CN203928222U - Ship Waste Heat solution dehumidification energy-saving type air conditioner - Google Patents
Ship Waste Heat solution dehumidification energy-saving type air conditioner Download PDFInfo
- Publication number
- CN203928222U CN203928222U CN201420185876.3U CN201420185876U CN203928222U CN 203928222 U CN203928222 U CN 203928222U CN 201420185876 U CN201420185876 U CN 201420185876U CN 203928222 U CN203928222 U CN 203928222U
- Authority
- CN
- China
- Prior art keywords
- solution
- cooler
- air
- waste heat
- dehumidifier
- Prior art date
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- 239000003570 air Substances 0.000 title claims abstract description 54
- 239000002918 waste heat Substances 0.000 title claims abstract description 26
- 238000007791 dehumidification Methods 0.000 title claims abstract description 14
- AMXOYNBUYSYVKV-UHFFFAOYSA-M Lithium bromide Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 claims abstract description 12
- 229940059936 lithium bromide Drugs 0.000 claims abstract description 12
- 229910001517 lithium bromide Inorganic materials 0.000 claims abstract description 12
- 238000000034 methods Methods 0.000 abstract description 11
- 238000005057 refrigeration Methods 0.000 abstract description 7
- 239000011901 water Substances 0.000 abstract description 6
- KWGKDLIKAYFUFQ-UHFFFAOYSA-M Lithium chloride Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [Li+].[Cl-] KWGKDLIKAYFUFQ-UHFFFAOYSA-M 0.000 abstract description 4
- 238000010521 absorption reactions Methods 0.000 abstract description 4
- 229910001522 lithium chloride Inorganic materials 0.000 abstract description 4
- 238000005516 engineering processes Methods 0.000 abstract description 3
- 239000000243 solutions Substances 0.000 description 53
- 238000001816 cooling Methods 0.000 description 8
- 238000004378 air conditioning Methods 0.000 description 3
- 239000000498 cooling water Substances 0.000 description 3
- 239000007788 liquids Substances 0.000 description 3
- 230000001172 regenerating Effects 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 2
- 239000000284 extracts Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000002699 waste materials Substances 0.000 description 2
- 206010009866 Cold sweat Diseases 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N chlorine atom Chemical compound 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[Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000002274 desiccants Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
Classifications
-
- 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
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
- Y02A30/274—Relating to heating, ventilation or air conditioning [HVAC] technologies using waste energy, e.g. from internal combustion engine
-
- 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]
- Y02B30/62—Absorption based systems
- Y02B30/625—Absorption based systems combined with heat or power generation [CHP], e.g. trigeneration
Abstract
Ship Waste Heat solution dehumidification energy-saving type air conditioner, comprise the first air cooler, solution cooler, solution tank, solution pump, air duct, the second air cooler, cabin, coiled pipe cooler, lithium-bromide absorption-type refrigerating machine group, dehumidifier, heater heated by waste heat and regenerator, described solution cooler, solution tank, solution pump, dehumidifier, heater heated by waste heat, between regenerator, by pipeline, connect successively, lithium-bromide absorption-type refrigerating machine group is by pipeline and dehumidifier, the second air cooler, coiled pipe cooler is connected, coiled pipe cooler is arranged in cabin, air duct connects the first air cooler successively, the second air cooler, after dehumidifier, enter in cabin, this technology adopts LiCl solution to absorb airborne moisture dehumidifying, utilize 70-90 ℃ of hot water to regenerate to LiCl weak solution, utilize exhaust-heat absorption formula refrigeration unit to produce high temperature cold water and process cabin thermic load, thereby realize humidity load and thermic load independent process, cabin humidity and temperature is independently controlled.
Description
Technical field
The utility model relates to Ship Waste Heat solution dehumidification energy-saving type air conditioner, belongs to air-conditioning technical field.
Background technology
Modern ships is in navigation process, and diesel main engine is the capital equipment that boats and ships consume the energy, and its power consumption has occupied the 70%-90% of the total power consumption of whole boats and ships.But main frame thermal efficiency is low, it is only 50% left and right.Other heats are to be disposed in atmosphere or marine environment by approach such as exhaust, cooling and heat radiations, and also contaminated environment not only wastes energy.
The discarded temperature of main frame is 260 ℃ to 400 ℃, and the outlet temperature of jacket-cooling water is at 70 ℃ to 90 ℃ etc.A large amount of waste heats can be aboard ship for refrigeration, ship air conditioning equipment mainly be take steam compression type refrigeration as main at present, air-treatment is carried out to dehumidification by condensation and cooling by refrigeration system evaporator to air, this processing mode shortcoming is that refrigeration system evaporating moisture is too low, efficiency is too low, containing the cold-producing medium R22 of chlorine element and a large amount of carbon emissions simultaneously and can destroy ecological environment, is a urgent problem.
Summary of the invention
The purpose of this utility model is to provide Ship Waste Heat solution dehumidification energy-saving type air conditioner.
Problem to be solved in the utility model is the not energy-conservation deficiency of existing marine air conditioner.
For realizing the purpose of this utility model, the technical solution adopted in the utility model is:
Ship Waste Heat solution dehumidification energy-saving type air conditioner, comprise the first air cooler, solution cooler, solution tank, solution pump, air duct, the second air cooler, cabin, coiled pipe cooler, lithium-bromide absorption-type refrigerating machine group, dehumidifier, heater heated by waste heat and regenerator, described solution cooler, solution tank, solution pump, dehumidifier, heater heated by waste heat, between regenerator, by pipeline, connect successively, lithium-bromide absorption-type refrigerating machine group is by pipeline and dehumidifier, the second air cooler, coiled pipe cooler is connected, coiled pipe cooler is arranged in cabin, air duct connects the first air cooler successively, the second air cooler, after dehumidifier, enter in cabin.
Between described solution cooler, solution tank, solution pump, dehumidifier, heater heated by waste heat, regenerator, by pipeline, realize successively closed connection.
Described the first air cooler, solution cooler are all connected with seawater.
Advantage of the present utility model: this technology adopts LiCl solution to absorb airborne moisture dehumidifying, utilize 70-90 ℃ of hot water to regenerate to LiCl weak solution, utilize exhaust-heat absorption formula refrigeration unit to produce high temperature cold water and process cabin thermic load, thereby realize humidity load and thermic load independent process, cabin humidity and temperature is independently controlled.
Solution dehumidification system, can adopt low-grade heat source to drive, and utilizes day hot low-temperature receiver a---cooled with seawater, has good energy saving.
Lithium-bromide absorption-type refrigerating machine group only need be born air thermic load, has improved the evaporating temperature of cold-producing medium, can be promoted to 15 ℃ by original 7 ℃, and energy-saving potential is large.
Liquid desiccant air conditioning is independently controlled temperature and humidity, and temperature is controlled by cooler, and humidity is controlled by solution moisture removing device, can realize the accurate control to aerial temperature and humidity, improves air-supply quality.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model Ship Waste Heat solution dehumidification energy-saving type air conditioner;
In figure: 1, the first air cooler 2, solution cooler 3, solution tank 4, solution pump 5, air duct 6, the second air cooler 7, cabin 8, coiled pipe cooler 9, lithium-bromide absorption-type refrigerating machine group 10, dehumidifier 11, heater heated by waste heat 12, regenerator.
The specific embodiment
Below in conjunction with drawings and Examples, the utility model is further described.
Ship Waste Heat solution dehumidification energy-saving type air conditioner, comprise the first air cooler 1, solution cooler 2, solution tank 3, solution pump 4, air duct 5, the second air cooler 6, cabin 7, coiled pipe cooler 8, lithium-bromide absorption-type refrigerating machine group 9, dehumidifier 10, heater heated by waste heat 11 and regenerator 12, described solution cooler 2, solution tank 3, solution pump 4, dehumidifier 10, heater heated by waste heat 11, between regenerator 12, by pipeline, connect successively, lithium-bromide absorption-type refrigerating machine group 9 is by pipeline and dehumidifier 10, the second air cooler 6, coiled pipe cooler 8 is connected, coiled pipe cooler 8 is arranged in cabin 7, air duct 5 connects the first air cooler 1 successively, the second air cooler 6, after dehumidifier 10, enter in cabin 7, send into compared with dry air.
Between described solution cooler 2, solution tank 3, solution pump 4, dehumidifier 10, heater heated by waste heat 11, regenerator 12, by pipeline, realize successively closed connection, realize waste heat dehumidifying.
Described the first air cooler 1, solution cooler 2 are all connected with seawater, for cooling.
Solution system is divided into two loops: dehumidifying loop and regenerative loop, two loops cross at solution tank 3 places.The function that solution tank 3 is separated solution make the to dehumidify solution pump 4 of loop can extract the higher solution of concentration by solution pump 4A from solution tank 3, pass into the liquid distributor at dehumidifier 10 tops, by the nozzle on liquid distributor, sprayed, after absorbing airborne steam, solution concentration reduces, cooling coil in dehumidifier 10 can be taken away dehumidification process liberated heat simultaneously, and weak solution flows back to solution tank 3 by Action of Gravity Field.The solution pump 4B of regenerative loop extracts the solution that concentration is lower from solution heat exchanger, and passing into heater heated by waste heat 11 will heat in weak solution, and the thermal source in heater heated by waste heat 11 can be from main engine jacket cooling water, 80-90 ℃ of exit temperature.In regenerator 12, outdoor new wind directly contacts with heated solution the exchange of carrying out heat and quality, and air is directly discharged after being heated humidification.The concentrated solution of regeneration, flows back to solution tank 3 by Action of Gravity Field, simultaneously can be cooling by brine cooler, complete regenerative process, and continual absorption airborne steam like this goes round and begins again.
The exhaust-heat absorption formula refrigeration unit that native system is selected is lithium-bromide absorption-type refrigerating machine 9, in running, can utilize boat diesel engine cylinder cooling water (85 ℃ of left and right of outlet temperature) as the heat source of generator.
Operation principle of the present utility model: new wind (38 ℃) is by 32 ℃ of the first air cooler 1(ocean temperatures) cooling, temperature is down to 33 ℃, and this is a wet cooling procedure such as grade.
New wind is through internally-cooled solution dehumidifying device 10, and airborne steam is absorbed, and water capacity reduces, and liberated heat is pulled away, i.e. the process of isothermal dehumidifying, and temperature maintains 33 ℃.
After 17 ℃ of cold water that new wind is produced by lithium-bromide absorption-type refrigerating machine group 9 are cooled to 25 ℃, send in cabin, this is the clammy process but such as.
After new wind mixes with room air, pass through dry-type fan coil cooler 8 cooling, selecting supply air temperature difference is 6 ℃ again, mixes after wind is cooled to 21 ℃ and sends in cabin, completes air-supply process.
Claims (3)
1. Ship Waste Heat solution dehumidification energy-saving type air conditioner, comprise the first air cooler (1), solution cooler (2), solution tank (3), solution pump (4), air duct (5), the second air cooler (6), cabin (7), coiled pipe cooler (8), lithium-bromide absorption-type refrigerating machine group (9), dehumidifier (10), heater heated by waste heat (11) and regenerator (12), it is characterized in that: described solution cooler (2), solution tank (3), solution pump (4), dehumidifier (10), heater heated by waste heat (11), regenerator connects successively by pipeline between (12), lithium-bromide absorption-type refrigerating machine group (9) is by pipeline and dehumidifier (10), the second air cooler (6), coiled pipe cooler (8) is connected, coiled pipe cooler (8) is arranged in cabin (7), air duct (5) connects the first air cooler (1) successively, the second air cooler (6), after dehumidifier (10), enter in cabin (7).
2. Ship Waste Heat solution dehumidification energy-saving type air conditioner according to claim 1, is characterized in that: between described solution cooler (2), solution tank (3), solution pump (4), dehumidifier (10), heater heated by waste heat (11), regenerator (12), by pipeline, realize successively closed connection.
3. Ship Waste Heat solution dehumidification energy-saving type air conditioner according to claim 1, is characterized in that: described the first air cooler (1), solution cooler (2) are all connected with seawater.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420185876.3U CN203928222U (en) | 2014-04-17 | 2014-04-17 | Ship Waste Heat solution dehumidification energy-saving type air conditioner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420185876.3U CN203928222U (en) | 2014-04-17 | 2014-04-17 | Ship Waste Heat solution dehumidification energy-saving type air conditioner |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203928222U true CN203928222U (en) | 2014-11-05 |
Family
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|---|---|---|---|
| CN201420185876.3U CN203928222U (en) | 2014-04-17 | 2014-04-17 | Ship Waste Heat solution dehumidification energy-saving type air conditioner |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104566688A (en) * | 2014-12-22 | 2015-04-29 | 宁波工程学院 | Open type refrigeration and dehumidification air conditioner unit |
| CN104908919A (en) * | 2015-05-26 | 2015-09-16 | 浙江海洋学院 | Air conditioning device of ship cabin |
| CN105352079A (en) * | 2015-11-24 | 2016-02-24 | 东南大学 | Independent temperature and humidity processing air conditioner system driven by low-level thermal energy |
| CN105737285A (en) * | 2016-03-11 | 2016-07-06 | 中国科学院工程热物理研究所 | Low-temperature afterheat-driven solution dehumidifying system and method |
| CN105841272A (en) * | 2016-04-07 | 2016-08-10 | 西安交通大学 | Temperature and humidity independent control type air-conditioning system driven by solar energy |
| CN106989460A (en) * | 2017-03-15 | 2017-07-28 | 南昌大学 | A kind of independent temperature-humidity control system of combination heat pump and solution dehumidification |
| CN109353181A (en) * | 2018-08-13 | 2019-02-19 | 东南大学 | A kind of efficient multi-mode operation air-conditioning system utilized based on automotive residual heat |
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2014
- 2014-04-17 CN CN201420185876.3U patent/CN203928222U/en not_active IP Right Cessation
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104566688A (en) * | 2014-12-22 | 2015-04-29 | 宁波工程学院 | Open type refrigeration and dehumidification air conditioner unit |
| CN104566688B (en) * | 2014-12-22 | 2017-02-22 | 宁波工程学院 | Open type refrigeration and dehumidification air conditioner unit |
| CN104908919A (en) * | 2015-05-26 | 2015-09-16 | 浙江海洋学院 | Air conditioning device of ship cabin |
| CN105352079A (en) * | 2015-11-24 | 2016-02-24 | 东南大学 | Independent temperature and humidity processing air conditioner system driven by low-level thermal energy |
| CN105352079B (en) * | 2015-11-24 | 2018-02-06 | 东南大学 | A kind of humiture independent treating air-conditioning system of Lowlevel thermal energy driving |
| CN105737285A (en) * | 2016-03-11 | 2016-07-06 | 中国科学院工程热物理研究所 | Low-temperature afterheat-driven solution dehumidifying system and method |
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| CN105841272B (en) * | 2016-04-07 | 2019-02-05 | 西安交通大学 | A kind of humiture independence control air conditioner system of Driven by Solar Energy |
| CN106989460A (en) * | 2017-03-15 | 2017-07-28 | 南昌大学 | A kind of independent temperature-humidity control system of combination heat pump and solution dehumidification |
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