CN203291683U - Organic waste gas treatment device - Google Patents
Organic waste gas treatment device Download PDFInfo
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- CN203291683U CN203291683U CN2013203221952U CN201320322195U CN203291683U CN 203291683 U CN203291683 U CN 203291683U CN 2013203221952 U CN2013203221952 U CN 2013203221952U CN 201320322195 U CN201320322195 U CN 201320322195U CN 203291683 U CN203291683 U CN 203291683U
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- 239000007789 gas Substances 0.000 title claims abstract description 153
- 239000010815 organic waste Substances 0.000 title claims abstract description 74
- 238000010438 heat treatment Methods 0.000 claims abstract description 14
- 238000001816 cooling Methods 0.000 claims abstract description 9
- 239000002912 waste gas Substances 0.000 claims abstract description 7
- 238000001179 sorption measurement Methods 0.000 claims description 25
- 238000007791 dehumidification Methods 0.000 claims description 19
- 238000003795 desorption Methods 0.000 claims description 14
- 238000001035 drying Methods 0.000 claims description 14
- 239000012229 microporous material Substances 0.000 claims description 11
- 238000004064 recycling Methods 0.000 claims description 7
- 238000005057 refrigeration Methods 0.000 claims description 7
- 238000009833 condensation Methods 0.000 claims description 4
- 230000005494 condensation Effects 0.000 claims description 4
- 238000005496 tempering Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 7
- 238000007639 printing Methods 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000002957 persistent organic pollutant Substances 0.000 abstract description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical class [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 26
- 238000000034 method Methods 0.000 description 17
- 230000008569 process Effects 0.000 description 11
- 238000005265 energy consumption Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 238000007602 hot air drying Methods 0.000 description 6
- 239000005416 organic matter Substances 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 4
- 230000001172 regenerating effect Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 229920000049 Carbon (fiber) Polymers 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 125000004122 cyclic group Chemical group 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000010186 staining Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
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- Drying Of Gases (AREA)
- Treating Waste Gases (AREA)
Abstract
The utility model discloses an organic waste gas treatment device which is designed for solving the problems, such as incomplete treatment on organic pollutants, of the existing device. The organic waste gas treatment device comprises a hot air dryer, a surface cooler, an absorbing unit, a dehumidifying unit and a heater, which are orderly communicated through pipelines to form a closed loop. The surface cooler and the heater are respectively an evaporator and a condenser of the same heat pump system, or a cooling end liquid-gas heat exchanger and a heating end liquid-gas heat exchanger of the same heat pump. The organic waste gas treatment device is reasonable in structure, convenient to use and low in manufacture cost, and has a good treatment effect on the organic waste gases including the printing waste gas.
Description
Technical Field
The utility model relates to an organic waste gas administers device.
Background
At present, the organic waste gas is treated by adopting microporous materials such as activated carbon, activated carbon fiber and the like for adsorption treatment, and then the microporous materials after saturated adsorption are subjected to organic solvent desorption by high-temperature steam for recycling. Because the microporous material after the organic solvent is desorbed by using steam has much moisture, the air discharged from the adsorption tower can not be reused for cyclic drying in production due to overhigh humidity and can only be directly discharged. However, the part of the discharged gas also has a certain concentration of organic waste gas components and temperature, which can pollute the environment and waste heat. That is, the prior art cannot completely solve the problem of environmental pollution, and the operation energy consumption of the whole system is high due to the hot gas discharged from the adsorption tower and the heat dissipation of the circulating water of the cooling tower, thereby increasing the operation cost.
SUMMERY OF THE UTILITY MODEL
The utility model aims at providing an organic waste gas treatment device of non-staining environment.
The utility model also aims to provide an organic waste gas treatment device that the energy consumption is low.
The utility model discloses a still another purpose is to provide an effectual organic waste gas of dehumidification administers device.
To achieve the purpose, the utility model adopts the following technical proposal:
an organic waste gas treatment device comprises a hot air dryer 6, a surface air cooler 2, an adsorption unit, a dehumidification unit and a heater 5 which are communicated through pipelines to form a closed loop; the surface air cooler 2 is connected to an air outlet of the hot air dryer 6, and the heater 5 is connected to an air return inlet of the hot air dryer 6; the hot air dryer 6 is used for processing organic waste gas, conveying the organic waste gas to a surface cooler, and introducing treated clean gas for recycling; the surface cooler 2 is used for cooling the waste gas to be treated; the adsorption unit is used for adsorbing the cooled gas by using a microporous material; the dehumidification component has condensation and gas heat exchange functions and is used for dehumidifying and tempering adsorbed gas; the heater 5 is used for heating the dehumidified and reheated gas.
In particular, the surface cooler 2 and the heater 5 are an evaporator and a condenser of the same heat pump system.
Particularly, the surface cooler 2 and the heater 5 are a liquid-gas heat exchanger at a refrigerating end of the same heat pump and a liquid-gas heat exchanger at a heating end of the same heat pump.
In particular, the dehumidification unit is a dehumidifier 4; in particular, the bottom of the dehumidifier 4 is provided with a drainage control outlet.
In particular, the dehumidification unit comprises a dehumidifier 4 and an air reservoir 7 connected in series; an air inlet of the air storage chamber 7 is connected with an air outlet of the dehumidifier 4, an air outlet of the air storage chamber 7 is connected with an air inlet of the heater 5, and an air outlet pipe of the hot air dryer 6 is connected with an air return inlet of the air storage chamber 7.
Further, the dehumidifier 4 is constituted by a combination of an evaporator and a condenser of a refrigeration system.
In particular, the adsorption unit of the device comprises at least two adsorbers arranged between the surface cooler 2 and the dehumidification unit in parallel, a second surface cooler 22 and an air valve; one end of the second surface cooler 22 is connected with the outlet of the desorption discharge pipeline of the adsorption unit, and the other end is connected with the condenser; the air valve is used for switching each adsorber to carry out adsorption or desorption drying process in turn.
The utility model discloses each part of organic waste gas treatment device communicates in proper order through the pipeline and forms closed return circuit, has absorbed the organic matter effectively and has not discharged substandard gas in to the environment. The surface cooler and the heater are an evaporator and a condenser of the same heat pump system, or a refrigerating end liquid-gas heat exchanger of the same heat pump and a heating end liquid-gas heat exchanger of the heat pump, so that heat is fully recycled, and energy consumption is reduced. When the concentration of organic matters in the organic waste gas to be treated is lower than a set value or the air volume of the organic waste gas to be treated is overlarge, closed circulation can be carried out through the arrangement of the air storage chamber to increase the concentration of the organic matters or partially purify to reduce the single treatment amount, the adsorption and purification efficiency is improved, and the cost is reduced.
The utility model discloses organic waste gas administers device is rational in infrastructure, convenient to use, low in manufacturing cost, it is effectual to organic waste gas's treatment.
Drawings
FIG. 1 is a schematic structural diagram of a first preferred embodiment of the organic waste gas treatment device of the present invention;
FIG. 2 is a schematic structural view of a second preferred embodiment of the organic waste gas treatment device of the present invention;
FIG. 3 is a schematic structural diagram of a third preferred embodiment of the organic waste gas treatment device of the present invention.
Labeled as:
1. a heat pump system; 2. a surface cooler; 3. an adsorber; 4. a dehumidifier; 5. a heater; 6. a hot air dryer; 7. an air storage chamber; 22. a second surface air cooler; 31. a first adsorber unit; 32. a second adsorber unit.
Detailed Description
The technical solution of the present invention is further explained by the following embodiments with reference to the accompanying drawings.
The utility model discloses organic waste gas treatment method purifies through cooling, absorption, dehumidification and heating step to the organic waste gas that contains organic matter in closed loop, has realized gaseous cyclic utilization through the closed method of pipeline that will administer, avoids not handling complete gas emission and contaminated air. The treated organic waste gas comprises printing waste gas, but not limited to the printing waste gas, and all the organic waste gas which can be generated by a hot air drying process can be treated by using the method.
The organic waste gas treatment method of the utility model has the advantages that the concrete steps are not limited, and the purpose of organic waste gas treatment can be realized in the closed pipeline. Wherein the following steps are preferably included:
and step 1, processing in a hot air dryer to obtain the organic waste gas to be treated. Putting the product to be treated with the organic pollution source into a hot air dryer, and drying the product to be treated by hot air. After drying, the hot air contains organic pollutants and becomes organic waste gas to be treated.
And 2, cooling the organic waste gas to be treated. The cooling process is beneficial to carrying out subsequent adsorption treatment on the organic waste gas.
And 6, returning the heated gas to the hot air dryer for recycling, and continuously drying the product to be treated or the next product to be treated.
The organic waste gas can be effectively treated after the process steps, and the gas is recycled in the closed loop, so that the environmental pollution is avoided.
In order to fully utilize energy and reduce energy consumption, the evaporator and the condenser of the same heat pump system respectively realize temperature reduction in the step 2 and heating in the step 5.
The organic waste gas treatment device of the utility model comprises a hot air drier, a surface air cooler, an adsorption unit, a dehumidification unit and a heater which are sequentially communicated through pipelines to form a closed loop; processing the organic waste gas in a hot air dryer to obtain organic waste gas, conveying the organic waste gas to a surface cooler for treatment, and simultaneously recovering the treated gas for recycling; the surface cooler cools the waste gas to be treated; the absorber uses microporous material to absorb the cooled gas, to be processed into clean gas; the dehumidifier carries out dehumidification and temperature return treatment on the adsorbed gas; and the heated gas returns to the hot air dryer after being heated by the heater, and is continuously recycled and processed to obtain the organic waste gas.
The utility model discloses each part of organic waste gas treatment device communicates in proper order through the pipeline and forms closed return circuit, has absorbed the organic matter in the gas effectively and has not discharged substandard gas in to the environment.
Wherein, the surface cooler and the heater are an evaporator and a condenser of the same heat pump system; or the surface cooler and the heater are a liquid-gas heat exchanger at the heating end of the same heat pump and a liquid-gas heat exchanger at the heating end of the heat pump. Through the structure, the heat energy can be recycled, and the energy consumption in organic waste gas treatment is reduced.
In order to facilitate the discharge of water vapor, a drainage control outlet is arranged at the bottom of the dehumidifier; the dehumidifier is composed of an evaporator and a condenser of a refrigeration system.
The first preferred embodiment:
as shown in fig. 1, the organic waste gas treatment device comprises a hot air dryer 6, a surface air cooler 2, an adsorber 3, a dehumidifier 4 and a heater 5 which are sequentially communicated through pipelines to form a closed loop; wherein, the surface cooler 2 and the heater 5 are an evaporator and a condenser of the same heat pump system 1. The dehumidifier is composed of an evaporator and a condenser of a refrigeration system, and a drainage control outlet is arranged at the bottom of the dehumidifier.
The arrows in the figure show the flow paths of the process gas. And putting the product to be treated with the printing ink into a hot air dryer, and drying the product to be treated by using hot air. The hot air is thus rich in organic matter, forming organic waste gas. The organic waste gas is driven by the fan to reach the surface cooler through the pipeline, the surface cooler cools the organic waste gas to be treated, and then the organic waste gas enters the adsorber. The adsorber is filled with active carbon, and the cooled organic waste gas passes through the active carbon for adsorption treatment to become clean gas. Since the activated carbon has a large amount of moisture after desorption, the resulting clean gas also contains moisture and cannot be directly reused. The wet clean gas enters a dehumidifier, the dehumidifier with the functions of condensation and gas heat exchange is used for dehumidifying and rewarming the gas, and the treated gas enters a heater. High-heat gas is formed after being heated by the heater, the standard required by the hot air drying process is achieved, and the hot air drying process returns to the hot air dryer to continuously dry the product to be treated.
The surface temperature of the surface cooler 2 is 7-12 ℃, and the temperature of the organic waste gas passing through the surface of the surface cooler can be reduced to 20-35 ℃. After the organic exhaust gas passes through the microporous material, the temperature of the adsorber is reduced from a high temperature of about 100 ℃ to about 40 ℃.
The air continuously passes through the evaporator and the condenser of the refrigerating system to realize constant temperature dehumidification, the temperature change of the air before and after dehumidification is less, and the energy consumed by the subsequent temperature rise of the condensed and dehumidified cold air is greatly reduced. Since the temperature of the dehumidified air is maintained substantially the same as that before dehumidification (20-30 c), it is easier to heat the air to a higher temperature for drying when passing through the air heater 5.
Because the surface air cooler 2 and the heater 5 are the evaporator and the condenser of the same heat pump system 1, and the evaporator is located in a high-temperature organic gas area, the temperature of the evaporator is generally between 40 ℃ and 60 ℃, the evaporator can greatly improve the heating energy efficiency ratio of the heat pump under the environment of sufficient heat source, the heating capacity of the condenser of the heat pump system 1 to the dehumidified air is greatly improved, and the adsorber 3 is matched with the heat pump system 1 with high-efficiency heating performance for use, so that the problem of high energy consumption troubled by the original adsorption technology is solved.
In the preferred embodiment, all parts of the organic waste gas treatment device are sequentially communicated through pipelines to form a closed loop, so that organic matters are effectively absorbed, and substandard gas is not discharged into the environment.
The second preferred embodiment:
as shown in fig. 2, the organic waste gas treatment device comprises a hot air dryer 6, a surface air cooler 2, an adsorber 3, a dehumidifier 4, a gas storage chamber 7 and a heater 5 which are sequentially communicated through pipelines to form a closed loop. An air inlet of the air storage chamber 7 is connected with an air outlet of the dehumidifier 4, an air outlet of the air storage chamber 7 is connected with an air inlet of the heater 5, and an air outlet pipe of the hot air dryer 6 is connected with an air return inlet of the air storage chamber 7. The surface air cooler 2 and the heater 5 are an evaporator and a condenser of the same heat pump system 1; the bottom of the dehumidifier 4 is provided with a drainage control outlet; the dehumidifier 4 is composed of a combination of an evaporator and a condenser of a refrigeration system.
The arrows in the figure show the flow paths of the process gas.
The flow of the first working mode is as follows: and (3) putting the product to be treated with the organic pollution source into a hot air dryer, and drying the product to be treated by using hot air. The hot air is thus rich in organic matter, forming organic waste gas to be treated.
When the concentration of organic matters in the organic waste gas to be treated from the hot air dryer is lower than a set value, if the organic waste gas is directly treated, the adsorption effect is poor, and the cost is increased. Therefore, the surface cooler 2, the absorber 3 and the dehumidifier 4 are disconnected at the moment, the gas returns to the hot air dryer 6 through the gas storage chamber 7 and the heater 5, and the concentration of organic matters in the gas is increased through two or more times of closed circulation. The concentration of organic matters in the gas does not influence the drying processing of the product to be treated.
When the concentration of organic matters in the gas is more than or equal to a set value, the fan drives the organic waste gas to reach the surface cooler through the pipeline, the surface cooler cools the organic waste gas to be treated, and then the organic waste gas enters the adsorber. The adsorber is filled with active carbon, and the cooled organic waste gas passes through the active carbon for adsorption treatment to become clean gas. Since the activated carbon has a large amount of moisture after desorption, the resulting clean gas also contains moisture and cannot be directly reused. The wet clean gas enters the dehumidifier, the dehumidifier with the functions of condensation and gas heat exchange condenses and dehumidifies the gas and regenerates the gas to be close to the temperature before dehumidification, and the processed gas passes through the gas storage chamber 7 and enters the heater. High-heat gas is formed after being heated by the heater, the standard required by the hot air drying process is achieved, and the hot air drying process returns to the hot air dryer to continuously dry the product to be treated.
The flow of the second working mode is as follows: when the temperature of the gas in the hot air dryer 6 is high and the air volume is large, the drying effect of the product to be treated is better, but when the air volume to be treated is too large, the treatment component formed by the surface cooler 2, the adsorber 3 and the dehumidifier 4 is required to be large in scale, high in investment and high in operation cost.
So that a part of the large amount of gas output from the hot air dryer 6 is sent to the surface cooler through a pipeline to perform the same treatment process as the first working mode, i.e. partial purification; the other part of the gas directly enters the gas storage chamber 7 and is mixed with the clean gas sent from the dehumidifier 4, and the mixed gas returns to the hot air dryer 6 after passing through the heater 5 for recycling.
The cooling effect and the energy-saving effect of the high-temperature organic waste gas before entering the adsorber are greatly improved compared with those of the traditional cooling tower by adopting the evaporator of the heat pump system in the preferred embodiment. All parts in the device are connected into a closed loop through pipelines, so that the recycling of mixed hot air after organic waste gas treatment is well realized, the treatment effect is good, and the energy consumption is low. The arrangement of the gas storage chamber enables waste gas treatment to have various selectable schemes, a proper scheme can be selected according to the air quantity and the concentration of organic matters in the gas, the drying effect is improved, and meanwhile, the scale of a treatment assembly is reduced, the investment is reduced, and the operation cost is reduced.
The third preferred embodiment:
as shown in fig. 3, the organic waste gas treatment device includes a hot air dryer 6, a surface air cooler 2, an adsorption unit composed of a first adsorber 31 and a second adsorber 32, a dehumidifier 4, a heater 5, a second surface air cooler 22, and an air valve (not shown) connected in sequence through a pipeline. The dehumidifier 4 is composed of an evaporator and a condenser of a refrigeration system, and a drainage control outlet is arranged at the bottom of the dehumidifier.
The working state of the adsorbers is switched through the air valve, namely when the first adsorber 31 is in the adsorption working state, the second adsorber 32 and the second surface cooler 22 form a desorption regenerative system; when the second adsorber 32 is in the adsorption working state, the first adsorber 31 and the second surface cooler 22 form a desorption regenerative system. In the desorption regenerative system, desorption gas such as water vapor enters the adsorber, desorbs organic substances, passes through the second surface cooler 22, and then reaches the condenser.
The using method comprises the following steps: the single-sided arrows show the flow path of the process gas and the double-sided arrows show the flow path of water vapor for desorption of the microporous material in the adsorber. Driven by a fan, the high-temperature organic waste gas in the hot air dryer 6 flows through the surface air cooler 2 through a pipeline. The surface temperature of the surface cooler 2 is 7-12 ℃, and the temperature of the organic waste gas can be reduced to 20-35 ℃. The organic waste gas enters the first adsorber 31 and passes through the activated carbon therein. The organic waste gas is passed through the adsorber to reduce the temperature from a high temperature of about 100 c to about 40 c.
Since the activated carbon in the first adsorber 31 is desorbed by the water vapor before, so that a large amount of moisture is stored therein, the gas passing through the activated carbon also carries a large amount of moisture, and needs to be dehumidified and cooled. The gas continuously passes through an evaporator and a condenser of the refrigeration system to realize constant temperature dehumidification, the temperature change of the air before and after dehumidification is less, and the energy consumed by the subsequent temperature rise of the condensed and dehumidified cold air is greatly reduced. Since the temperature of the dehumidified air is maintained substantially the same as that before dehumidification (20-30 ℃), it is easier to heat the air to a higher temperature when the air passes through the first air heater 5 thereafter, so as to meet the drying requirement.
Meanwhile, the high-temperature water vapor (or high-temperature nitrogen) is introduced into the second adsorber 32 to desorb the activated carbon therein, so that the activated carbon can be reused after organic pollutants in the activated carbon are cleaned. The high temperature steam then transfers the heat energy to the system as it flows through the second surface air cooler 22, enabling the heat energy to be recovered for reuse.
In the preferred embodiment, two adsorbers are provided, and the decontamination of the organic waste gas and the desorption of the activated carbon are alternately carried out, so that the heat energy is fully utilized and recovered.
Claims (8)
1. The organic waste gas treatment device is characterized by comprising a hot air dryer (6), a surface air cooler (2), an adsorption unit, a dehumidification unit and a heater (5) which are communicated through pipelines to form a closed loop; the surface air cooler (2) is connected to an air outlet of the hot air dryer (6), and the heater (5) is connected to an air return inlet of the hot air dryer (6); wherein,
the hot air dryer (6) is used for processing the organic waste gas, conveying the organic waste gas to the surface cooler and introducing the treated clean gas for recycling;
the surface cooler (2) is used for cooling the waste gas to be treated;
the adsorption unit is used for adsorbing the cooled gas by using a microporous material;
the dehumidification component has condensation and gas heat exchange functions and is used for dehumidifying and tempering adsorbed gas;
and the heater (5) is used for heating the dehumidified and reheated gas.
2. An organic waste gas treatment device according to claim 1, wherein the surface cooler (2) and the heater (5) are an evaporator and a condenser of the same heat pump system.
3. The organic waste gas treatment device according to claim 1, wherein the surface cooler (2) and the heater (5) are a heating-side liquid-gas heat exchanger of the same heat pump and a heating-side liquid-gas heat exchanger of the same heat pump.
4. An organic exhaust gas treatment device according to claim 1, wherein the dehumidifying unit is a dehumidifier (4).
5. An organic waste gas treatment device according to claim 4, wherein the bottom of the dehumidifier (4) is provided with a drain control outlet.
6. The organic waste gas treatment device according to claim 1, wherein the dehumidifying unit comprises a dehumidifier (4) and an air receiver (7) connected in series; an air inlet of the air storage chamber (7) is connected with an air outlet of the dehumidifier (4), an air outlet of the air storage chamber (7) is connected with an air inlet of the heater (5), and an air outlet pipe of the hot air dryer (6) is connected with an air return inlet of the air storage chamber (7).
7. An organic waste gas treatment plant according to claim 4, 5 or 6, characterized in that the dehumidifier (4) is constituted by a combination of an evaporator and a condenser of a refrigeration system.
8. An organic waste gas treatment device according to claim 1, wherein the adsorption unit of the device comprises at least two adsorbers arranged in parallel between the surface cooler (2) and the dehumidification unit, a second surface cooler (22) and an air valve; one end of the second surface cooler (22) is connected with the outlet of the desorption discharge pipeline of the adsorption unit, and the other end of the second surface cooler is connected with the condenser; the air valve is used for switching each adsorber to carry out adsorption or desorption drying process in turn.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203221952U CN203291683U (en) | 2013-06-05 | 2013-06-05 | Organic waste gas treatment device |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203221952U CN203291683U (en) | 2013-06-05 | 2013-06-05 | Organic waste gas treatment device |
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| CN203291683U true CN203291683U (en) | 2013-11-20 |
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| CN2013203221952U Expired - Lifetime CN203291683U (en) | 2013-06-05 | 2013-06-05 | Organic waste gas treatment device |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103272454A (en) * | 2013-06-05 | 2013-09-04 | 中节能天辰(北京)环保科技有限公司 | Organic exhaust gas treatment method and apparatus |
| CN105928259A (en) * | 2016-04-21 | 2016-09-07 | 武汉旭日华科技发展有限公司 | Treating system and method for organic waste gas in coating industry |
-
2013
- 2013-06-05 CN CN2013203221952U patent/CN203291683U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103272454A (en) * | 2013-06-05 | 2013-09-04 | 中节能天辰(北京)环保科技有限公司 | Organic exhaust gas treatment method and apparatus |
| CN103272454B (en) * | 2013-06-05 | 2016-07-20 | 中节能天辰(北京)环保科技有限公司 | VOCs treatment method and device |
| CN105928259A (en) * | 2016-04-21 | 2016-09-07 | 武汉旭日华科技发展有限公司 | Treating system and method for organic waste gas in coating industry |
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Granted publication date: 20131120 Effective date of abandoning: 20160720 |
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