CN1232785C - Separation heat-pipe type absorbing ice machine used for ship - Google Patents
Separation heat-pipe type absorbing ice machine used for ship Download PDFInfo
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- CN1232785C CN1232785C CNB2003101089245A CN200310108924A CN1232785C CN 1232785 C CN1232785 C CN 1232785C CN B2003101089245 A CNB2003101089245 A CN B2003101089245A CN 200310108924 A CN200310108924 A CN 200310108924A CN 1232785 C CN1232785 C CN 1232785C
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Abstract
The present invention relates to an adsorption ice-making machine of a similar separation heat pipe type for a ship, which belongs to the field of adsorption and refrigeration. The adsorption bed of the present invention is directly heated by a fume pipeline, and a middle cooler is welded with a second ammonia tank and is connected with the adsorption bed through the ascending segment of a heat pipe and the descending segment of the heat pipe; an electromagnetic valve is arranged on the descending segment of the heat pipe, the condenser is welded with the first ammonia tank, and the condenser is connected with the adsorption bed; a one-way valve is connected with a connection pipe; the first ammonia tank is connected with a slice ice machine, and the slice ice machine is connected with the adsorption bed; a return valve is arranged on the connection pipe of the condenser, the slice ice machine and the adsorption bed; a cold sea water return circuit is in a mode of connection in series, and a sea water valve and a cold sea water pump are arranged on a pipeline of a cold sea water inlet; the cold sea water return circuit is communicated with the condenser firstly, and communicated with the middle cooler and a cold sea water outlet then. The present invention mixes adsorbing agents with ammonia working substances, and the adsorption bed is cooled by adopting ammonia as cooling media. The present invention can solve the problem of corrosion generated by that the adsorption bed is directly cooled by sea water, and simultaneously, the present invention can simplify structures. Heat exchange effects can be enhanced.
Description
Technical field
What the present invention relates to is a kind of absorbing refrigeration system peculiar to vessel that is used for, and specifically is a kind separation heat pipe marine adsorption ice making machine.Belong to the absorption refrigeration field.
Background technology
At present, the coastal middle-size and small-size fishing boat of China is mostly fresh-keeping based on iced storage, and mechanical refrigeration is fresh-keeping to be auxilliary.Therefore, the fishing boat refrigeration machine is the equipment that current medium and small fishing boat presses for equipment, develops the steam compression type refrigerating mode that still concentrates on.Meanwhile, the diesel engine on the fishing boat has 30% heat to enter atmosphere and waste from tail gas approximately.If can utilize this part waste heat to drive adsorption refrigeration system, can not increase any oil consumption of diesel engine, only reclaim its using waste heat from tail gas and realize ice making, satisfy fisherman's demand.
The absorption refrigeration equipment of being studied at present peculiar to vessel, main employing water, ammonia and methyl alcohol are cold-producing medium, wherein adopting water, methyl alcohol is that the system of cold-producing medium generally adopts physical absorbent, with respect to adopt chemosorbent one ammonia be working medium for system, refrigerating capacity is less than normal.Consider compatibility, generally adopt the steel material, owing to have incompatibility between seawater and the steel material, be that the system of cold-producing medium generally can not adopt seawater directly to cool off so adopt ammonia at present, otherwise can have serious etching problem for the ammonia system adsorbent bed.Fishing boat absorption refrigeration equipment, currently used adsorbent bed form mostly is unit tubular type and shell-tube type.
Find Chinese patent application number by literature search: 99232616, name is called: seagoing fishing vessel diesel engine vent gas ice machine, it is cold-producing medium that this patent adopts ammonia, calcium chloride is adsorbent.Adsorbent bed adopts flue gas directly to heat, and cooling adopts cold water directly to cool off.This adsorption ice making machine generator is 1.05m
3About, refrigerating capacity is about 12kW.This system adopts water-cooled then to have dual mode to select, and one of mode is to adopt Mare Frigoris water directly to cool off, and this inevitable also can generation adsorbent bed is corroded.Two of mode is to adopt Intermediate Heat Exchanger fresh water to cool off, and needs to increase a water supply pump like this in the adsorption system, and this must increase consumption of electric.Adsorbent bed employing water-cooled is the heat convection mode in addition, and its heat-transfer effect is comparatively limited.
Summary of the invention
The objective of the invention is to overcome above-mentioned the deficiencies in the prior art, one kind separation heat pipe marine adsorption ice making machine is provided, so, it with ammonia the etching problem in the time of can effectively avoiding adsorbent bed to adopt seawater directly to cool off in the adsorption ice making machine peculiar to vessel of cold-producing medium, adopting ammonia in the opposing party's Noodles separating heat tube type of cooling is cooling medium, can save the cooling liquid circulating pump, because the cooling procedure of ammonia adopts the phase transformation evaporation process, this can improve the heat exchange effect of adsorbent bed simultaneously.
The present invention is achieved by the following technical solutions, the present invention includes: smoke inlet, thermometer, mass return valve, gas fume valve, first adsorbent bed, Pressure gauge, exhanst gas outlet, second adsorbent bed, the heat pipe ascent stage, heat pipe descending branch, first magnetic valve, second magnetic valve, first, second, third, fourth check valve, Mare Frigoris water inlet, the Mare Frigoris water pump, kingston valve, Mare Frigoris water loop, the first ammonia jar, the second ammonia jar, condenser, slice ice machine, intercooler, Mare Frigoris water out, choke valve, first takes over, and second takes over.Its connected mode is: thermometer and gas fume valve are arranged on the smoke inlet pipeline, are used for controlling the heating and the cooling procedure of first, second adsorbent bed.The intercooler and the second ammonia jar weld together by pipeline, link to each other by heat pipe ascent stage and heat pipe descending branch with first, second adsorbent bed.First, second magnetic valve is arranged on the heat pipe descending branch, is used to control the cooling procedure of first, second adsorbent bed.The condenser and the first ammonia jar weld together by pipeline, and condenser is taken over by second with first, second adsorbent bed and is connected, and the 3rd, the 4th check valve is connected second and takes over, and is used to control the desorption process of first, second adsorbent bed.The first ammonia jar links to each other by pipeline with slice ice machine, and the course of work is by throttle valve control.Slice ice machine is taken over by first and is linked to each other with first, second adsorbent bed.First, second check valve is arranged on first and takes over, and is used to control the adsorption process of first, second adsorbent bed.Mass return valve is arranged in the adapter of condenser and slice ice machine and first, second adsorbent bed, returns matter in the time of can switching in working order.The Mare Frigoris water loop is a series system, and seawater valve and Mare Frigoris water pump are arranged on the Mare Frigoris water inlet pipeline, and the Mare Frigoris water loop is connected with condenser earlier, is communicated with intercooler again, is communicated with the Mare Frigoris water out at last.
First, second adsorbent bed is all selected the curing mixed adsorbent for use, and ammonia is cold-producing medium.First, second adsorbent bed structure is identical, specifically comprises: upper perforated plate, ammoniacal liquor outlet, vacuum orifice, adsorbent, fin, shell, ammoniacal liquor import, lower perforated plate, flue gas pipeline, ammoniacal liquor pipeline, adsorption/desorption mouth, screen casing.Its connected mode is: upper perforated plate, lower perforated plate adopt the mode of welding to be connected with flue gas pipeline respectively, adopt welding between ammoniacal liquor outlet, vacuum orifice, ammoniacal liquor import and adsorption/desorption mouth and the shell.The ammoniacal liquor import is connected with the ammoniacal liquor pipeline of first, second adsorbent bed inside.The both sides of adsorbent are provided with fin, and fin adopts the mode that connects that rises to be connected with ammoniacal liquor pipeline and flue gas pipeline, and the mode that screen casing adopts bourdon tube to be surrounded by screen cloth is outward made, and is connected with fin, is mainly used in mass transfer.
Smoke inlet is the waste gas outlet of diesel engine, inserts the flue gas pipeline in first, second adsorbent bed, and exhanst gas outlet flue gas pipeline in first, second adsorbent bed picks out, and flue gas enters atmosphere from exhanst gas outlet.Pressure gauge is connected on first, second adsorbent bed outer wall, communicates with the inner chamber of first, second adsorbent bed.
First, second adsorbent bed is directly heated by the flue gas heating circuit when heating desorption, when cooling absorption, is then cooled off by ammonia working medium by class separating heat tube cooling adsorbent bed loop.Ammoniacal liquor evaporates under first, second adsorbent bed institute liberated heat in the ammoniacal liquor pipeline, takes away heat of adsorption, cools off by Mare Frigoris water in intercooler.Be provided with mass return valve between first, second adsorbent bed, return matter in the time of can switching in working order.First, second adsorbent bed desorb realizes by first, second, third, fourth check valve that with absorption the direct input chip ice maker of cold that absorption is produced carries out ice making.
Condenser and intercooler all adopt multitube type cross-flow heat exchanger, the intercooler bottom links to each other with the second ammonia jar, the second ammonia jar bottom links to each other with first, second adsorbent bed bottom by the heat pipe descending branch, first, second adsorbent bed top linked to each other with the heat pipe ascent stage, the heat pipe ascent stage is inserted intercooler top again, first, second magnetic valve is connected on the heat pipe descending branch, forms class separating heat tube type cooling system.
In condenser and the intercooler pipe is the Mare Frigoris water loop, and pipe is outer to be ammonia solution, and intercooler no longer adopts the type of cooling of traditional heat pipe, and this can improve cooling effect.The first ammonia pot bottom is linked slice ice machine through a choke valve, and the first ammonia jar and slice ice machine are formed the combined type evaporimeter.
The operational process of the present invention's residual heat drive adsorption type ice machine peculiar to vessel comprises following loop:
1. the flue gas heating circuit is made up of gas fume valve, thermometer and flue gas pipeline.2. class separating heat tube cooling adsorbent bed loop is made up of ammonia pipeline (comprising ammoniacal liquor pipeline, heat pipe ascent stage and heat pipe descending branch in first, second adsorbent bed), first and second magnetic valve, intercooler, the second ammonia jar.3. series system is adopted in Mare Frigoris water cooling loop, and Mare Frigoris water is introduced into condenser, enters intercooler again, comprises compositions such as valve and Mare Frigoris water pump.4. adsorb the loop, first, second adsorbent bed adsorbs from evaporimeter, thereby produces refrigerating capacity, is controlled by first, second check valve.5. desorb loop, cold-producing medium is separated and is drawn onto condenser in first, second adsorbent bed, by the Mare Frigoris water condensation.Control by the 3rd, the 4th check valve.6. go back to the matter loop, control by mass return valve.7. slice ice machine goes out the ice system, low temperature liquid cold-producing medium in the fluid reservoir relies on the pressure reduction in fluid reservoir and the ice machine to enter into slice ice machine, slice ice machine is the evaporimeter that a stainless steel disc is rotated continuously, and the inside of evaporimeter is cold-producing medium, and the mode ice making of water spray is taked in the outside.The suction-operated of first, second adsorbent bed makes cold-producing medium in the inner evaporation of the evaporimeter of slice ice machine, and evaporation reduces the refrigerant temperature in the slice ice machine and produces cold.After the temperature of cold-producing medium was reduced to a certain degree, the shower water of evaporator of flake ice maker outside began to freeze on the surface of evaporimeter, and made ice is stripped down from evaporator surface by the sharpener of slice ice machine, forms the ice of sheet, finishes ice-making process.
The 25%-35% of the diesel engine intermediate fuel oil burning heat of supplying with is taken away by waste gas to be lost, and delivery temperature is generally about 400 ℃.With 6160A type ship diesel engine is example (rated power 101kW, rotating speed 750r/min), and when it inserted the 75kW load running, surveying its recyclable waste heat amount was about 34kW.The coefficient of refrigerating performance COP of absorption type ice machine calculates by 0.3, and then refrigerating capacity is output as 10kW.Per hour approximately can produce ice 60kg.The pipeline of absorption type ice-making system switches by machinery, electric device to be finished automatically.Because fishing boat can only be done simple maintenance in the navigation operation, to the requirement higher than Lu Yongyou of refrigeration plant security reliability and spare part aspect.Therefore each running control programization of whole system is convenient to fisherman's execute-in-place.
The absorption type ice machine that waste heat peculiar to vessel of the present invention drives, between fishing boat navigation and operational period,, it drives owing to directly utilizing the diesel engine vent gas waste heat, with the seawater is that low-temperature receiver cools off first, second adsorbent bed and condenser is realized continuous ice-making, with drive traditional vapor compression refrigeration mode by electric energy and compare, save the consumption of diesel oil, improved rate of energy; Overcome absorption system and must equip solution pump or fractionating device, not too be fit to the shortcomings such as balleting state of hull; Have that structure is simple with control, moving component is few, plurality of advantages such as good anti-vibration, operating cost are low, long service life, be a kind ofly both to have saved the energy, improve energy utilization rate, be beneficial to effective refrigeration modes of environmental protection again.
Description of drawings
Fig. 1 is a system architecture schematic diagram of the present invention
Fig. 2 is first, second adsorbent bed structural front view of the present invention
Fig. 3 is first, second adsorbent bed structural section of the present invention figure
The specific embodiment
As shown in Figure 1, the present invention includes: smoke inlet 1, thermometer 2, mass return valve 3, gas fume valve 4, the first adsorbent beds 5, Pressure gauge 6, exhanst gas outlet 7, the second adsorbent beds 8, the heat pipe ascent stage 9, heat pipe descending branch 10, the first magnetic valves 11, second magnetic valve 12, first check valve, 13, the second check valves, 14, the three check valves 15, the 4th check valve 16, Mare Frigoris water inlet 17, Mare Frigoris water pump 18, kingston valve 19, Mare Frigoris water loop 20, the first ammonia jars 21, condenser 22, slice ice machine 23, the second ammonia jars 24, intercooler 25, Mare Frigoris water out 26, choke valve 27, first takes over 28, the second takes over 29.Its connected mode is: thermometer 2 and gas fume valve 4 are arranged on smoke inlet 1 pipeline, the intercooler 25 and the second ammonia jar 24 weld together by pipeline, link to each other by heat pipe ascent stage 9 and heat pipe descending branch 10 with first adsorbent bed 5, second adsorbent bed 8.First magnetic valve 11, second magnetic valve 12 are arranged on the heat pipe descending branch 10, the condenser 22 and the first ammonia jar 21 weld together by pipeline, condenser 22 is taken over 29 with first adsorbent bed 5, second adsorbent bed 8 by second and is connected, the 3rd check valve 15, the 4th check valve 16 are connected second and take on 29, the first ammonia jar 21 and slice ice machine 23 link to each other by pipeline, and slice ice machine 23 is taken over 28 by first and linked to each other with first adsorbent bed 5, second adsorbent bed 8.First check valve 13, second check valve 14 are arranged on first and take on 28, mass return valve 3 is arranged in the adapter of condenser 22 and slice ice machine 23 and first adsorbent bed 5, second adsorbent bed 8, Mare Frigoris water loop 20 is a series system, seawater valve 19 and Mare Frigoris water pump 18 are arranged on Mare Frigoris water inlet 17 pipelines, Mare Frigoris water loop 20 is connected with condenser 22 earlier, be communicated with intercooler 25 again, be communicated with Mare Frigoris water out 26 at last.Smoke inlet 1, Pressure gauge 6 and exhanst gas outlet 7 link to each other with first adsorbent bed 5, second adsorbent bed 8 respectively.
Condenser 22 all adopts multitube type cross-flow heat exchanger with intercooler 25.The first ammonia jar, 21 bottoms link slice ice machine 23, the first ammonia jars 21 through a choke valve and slice ice machine 23 is formed the combined type evaporimeter.
As Fig. 2, shown in Figure 3, first adsorbent bed 5 and second adsorbent bed 8 are all selected the curing mixed adsorbent for use, and ammonia is cold-producing medium.
First adsorbent bed 5 is identical with second adsorbent bed, 8 structures, specifically comprises: upper perforated plate 30, ammoniacal liquor outlet 31, vacuum orifice 32, adsorbent 33, fin 34, shell 35, ammoniacal liquor import 36, lower perforated plate 37, flue gas pipeline 38, ammoniacal liquor pipeline 39, adsorption/desorption mouth 40, screen casing 41.Its connected mode is: upper perforated plate 30, lower perforated plate 37 adopt the mode of welding to be connected with flue gas pipeline 38 respectively, adopt welding between ammoniacal liquor outlet 31, vacuum orifice 32, ammoniacal liquor import 36 and adsorption/desorption mouth 40 and the shell 35.Ammoniacal liquor import 36 is connected with the ammoniacal liquor pipeline 39 of first, second adsorbent bed inside.The both sides of adsorbent 33 are provided with fin 34, and fin 34 adopts the mode that connects that rises to be connected with ammoniacal liquor pipeline 39 and flue gas pipeline 38, and the mode that screen casing 41 adopts bourdon tube to be surrounded by screen cloth is outward made, and is connected with fin 34.
Smoke inlet 1 is the waste gas outlet of diesel engine, insert the flue gas pipeline 38 in first adsorbent bed 5, second adsorbent bed 8, exhanst gas outlet 7 picks out from first adsorbent bed 5, second adsorbent bed, 8 interior flue gas pipelines, Pressure gauge 6 is connected on first, second adsorbent bed shell 35, communicates with the inner chamber of first adsorbent bed 5, second adsorbent bed 8.
Condenser 22 all adopts multitube type cross-flow heat exchanger with intercooler 25, intercooler 25 bottoms link to each other with the second ammonia jar 24, the second ammonia jar, 24 bottoms link to each other with first adsorbent bed 5, second adsorbent bed, 8 bottoms by heat pipe descending branch 10, first adsorbent bed 5, second adsorbent bed, 8 tops linked to each other with the heat pipe ascent stage 9, the heat pipe ascent stage 9 is inserted intercooler 25 tops again, first magnetic valve 11, second magnetic valve 12 are connected on the heat pipe descending branch 10, form class separating heat tube type cooling system.
The present invention adopts the class separating heat tube type type of cooling to cool off.In first adsorbent bed 5, second adsorbent bed, 8 cooling procedures, ammoniacal liquor enters ammoniacal liquor pipelines 39 in first adsorbent bed 5, second adsorbent bed 8 by the second ammonia jar 24 and first magnetic valve 11, second magnetic valve 12, heat of adsorption is taken away in evaporation in first adsorbent bed 5, second adsorbent bed 8 then, enter into intercooler 25 by the heat pipe ascent stage 9, enter into the second ammonia jar 24 after being cooled to ammoniacal liquor, enter first adsorbent bed 5, the 8 formation circulations of second adsorbent bed again.25 of intercoolers rely on Mare Frigoris water to cool off.The Mare Frigoris water cooling adopts the mode of series connection, enters into condenser 22 by Mare Frigoris water inlet 17 and Mare Frigoris water pump 18, kingston valve 19 earlier, enters into intercooler 25 by Mare Frigoris water loop 20 again, enters the sea by Mare Frigoris water out 26.
Claims (5)
1, one kind separation heat pipe marine adsorption ice making machine, comprise: smoke inlet (1), thermometer (2), gas fume valve (4), first adsorbent bed (5), Pressure gauge (6), exhanst gas outlet (7), second adsorbent bed (8), first check valve (13), second check valve (14), the 3rd check valve (15), the 4th check valve (16), condenser (22), first takes over (28), second takes over (29), it is characterized in that also comprising: mass return valve (3), the heat pipe ascent stage (9), heat pipe descending branch (10), first magnetic valve (11), second magnetic valve (12), Mare Frigoris water inlet (17), Mare Frigoris water pump (18), kingston valve (19), Mare Frigoris water loop (20), the first ammonia jar (21), slice ice machine (23), the second ammonia jar (24), intercooler (25), Mare Frigoris water out (26), choke valve (27), its connected mode is: thermometer (2) and gas fume valve (4) are arranged on smoke inlet (1) pipeline, intercooler (25) welds together by pipeline with the second ammonia jar (24), with first adsorbent bed (5), second adsorbent bed (8) links to each other by heat pipe ascent stage (9) and heat pipe descending branch (10), first magnetic valve (11), second magnetic valve (12) is arranged on the heat pipe descending branch (10), condenser (22) welds together by pipeline with the first ammonia jar (21), condenser (22) and first adsorbent bed (5), second adsorbent bed (8) is taken over (29) by second and is connected, the 3rd check valve (15), the 4th check valve (16) is connected second and takes on (29), the first ammonia jar (21) links to each other by pipeline with slice ice machine (23), slice ice machine (23) is taken over (28) and first adsorbent bed (5) by first, second adsorbent bed (8) links to each other, first check valve (13), second check valve (14) is arranged on first and takes on (28), mass return valve (3) is arranged on condenser (22) and slice ice machine (23) and first adsorbent bed (5), in the adapter of second adsorbent bed (8), Mare Frigoris water loop (20) is a series system, seawater valve (19) and Mare Frigoris water pump (18) are arranged on Mare Frigoris water inlet (17) pipeline, Mare Frigoris water loop (20) is connected with condenser (22) earlier, be communicated with intercooler (25) again, at last be communicated with smoke inlet (1) with Mare Frigoris water out (26), Pressure gauge (6), and exhanst gas outlet (7) respectively with first adsorbent bed (5), second adsorbent bed (8) links to each other.
2, class separating heat tube type according to claim 1 adsorption ice making machine peculiar to vessel, it is characterized in that, condenser (22) all adopts multitube type cross-flow heat exchanger with intercooler (25), intercooler (25) bottom links to each other with the second ammonia jar (24), second ammonia jar (24) bottom is by heat pipe descending branch (10) and first adsorbent bed (5), second adsorbent bed (8) bottom links to each other, first adsorbent bed (5), second adsorbent bed (8) top linked to each other with the heat pipe ascent stage (9), the heat pipe ascent stage (9) is inserted intercooler (25) top again, first magnetic valve (11), second magnetic valve (12) is connected on the heat pipe descending branch (10), forms class separating heat tube type cooling system.
3, class separating heat tube type according to claim 1 adsorption ice making machine peculiar to vessel is characterized in that, slice ice machine (23) is linked through a choke valve in the first ammonia jar (21) bottom, and the first ammonia jar (21) and slice ice machine (23) are formed the combined type evaporimeter.
4, class separating heat tube type according to claim 1 adsorption ice making machine peculiar to vessel, it is characterized in that, first adsorbent bed (5) is identical with second adsorbent bed (8) structure, specifically comprise: upper perforated plate (30), ammoniacal liquor outlet (31), vacuum orifice (32), adsorbent (33), fin (34), shell (35), ammoniacal liquor import (36), lower perforated plate (37), flue gas pipeline (38), ammoniacal liquor pipeline (39) and adsorption/desorption mouth (40), its connected mode is: upper perforated plate (30), lower perforated plate (37) adopts the mode of welding to be connected with flue gas pipeline (38) respectively, ammoniacal liquor outlet (31), vacuum orifice (32), adopt welding between ammoniacal liquor import (36) and adsorption/desorption mouth (40) and the shell (35), ammoniacal liquor import (36) and first, the ammoniacal liquor pipeline (39) of the second adsorbent bed inside is connected, the both sides of adsorbent (33) are provided with fin (34), fin (34) adopts the mode that connects that rises to be connected with ammoniacal liquor pipeline (39) and flue gas pipeline (38), the mode that screen casing (41) adopts bourdon tube to be surrounded by screen cloth is outward made, and is connected with fin (34).
According to claim 1 or 4 described class separating heat tube types adsorption ice making machine peculiar to vessel, it is characterized in that 5, first adsorbent bed (5) is all selected the curing mixed adsorbent for use with second adsorbent bed (8), ammonia is cold-producing medium.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2003101089245A CN1232785C (en) | 2003-11-27 | 2003-11-27 | Separation heat-pipe type absorbing ice machine used for ship |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2003101089245A CN1232785C (en) | 2003-11-27 | 2003-11-27 | Separation heat-pipe type absorbing ice machine used for ship |
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| CN1544864A CN1544864A (en) | 2004-11-10 |
| CN1232785C true CN1232785C (en) | 2005-12-21 |
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Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100414219C (en) * | 2004-11-25 | 2008-08-27 | 上海交通大学 | Ice maker on fishing boat waste heat driven by and with double hot-pipe chemical adsorption |
| CN1327172C (en) * | 2005-03-24 | 2007-07-18 | 上海交通大学 | Pump fluid type composite alternating separation heat pipe marine compound adsorption ice making machine |
| CN102338499A (en) * | 2010-07-15 | 2012-02-01 | 中兴电工机械股份有限公司 | Separated solid-adsorption-type refrigerating system |
| CN104048440B (en) * | 2014-05-30 | 2016-05-25 | 武汉畅能鑫悦新能源科技有限公司 | Alkaline-earth halide chemisorbed formula thermal refrigerating system |
| CN104048442B (en) * | 2014-05-30 | 2016-05-25 | 武汉畅能鑫悦新能源科技有限公司 | The chemical adsorption refrigeration system driving with automobile engine tail gas |
| CN104048443B (en) * | 2014-05-30 | 2016-05-25 | 武汉畅能鑫悦新能源科技有限公司 | Chemical adsorption refrigeration system taking motor exhaust as driven by energy |
| CN106288498B (en) * | 2016-08-19 | 2019-03-15 | 上海交通大学 | Adsorb bed system |
| CN109237973A (en) * | 2018-07-28 | 2019-01-18 | 中国舰船研究设计中心 | Ship Waste Heat multifunction control system based on separate heat pipe technology |
| TR2022001122A2 (en) * | 2022-01-28 | 2022-02-21 | Piri Reis Ueniversitesi | AN ADSORPTION COOLING AND HEATING SYSTEM FOR USE IN MARINE VEHICLES |
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