020-02-11 北狄空气应对加拿大公司 Desiccant enhanced evaporative cooling system and method
US11892193B2 (en) 2017-04-18 2024-02-06 Nortek Air Solutions Canada, Inc. Desiccant enhanced evaporative cooling systems and methods

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BR112014004412B1 (en) 2021-09-08
KR20140081803A (en) 2014-07-01
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CO7030938A2 (en) 2014-08-21
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BR112014004412A2 (en) 2017-04-04
IL231112A0 (en) 2014-04-30

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