GB2381061A - Dehumidifiers - Google Patents

Dehumidifiers Download PDF

Info

Publication number
GB2381061A
GB2381061A GB0125052A GB0125052A GB2381061A GB 2381061 A GB2381061 A GB 2381061A GB 0125052 A GB0125052 A GB 0125052A GB 0125052 A GB0125052 A GB 0125052A GB 2381061 A GB2381061 A GB 2381061A
Authority
GB
United Kingdom
Prior art keywords
coil
scraper
air
ice
scrapers
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
GB0125052A
Other versions
GB0125052D0 (en
Inventor
John Edward Gough
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to GB0125052A priority Critical patent/GB2381061A/en
Publication of GB0125052D0 publication Critical patent/GB0125052D0/en
Publication of GB2381061A publication Critical patent/GB2381061A/en
Withdrawn legal-status Critical Current

Links

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
    • F24F3/1405Air-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 in which the humidity of the air is exclusively affected by contact with the evaporator of a closed-circuit cooling system or heat pump circuit
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D21/00Defrosting; Preventing frosting; Removing condensed or defrost water
    • F25D21/06Removing frost
    • F25D21/065Removing frost by mechanical means
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D1/00Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
    • F28D1/02Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
    • F28D1/03Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits
    • F28D1/0308Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other
    • F28D1/0325Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other the plates having lateral openings therein for circulation of the heat-exchange medium from one conduit to another
    • F28D1/0333Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with plate-like or laminated conduits the conduits being formed by paired plates touching each other the plates having lateral openings therein for circulation of the heat-exchange medium from one conduit to another the plates having integrated connecting members
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • F28D7/12Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically the surrounding tube being closed at one end, e.g. return type
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • F28F19/008Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using scrapers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24FAIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
    • F24F11/00Control or safety arrangements
    • F24F11/30Control or safety arrangements for purposes related to the operation of the system, e.g. for safety or monitoring
    • F24F11/41Defrosting; Preventing freezing

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Drying Of Gases (AREA)

Abstract

A dehumidifier may be in the form of a plurality of hollow flat plates or a number of tubes (8,9) located in an air stream requiring moisture removal without the risk of freezing and preventing air flow. Frost formed on the flat plates is removed by a plurality of parallel scrapers (5) which are mechanically driven by a motor (6) vertically upwards and downwards between and in contact with the respective plates. Frost formed on the tubes (8,9) is removed by a similarly vertically movable plate (10) having scraper rings (11, Fig.6) surrounding the respective tubes (8,9). A second scraper (12) travels horizontally across the bottom of the dehumidifier within a drip tray (16) collecting frost from the scrapers (5) or plate (10). The scrapers (5) or plate (10) remain static at the bottom of their stroke until passed by the scraper (12). The scraper (12) is an inverted bucket scoop which at the end of its stroke comes into contact with a worm screw (14) which removes ice deposits from the scoop. The worm screw (14) pushes the ice into an insulated collection device (18, Fig.9). The collection device includes a level switch which is able to stop frost collection when liquid in the device reaches a predetermined level.

Description

<Desc/Clms Page number 1>
THIS INVENTION RELATES TO LOW AIR TEMPERATURE DEHUMIDIFICATION. Dehumidifiers are available in two forms, the first utilising a desiccant and the second utilising the refrigerant vapour compression cycle.
With the first the desiccant is better suited to low temperatures but needs to be reactivated to remain operational i. e. dried and so a wet air stream is created in achieving this. This wet air requires discharging via a pipe or duct to a point outside of the controlled space. This is not practical in many situations and limits the potential of the dehumidifier in it not being portable. In addition air is required to replenish that exhausted by the reactivation process and such air could be higher in moisture content than that being dehumidified therefore increasing the work load.
With the second the evaporator comprising of tubes with fins mechanically bonded to them is not suitable in low air temperatures. This is because the fluid within the tubes needs to be at a temperature below the dew point of the air to condense the moisture within the air. When the moisture condenses it immediately freezes onto the coil surface unlike at higher air temperatures where it naturally drips out of the coil into a collection tray.
If the cycle is allowed to continue in low air temperature conditions the ice formed builds up until there is no airflow across the coil. When airflow ceases the process is non-operational, i. e. No further dehumidification takes place. In these situations liquid refrigerant can return to the compressor, which will result in equipment failure. Should a defrost cycle be incorporated the dehumidifier is not operational during this cycle and some moisture previously removed is allowed to evaporate back into the controlled space. The process should be continuous to maximise plant thermal efficiency in low air temperature conditions where the refrigeration performance is at its minimum.
With the present invention a dehumidification cooling coil provides operation without the need for defrost cycles even at low air temperature achieved by mechanically removing the ice formed on the coil surface in contact with the air being processed and a means for subsequent collection to minimise moisture migration back into the controlled space.
With this invention there are two forms of dehumidification coil, the first having hollow plates and the second having fin less tubes. Both forms utilise a refrigeration plant with refrigerant directly passing through them or with a secondary coolant such as brine, thermofluid or glycol solution passing through them.
Continuous operation is achieved by mechanically removing the ice formed on the dehumidification coil surface in contact with the air being processed. By regular removal of the ice the air path is kept clear and the need for defrost cycles eliminated.
For simplicity the dehumidification coil is referred to as an evaporator due to the fact that if refrigerant passes through it as a component of the refrigerant vapour compression cycle then it would be called an evaporator even though its function condenses moisture from the air it is processing.
<Desc/Clms Page number 2>
Making reference to the following accompanying drawings the first form of this invention i. e. hollow plates is now described where: Figure 1 shows the vertical hollow panels, which form the evaporator.
Figure 2 shows an isometric view of the scraper assembly with one of the parallel motion guides not shown for clarity.
Figure 3 shows an isometric exploded view of part of the scraper and frame.
Figure 4 shows a section through the evaporator assembly and demonstrates the location of the scraper.
Referring to the drawings, for demonstration purposes twelve hollow panels (1) are shown.
These are positioned and bonded side by side to provide a common hollow vessel in which the liquid refrigerant enters each panel at the distributor connection (2) where it evaporates and exits at the common suction outlet (3). Depending upon the design duty required the size and quantity of panels (1) would vary to provide the required surface area. These panels would be brazed or metalurgically bonded in sequence to from the single evaporator. The clearance gap between the panels (1) allows the process air to pass in a single direction. It is within this gap where ice is formed and collects during dehumidification and where the scrapers (5) shown in figure 2 are accommodated. The scrapers (5) extend the depth of the evaporator panels (1) as shown in figure 4. To improve efficiency the panels (1) could be corrugated when viewed from above with the scraper (5) having the same profile, offset to interlock. This would increase the contact factor and minimise the volume of air not being processed.
For the demonstration with twelve panels (1) forming the evaporator assembly there are eleven scrapers (5), one located in each air gap. The quantity of scrapers (5) is dependent upon the number of panels (1). Each scraper (5) is connected to the adjoining scraper (5) if manufactured as individual items or may be manufactured as a single comb component. The cross section of each scraper (5) blade has a profile to encourage easy vertical upward motion within the air gap whilst in the downward motion the panels are cleared of ice deposits formed during the dehumidification process. The parallel scrapers (5) have a timed, temperature controlled, pressure controlled or continuous vertical motion upwards and downwards by means of a drive motor through worm screw (6), rack and pinion or similar device maintaining parallel motion of the scrapers (5) between the evaporator panels (1). A frame (7) sized to suit the face area of the evaporator, house the drive device and its components is used to locate and secure the scraper (5) assembly to the evaporator panels (1) assembly.
During operation the ice formed on the evaporator panels (1) is removed from the air gap by scrapers (5) during their downward motion, the ice is pushed out of the bottom gap where it is collected and removed. This part of the process is described for both forms of the device later within this document.
In figure I and figure 4, insulation (4) is shown on the external perimeter surfaces of the evaporator panels (1) and the suction header of the evaporator panels assembly where air is not passed across and the scrapers (5) do not operate. This is to enhance performance of the
<Desc/Clms Page number 3>
evaporator assembly, eliminate ice formation to these surfaces and minimise risk of frost damage to other surrounding components.
And now by making reference to the following accompanying drawings the second form of this invention is now described where Figure 5 shows a section of the tube in tube evaporator and typical coolant circuiting diagram and Figure 6 shows a section of the ice removal plate (10) with scraper rings (11) together with the tube in tube evaporator and plug (22).
Referring to the drawings tubes (8), capped at the bottom by means of a plug (22) formed with a parallel shoulder to recess into tube (8) having a flat bottom and concave top to encourage fluid flow upwards. The overall diameter of plug (22) would equal that of tube (8) and be metalurgically bonded and finished to ensure the plug (22) and tube (8) are parallel on their external surface. These are positioned in a manner similar to a conventional fluid to air evaporator coil to maximise air contact however do not have fins, are vertical in orientation and have a tube (9) positioned within thus eliminating the need for return bends, common to a conventional coil. The outer surfaces of the tubes (8) are in contact with the process air and it is upon these surfaces that the moisture contained within the process air condenses and either drips off or condenses onto and freezes.
The first point of entry of the coolant is at the air off coil position of the evaporator assembly.
The coolant is delivered into the inner tube (9) where it moves downward, exits the open end of the inner tube (9) and enters the evaporator tube (8) travelling upwards. The coolant, no longer at its coldest condition, having been passed through the last row of evaporator tubes (8) is then delivered by pipes to the inner tube (9) of the second row nearest air off coil position of the evaporator where it extends downward to exit the open end of tube (9) and rise through the associated tube (8). Again at the top of evaporator tube (8) the coolant, slightly warmer than the previous, continues through the evaporator assembly in the same manner until it reaches the last row. At this point, the entry point of the process air, the coolant passes down through inner tube (9) and after absorbing heat from the process air exits by a pipe work header at the top connecting the several rows forming the evaporator where it is returned to the cooling plant.
The scraper plate (10) is formed from a stable plastic material either machined from sheet material or moulded prior machine finish. The horizontal plate (10) connects to a drive device (6) such as that of the first form evaporator to provide vertical upward and downward motion. The Plate (10) has a series of holes to suit the centres of the evaporator tubes (8), these holes having clearance and a rebate on the underside. A bonded type seal comprising Annulus and V-type ring forms the scraper ring (11) which is secured into the rebates of the scraper plate (10). The V-type ring permits unrestricted upward motion however grips the evaporator tube (8) on the downward motion of the scraper plate (10) thus forcing the ice formed to the bottom of the evaporator block where it is disposed of prior the return of the same scraper plate (10) to its uppermost position.
To complete the evaporator assembly, of both forms of this invention, by making reference to the following drawings the ice disposal is now described where: Figure 7 shows views of the drip tray, horizontal ice scraper and worm screw.
Figure 8 shows a section of the drip tray, horizontal ice scraper, worm screw and evaporator assembly, of the second form, with scraper plate, tubes and scraper rings.
<Desc/Clms Page number 4>
For both forms the ice cleared from the evaporator surface is pushed to the bottom by the prongs (5) or the plate (10) and drive device (6). When the prongs (5) or the plate (10) reach the bottom of their stroke a second scraper (12) moves horizontally across the width of the prongs (5) or plates (10) by means of a parallel motion device (15) similar to drive device (6).
This scraper (12) is in contact with the bottom of the prongs (5) or plate (10) both of which remain static at the bottom of their stroke until the width has been passed by the scraper (12). This scraper (12) formed of a similar material to that of the prongs (5) or plate (10) is formed like an inverted bucket scoop as shown in figure (10) and when at the end of its stroke comes into contact with the worm screw (14) at which point the prongs (5) or plate (10) return to their top position. The bottom scraper (12) remains static for a period of time while the worm screw (14) removes the ice deposits from the scraper (12) following which the drive device (15) returns the scraper (12) back to its housing within the drip tray (16). The drip tray (16) moulded or formed from several mouldings, has insulation to assist performance and efficiency.
Figure 9 shows a section through the worm screw (14), drip tray (16), delivery tube (17), collection device (18), delivery tube airtight collar (19), air release valve (20), level switch (21) and location of heat source together with the second form of evaporator.
Making reference to figure 9 the worm screw (14) pushes the ice into a suitably sealed and insulated collection device (18) beneath the complete assembly via a tube (17) with air tight collar (19) preventing moisture migration back into the controlled space from the collection device. If the evaporator assembly is used within, for example a conventional packaged dehumidifier of the refrigeration compression cycle type, the evaporator collection device (18) could utilise some of the heat of rejection to melt the ice deposited into the collection device (18) allowing it to level off rather than collecting into a frozen heap. The level switch (21) is incorporated to stop the process when the collection device (18) reaches a predetermined liquid level. As the condensate fills the collection device (18) the air being displaced is allowed into the controlled space via the air release valve (20). The collection device (18) would comprise of a fixed top section and removable bottom section to allow manual removal when full. The bottom section of the collection device (18) would incorporate a gasket joint and means of securing to the fixed top section, this joint being located above the maximum condensate level. The drain could be piped to a suitable drainage point out of the conditioned space if this is desirable and practical.
The completed assembly, evaporator, scraper plate, drip tray etc. is tilted slightly backward at the top in the direction of air flow and side wards at the top towards the worm screw assembly (14) to encourage the ice or water to move down towards and into the worm screw assembly (14) and hence into the collection device (18). When incorporated within a conventional dehumidifier the casework design of the finished product would accommodate and conceal this design feature. Air being processed requires fan assistance in the normal manner, which connects to inlet and outlet spigots (23) secured to the evaporator case, these spigots being suitably sized for the air volume and coil face area.

Claims (7)

  1. CLAIMS 1. A dehumidification cooling coil providing operation without the need for defrost cycles even at low air temperature achieved by mechanically removing the ice formed on the coil surface in contact with the air being processed and subsequent collection to minimise moisture migration back into the controlled space.
  2. 2. A dehumidification cooling coil as in claim 1 where in the coil takes 2 forms, the first having hollow plates forming a single vessel vertically side by side with an air gap between each plate and the second having vertical tubes capped at the bottom and containing an internal tube providing coolant inlet. The vertical tubes supported and connected to one another by pipe work in an arrangement to maximise air contact.
  3. 3. A dehumidification cooling coil as in claim 1 or claim 2 where in ice removal from the coil surface in contact with the air being processed is provided by 2 forms of scraper positioned within the air gap and achieving contact with the coil surface. To satisfy coil form 1 the scraper takes the form of a comb having prongs extending into the air gap between the hollow plates and to satisfy coil form 2 the scraper takes the form of a horizontal plate with a series of holes to accommodate the vertical tubes. The scrapers are driven downwards to collect the ice deposited upon the coil and then return to their starting position at the top of the coil out of the air stream.
  4. 4. A dehumidification cooling coil as in claim lor claim 2 or claim 3 provided with a horizontal scraper located within a drip tray beneath the coil, mechanically engaged to remove the ice previously collected from the coil surface by the vertically moving scraper at its bottom stroke.
  5. 5. A dehumidification cooling coil as in claim 1 or claim 2 or claim 3 or claim 4 provided with a drip tray to accommodate a horizontal scraper beneath the coil and a rotating worm screw which is contacted by the horizontal scraper at the end of its stroke. The continuous rotation and direction of screw moves the ice deposit off the horizontal scraper and into a delivery tube leading into a collection device.
  6. 6. A dehumidification cooling coil as in claim 1 or claim 2 or claim 3 or claim 4 or claim 5 provided with an insulated casing complete with spigots providing effective coil face area, means of directing the air being processed and incorporate the guides and drive devices for the scrapers and worm screw.
  7. 7. A dehumidification cooling coil as in any preceding claim provided with a semi- detatchable collection device equipped with gasketed joint, level switch, air release valve and heat source to melt the ice collected.
GB0125052A 2001-10-18 2001-10-18 Dehumidifiers Withdrawn GB2381061A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB0125052A GB2381061A (en) 2001-10-18 2001-10-18 Dehumidifiers

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB0125052A GB2381061A (en) 2001-10-18 2001-10-18 Dehumidifiers

Publications (2)

Publication Number Publication Date
GB0125052D0 GB0125052D0 (en) 2001-12-12
GB2381061A true GB2381061A (en) 2003-04-23

Family

ID=9924101

Family Applications (1)

Application Number Title Priority Date Filing Date
GB0125052A Withdrawn GB2381061A (en) 2001-10-18 2001-10-18 Dehumidifiers

Country Status (1)

Country Link
GB (1) GB2381061A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019200448A1 (en) * 2018-04-20 2019-10-24 Okanagan Winery & Ciders Condensing dehumidifier for an arena or the like
WO2021096343A1 (en) * 2019-11-12 2021-05-20 HERNÁNDEZ MAYÉN, Alfonso Device for harvesting atmospheric water vapour

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2785541A (en) * 1953-11-25 1957-03-19 Borg Warner Refrigerating apparatus and manually operable mechanical defrosting means therefor
GB1463210A (en) * 1975-01-11 1977-02-02 Richardson D W Ice-free evaporator
US4126015A (en) * 1976-08-20 1978-11-21 Hitachi, Ltd. Air cooling apparatus
US4332143A (en) * 1979-02-01 1982-06-01 Messer Griesheim Gmbh Device for cooling a gas to below its dew point
FR2496247A1 (en) * 1980-12-12 1982-06-18 Perot Georges Continuous defroster for heat pump evaporator - has threaded nut on driven screw with chain or gear drive
GB2171191A (en) * 1985-02-19 1986-08-20 Starfrost Systems Ltd Evaporator mechanical defrost system
GB2195710A (en) * 1986-09-24 1988-04-13 Sec Dep For Trade & Industry T Integrated heat exchanger and pump
GB2232469A (en) * 1989-05-26 1990-12-12 Unilever Plc Ice-making apparatus and method
US5273106A (en) * 1992-07-21 1993-12-28 Mechanical Technology Inc. Self-defrosting recuperative air-to-air heat exchanger

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2785541A (en) * 1953-11-25 1957-03-19 Borg Warner Refrigerating apparatus and manually operable mechanical defrosting means therefor
GB1463210A (en) * 1975-01-11 1977-02-02 Richardson D W Ice-free evaporator
US4126015A (en) * 1976-08-20 1978-11-21 Hitachi, Ltd. Air cooling apparatus
US4332143A (en) * 1979-02-01 1982-06-01 Messer Griesheim Gmbh Device for cooling a gas to below its dew point
FR2496247A1 (en) * 1980-12-12 1982-06-18 Perot Georges Continuous defroster for heat pump evaporator - has threaded nut on driven screw with chain or gear drive
GB2171191A (en) * 1985-02-19 1986-08-20 Starfrost Systems Ltd Evaporator mechanical defrost system
GB2195710A (en) * 1986-09-24 1988-04-13 Sec Dep For Trade & Industry T Integrated heat exchanger and pump
GB2232469A (en) * 1989-05-26 1990-12-12 Unilever Plc Ice-making apparatus and method
US5273106A (en) * 1992-07-21 1993-12-28 Mechanical Technology Inc. Self-defrosting recuperative air-to-air heat exchanger

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
WPI Abstract for SU724904A *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019200448A1 (en) * 2018-04-20 2019-10-24 Okanagan Winery & Ciders Condensing dehumidifier for an arena or the like
WO2021096343A1 (en) * 2019-11-12 2021-05-20 HERNÁNDEZ MAYÉN, Alfonso Device for harvesting atmospheric water vapour

Also Published As

Publication number Publication date
GB0125052D0 (en) 2001-12-12

Similar Documents

Publication Publication Date Title
RU2125693C1 (en) Method of heat exchanger and device for realization of this method
US4235081A (en) Compressed air dryer
ES2312416T3 (en) A COOLING AND PRE-COOLING HEAT EXCHANGER FOR THE CONDITIONING OF THE ADMISSION AIR OF A TURBINE.
US4730464A (en) Refrigerator and freezer
EP3081871B1 (en) Dehumidifier
EP1946027A2 (en) Multi-stage hybrid evaporative cooling system
WO2007041804A1 (en) A method and apparatus for extracting water from air containing moisture
EP2992272B1 (en) Energy recovery system and method
GB2057117A (en) Compressed gas drying apparatus
US20130175003A1 (en) Air dryer assembly
US11639800B2 (en) Dehumidification drainage system with mist eliminator
CN102794087A (en) Energy efficient refrigeration large industrial dehumidifier
US4370816A (en) Closed-circuit condensation purifier for gaseous flows containing solvents and moisture
US5249433A (en) Method and apparatus for providing refrigerated air
EP0170347B1 (en) A dehumidifier for a compressed gas
JP5196722B2 (en) Compressed air dehumidifier
WO2011087505A1 (en) Air dryer assembly
GB2381061A (en) Dehumidifiers
US3967940A (en) Apparatus for cooling and dehumidication of compressed air
EP0162095B1 (en) Method and equipment for utilization of the freezing heat of water as a source of heat of a heat pump
CN105986453A (en) Drying system
JP3932385B2 (en) Oil separator for refrigerant recovery filling of equipment to be recovered
JPH1119461A (en) Water-cooled condenser and air dryer
RU2200281C1 (en) Solar plant
KR100766104B1 (en) dehumidifiter

Legal Events

Date Code Title Description
WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)