WO1997011318A1 - A method and arrangement for recovering heat including freezing prevention means involving the spreading of non-freezing liquid - Google Patents
A method and arrangement for recovering heat including freezing prevention means involving the spreading of non-freezing liquid Download PDFInfo
- Publication number
- WO1997011318A1 WO1997011318A1 PCT/FI1996/000492 FI9600492W WO9711318A1 WO 1997011318 A1 WO1997011318 A1 WO 1997011318A1 FI 9600492 W FI9600492 W FI 9600492W WO 9711318 A1 WO9711318 A1 WO 9711318A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- liquid
- heat
- recovery unit
- heat recovery
- freezing
- Prior art date
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 50
- 238000007710 freezing Methods 0.000 title claims abstract description 32
- 230000008014 freezing Effects 0.000 title claims abstract description 31
- 238000000034 method Methods 0.000 title claims abstract description 16
- 230000007480 spreading Effects 0.000 title claims description 7
- 238000003892 spreading Methods 0.000 title claims description 7
- 230000002265 prevention Effects 0.000 title 1
- 238000011084 recovery Methods 0.000 claims abstract description 45
- 150000003839 salts Chemical class 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 6
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 3
- 238000004378 air conditioning Methods 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 230000008929 regeneration Effects 0.000 description 3
- 238000011069 regeneration method Methods 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 238000010257 thawing Methods 0.000 description 2
- WWYNJERNGUHSAO-XUDSTZEESA-N (+)-Norgestrel Chemical compound O=C1CC[C@@H]2[C@H]3CC[C@](CC)([C@](CC4)(O)C#C)[C@@H]4[C@@H]3CCC2=C1 WWYNJERNGUHSAO-XUDSTZEESA-N 0.000 description 1
- 241000282414 Homo sapiens Species 0.000 description 1
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- LUYGICHXYUCIFA-UHFFFAOYSA-H calcium;dimagnesium;hexaacetate Chemical compound [Mg+2].[Mg+2].[Ca+2].CC([O-])=O.CC([O-])=O.CC([O-])=O.CC([O-])=O.CC([O-])=O.CC([O-])=O LUYGICHXYUCIFA-UHFFFAOYSA-H 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000002301 combined effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000009972 noncorrosive effect Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000001223 reverse osmosis Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F12/00—Use of energy recovery systems in air conditioning, ventilation or screening
- F24F12/001—Use of energy recovery systems in air conditioning, ventilation or screening with heat-exchange between supplied and exhausted air
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24F—AIR-CONDITIONING; AIR-HUMIDIFICATION; VENTILATION; USE OF AIR CURRENTS FOR SCREENING
- F24F13/00—Details common to, or for air-conditioning, air-humidification, ventilation or use of air currents for screening
- F24F13/24—Means for preventing or suppressing noise
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
- F28C3/00—Other direct-contact heat-exchange apparatus
- F28C3/06—Other direct-contact heat-exchange apparatus the heat-exchange media being a liquid and a gas or vapour
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
- F28F19/006—Preventing deposits of ice
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/56—Heat recovery units
Definitions
- the invention relates to a method for recovering heat, in which method heat is recovered from exhaust air by a heat recovery unit arranged on the exhaust side and the recovered heat is transferred to supply air.
- the invention also relates to an arrangement for recovering heat.
- the object of the invention is to provide a method and an arrangement by which the drawbacks of the prior art can be eliminated. This is achieved by the method and arrangement provided by the invention.
- the method of the invention is characterized by spreading non-freezing liquid on the surfaces of the heat recovery unit on the exhaust side.
- the arrangement according to the invention is characterized in that in connection with the heat recovery unit are arranged means for spreading non-freezing liquid on the surfaces of the heat recovery unit.
- the advantage of the invention is, above all, that it makes it possible to provide protection against freezing and, in addition, that the efficiency of heat recovery is increased unlike in the previously known units, where it is reduced.
- the improvement in the heat recovery results from the fact that the heat-transfer coefficient of a wet heat-transfer radiator is higher than that of a dry radiator. This is described in Finnish Patent Application 933,534. In fact, the efficiency of the unit in the summer can be increased and the freezing in the winter prevented with one and the same unit.
- a further advantage is that the non- freezing liquids used are hygroscopic, in other words, they significantly drop the partial pressure of saturated steam. They dry the air, and so the heat of evaporation can be recovered.
- fig. 1 shows a general view of a first embodiment of an arrangement according to the invention
- fig. 2 shows a general view of a second embodiment according to the invention
- fig. 3 shows a general view of a third embodiment according to the invention
- fig. 4 shows a general view of a fourth embodiment according to the invention.
- Fig. 1 shows a general view of an arrangement according to the invention.
- Reference number 1 indicates an outlet channel through which the indoor air flows from the building. The flow of the indoor air through the outlet channel 1 is indicated in the figure by arrows.
- Reference number 2 indicates, generally, a heat recovery unit, i.e. heat exchanger, arranged in the outlet channel 1 to recover heat from the exhaust air. The heat recovered from the exhaust air is transferred from the heat recovery unit 2 to a second heat exchanger arranged in the inlet channel, and the recovered heat is transferred by the heat exchanger to the supply air.
- the inlet channel and the second heat exchanger arranged in it are not shown in fig. 1, since they are conventional technology to a person skilled in the art.
- non-freezing liquid is spread on the surfaces of the heat recovery unit 2 on the exhaust side.
- Means spreading non-freezing liquid are indicated in the figure by number 3.
- the means 3 may comprise, for example, a moistening mat, which is moistened with non- freezing liquid and which spreads the liquid on the surfaces of the heat recovery unit.
- the non-freezing liquid spread on the surfaces of the heat recovery unit runs along the surfaces in the manner indicated by arrows in the figure.
- the non-freezing liquid may be any non-corrosive substance that is safe to the environment. Examples for suitable liquids include calcium magnesium acetate/water, propylene glycol/ water, urea/water, etc.
- an accumulating device 4 which is arranged to receive the non-freezing liquid running from the surfaces of the heat recovery unit 2.
- the accumulating device 4 may be, for example, a reservoir.
- the arrangement further comprises a concentrator 5, which is arranged to increase the concentration of the non-freezing liquid before the liquid is re-spread on the surfaces of the heat recovery unit.
- the diluted but still non-freezing liquid running from the heat recovery unit 2 is conducted from the accumulating device 4 through a pipe 6 to the concentrator 5.
- the pipe 6 can be provided with an equalizing reservoir 7.
- a pump 8 can also be arranged in the pipe 6.
- the concentration of the liquid is increased in the concentrator 5 and the liquid is conducted with a spray pipe 9 from the concentrator 5 to a moistening mat serving as a spreader 3.
- the liquid is spread on the moistening mat by means of nozzles 10 arranged in the spray pipe 9.
- the flow direction of the liquid from the accumulating device 4 to the moistening mat serving as a spreader 3 is indicated in the figure by arrows.
- the concentrator 5 may be any suitable apparatus, such as a reverse osmosis apparatus, an apparatus operating on the evaporation principle, etc.
- the water separated from the liquid can be removed from the concentrator e.g. by means of an aggregate 11. The combined effect may be e.g.
- the minimum temperature of the exhaust air is 0°C: nominal efficiency of recovery 70% actual efficiency 46% recovered energy 32.5 kJ/kg dry air heating energy needed 47.5 kJ/kg dry air additional heating demand 15.0 kJ/kg dry air.
- the apparatus provided by the invention does not have a temperature limit for the exhaust air: actual efficiency > 70% final temperature of exhaust air > -12.5°C recovered energy > 45.5 kJ/kg dry air additional heating demand ⁇ 2.0 kJ/kg dry air.
- the final temperature of the exhaust air may be slightly below 0°C without causing too much freezing.
- the effects of a wet radiator and of hygroscopicity have not been taken into account except with marks ⁇ and >.
- the basic idea of the invention can also be applied by not attempting to prevent freezing altogether but by stopping icing and/or by defrosting when the ice starts to impair heat recovery. Heat recovery then becomes periodical.
- the advantage of this kind of embodiment is that less non-freezing liquid is needed.
- the above operation can be controlled e.g. such that the supply of liquid is started when the pressure loss of the heat recovery unit exceeds a certain value, or when the outdoor temperature is below a certain value.
- the start-up can also be based on measuring the temperatures of the heat transfer liquid and/or the exhaust air and/or the supply air of the heat recovery unit, or in more advanced systems, on reduction of the efficiency of recovery computed at a control centre. All these control methods, which are known per se, are naturally included in the invention.
- the equipment can be simplified by not including a regeneration unit.
- the liquid is accumulated in a reservoir 7, from where it can be taken elsewhere for regeneration, or the regeneration can also be performed on the spot e.g. by manually adding concentrated liquid, salt, etc.
- This kind of embodiment is shown in fig. 2. Accumulation is not always necessary, if the liquid can be directly conducted e.g. by a pipe 15 e.g. to sewage purification or to a utilization process.
- This kind of embodiment is shown in fig. 3.
- the liquid is supplied from a supply reservoir 14.
- the non-freezing liquid can also be concentrated without an actual concentrator using the air-conditioning unit itself e.g. in a situation where air-conditioning units are used for heating a building at night or at other times when the building is not in use.
- This kind of embodiment is presented in fig. 4.
- exhaust air is conducted from the heat recovery unit 2 back to the building, to which no outdoor air is supplied at all.
- a heat exchanger for supply air is indicated in fig. 3 by reference number 12.
- Additional air L is supplied to the recovery unit 2 e.g. at point 13. The additional heat heat heats the air and also vaporizes water from the liquid spread on the surfaces of the recovery unit 2, whereby the liquid is concentrated.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Drying Of Gases (AREA)
- Steam Or Hot-Water Central Heating Systems (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU69897/96A AU6989796A (en) | 1995-09-22 | 1996-09-18 | A method and arrangement for recovering heat including freezing prevention means involving the spreading of non-freezing liquid |
SE9800933A SE9800933L (en) | 1995-09-22 | 1998-03-20 | Methods and apparatus for heat recovery |
NO981274A NO981274L (en) | 1995-09-22 | 1998-03-20 | Method and device for heat recovery |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI954508 | 1995-09-22 | ||
FI954508A FI102319B1 (en) | 1995-09-22 | 1995-09-22 | Method and arrangement for heat recovery |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1997011318A1 true WO1997011318A1 (en) | 1997-03-27 |
Family
ID=8544077
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FI1996/000492 WO1997011318A1 (en) | 1995-09-22 | 1996-09-18 | A method and arrangement for recovering heat including freezing prevention means involving the spreading of non-freezing liquid |
Country Status (6)
Country | Link |
---|---|
AU (1) | AU6989796A (en) |
CA (1) | CA2232718A1 (en) |
FI (1) | FI102319B1 (en) |
NO (1) | NO981274L (en) |
SE (1) | SE9800933L (en) |
WO (1) | WO1997011318A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007106030A1 (en) * | 2006-03-10 | 2007-09-20 | Mikael Nutsos | Method and arrangement for optimizing heat transfer properties in heat exchange ventilation systems |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE117943C (en) * | ||||
US2747382A (en) * | 1952-12-17 | 1956-05-29 | Vilter Mfg Co | System for concentrating anti-freeze solution |
SE337664B (en) * | 1967-12-19 | 1971-08-16 | Bahco Ventilation Ab | |
SE413052B (en) * | 1976-05-28 | 1980-03-31 | Axlander Axel | HEAT EXCHANGER WITH POROST DELIVERY |
EP0019603A2 (en) * | 1979-05-21 | 1980-11-26 | Axel N.A. Axlander | Porous hygroscopic heat exchanger wall element |
US5024062A (en) * | 1987-11-20 | 1991-06-18 | Hellman Lars G | Multistage isothermal air dehumidification |
WO1995004902A1 (en) * | 1993-08-10 | 1995-02-16 | Abb Installaatiot Oy | Arrangement for cooling supply air in an air-conditioning installation |
-
1995
- 1995-09-22 FI FI954508A patent/FI102319B1/en active
-
1996
- 1996-09-18 CA CA002232718A patent/CA2232718A1/en not_active Abandoned
- 1996-09-18 AU AU69897/96A patent/AU6989796A/en not_active Abandoned
- 1996-09-18 WO PCT/FI1996/000492 patent/WO1997011318A1/en active Application Filing
-
1998
- 1998-03-20 NO NO981274A patent/NO981274L/en unknown
- 1998-03-20 SE SE9800933A patent/SE9800933L/en unknown
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE117943C (en) * | ||||
US2747382A (en) * | 1952-12-17 | 1956-05-29 | Vilter Mfg Co | System for concentrating anti-freeze solution |
SE337664B (en) * | 1967-12-19 | 1971-08-16 | Bahco Ventilation Ab | |
SE413052B (en) * | 1976-05-28 | 1980-03-31 | Axlander Axel | HEAT EXCHANGER WITH POROST DELIVERY |
EP0019603A2 (en) * | 1979-05-21 | 1980-11-26 | Axel N.A. Axlander | Porous hygroscopic heat exchanger wall element |
US5024062A (en) * | 1987-11-20 | 1991-06-18 | Hellman Lars G | Multistage isothermal air dehumidification |
WO1995004902A1 (en) * | 1993-08-10 | 1995-02-16 | Abb Installaatiot Oy | Arrangement for cooling supply air in an air-conditioning installation |
Non-Patent Citations (1)
Title |
---|
PATENT ABSTRACTS OF JAPAN, Vol. 95, No. 7; & JP,A,07 108 142 (HITACHI LTD), 25 April 1995. * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007106030A1 (en) * | 2006-03-10 | 2007-09-20 | Mikael Nutsos | Method and arrangement for optimizing heat transfer properties in heat exchange ventilation systems |
US8464783B2 (en) | 2006-03-10 | 2013-06-18 | Mikael Nutsos | Method and arrangement for optimizing heat transfer properties in heat exchange ventilation systems |
Also Published As
Publication number | Publication date |
---|---|
SE9800933D0 (en) | 1998-03-20 |
CA2232718A1 (en) | 1997-03-27 |
SE9800933L (en) | 1998-03-20 |
FI102319B (en) | 1998-11-13 |
FI954508A0 (en) | 1995-09-22 |
FI102319B1 (en) | 1998-11-13 |
AU6989796A (en) | 1997-04-09 |
NO981274L (en) | 1998-05-20 |
NO981274D0 (en) | 1998-03-20 |
FI954508A (en) | 1997-03-23 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6728130B2 (en) | Air conditioning method using stepwise process with liquid desiccant | |
US8826676B2 (en) | Greenhouse, greenhouse climate control system and method of controlling greenhouse climate | |
WO1994017345A1 (en) | Efficiency directed supplemental condensing system for high ambient refrigeration operation | |
CN104713266A (en) | Heat pump type cold and heat source unit capable of achieving frost-free and evaporative cooling | |
JP2010255992A (en) | Heat exchanger and humidifier | |
US20140231042A1 (en) | System for Reducing the Condensing Temperature of a Refrigeration or Air Conditioning System by Utilizing Harvested Rainwater | |
RU2125209C1 (en) | Device for cooling supply air in air-conditioning plant | |
US8517355B2 (en) | Evaporative cooling tower and method | |
WO1997011318A1 (en) | A method and arrangement for recovering heat including freezing prevention means involving the spreading of non-freezing liquid | |
CA2214409A1 (en) | Arrangement in connection with an air conditioning unit comprising heat recovery means and means for introducing additional heating and cooling | |
JP3077175B2 (en) | Heat pump air conditioner | |
FI102320B (en) | Method and apparatus for heat transfer | |
CN105571024A (en) | Haze low-temperature energy absorption purification heat pump VRV (Variable Refrigerant Volume) system device | |
JP5949844B2 (en) | Heat exchanger and humidifier | |
WO2000034719A1 (en) | Method and arrangement for recovering heat and moisture | |
EP0239573A1 (en) | Method of recovering ice formation energy | |
WO1991002927A1 (en) | A method of and an arrangement for cooling a building | |
JPH0447571Y2 (en) | ||
RU2151973C1 (en) | Process of winning of water from air ( air drying ) and gear for its realization | |
GB2588427A (en) | Condensate recovery | |
AU697594B2 (en) | Vacuum dewatering of desiccant brines | |
GB2336891A (en) | Dehumidifier | |
RU2262037C2 (en) | Plant for thorough utilization of waste gas heat and method of avoidance of condensation in tail section of gas duct | |
SU765602A1 (en) | Heat utilization plant in air-conditioning unit | |
RU2301310C1 (en) | Combined icicle formation prevention device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AL AM AT AU AZ BA BB BG BR BY CA CH CN CU CZ DE DK EE ES FI GB GE HU IL IS JP KE KG KP KR KZ LC LK LR LS LT LU LV MD MG MK MN MW MX NO NZ PL PT RO RU SD SE SG SI SK TJ TM TR TT UA UG US UZ VN AM AZ BY KG KZ MD RU TJ TM |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): KE LS MW SD SZ UG AT BE CH DE DK ES FI FR GB GR IE IT LU MC NL PT SE BF BJ CF CG |
|
DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
ENP | Entry into the national phase |
Ref document number: 2232718 Country of ref document: CA Ref country code: CA Ref document number: 2232718 Kind code of ref document: A Format of ref document f/p: F |
|
WWE | Wipo information: entry into national phase |
Ref document number: 98009335 Country of ref document: SE |
|
REG | Reference to national code |
Ref country code: DE Ref legal event code: 8642 |
|
122 | Ep: pct application non-entry in european phase |