CN206372691U - A kind of spraying/baking vanish/painting exhaust-gas efficient condensation heat-energy secondary utilizes and handles recovery system - Google Patents
A kind of spraying/baking vanish/painting exhaust-gas efficient condensation heat-energy secondary utilizes and handles recovery system Download PDFInfo
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- CN206372691U CN206372691U CN201621299747.2U CN201621299747U CN206372691U CN 206372691 U CN206372691 U CN 206372691U CN 201621299747 U CN201621299747 U CN 201621299747U CN 206372691 U CN206372691 U CN 206372691U
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- absorbent charcoal
- charcoal adsorber
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- heat exchanger
- condenser
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Abstract
The utility model is related to a kind of spraying/baking vanish/painting exhaust-gas efficient condensation heat-energy secondary using recovery system is handled, and includes exhaust gas discharge conduit, an absorbent charcoal adsorber is set on exhaust gas discharge conduit；Main switching valve is equipped with the air intake vent and air outlet of absorbent charcoal adsorber；A condenser is set in absorbent charcoal adsorber one end, the other end sets a heat exchanger, described absorbent charcoal adsorber, hot blast conveying pipe interconnection is respectively equipped between condenser and heat exchanger, when main switching valve closes the air intake vent and air outlet of absorbent charcoal adsorber, the heat energy that heat exchanger obtains condenser cooling recovery waste gas organic matter generation by hot blast conveying pipe is delivered in absorbent charcoal adsorber, waste gas harmful substance to absorption is separated, then condenser is delivered to again to carry out cooling down the recovery that is in a liquid state rapidly, condenser, which cools down rapidly the heat of generation and is conveyed to heat exchanger by hot blast conveying pipe and is converted into heat energy, to be reused, the utility model not only has good energy-saving effect, also there is significant desorption effect.
Description
Technical field
The utility model is related to a kind of exhaust treatment system, and in particular to be used to spray/baking vanish/painting waste gas height in one kind
Imitate condensation process recovery system.
Background technology
In industry manufacture, the organic exhaust gas produced in the technique productions of spraying/baking vanish/painting is especially prominent, serious shadow
Ring our living environment.At present, it is usually to be carried out using absorption organic exhaust gas at recovery to commonly use effective waste gas processing method
Reason.And existing adsorption method is only that organic exhaust gas is carried out into adsorption and desorption processing using adsorbent equipment to reclaim, it is desorbed logical
It is often that cooling treatment recovery is carried out using condenser, but because the organic exhaust gas that adsorbent equipment is adsorbed is difficult to separate, causes absorption
It is easily saturated, so as to influence adsorption effect, causes organic exhaust gas to recycle effect unsatisfactory.
Utility model content
The purpose of this utility model is, in order to solve existing spraying/baking vanish/painting VOCs treatment reclaim exist it is above-mentioned
Technical problem there is provided a kind of spraying/baking vanish/painting exhaust-gas efficient condensation heat-energy secondary using handling recovery system.
A kind of spraying/baking vanish/painting exhaust-gas efficient condensation the heat-energy secondary for solving the utility model purpose is utilized and handled back
Receipts system, includes exhaust gas discharge conduit, sets an absorbent charcoal adsorber to adsorb waste gas discharge on exhaust gas discharge conduit logical
The waste gas organic matter of road discharge；Main switching valve is equipped with the air intake vent and air outlet of absorbent charcoal adsorber, the main switching valve
For closing or opening the ventilating duct in absorbent charcoal adsorber；A condenser, the other end are set in absorbent charcoal adsorber one end
If a heat exchanger, hot blast conveying pipe interconnection is respectively equipped between described absorbent charcoal adsorber, condenser and heat exchanger,
When main switching valve closes the air intake vent and air outlet of absorbent charcoal adsorber, heat exchanger obtains condenser by hot blast conveying pipe
The heat energy that the generation of waste gas organic matter is reclaimed in cooling is delivered in absorbent charcoal adsorber, useless to what is adsorbed in absorbent charcoal adsorber
Gas harmful substance is separated, and condenser is then delivered to again and carries out cooling down the recovery that is in a liquid state rapidly, condenser cools down rapidly production
Raw heat, which is conveyed to heat exchanger by hot blast conveying pipe and is converted into heat energy, to be reused, and is consequently formed the height that heat-energy secondary is utilized
Imitate exhaust-gas treatment recovery system.
Further, the heat energy of the heat exchanger enters absorbent charcoal adsorber in the air outlet of absorbent charcoal adsorber
Interior, the waste gas harmful substance in the absorbent charcoal adsorber is emitted into condenser in the air inlet of absorbent charcoal adsorber and carried out
Liquid is reclaimed, and the heat energy of heat exchanger is inversely delivered in absorbent charcoal adsorber, forms reverse in absorbent charcoal adsorber
It is desorbed waste gas harmful substance function.
Further, described heat exchanger is provided with the steam for being connected to spraying, baking vanish or/and painting high pressure vapor line
Pipe, the steam pipe introduces spraying, baking vanish or/and painting high pressure when heat exchanger heat supply temperature does not reach requirement by steam pipe
Steam heat, is changed, the desorption requirement for making it meet waste gas organic matter in absorbent charcoal adsorber with the heat energy for increasing heat exchanger.
Further, described high-efficiency condensation processing unit also includes a temperature controller, and the temperature controller, which is used to detect, to be condensed
The cryogenic temperature of device, the discharge thermal temperature of heat exchanger or/and the waste gas organic matter desorption temperature of absorbent charcoal adsorber, cold
Condenser cryogenic temperature automatically adjusts the operation power of condenser when too low or too high, in heat exchanger or absorbent charcoal adsorber temperature
The thermal energy conversion rate of heat exchanger is automatically adjusted when too low or too high.
Further, the hot blast conveying pipe between described condenser and heat exchanger is provided with desorption blower fan, the desorption wind
Machine is used to increase the speed of hot air circulation in exhaust treatment system.
Further, an apparatus for low-temperature plasma treatment or/and photocatalyst are additionally provided with described exhaust gas discharge conduit
Catalysis system, the apparatus for low-temperature plasma treatment or/and photocatalyst catalysis system are located at the air outlet of absorbent charcoal adsorber
One end.
Further, the hot blast conveying pipe being connected with each other between described condenser, heat exchanger and absorbent charcoal adsorber
With auxiliary switching valve is equipped with steam pipe, the auxiliary switching valve or/main switching valve are automatically controlled autocontrol valve, pass through and set one
Master controller automatically controls open and close function.
The utility model has substantive distinguishing features following prominent and significant progressive：
1st, heat exchanger of the present utility model obtains condenser cooling by hot blast conveying pipe and reclaims what waste gas organic matter was produced
Heat energy is delivered in absorbent charcoal adsorber, the waste gas harmful substance adsorbed in absorbent charcoal adsorber is separated, then
It is delivered to condenser again to carry out cooling down the recovery that is in a liquid state rapidly, the heat that condenser cools down rapidly generation is defeated by hot blast conveying pipe
Give heat exchanger and be converted into heat energy and reuse, be consequently formed the efficiency of waste gas processing recovery system that heat-energy secondary is utilized.Thus
It can be seen that, the heat that the utility model makes full use of condenser cooling treatment waste gas organic matter to produce is converted to absorbent charcoal adsorber
Desorption heat energy, make its not only have good energy-saving effect, also with significant desorption effect.
2nd, the heat energy of heat exchanger of the present utility model enters absorbent charcoal adsorber in the air outlet of absorbent charcoal adsorber
Interior, the waste gas harmful substance in the absorbent charcoal adsorber is emitted into condenser in the air inlet of absorbent charcoal adsorber and carried out
Liquid is reclaimed, and the heat energy of heat exchanger is inversely delivered in absorbent charcoal adsorber, forms reverse in absorbent charcoal adsorber
It is desorbed waste gas harmful substance function.Thus, the waste gas harmful substance in absorbent charcoal adsorber passes through reverse heat energy (i.e. hot blast)
Blow so that waste gas harmful substance is more prone to separate with absorbent charcoal adsorber, make that its desorption is more thorough, desorption effect is more
It is good.
3rd, heat exchanger of the present utility model is provided with the steam pipe for being connected to spray painting, baking vanish or/and painting high pressure vapor line,
The steam pipe introduces spray painting, baking vanish or/and painting high steam when heat exchanger heat supply temperature does not reach requirement by steam pipe
Heat, is changed, the desorption requirement for making it meet waste gas organic matter in absorbent charcoal adsorber with the heat energy for increasing heat exchanger.Thus
Absorbent charcoal adsorber of the present utility model is set to keep good waste gas noxious substance, desorption effect for a long time, it is long-term to keep
The use function of absorbent charcoal adsorber purification waste gas discharge.
4th, high-efficiency condensation processing unit of the present utility model also includes a temperature controller, and the temperature controller is used to detect condenser
Cryogenic temperature, the discharge thermal temperature or/and absorbent charcoal adsorber of heat exchanger, it is too low or too high in condenser cryogenic temperature
When automatically adjust the operation power of condenser, automatically adjust heat in heat exchanger or too low or too high absorbent charcoal adsorber temperature
Hand over the thermal energy conversion rate of device.Thus, the use power of heat exchanger and condenser can be preferably controlled, so that optimization operation is realized,
The beneficial effects such as energy-saving run.
5th, hot blast conveying pipe is provided with desorption blower fan between condenser and heat exchanger of the present utility model, and the desorption blower fan is used
The speed of hot air circulation in increase exhaust treatment system.Thus the waste gas harmful substance of absorbent charcoal adsorber can be effectively improved
Desorption effect, so as to improve the function of purification discharge waste gas.
6th, it is additionally provided with an apparatus for low-temperature plasma treatment on exhaust gas discharge conduit of the present utility model or/and photocatalyst is urged
Change system, thus can further improve the purification function of discharge waste gas, improve clean-up effect.
7th, the hot blast being connected with each other between described condenser, heat exchanger and absorbent charcoal adsorber of the present utility model is defeated
Send and auxiliary switching valve is equipped with pipe and steam pipe, the auxiliary switching valve and main switching valve are automatically controlled autocontrol valve, by setting
Put a master controller and automatically control open and close function.Thus intelligent control function of the present utility model can be increased, using more
Simply, it is convenient, fast.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
Embodiment
Below in conjunction with accompanying drawing, the utility model is described in further detail.
A kind of spraying/baking vanish/painting exhaust-gas efficient condensation heat-energy secondary shown in reference picture 1 utilizes and handles recovery system,
Include spraying/baking vanish or/and painting exhaust gas discharge conduit 1, an absorbent charcoal adsorber 2 is set on exhaust gas discharge conduit 1
Adsorb the waste gas organic matter that exhaust gas discharge conduit 1 is discharged；It is equipped with the air intake vent 21 and air outlet 22 of absorbent charcoal adsorber 2
Main switching valve 3, the main switching valve 3 is used to closing or opening the ventilating duct in absorbent charcoal adsorber 2；In absorbent charcoal adsorber
2 one end set a condenser 4, and the other end is set between a heat exchanger 5, described absorbent charcoal adsorber 2, condenser 4 and heat exchanger 5
Hot blast conveying pipe 6 is respectively equipped with to be connected with each other, when main switching valve 3 closes the air intake vent and air outlet of absorbent charcoal adsorber 2,
The heat energy (i.e. hot blast) that heat exchanger 5 obtains the cooling recovery waste gas organic matter generation of condenser 4 by hot blast conveying pipe 6 is delivered to work
Property charcoal adsorbent equipment 2 in, the waste gas harmful substance to absorption in absorbent charcoal adsorber 2 is separated, and is then delivered to again cold
Condenser 4 carries out cooling down the recovery that is in a liquid state rapidly, and the heat that cooling is produced rapidly of condenser 4 is conveyed to heat by hot blast conveying pipe 6
Hand over device 5 to be converted into heat energy to reuse, be consequently formed the efficiency of waste gas processing recovery system that heat-energy secondary is utilized.
In specific embodiment, by hot blast conveying pipe 6 between described condenser 4, heat exchanger 5 and absorbent charcoal adsorber 2
It is connected with each other, described heat exchanger 5 is located at air outlet one end of absorbent charcoal adsorber 2, the main switching valve 3 at air outlet
Inner side, described condenser 4 is located at air inlet one end of absorbent charcoal adsorber 2, in the main switching valve 3 of air inlet
Side.Specifically, the heat energy of the heat exchanger 5 enters in absorbent charcoal adsorber 2 in the air outlet of absorbent charcoal adsorber 2, i.e.,
Heat exchanger 5 by hot blast conveying pipe 6 in air outlet one end of absorbent charcoal adsorber 2, at air outlet in main switching valve 3
Side position is accessed；Waste gas harmful substance in the absorbent charcoal adsorber 2 is emitted into the air inlet of absorbent charcoal adsorber 2
Condenser 4 carries out liquid recovery, i.e. condenser 4 by hot blast conveying pipe 6 in air inlet one end of absorbent charcoal adsorber 2, position
Accessed in the inner side of the main switching valve 3 of air inlet, the heat energy of heat exchanger 5 is inversely delivered in absorbent charcoal adsorber 2,
Reverse desorption waste gas harmful substance function is formed in absorbent charcoal adsorber 2.The heat energy of heat exchanger 5 is set inversely to be delivered to activity
In charcoal adsorbent equipment 2, reverse desorption waste gas harmful substance function is formed in absorbent charcoal adsorber 2, when specifically used, is closed
The air intake vent of absorbent charcoal adsorber 2 and the main switching valve 3 of air outlet, make heat exchanger 5 obtain condenser by hot blast conveying pipe 6
4 heat energy is delivered in absorbent charcoal adsorber 2, and the waste gas harmful substance to absorption in absorbent charcoal adsorber 2 is separated,
Then rapid cooling is carried out by condenser 4 to reclaim.
Supplied in order to avoid heat energy (i.e. hot blast) supply of condenser 4 can not meet the conversion thermal energy of heat exchanger 5 (i.e. hot blast)
The requirement of organic exhaust gas (i.e. waste gas harmful substance) should be desorbed to absorbent charcoal adsorber 2, is provided with heat exchanger 5 and is connected to spray
Apply, the steam pipe 7 of baking vanish or/and painting high pressure vapor line, the steam pipe 7 when the heat supply temperature of heat exchanger 5 does not reach requirement,
Spraying, baking vanish or/and painting high steam heat are introduced by steam pipe 7, is changed with the heat energy for increasing heat exchanger 5, expires it
The desorption requirement of waste gas organic matter in sufficient absorbent charcoal adsorber 2.
The hot blast temperature for being desorbed organic exhaust gas in view of absorbent charcoal adsorber 2 is uneven, and such as thermo-field thoery or too low surpasses
Height causes to waste unnecessary heat energy, while the operation power of increase condenser 4 is required, on the contrary the waste gas of influence condenser 4 is harmful to
The recovery of material, and desorption effect is influenceed, the too low desorption function of not reaching waste gas harmful substance but, therefore, in high-efficiency condensation
Processing unit is additionally provided with a temperature controller, and the temperature controller controls circuit by temperature sensor, and temperature controller is used to detect condenser 4
The discharge thermal temperature or/and the waste gas organic matter desorption temperature of absorbent charcoal adsorber 2 of cryogenic temperature, heat exchanger 5, in condensation
The cryogenic temperature of device 4 automatically adjusts the operation power of condenser 4 when too low or too high, in heat exchanger 5 or the temperature of absorbent charcoal adsorber 2
The thermal energy conversion rate of heat exchanger 5 is automatically adjusted when spending low or too high.
In order to increase heat energy (i.e. hot blast) transporting velocity of heat exchanger 5, the organic exhaust gas of absorbent charcoal adsorber 2 is improved
(i.e. waste gas harmful substance) is desorbed function, the hot blast conveying pipe 6 between condenser 4, heat exchanger 5 and absorbent charcoal adsorber 2
On have additional a desorption blower fan 9, specifically, desorption blower fan 9 may be provided in position between condenser 4 and heat exchanger 5 hot blast conveying
On pipe 6, thus increase the speed of hot air circulation in exhaust treatment system, increase heat energy transfer efficiency, improve the de- of organic exhaust gas
Attached function.Meanwhile, in order to further lift the clean-up effect of discharge gas, low temperature etc. is additionally provided with exhaust gas discharge conduit 1
Gas ions processing unit or/and photocatalyst catalysis system 10, the apparatus for low-temperature plasma treatment or/and photocatalyst catalysis system
10 are located at air outlet one end of absorbent charcoal adsorber 2, described apparatus for low-temperature plasma treatment or/and photocatalyst catalysis system
System can effectively degrade toxic and harmful gas in discharge gas, effectively kill various bacteria, and bacterium or fungi can be discharged
Toxin decompose and harmless treatment, while being also equipped with, except formaldehyde, deodorization, anti-soil, the purification function such as air, realizing further excellent
Change the quality of discharge gas.
The hot blast conveying pipe 6 and steam being connected with each other between described condenser 4, heat exchanger 5 and absorbent charcoal adsorber 2
Auxiliary switching valve 11 is equipped with pipe 7, the auxiliary switching valve 11 or/and main switching valve 3 are automatically controlled autocontrol valve, by setting
One master controller automatically controls open and close function, and described master controller is spraying/baking vanish/painting exhaust-gas efficient condensation
Heat-energy secondary utilizes and handles one total control system of recovery system.
The application process of above-mentioned spraying/baking vanish/painting exhaust-gas efficient condensate disposal systems is：
1) when waste gas is discharged, inhaled by the activated carbon set on the exhaust gas discharge conduit of spray painting, baking vanish or/and painting
Adsorption device 2 intercepts the harmful substance in absorption waste gas；
2) when stopping waste gas discharge, charcoal absorption is inversely entered through by using hot gas (i.e. described heat energy)
Reacted in device 2 with the harmful substance in absorption waste gas, harmful substance is departed from absorbent charcoal adsorber 2；
3) after harmful substance departs from absorbent charcoal adsorber 2, reclaimed by cooling to be in a liquid state rapidly.
Above-mentioned method 3) cool realized by the condenser 4 for being arranged on the outlet of the waste gas recovery of absorbent charcoal adsorber 2 rapidly,
Reclaimed using harmful substance and gas are formed into liquid after the fast cooling of condenser 4；Method 2) in hot gas pass through heat hand over
The heat energy that device 5 obtains the generation of the fast cooling of condenser 4 is delivered to the secondary utilization of progress in absorbent charcoal adsorber 2.When heat exchanger 5
By obtain condenser 4 rapidly cooling produce heat can not meet waste gas harmful substance desorption require when, by introduce spray painting,
Baking vanish or/and the high steam heat of painting are fed, i.e., be connected to spray painting, baking vanish or/and system by being set in heat exchanger 5
The steam pipe 7 of high pressure vapor line is painted, the heat energy for conveying spray painting, baking vanish or/and painting high steam by steam pipe 7 is handed over to heat
Device 5 is fed, so that increase heat energy, that is, increase the hot blast feeding amount of heat exchanger 5.
When the utility model is applied, being turned on and off for auxiliary switching valve 11 and main switching valve 3 is controlled by master controller
Working condition, or simultaneously by master controller according to temperature controller detect data automatically adjust and control be turned on and off it is cold
The auxiliary switching valve on hot blast conveying pipe 6 and steam pipe 7 being connected with each other between condenser 4, heat exchanger 5 and absorbent charcoal adsorber 2
11, and adjust and control to be turned on and off the main switching valve 3 of air intake vent and air outlet of absorbent charcoal adsorber 2, inhale activated carbon
Optimal organic exhaust gas desorption effect is realized in adsorption device 2.
Claims (7)
1. a kind of spraying/baking vanish/painting exhaust-gas efficient condensation heat-energy secondary includes waste gas discharge logical using recovery system is handled
Road (1), it is characterized in that：An absorbent charcoal adsorber (2) is set to adsorb exhaust gas discharge conduit (1) on exhaust gas discharge conduit (1)
The waste gas organic matter of discharge；Main switching valve (3) is equipped with the air intake vent and air outlet of absorbent charcoal adsorber (2), the master cuts
Changing valve (3) is used to closing or opening the ventilating duct in absorbent charcoal adsorber (2)；One is set in absorbent charcoal adsorber (2) one end
Condenser (4), the other end sets a heat exchanger (5), described absorbent charcoal adsorber (2), condenser (4) and heat exchanger (5) it
Between be respectively equipped with hot blast conveying pipe (6) interconnection, main switching valve (3) close absorbent charcoal adsorber (2) air intake vent and
During air outlet, heat exchanger (5) obtains condenser (4) cooling by hot blast conveying pipe (6) and reclaims the heat energy that waste gas organic matter is produced
It is delivered in absorbent charcoal adsorber (2), the waste gas harmful substance to absorption in absorbent charcoal adsorber (2) is separated, so
It is delivered to condenser (4) again afterwards to carry out cooling down the recovery that is in a liquid state rapidly, condenser (4) heat that cooling is produced rapidly passes through hot blast
Delivery pipe (6), which is conveyed to heat exchanger (5) and is converted into heat energy, to be reused, and is consequently formed the efficiency of waste gas processing that heat-energy secondary is utilized
Recovery system.
2. a kind of spraying/baking vanish according to claim 1/painting exhaust-gas efficient condensation heat-energy secondary reclaims system using processing
System, it is characterized in that：The heat energy of the heat exchanger (5) enters absorbent charcoal adsorber in the air outlet of absorbent charcoal adsorber (2)
(2) in, the waste gas harmful substance in the absorbent charcoal adsorber (2) is emitted into the air inlet of absorbent charcoal adsorber (2)
Condenser (4) carries out liquid recovery, the heat energy of heat exchanger (5) is inversely delivered in absorbent charcoal adsorber (2), in activated carbon
Reverse desorption waste gas harmful substance function is formed in adsorbent equipment (2).
3. a kind of spraying/baking vanish according to claim 1 or 2/painting exhaust-gas efficient condensation heat-energy secondary is utilized and handled back
Receipts system, it is characterized in that：Described heat exchanger (5) is provided with the steam for being connected to spraying, baking vanish or/and painting high pressure vapor line
Manage (7), the steam pipe (7) introduces spraying, baking vanish when heat exchanger (5) heat supply temperature does not reach requirement by steam pipe (7)
Or/and painting high steam heat, changed with the heat energy for increasing heat exchanger (5), it is met in absorbent charcoal adsorber (2) and give up
The desorption requirement of gas organic matter.
4. a kind of spraying/baking vanish according to claim 1/painting exhaust-gas efficient condensation heat-energy secondary reclaims system using processing
System, it is characterized in that：Described high-efficiency condensation processing unit also includes a temperature controller, and the temperature controller is used to detect condenser (4)
Cryogenic temperature, the waste gas organic matter desorption temperature of the discharge thermal temperature of heat exchanger (5) or/and absorbent charcoal adsorber (2),
The operation power of condenser (4) is automatically adjusted when condenser (4) cryogenic temperature is too low or too high, in heat exchanger (5) or activity
Charcoal adsorbent equipment (2) temperature automatically adjusts the thermal energy conversion rate of heat exchanger (5) when too low or too high.
5. a kind of spraying/baking vanish according to claim 1/painting exhaust-gas efficient condensation heat-energy secondary reclaims system using processing
System, it is characterized in that：Hot blast conveying pipe (6) between described condenser (4) and heat exchanger (5), should provided with desorption blower fan (9)
Desorption blower fan (9) is used to increase the speed of hot air circulation in exhaust treatment system.
6. a kind of spraying/baking vanish according to claim 1/painting exhaust-gas efficient condensation heat-energy secondary reclaims system using processing
System, it is characterized in that：An apparatus for low-temperature plasma treatment is additionally provided with described exhaust gas discharge conduit (1) or/and photocatalyst is urged
Change system (10), the apparatus for low-temperature plasma treatment or/and photocatalyst catalysis system (10) are located at absorbent charcoal adsorber (2)
Air outlet one end.
7. a kind of spraying/baking vanish according to claim 3/painting exhaust-gas efficient condensation heat-energy secondary reclaims system using processing
System, it is characterized in that：The hot blast being connected with each other between described condenser (4), heat exchanger (5) and absorbent charcoal adsorber (2) is defeated
Send and be equipped with auxiliary switching valve (11) on pipe (6) and steam pipe (7), the auxiliary switching valve (11) or/and main switching valve (3) are automatically controlled
Autocontrol valve, by setting a master controller to automatically control open and close function.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621299747.2U CN206372691U (en) | 2016-11-29 | 2016-11-29 | A kind of spraying/baking vanish/painting exhaust-gas efficient condensation heat-energy secondary utilizes and handles recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621299747.2U CN206372691U (en) | 2016-11-29 | 2016-11-29 | A kind of spraying/baking vanish/painting exhaust-gas efficient condensation heat-energy secondary utilizes and handles recovery system |
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| Publication Number | Publication Date |
|---|---|
| CN206372691U true CN206372691U (en) | 2017-08-04 |
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ID=59405859
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621299747.2U Expired - Fee Related CN206372691U (en) | 2016-11-29 | 2016-11-29 | A kind of spraying/baking vanish/painting exhaust-gas efficient condensation heat-energy secondary utilizes and handles recovery system |
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| CN (1) | CN206372691U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106492628A (en) * | 2016-11-29 | 2017-03-15 | 广州朗洁环保科技有限公司 | A kind of spraying/baking vanish/painting exhaust-gas efficient condensation heat-energy secondary is using process recovery system and application process |
| CN113694711A (en) * | 2021-10-28 | 2021-11-26 | 瑞润化工(南通)有限公司 | Method for recycling waste gas in production of soft-touch leather coating |
-
2016
- 2016-11-29 CN CN201621299747.2U patent/CN206372691U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106492628A (en) * | 2016-11-29 | 2017-03-15 | 广州朗洁环保科技有限公司 | A kind of spraying/baking vanish/painting exhaust-gas efficient condensation heat-energy secondary is using process recovery system and application process |
| CN113694711A (en) * | 2021-10-28 | 2021-11-26 | 瑞润化工(南通)有限公司 | Method for recycling waste gas in production of soft-touch leather coating |
| CN113694711B (en) * | 2021-10-28 | 2021-12-24 | 瑞润化工(南通)有限公司 | Method for recycling waste gas in production of soft-touch leather coating |
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