CN206160335U - Responsibility is dodged all to whole energy -saving heat - Google Patents

Responsibility is dodged all to whole energy -saving heat Download PDF

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Publication number
CN206160335U
CN206160335U CN201621063216.3U CN201621063216U CN206160335U CN 206160335 U CN206160335 U CN 206160335U CN 201621063216 U CN201621063216 U CN 201621063216U CN 206160335 U CN206160335 U CN 206160335U
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CN
China
Prior art keywords
fresh air
air
waste gas
heating
whole energy
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn - After Issue
Application number
CN201621063216.3U
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Chinese (zh)
Inventor
黄鹏
林涛
刘天力
王升建
韩俊
刘皓
赵学政
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.)
China Automobile Industry Engineering Co Ltd
Scivic Engineering Corp
Original Assignee
China Automobile Industry Engineering Co Ltd
Scivic Engineering Corp
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Publication date
Application filed by China Automobile Industry Engineering Co Ltd, Scivic Engineering Corp filed Critical China Automobile Industry Engineering Co Ltd
Priority to CN201621063216.3U priority Critical patent/CN206160335U/en
Application granted granted Critical
Publication of CN206160335U publication Critical patent/CN206160335U/en
Withdrawn - After Issue legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a responsibility is dodged all to whole energy -saving heat, including heating dehydrating unit, strong cold charge is put, and the heat pump, heating dehydrating unit including the heating mechanism with the dehumidification rotor machine, the new trend intake stack process of heating mechanism the processing region of dehumidification rotor machine after the intercommunication extremely the new trend of heating mechanism mend the entry, regeneration zone and the flue gas waste heat reutilization mechanism intercommunication of dehumidification rotor machine. The utility model discloses all dehumidify to the new trend with cold water coiler to the present responsibility of dodging, the new trend water capacity is still higher, needs the higher temperature and the amount of wind to reach dewater the futilely defect of demand of sudden strain of a muscle, and the wheel style dehumidification method that will dehumidify is arranged in dodging responsibility new trend all and mends the mechanism, reduces to dodge and does the temperature and practiced thrift natural gas consumption, reduces the energy consumption that the amount of wind has just also reduced the fan, can reduce preliminary investment with quaternary littleer that the heating cabinet did of personally experiencing sth. Part of the body simultaneously.

Description

Whole energy type heat-lightening dry systems
Technical field
The utility model is related to dodge dry dehumidification air conditioner technical field, more particularly to a kind of whole energy type heat-lightening responsibility System.
Background technology
It is the process conditions for meeting water paint with the appearance of the vehicle coating process such as water paint, the dry equipment of heat-lightening becomes The indispensable part of Painting Shop.Heating and dehumidification device is the important device dodged in dry equipment, and heating and dehumidification device is profit Heating and dehumidification is carried out with the circulated air of predetermined high temperature, while the fresh air supplement of scheduled volume is carried out in circulated air to reduce circulated air Humidity, improve the dry effect of heat, be to reduce the water content in fresh air, general using dehumidifying surface cooler in prior art, this is just needed First cool-down dehumidification carried out to fresh air, then reheat and heat up, cause overall energy consumption loss big.
Utility model content
The purpose of this utility model is to be directed to technological deficiency present in prior art, and provides a kind of whole energy type heat Dodge dry systems.
To realize that the technical scheme that the purpose of this utility model is adopted is:
A kind of whole energy type heat-lightening dry systems, including heating and dehumidification device, strong device for cooling, and heat pump, described adds Hot dehydrating unit includes heating arrangements and desiccant wheel machine, and the fresh air intake stack of described heating arrangements is through described dehumidifying The fresh air that described heating arrangements are communicated to after the processing region of rotor machine fills into mouth, the regeneration zone of described desiccant wheel machine Mechanism connection is recycled with fume afterheat,
The evaporimeter string of described heat pump is located on the strong SAPMAC method wind path of described strong device for cooling, described heat pump it is cold Condenser is arranged on fresh air and fills on pipeline and be located at desiccant wheel machine rear portion;
Described fume afterheat recycle mechanism include the high-temperature exhaust emission mouth of the described heating arrangements of connection with it is described Desiccant wheel machine regeneration zone high-temp waste gas pipe, side is connected on the fresh air temperature adjustment pipe on described high-temp waste gas pipe, arranges In the temperature sensor of regeneration zone air inlet side, and on the fresh air temperature adjustment pipe and high-temp waste gas pipe described in being separately positioned on simultaneously With the fresh air regulating valve and waste gas regulating valve of the described controllable connection of temperature sensor.
Cooling chamber is serially connected with described strong SAPMAC method wind path, described cooling interior sets successively from return side to air side It is equipped with strong cold return fan, evaporimeter and filter.
Described fresh air fills into pipeline and is provided with fresh air preheating room, and described fresh air preheating room is disposed with from inlet side Filter condenser and fresh-air fan, the air outlet of described fresh-air fan is connected to fresh air and fills into pipeline.
Bypass pipe has been arranged in parallel in described condenser side.
Described fresh air temperature adjustment pipe is located at described waste gas regulating valve rear portion with the access point of high-temp waste gas pipe.
Described waste gas regulating valve is triple valve, and one of valve port is connected to floss hole by discharge pipe.
Compared with prior art, the beneficial effects of the utility model are:
The utility model for it is existing sudden strain of a muscle dry systems fresh air is dehumidified with chilled water coil, fresh air water capacity still compared with Height, the higher temperature of needs and air quantity reach the defect for dodging dry dehydration demand, and desiccant wheel formula dehumanization method is used to dodge responsibility The fresh air of system is filled in mechanism, can be by fresh air inlet humid control in 3g/m3Hereinafter, reduce dodging the feelings of dry temperature and ventilation volume Meet under condition and dodge dry dehydration demand, save equipment operation energy consumption.And because humidity is reduced, also will dodge the temperature of dry circulated air from 70-80 degree Celsius is reduced to 50-60 degree Celsius, furthermore achieved that energy-saving and emission-reduction, and the dry temperature of reduction sudden strain of a muscle has been saved natural gas and disappeared Consumption, reduces air quantity and also just reduces the energy consumption of blower fan, at the same can by quaternary body heater box do it is less, reduce preliminary throwing Money, further, because dodging the reduction of dry temperature, can reduce air quantity and the time of strong cold step then, realize interlock type Energy-saving and emission-reduction, reduce overall cost.
Description of the drawings
Fig. 1 show the structural representation of whole energy type heat-lightening dry systems of the present utility model.
Specific embodiment
The utility model is described in further detail below in conjunction with the drawings and specific embodiments.It should be appreciated that this place The specific embodiment of description only to explain the utility model, is not used to limit the utility model.
As shown in figure 1, whole energy type heat-lightening dry systems of the present utility model include heating and dehumidification device 50 and strong cold charge 60 are put, described heating and dehumidification device includes heating arrangements 40 and desiccant wheel machine 30, described heating arrangements are quaternary body, are used In heating to fresh air and circulated air, the fresh air intake stack of described heating arrangements is through described desiccant wheel machine The fresh air that described heating arrangements are communicated to behind dehumidification treatments region fills into mouth, the regeneration zone of described desiccant wheel machine with High temperature desorbs gas connection.
Wherein, described high temperature desorbs gas and can be supplied by supporting independent burner, and temperature adjustment is possible with certainly The waste gas of heating arrangements afterwards.To realize that waste gas is recycled, then fume afterheat is needed to recycle mechanism, described fume afterheat is again Include the high-temperature exhaust emission mouth of the described heating arrangements 40 of connection and the regeneration zone of described desiccant wheel machine using mechanism 32 high-temp waste gas pipe 41, side is connected on the fresh air temperature adjustment pipe 42 on described high-temp waste gas pipe, is arranged on the air inlet of regeneration zone 32 Pass on the temperature sensor of mouth side, and the fresh air temperature adjustment pipe and high-temp waste gas pipe described in being separately positioned on and with described temperature The fresh air regulating valve and waste gas regulating valve of the controllable connection of sensor, such as electrically-controlled valve.
Preferably, it is to improve temperature control controlling, described fresh air temperature adjustment pipe is located at described with the access point of high-temp waste gas pipe Waste gas regulating valve rear portion.Meanwhile, described waste gas regulating valve is triple valve, and one of valve port is connected to row by discharge pipe Put mouth.That is, according to the feedback of temperature sensor, a selected part high-temp waste gas mixes with indoor fresh air.
The utility model is effectively utilized high-temp waste gas, and the fresh air mixed with high-temp waste gas can rely on completely regeneration The regeneration blower fan suction of side, without being separately provided blower fan, further control realization cost and simplify control.
The utility model for it is existing sudden strain of a muscle dry systems fresh air is dehumidified with chilled water coil, fresh air water capacity still compared with Height, the higher temperature of needs and air quantity reach the defect for dodging dry dehydration demand, and desiccant wheel formula dehumanization method is used to dodge responsibility The fresh air of system is filled in mechanism, can be by fresh air inlet humid control in 3g/m3Hereinafter, reduce dodging the feelings of dry temperature and ventilation volume Meet under condition and dodge dry dehydration demand, save equipment operation energy consumption.And because humidity is reduced, also will dodge the temperature of dry circulated air from 70-80 degree Celsius is reduced to 50-60 degree Celsius, furthermore achieved that energy-saving and emission-reduction, and the dry temperature of reduction sudden strain of a muscle has been saved natural gas and disappeared Consumption, reduces air quantity and also just reduces the energy consumption of blower fan, at the same can by quaternary body heater box do it is less, reduce preliminary throwing Money, further, because dodging the reduction of dry temperature, can reduce air quantity and the time of strong cold step then, realize interlock type Energy-saving and emission-reduction, reduce overall cost.Using heating arrangements, the clean high-temp waste gas as produced by quaternary body burning turn as dehumidifying The regeneration thermal source of turbine, realize will dodge dry systems in quaternary body discharge fume afterheat use in desiccant wheel, realize The energy makes full use of.Simultaneously as desiccant wheel regeneration heat source temperature is 115 DEG C or so, and flue gas after quaternary body combustion heat-exchange For 200 DEG C or so, the utility model regulates and controls by way of fresh air is filled into flue-gas temperature, and regeneration side air is effectively ensured Temperature constant, it is ensured that the normal operation of desiccant wheel machine.
Used as further improvement, heat-lightening dry systems of the present utility model also include heat pump 20, the evaporation of described heat pump 20 The string of device 4 is located on the strong SAPMAC method wind path 61 of described strong device for cooling, and the condenser 3 of described heat pump 20 is arranged on heating and dehumidification The fresh air of device is filled on pipeline 51.Wherein, heat pump itself similarly to the prior art, herein by the evaporimeter and condenser of heat pump Heat interaction made substantive application, using the transfer of heat, at the same realize cooling and heating need, effectively increase Overall energy use level.
Specifically, it is serially connected with cooling chamber on described strong SAPMAC method wind path, described cooling is indoor from return side to going out Wind side is disposed with strong cold return fan 21, evaporimeter 4 and filter 22, and described strong SAPMAC method wind path Jing air-valves 5 enter strong Cold section 60 of both sides with carry out heat-lightening it is dry after strong cold operation.Meanwhile, described fresh air fills into pipeline 51 through above-mentioned dehumidifying The processing region of runner carries out entering fresh air preheating room after dehumidification treatments, and described fresh air preheating room is disposed with from inlet side Filter 52, condenser 3 and fresh-air fan 53, the air outlet of described fresh-air fan is connected to fresh air and fills into mouth.Fresh air Addition first passes through preheating through condenser again after dehumidifying, effectively reduces the requirement of later stage heating, realizes the total of heat Body distributes and effective use.Wherein, it has been arranged in parallel bypass pipe to be used as maintenance in described condenser side.
That is, handpiece Water Chilling Units, the evaporimeter of heat pump are replaced to be arranged into inside strong device for cooling, make with one or more heat pump assembly Cold-producing medium and strong cold air-supply direct heat transfer are obtained, strong cold air-supply 15 DEG C is reduced to into by 30 DEG C, in addition the condenser cloth of heat pump assembly Put heat-lightening to do inside new air heating device, the heat produced using heat pump assembly dodges dry fresh air.
In sum, the utility model has advantages below:
(1) cooling of strong cold air-supply is completed by heat pump assembly evaporimeter so that strong cold air-supply and cold-producing medium direct heat transfer, is steamed Sending out temperature can improve to 8 DEG C, reduce heat transfer temperature difference, increased heat exchange efficiency.
(2) heat that heat pump assembly is produced is not wasted, but is used in new air heating device.
(3) heat pump assembly replaces handpiece Water Chilling Units, freezing water circulation, the expense of control is saved, while saving tradition side The expense of combustor in the new air heating device of case.
Parameter comparison, for traditional scheme, 0 DEG C of handpiece Water Chilling Units evaporating temperature, 45 DEG C of condensation temperature is cold due to only make use of Amount, heat is drained under outdoor, therefore the operating mode via cooling tower, and the calculating coefficient of performance EER of handpiece Water Chilling Units (freeze by handpiece Water Chilling Units The ratio of amount and compressor wasted work) (do not contain chilled water circulating pump, cooling tower energy consumption, if counting, the performance system for 3.2 Can be lower), and, source pump evaporating temperature 8 DEG C new for this application, 60 DEG C of condensation temperature, because the system both make use of Source pump refrigerating capacity make use of under source pump heating capacity, therefore the operating mode again, the calculating coefficient of performance EER of source pump (ratio of source pump refrigerating capacity and heating capacity) is 6.4.
With strong cold air output 50000Nm3/ h, resh air requirement 25000Nm3As a example by/h, the energy input of traditional scheme is:Cooling-water machine Group power consumption is 20.2kwh, and it is 405.3kwh that combustor adds thermal energy consumption;And apply after the utility model, the energy consumption of whole system Measure as 73.4kwh, realize the requirement of energy-saving and emission-reduction.
In sum, desiccant wheel is used for the utility model the dehumidifying of fresh air, humidity is effectively reduced, using heating arrangements Relative clean burning waste gas temperature adjustment after desorb high-temperature gas as desiccant wheel, meanwhile, strong cold section is put using heat pump The heat for going out is transferred to fresh air bringing-up section, and 3 points be combined with each other, and effectively reduces the dry circulation air temperature of heat-lightening, internal circulating load and new The wind amount of filling into, is reduced to strong cold blast rate, the requirement of strong cold wind temperature, realizes the global optimization configuration of the energy, substantially reduces energy Consumption, it is cost-effective.
The above is only preferred embodiment of the present utility model, it is noted that general for the art For logical technical staff, on the premise of without departing from the utility model principle, some improvements and modifications can also be made, these change Enter and retouch also to should be regarded as protection domain of the present utility model.

Claims (6)

1. a kind of whole energy type heat-lightening dry systems, it is characterised in that including heating and dehumidification device, strong device for cooling, and heat pump, Described heating and dehumidification device includes heating arrangements and desiccant wheel machine, and the fresh air intake stack of described heating arrangements is through institute The fresh air that described heating arrangements are communicated to after the processing region of the desiccant wheel machine stated fills into mouth, described desiccant wheel machine Regeneration zone recycles mechanism connection with fume afterheat,
The evaporimeter string of described heat pump is located on the strong SAPMAC method wind path of described strong device for cooling, the condenser of described heat pump It is arranged on fresh air and fills on pipeline and be located at desiccant wheel machine rear portion;
Described fume afterheat recycles mechanism to include that the high-temperature exhaust emission mouth of the described heating arrangements of connection is removed with described The high-temp waste gas pipe of the regeneration zone of wet rotor machine, side is connected on the fresh air temperature adjustment pipe on described high-temp waste gas pipe, is arranged on again The temperature sensor of raw region air inlet side, and be separately positioned on described fresh air temperature adjustment pipe and high-temp waste gas pipe and with institute The fresh air regulating valve and waste gas regulating valve of the controllable connection of temperature sensor stated.
2. whole energy type heat-lightening dry systems as claimed in claim 1, it is characterised in that go here and there on described strong SAPMAC method wind path Cooling chamber is connected to, described cooling is indoor to be disposed with strong cold return fan, evaporimeter and filter from return side to air side.
3. whole energy type heat-lightening dry systems as claimed in claim 2, it is characterised in that described fresh air fills into pipeline setting There is fresh air preheating room, described fresh air preheating room is disposed with filter condenser and fresh-air fan from inlet side, described The air outlet of fresh-air fan be connected to fresh air and fill into pipeline.
4. whole energy type heat-lightening dry systems as claimed in claim 2, it is characterised in that in parallel in described condenser side It is provided with bypass pipe.
5. whole energy type heat-lightening dry systems as claimed in claim 1, it is characterised in that described fresh air temperature adjustment pipe and high temperature The access point of flue gas leading is located at described waste gas regulating valve rear portion.
6. whole energy type heat-lightening dry systems as claimed in claim 1, it is characterised in that described waste gas regulating valve is threeway Valve, one of valve port is connected to floss hole by discharge pipe.
CN201621063216.3U 2016-09-20 2016-09-20 Responsibility is dodged all to whole energy -saving heat Withdrawn - After Issue CN206160335U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621063216.3U CN206160335U (en) 2016-09-20 2016-09-20 Responsibility is dodged all to whole energy -saving heat

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621063216.3U CN206160335U (en) 2016-09-20 2016-09-20 Responsibility is dodged all to whole energy -saving heat

Publications (1)

Publication Number Publication Date
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Country Status (1)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106288090A (en) * 2016-09-20 2017-01-04 中国汽车工业工程有限公司 Whole energy type heat-lightening dry systems

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106288090A (en) * 2016-09-20 2017-01-04 中国汽车工业工程有限公司 Whole energy type heat-lightening dry systems
CN106288090B (en) * 2016-09-20 2021-12-17 中国汽车工业工程有限公司 Integral energy-saving type hot flash drying system

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AV01 Patent right actively abandoned
AV01 Patent right actively abandoned
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Granted publication date: 20170510

Effective date of abandoning: 20211217

AV01 Patent right actively abandoned

Granted publication date: 20170510

Effective date of abandoning: 20211217