CN102506564B - Condensation water residual heat first-effect flash evaporation natural air dehumidifying, preheating and drying baking oven system - Google Patents

Condensation water residual heat first-effect flash evaporation natural air dehumidifying, preheating and drying baking oven system Download PDF

Info

Publication number
CN102506564B
CN102506564B CN2011104471077A CN201110447107A CN102506564B CN 102506564 B CN102506564 B CN 102506564B CN 2011104471077 A CN2011104471077 A CN 2011104471077A CN 201110447107 A CN201110447107 A CN 201110447107A CN 102506564 B CN102506564 B CN 102506564B
Authority
CN
China
Prior art keywords
air
outlet
baking oven
water
steam
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.)
Active
Application number
CN2011104471077A
Other languages
Chinese (zh)
Other versions
CN102506564A (en
Inventor
张基虎
杨晓辉
杨思伦
张梦颖
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.)
YIHENG ENERGY-SAVING TECHNOLOGY JIANGSU CO LTD
Original Assignee
YIHENG ENERGY-SAVING TECHNOLOGY JIANGSU CO LTD
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 YIHENG ENERGY-SAVING TECHNOLOGY JIANGSU CO LTD filed Critical YIHENG ENERGY-SAVING TECHNOLOGY JIANGSU CO LTD
Priority to CN2011104471077A priority Critical patent/CN102506564B/en
Publication of CN102506564A publication Critical patent/CN102506564A/en
Application granted granted Critical
Publication of CN102506564B publication Critical patent/CN102506564B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention relates to a condensation water residual heat first-effect flash evaporation natural air dehumidifying, preheating and drying baking oven system. A baking oven is internally provided with a coil heat exchanger set; the outlet of the coil heat exchanger set is respectively provided with a water draining valve and is connected with a high-temperature condensation water pipe; the high-temperature condensation water accesses to a flash evaporation tank; flash evaporation steam enters a flash evaporation steam pipe from a constant-pressure overflow valve; one way of the outlet of the flash evaporation steam pipe is connected to a lithium bromide refrigerating machine, and the other way of the outlet of the flash evaporation steam pipe is connected to an air preheater through a front pressure automatic regulating valve; the refrigeration water outlet of the refrigerating machine is connected with the water inlet of a cooler of a superficial cooling mist extractor, and the water outlet of the cooler is connected with refrigeration water inlet of the lithium bromide refrigerating machine; and natural air accesses to the humid air inlet of the superficial cooling mist extractor, the dry air outlet of the superficial cooling mist extractor accesses into an air blower, and is sent into the air inlet of the baking oven through the air preheater by the air blower. The system not only can guarantee the drying degree of materials to achieve the technological requirements, but also the utilization efficiency of steam can be improved, and the dissipation of energy of unit product is reduced.

Description

Condensation water residual heat one effect flash evaporation natural air dehumidifying preheating and drying baking oven system
Technical field
The present invention relates to a kind of drying oven, particularly a kind of condensation water residual heat one effect flash evaporation natural air dehumidifying preheating and drying baking oven system.
Background technology
The air drying oven is provided with baking oven air inlet, baking oven gas outlet, wet stock import and dry material outlet, in baking oven, generally include many groups coil heat exchanger group in parallel, each coil heat exchanger group is formed in parallel by a plurality of coil heat exchangers, the import of each coil heat exchanger group is connected with main steam pipe by steam stop respectively, the outlet of each coil heat exchanger is respectively equipped with drain valve, and the outlet of each drain valve accesses respectively total condensate pipe.When vapor stream is crossed each coil heat exchanger and air heat-exchange and, after discharging latent heat, be condensed into the high-temperature condensation water under uniform pressure, high-temperature condensation water enters total condensate pipe through each drain valve; Air enters from the baking oven air inlet, the outer surface of each coil heat exchanger of flowing through, through with steam heat-exchanging after, become hot-air, hot-air and moist material carry out the wet exchange of heat, from the baking oven gas outlet, flow out after taking away the moisture of wet stock, realize the oven dry of material.
After high-temperature condensation water enters total condensate pipe, along the continuous pressure drop of journey, part high-temperature condensation water flash-off of steam, doubly, flow velocity increases approximately 10 times in volumetric expansion more than 1600, and causing prevailing in total condensate pipe is not condensed water, but flash-off steam very easily forms vapour locking; After vapour locking, the back pressure of drain valve increases, and drain valve two ends pressure reduction reduces, and the drain valve discharge capacity descends, and causes the condensed water produced in coil heat exchanger not get rid of in time, and heat exchanger efficiency descends, and hot air temperature can not reach technological requirement, produces thereby impact is normal.For guarantee producing, often need to open the stop valve in parallel with drain valve and carry out in linely, result is that steam leakage when discharging condensed water, steam head on condensed water and flow at total condensate pipe, to overcome the vapour locking resistance; Though guaranteed production, steam utilization reduces, and the unit product steam consumption increases.Therefore existing system or can not normally produce, otherwise waste of steam is serious, and the condensed water sensible heat is not fully used.
Natural air is comprised of dry air and steam, namely in natural air, contains moisture, and especially humidity high season, water capacity can reach 20g/Nm 3Above, water ratio under gaseous state expands more than 1600 doubly in liquid lower volume, so the moisture in natural air has occupied certain volume.When the relative humidity of air reached 100%, airborne moisture reached capacity, and no longer had from the ability of moisture absorption material, and air themperature now is called dew-point temperature, and when air themperature dropped to dew-point temperature, airborne water vapour will condense into dew.The relative humidity of air is lower, stronger to the drying capacity of material.Baking oven in the course of the work, by air blast, blown in baking oven, air blast is when sending into dry air, also steam is sent in baking oven, steam not only hinders the moisture absorption of air to material, reduce the moisture pick-up properties of air, self go back after the heat that the absorption coil heat exchanger discharges as toxic emission, wasted a large amount of heat energy; In addition, due to the existence of steam, air blast need to be sent into more air to meet the needs of the wet exchange of heat, has both increased power consumption, has increased again the air exhaust heat loss.
According to the second law of thermodynamics, heat can not spontaneously be transferred to high temp objects from cryogenic object, realize this process, must consume certain merit, just can make the temperature of cryogenic object lower, reaches the purpose of refrigeration.Lithium-bromide absorption-type refrigerating machine is a kind ofly to take thermal source and be the refrigeration machine of power, mainly generator, condenser, evaporimeter, absorber four major parts and the equipment such as heat exchanger and solution pump, consists of.Lithium bromide refrigerator inside is vacuum environment, for example the shell side of evaporimeter maintenance absolute pressure is 6.54mmHg, water is 5 ℃ of boilings, the water as refrigerant spirt is gone will explosive evaporation, for example, when the higher chilled water of temperature (the being 12 ℃) evaporimeter of flowing through tube side, the water as refrigerant sprayed so outside copper pipe will absorb heat and evaporate from copper pipe, and the chilled water temperature in copper pipe has just reduced (12 ℃ → 7 ℃); After the water as refrigerant evaporation, the pressure of evaporimeter will raise, and in order to keep the pressure very low (6.54mmHg) in evaporimeter, absorber absorbs water vapour by the spray bromize lithium concentrated solution, lithium-bromide solution after the absorption water vapour becomes weak solution, and concentration reduces can not absorb steam again; By generator, weak solution is concentrated, it is thermal source that generator adopts steam usually, and weak solution is heated again, and the rear solution of moisture evaporation in weak solution is concentrated, and keeps absorbability; The isolated steam of generator is undertaken indirectly cooling by cooling water in condenser, the water as refrigerant of liquefy enters the evaporimeter spray again, so moves in endless cycles.Therefore the external pipeline of lithium bromide refrigerator has chilled water import, chilled water outlet; Cooling water inlet, coolant outlet; Steam inlet, refrigeration machine condensation-water drain.
Summary of the invention
The object of the invention is to, overcome problems of the prior art, a kind of condensation water residual heat one effect flash evaporation natural air dehumidifying preheating and drying baking oven system is provided, degree of drying and the rate of drying that can guarantee material reach technological requirement, can improve the utilization ratio of steam again, reduce the energy consumption of unit product.
For solving above technical problem, condensation water residual heat one effect flash evaporation natural air dehumidifying preheating and drying baking oven system provided by the present invention, comprise the air drying oven, described air drying oven is provided with the baking oven air inlet, the baking oven gas outlet, wet stock import and dry material outlet, in baking oven, be provided with the coil heat exchanger group be formed in parallel by a plurality of coil heat exchangers, the import of each coil heat exchanger is connected with main steam pipe by steam stop respectively, the outlet of coil heat exchanger group is respectively equipped with drain valve, also comprise flash tank, lithium bromide refrigerator, the surface cool demister, air blast and air preheater, the drain valve outlet of each coil heat exchanger accesses respectively the high-temperature condensation water pipe, the outlet access flash tank diffusion of high-temperature condensation water pipe produces flash steam, flash steam enters the flash distillation steam pipe by the level pressure overflow valve of flash drum overhead, the steam inlet of the described lithium bromide refrigerator of outlet one tunnel access of described flash distillation steam pipe, another road is by the preheater air intake of the described air preheater of front pressure automatic regulating valve access, the chilled water outlet of lithium bromide refrigerator is connected with the cooler water inlet of described surface cool demister, and the cooler delivery port of surface cool demister is connected with the chilled water import of lithium bromide refrigerator, the humid air entrance of natural air access surface cool demister after air cleaner filters, the described air blast of dry air outlet access of surface cool demister, the air inlet of the described air preheater of outlet access of air blast, the baking oven air inlet of the described air drying oven of air outlet access of air preheater.
With respect to prior art, the present invention has obtained following beneficial effect: (1) in the present invention, coil heat exchanger is used main steam, the high-temperature condensation water access flash tank diffusion flash distillation of discharging, the pressure of flash steam is set by the level pressure overflow valve, its temperature and pressure is lower than main steam, and flash steam is sent to air preheater the air that enters baking oven is carried out to preheating, improves temperature and the moisture pick-up properties of air; (2) flash steam access lithium bromide refrigerator, realized the cascade utilization of waste heat, guarantees that heat energy eats dry bleeding, and totally kept the very high thermal efficiency.(3) the chilled water access surface cool demister that makes of lithium bromide refrigerator, the surface cool demister is united two into one and is formed by surface-cooler, demister, cryogenic freezing water enters surface-cooler, with the air of the surface-cooler of flowing through, carry out indirect heat exchange, the temperature of air is cooled to below dew-point temperature, airborne steam condenses into the globule, and flows into the Auto-drainage groove along the surface cooler wall, and the remaining water smoke of air quenched generation is caught and entered the Auto-drainage groove by demister; The cooled dry air that dehumidifies enters the inlet scoop of air blast, is sent to air preheater by air blast, and cooled drying-air temperature reduces, and density increases, and blower efficiency improves, and the unit air volume power consumption reduces; (4) air is after drying, and moisture significantly descends, and the dry air increased content, reduced air output, has also reduced the power consumption of air blast; (5) steam not only hinders the moisture absorption of air to material, reduces the moisture pick-up properties of air, self goes back after the heat that the absorption coil heat exchanger discharges as toxic emission, has wasted a large amount of heat energy; Air is after drying, and the water vapour amount be discharged in atmosphere after the coil heat exchanger heating descends, and the air exhaust heat loss significantly descends; (6) from air preheater dry air out, enter baking oven, because its temperature is high, water capacity is low, wettability power is strong, better to the drying effect of material; (7) quantity of steam that uses of air preheater is regulated by front pressure automatic regulating valve, to the pressure of steam supply of lithium bromide refrigerator during higher than setting value, and front pressure automatic regulating valve aperture increase, the flash steam amount increase of air supply preheater; During lower than setting value, front pressure automatic regulating valve aperture reduces to the pressure of steam supply of lithium bromide refrigerator, and the flash steam amount of air supply preheater reduces.
As preferred version of the present invention, the cryogenic condensation water of the preheater condensation-water drain of described air preheater, the refrigeration machine condensation-water drain of lithium bromide refrigerator and flash tank bottom all accesses condensate pump, described condensed water delivery side of pump access condensation water recovery system.Water base of cryogenic condensation does not have pressure, is pressurised into subcooled water by condensate pump, along the Cheng Buzai flash distillation, has avoided vapour locking; And condensate temperature is lower, in course of conveying, thermal loss is less.
As preferred version of the present invention, described condensate pump is the steam-operating condensate pump, and described main steam pipe is connected with the vapor interface of described steam-operating condensate pump by steam stop.Adopting the steam-operating condensate pump can make system of the present invention not rely on electric power can move.
As preferred version of the present invention, described coil heat exchanger group is provided with between many groups and each group parallel with one another in described baking oven.Can be according to the size of load, the group number that comes into operation of selective pan heat exchange of heat pipe group.
As preferred version of the present invention, the front and back of each described drain valve are respectively equipped with the condensed water stop valve.After opening the condensed water stop valve of drain valve front and back, drain valve is started working, and closes the condensed water stop valve of drain valve front and back, just can safeguard or change drain valve, does not affect the operation of system; Can also close simultaneously as required the steam stop of certain coil heat exchanger and the condensed water stop valve before and after drain valve, end the operation of this coil heat exchanger.
As preferred version of the present invention, the flash tank condensed water import of described flash tank also is connected with other heat exchanger drain valve outlet nearby.
The accompanying drawing explanation
The present invention is further detailed explanation below in conjunction with the drawings and specific embodiments, and accompanying drawing only provides reference and explanation use, non-in order to limit the present invention.
Fig. 1 is the schematic diagram of condensation water residual heat one effect flash evaporation natural air dehumidifying preheating and drying baking oven system of the present invention.
In figure: 1 main steam pipe; 2 air drying ovens; 2a baking oven air inlet; 2a ' baking oven gas outlet; The import of 2b wet stock; The outlet of 2b ' dry material; 3 coil heat exchangers; The 3a steam stop; The 3b drain valve; 3c condensed water stop valve; 4a high-temperature condensation water pipe; 4b cryogenic condensation water pipe; 5 flash tanks; The import of 5a flash tank condensed water; 5b level pressure overflow valve; Other condensed waters of 5c; 7 flash distillation steam pipes; Before 7a, press automatic regulating valve; 9 lithium bromide refrigerators; The import of 9a chilled water; 9a ' chilled water outlet; The 9b cooling water inlet; 9b ' coolant outlet; The 9c steam inlet; 9c ' refrigeration machine condensation-water drain; 10 cooling towers; 10a cooling tower upper hose; 10a ' cooling tower outlet pipe; 11 surface cool demisters; 11a cooler water inlet; 11a ' cooler delivery port; 11b humid air entrance; The outlet of 11b ' dry air; 11c Auto-drainage groove; 12 air cleaners; 13 air blasts; 14 air preheaters; The 14a air inlet; 14a ' air outlet; 14b preheater air intake; 14b ' preheater condensation-water drain; 15 condensate pumps; 15a pump vapor interface; 16 condensation water recovery systems.
The specific embodiment
Condensation water residual heat one of the present invention is imitated flash evaporation natural air dehumidifying preheating and drying baking oven system as shown in Figure 1, comprise air drying oven 2, flash tank 5, lithium bromide refrigerator 9, surface cool demister 11, air blast 13 and air preheater 14, air drying oven 2 is provided with baking oven air inlet 2a, baking oven gas outlet 2a ', wet stock import 2b and dry material outlet 2b '.In baking oven, be provided with the coil heat exchanger group, the coil heat exchanger group can, for one group, also can be organized parallel connection more.Each coil heat exchanger group is formed in parallel by a plurality of coil heat exchangers 3, the import of each coil heat exchanger 3 is connected with main steam pipe 1 by steam stop 3a respectively, the outlet of coil heat exchanger group is respectively equipped with drain valve 3b, and the front and back of each drain valve 3b are respectively equipped with condensed water stop valve 3c.
Each drain valve 3b outlet accesses respectively high-temperature condensation water pipe 4a, the flash tank condensed water import 5a of the outlet access flash tank 5 of high-temperature condensation water pipe 4a, higher other condensed waters 5c of temperature that other heat exchangers nearby produce also can enter effect flash tank 5 flash distillation utilizations.
The level pressure overflow valve 5b outlet at flash tank 5 tops enters flash distillation steam pipe 7, the steam inlet 9c of the outlet one tunnel access lithium bromide refrigerator 9 of flash distillation steam pipe 7, and another road is by the preheater air intake 14b of front pressure automatic regulating valve 7a access air preheater 14.The quantity of steam that air preheater 14 uses is regulated by front pressure automatic regulating valve 7a, to the pressure of steam supply of lithium bromide refrigerator 9 during higher than setting value, and front pressure automatic regulating valve 7a aperture increase, the flash steam amount increase of air supply preheater; During lower than setting value, front pressure automatic regulating valve 7a aperture reduces to the pressure of steam supply of lithium bromide refrigerator 9, and the flash steam amount of air supply preheater reduces.
The chilled water outlet 9a ' of lithium bromide refrigerator 9 is connected with the cooler water inlet 11a of surface cool demister 11, and the cooler delivery port 11a ' of surface cool demister 11 is connected with the chilled water import 9a of lithium bromide refrigerator 9; The heat that the heat that in lithium bromide refrigerator 9, steam-condensation discharges and chilled water cooling discharge is taken away by cooling water, the coolant outlet 9b ' of lithium bromide refrigerator 9 is connected with the cooling tower upper hose 10a of cooling tower 10, and cooling tower outlet pipe 10a ' is connected with the cooling water inlet 9b of lithium bromide refrigerator 9.
The humid air entrance 11b of the outlet access surface cool demister 11 of air cleaner 12, dry air outlet 11b ' the access air blast 13 of surface cool demister 11, the air inlet 14a of the outlet access air preheater 14 of air blast 13, the baking oven air inlet 2a of air outlet 14a ' the access air drying oven 2 of air preheater 14.
The cryogenic condensation water of the preheater condensation-water drain 14b ' of air preheater 14, the refrigeration machine condensation-water drain 9c ' of lithium bromide refrigerator 9 and flash tank 5 bottoms is respectively by cryogenic condensation water pipe 4b access condensate pump 15, and the outlet of condensate pump 15 accesses condensation water recovery system 16.Condensate pump 15 is preferably the steam-operating condensate pump, and main steam pipe 1 is connected with the pump vapor interface 15a of steam-operating condensate pump by steam stop.
During work, natural air enters surface cool demister 11 after air cleaner 12 filters, surface cool demister 11 is united two into one and is formed by surface-cooler, demister, cryogenic freezing water enters surface-cooler, with the air of the surface-cooler of flowing through, carry out indirect heat exchange, the temperature of air is cooled to below dew-point temperature, airborne steam condenses into the globule, and flowing into Auto-drainage groove 11c along the surface cooler wall, the remaining water smoke of air quenched generation is caught and is entered Auto-drainage groove 11c by demister.Cold air after drying is sent into air preheater 14 by air blast 13, air after preheating enters baking oven, the flow through outer surface of each coil heat exchanger 3, through with steam heat-exchanging after, temperature further raises, hot-air and moist material carry out the wet exchange of heat, from baking oven gas outlet 2a ', flow out after taking away the moisture of wet stock, realize the oven dry of material.
In air drying oven 2, when vapor stream is crossed each coil heat exchanger 3 and air heat-exchange and after discharging latent heat, be condensed into the high-temperature condensation water under uniform pressure, high-temperature condensation water enters total condensate pipe through each drain valve 3b, then enter flash tank 5 diffusions and produce flash steam, flash steam enters air preheater 14 by the rear road of level pressure overflow valve 5b outflow at flash tank 5 tops, and another road enters lithium bromide refrigerator 9.The cryogenic condensation water that air preheater 14, lithium bromide refrigerator 9 and flash tank 5 produce pumps into condensation water recovery system 16 by condensate pump 15 respectively.
As described above, only for the present invention's better possible embodiments, non-so limit to the scope of the claims of the present invention, in addition to the implementation, the present invention can also have other embodiments, for example, air heater is set before air blast, from out high-temperature cooling water lithium bromide refrigerator, at first deliver to air heater, in air heater, high-temperature cooling water and cold air carry out indirect heat exchange, the temperature of cold air is promoted, and after the high-temperature cooling water release heat, temperature descends, enter again cooling tower cooling, cooling water after the cooling tower cooling flows out from the cooling tower outlet pipe, reenter the cooling water inlet of lithium bromide refrigerator, air heater had both reclaimed the waste heat of high-temperature cooling water, the cold air temperature is got a promotion, alleviated again the load of cooling tower, strengthened the cooling water outlet and inlet temperature difference of lithium bromide refrigerator, reduced the power consumption of blower fan of cooling tower, can alleviate the power consumption of cooling water circulating pump again.All employings are equal to the technical scheme of replacement or equivalent transformation formation, all drop in the protection domain of requirement of the present invention.

Claims (6)

1. a condensation water residual heat one is imitated flash evaporation natural air dehumidifying preheating and drying baking oven system, comprise the air drying oven, described air drying oven is provided with the baking oven air inlet, the baking oven gas outlet, wet stock import and dry material outlet, in baking oven, be provided with the coil heat exchanger group be formed in parallel by a plurality of coil heat exchangers, the import of each coil heat exchanger is connected with main steam pipe by steam stop respectively, the outlet of coil heat exchanger group is respectively equipped with drain valve, it is characterized in that: also comprise flash tank, lithium bromide refrigerator, the surface cool demister, air blast and air preheater, the drain valve outlet of each coil heat exchanger accesses respectively the high-temperature condensation water pipe, the outlet access flash tank diffusion of high-temperature condensation water pipe produces flash steam, flash steam enters the flash distillation steam pipe by the level pressure overflow valve of flash drum overhead, the steam inlet of the described lithium bromide refrigerator of outlet one tunnel access of described flash distillation steam pipe, another road is by the preheater air intake of the described air preheater of front pressure automatic regulating valve access, the chilled water outlet of lithium bromide refrigerator is connected with the cooler water inlet of described surface cool demister, and the cooler delivery port of surface cool demister is connected with the chilled water import of lithium bromide refrigerator, the humid air entrance of natural air access surface cool demister after air cleaner filters, the described air blast of dry air outlet access of surface cool demister, the air inlet of the described air preheater of outlet access of air blast, the baking oven air inlet of the described air drying oven of air outlet access of air preheater.
2. condensation water residual heat one according to claim 1 is imitated flash evaporation natural air dehumidifying preheating and drying baking oven system, it is characterized in that: the cryogenic condensation water of the preheater condensation-water drain of described air preheater, the refrigeration machine condensation-water drain of lithium bromide refrigerator and flash tank bottom all accesses condensate pump, described condensed water delivery side of pump access condensation water recovery system.
3. condensation water residual heat one according to claim 2 is imitated flash evaporation natural air dehumidifying preheating and drying baking oven system, it is characterized in that: described condensate pump is the steam-operating condensate pump, and described main steam pipe is connected with the vapor interface of described steam-operating condensate pump by steam stop.
4. condensation water residual heat according to claim 1 one effect flash evaporation natural air dehumidifying preheating and drying baking oven system is characterized in that: described coil heat exchanger group is provided with between many groups and each group parallel with one another in described baking oven.
5. condensation water residual heat one according to claim 1 is imitated flash evaporation natural air dehumidifying preheating and drying baking oven system, and it is characterized in that: the front and back of each described drain valve are respectively equipped with the condensed water stop valve.
6. according to the described condensation water residual heat one effect flash evaporation natural air dehumidifying preheating and drying baking oven system of any one in claim 1 to 5, it is characterized in that: the flash tank condensed water import of described flash tank also is connected with other heat exchanger drain valve outlet nearby.
CN2011104471077A 2011-12-28 2011-12-28 Condensation water residual heat first-effect flash evaporation natural air dehumidifying, preheating and drying baking oven system Active CN102506564B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011104471077A CN102506564B (en) 2011-12-28 2011-12-28 Condensation water residual heat first-effect flash evaporation natural air dehumidifying, preheating and drying baking oven system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011104471077A CN102506564B (en) 2011-12-28 2011-12-28 Condensation water residual heat first-effect flash evaporation natural air dehumidifying, preheating and drying baking oven system

Publications (2)

Publication Number Publication Date
CN102506564A CN102506564A (en) 2012-06-20
CN102506564B true CN102506564B (en) 2013-11-27

Family

ID=46218675

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011104471077A Active CN102506564B (en) 2011-12-28 2011-12-28 Condensation water residual heat first-effect flash evaporation natural air dehumidifying, preheating and drying baking oven system

Country Status (1)

Country Link
CN (1) CN102506564B (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102889577B (en) * 2012-10-17 2014-05-14 亿恒节能科技江苏有限公司 External dry steam flash evaporation two-effect heat exchange system
CN102901086B (en) * 2012-10-17 2014-04-23 亿恒节能科技江苏有限公司 Internal dried steam three-effect heat exchange system
CN102889579B (en) * 2012-10-17 2014-04-23 亿恒节能科技江苏有限公司 Inner drying steam flash evaporating double-effect heat exchanging system
CN102889576B (en) * 2012-10-17 2014-04-23 亿恒节能科技江苏有限公司 Low-humidity steam double-effect heat exchange system
CN104082887B (en) * 2014-07-30 2015-10-21 山东宏信化工股份有限公司 PVC plastic Rubber gloves preparation drying unit
CN109029045A (en) * 2018-07-17 2018-12-18 九三粮油工业集团有限公司 A kind of tempering tower high-temperature condensation water efficient heat energy is using system and utilizes method
CN112082398A (en) * 2020-09-08 2020-12-15 苏州弘大光电节能科技有限公司 Induced injection type waste heat step recovery device based on predictive control

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1393434A (en) * 1971-03-22 1975-05-07 Deuterium Corp Process feed and effluent treating systems
CN1050603A (en) * 1990-09-19 1991-04-10 江阴市溴化锂制冷机厂 Water cooling system for lithium bromide absorbing style refrigerator
CN2110835U (en) * 1991-03-13 1992-07-22 苏州振亚丝织厂 Lithium bromide absorption type refrigerator
CN202485343U (en) * 2011-12-28 2012-10-10 亿恒节能科技江苏有限公司 Primary-effective flash natural air dehydrating, preheating and drying oven device by using condensate water waste heat

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1393434A (en) * 1971-03-22 1975-05-07 Deuterium Corp Process feed and effluent treating systems
CN1050603A (en) * 1990-09-19 1991-04-10 江阴市溴化锂制冷机厂 Water cooling system for lithium bromide absorbing style refrigerator
CN2110835U (en) * 1991-03-13 1992-07-22 苏州振亚丝织厂 Lithium bromide absorption type refrigerator
CN202485343U (en) * 2011-12-28 2012-10-10 亿恒节能科技江苏有限公司 Primary-effective flash natural air dehydrating, preheating and drying oven device by using condensate water waste heat

Also Published As

Publication number Publication date
CN102506564A (en) 2012-06-20

Similar Documents

Publication Publication Date Title
CN102506564B (en) Condensation water residual heat first-effect flash evaporation natural air dehumidifying, preheating and drying baking oven system
CN102445066B (en) Natural air dehydrating and preheating drying oven system adopting condensate water waste heat for two-effect flash evaporation
CN202452808U (en) Dehumidified and preheated natural air drying oven device utilizing condensed water waste heat second-effect flashing
CN204063414U (en) A kind of heat pump drives pre-cold mould solution humidifying Fresh air handling units
CN106091187A (en) The low-temperature heat source absorption coupling air-conditioning device of a kind of dehumidification solution condensation heat regeneration and regulation and control method
CN107014015B (en) Recovery type heat evaporating condensation type handpiece Water Chilling Units
CN101666576A (en) Heat pump cyclic medium dehumidification curing barn
CN207738619U (en) A kind of sludge drying system with total heat recovery case
CN105841257A (en) Compression-type refrigeration and solution regeneration and dehumidification coupled air-conditioning system
CN202485343U (en) Primary-effective flash natural air dehydrating, preheating and drying oven device by using condensate water waste heat
CN203116193U (en) Water chilling unit with combined direct-type evaporative coolers and evaporative condenser
CN201138102Y (en) Novel return energy recovery heat pump device with secondary humidifying cooling condenser
CN201807261U (en) Environmental emission reduction type gas dehumidification dust removal machine
CN206669949U (en) Recovery type heat evaporating condensation type handpiece Water Chilling Units
CN107782125A (en) A kind of adaptive, self-interacting type heat pump hot blast stove system
CN201488479U (en) Cyclic medium dehumidification barn for heat pumpdehumidification
CN208000031U (en) A kind of heat pump hot-blast stove structure
CN206339064U (en) Pump type heat vermicelli drying equipment
CN206488527U (en) Dew point intelligent control refrigerator
CN202452514U (en) Gas and air independent dehumidification and heating device with gas circulation and waste gas refrigeration
CN102425802B (en) Air blowing dehumidifying and heating steam boiler system with deaerator
CN202371744U (en) Blast dehumidifying heating steam boiler device
CN107537167A (en) Evaporating, concentrating and crystallizing system and evaporation process method
CN202371743U (en) Blast dehumidifying heating steam boiler device with deaerator
CN106524717A (en) Heat pump type vermicelli drying equipment and method for vermicelli drying

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant