CN214552358U - Double-rotary-wheel high-concentration organic waste gas treatment system - Google Patents
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- CN214552358U CN214552358U CN202120219077.3U CN202120219077U CN214552358U CN 214552358 U CN214552358 U CN 214552358U CN 202120219077 U CN202120219077 U CN 202120219077U CN 214552358 U CN214552358 U CN 214552358U
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- 239000007789 gas Substances 0.000 title claims abstract description 229
- 239000010815 organic waste Substances 0.000 title claims abstract description 40
- 238000003795 desorption Methods 0.000 claims abstract description 67
- 238000001816 cooling Methods 0.000 claims abstract description 50
- 239000000112 cooling gas Substances 0.000 claims description 92
- 238000001179 sorption measurement Methods 0.000 claims description 87
- 238000002485 combustion reaction Methods 0.000 claims description 8
- 239000002912 waste gas Substances 0.000 claims description 5
- 230000003197 catalytic effect Effects 0.000 claims description 2
- 230000001172 regenerating effect Effects 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims 3
- 230000000694 effects Effects 0.000 abstract description 6
- 238000010521 absorption reaction Methods 0.000 abstract 6
- 238000000746 purification Methods 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 4
- 238000003915 air pollution Methods 0.000 description 3
- 239000004065 semiconductor Substances 0.000 description 3
- 230000006870 function Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000008450 motivation Effects 0.000 description 1
- 239000007800 oxidant agent Substances 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
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Abstract
The utility model provides a high concentration organic waste gas treatment system of double-runner, mainly used organic waste gas treatment system, and be equipped with an incineration equipment, a heat exchanger, a first absorption runner, a second absorption runner and a chimney, and be connected with the other end of this first steam conveying pipeline through this second steam conveying pipeline branch, and in the opposite side of desorption district of first absorption runner is carried with partial steam to the one end of this first steam conveying pipeline, in addition, carry desorption concentrated gas to one side of the cooling zone of first absorption runner through the other end of this second desorption concentrated gas pipeline, and carry the gas after partial absorption to the second desorption concentrated gas pipeline by this first gas purification branch pipeline, can adjust the temperature of the desorption concentrated gas of the cooling zone of first absorption runner by this second desorption concentrated gas pipeline, therefore, the organic waste gas treatment efficiency can be improved, and the effects of saving energy and reducing emission are achieved.
Description
Technical Field
The present disclosure relates to a dual-rotor high concentration organic waste gas treatment system, and more particularly, to an organic waste gas treatment system or the like which can improve the efficiency of organic waste gas treatment, save energy and reduce emissions, and is suitable for use in the semiconductor industry, the photovoltaic industry, or the chemical industry.
Background
At present, volatile organic gases (VOC) are generated in the manufacturing process of semiconductor industry or photoelectric industry, so that processing equipment for processing the VOC is installed in each factory to prevent the VOC from being directly discharged into the air to cause air pollution. At present, most of the concentrated gas desorbed by the treatment equipment is conveyed to the incinerator for combustion, and then the combusted gas is conveyed to a chimney for emission.
However, in recent years, with the attention of people on air pollution, relevant air quality standards are revised on the emission standards of chimneys, and the air pollution is developed and improved according to the international regulation trend.
Therefore, in view of the above-mentioned drawbacks, it is desirable to provide a dual-rotor high-concentration organic waste gas treatment system with improved organic waste gas treatment efficiency, which enables easy operation and assembly by a user, and based on this, a dual-rotor high-efficiency organic waste gas treatment system and a method thereof are provided to provide convenience to the user, which is motivation for the development of the present disclosure.
SUMMERY OF THE UTILITY MODEL
The main object of the present disclosure is to provide a dual-rotor high-concentration organic waste gas treatment system, which is mainly used for organic waste gas treatment systems, and is provided with an incineration device, a heat exchanger, a first adsorption rotor, a second adsorption rotor and a chimney, and is connected to the other end of the first hot gas delivery pipeline through the branch of the second hot gas delivery pipeline, and then part of the hot gas is delivered to the other side of the desorption region of the first adsorption rotor through one end of the first hot gas delivery pipeline, and in addition, the desorption concentrated gas is delivered to one side of the cooling region of the first adsorption rotor through the other end of the second desorption concentrated gas pipeline, and part of the adsorbed gas is delivered to the second desorption concentrated gas pipeline through the first purified gas branch pipeline, so that the temperature of the desorption concentrated gas delivered to the cooling region of the first adsorption rotor by the second desorption concentrated gas pipeline can be adjusted, therefore, the organic waste gas treatment efficiency can be improved, and the effects of saving energy and reducing emission are achieved, so that the overall practicability is improved.
Another object of the present disclosure is to provide a dual-rotor high concentration organic waste gas treatment system, wherein a first cooling gas bypass pipeline is disposed between the first cooling gas delivery pipeline and the first hot gas delivery pipeline, and a first cooling gas bypass control valve and a first cooling gas delivery control valve are disposed on the first cooling gas bypass pipeline and the first cooling gas delivery pipeline, respectively, and a proportional damper is formed by the first cooling gas bypass control valve and the first cooling gas delivery control valve, and in addition, a first cooling gas bypass control valve and a first hot gas delivery control valve are disposed on the first cooling gas bypass pipeline and the first hot gas delivery pipeline, respectively, and a proportional damper is formed by the first cooling gas bypass control valve and the first hot gas delivery control valve, so as to adjust the temperature of the hot gas delivered to the desorption region of the first adsorption rotor by the first hot gas delivery pipeline, so that the temperature control device has the function of improving and controlling the temperature, and further the whole usability is improved.
Another objective of the present disclosure is to provide a dual-rotor high-concentration organic waste gas treatment system, wherein a second cooling gas bypass pipeline is disposed between the second cooling gas delivery pipeline and the second hot gas delivery pipeline, and a second cooling gas bypass control valve and a second cooling gas delivery control valve are disposed on the second cooling gas bypass pipeline and the second cooling gas delivery pipeline, respectively, and a proportional air door is formed by the second cooling gas bypass control valve and the second cooling gas delivery control valve. In addition, also can be equipped with second cooling gas bypass control valve and a second steam on this second cooling gas bypass pipeline and this second steam delivery pipeline respectively and carry control valve to form the proportion air door through this second cooling gas bypass control valve and this second steam delivery control valve, consequently, can adjust the temperature of the steam of the desorption district that is carried this second adsorption rotating wheel by this second steam delivery pipeline, make it have the effect of promotion control temperature, and then increase holistic controllability.
So that the manner in which the features and characteristics of the present disclosure can be understood in detail, a more particular description of the disclosure, briefly summarized above, may be had by reference to embodiments, some of which are illustrated in the appended drawings.
Drawings
Fig. 1 is a schematic view of a dual-rotor high-concentration organic waste gas treatment system according to the present disclosure.
Fig. 2 is a schematic diagram of a dual-rotor high-concentration organic exhaust gas treatment system having a first cooling gas bypass pipeline and a second cooling gas bypass pipeline according to an embodiment of the disclosure.
Fig. 3 is a schematic diagram of a dual-rotor high-concentration organic exhaust gas treatment system with a first net gas bypass line according to another embodiment of the present disclosure.
FIG. 4 is a schematic diagram of a dual-rotor high-concentration organic waste gas treatment system with a first branch clean gas pipeline according to another embodiment of the present disclosure.
Description of the reference numerals
10. Incineration equipment
101. Inlet port
102. An outlet
11. Combustion chamber
20. Heat exchanger
201. Cold side way
202. Hot side road
21. Hot side conveying pipeline
22. Hot side exhaust pipe 30, first adsorption rotor
301. Adsorption zone 302, cooling zone
303. Desorption zone 31, exhaust gas inlet line
311. Fan 32, first clean gas discharge line
33. First cooling gas delivery pipeline 331 and first cooling gas delivery control valve
34. First hot gas delivery line 341, first exhaust gas delivery control valve
35. First desorption concentrated gas pipeline 351 and fan
40. First cooling gas bypass pipeline 401 and first cooling gas bypass control valve
50. Second adsorption rotor 501, adsorption zone
502. Cooling zone 503, desorption zone
51. Second purified gas discharge pipeline 511 and fan
52. Second cooling air inlet pipeline 53 and second cooling air delivery pipeline
531. A second cooling gas delivery control valve 54, a second hot gas delivery line
541. Second hot gas delivery control valve 55 and second desorption concentrated gas pipeline
551. Fan 60 and secondary cooling gas bypass line
601. Second cooling gas bypass control valve 70 and chimney
80. First purified gas bypass pipeline 801 and first purified gas bypass control valve
90. First clean gas branch pipeline 901 and first clean gas branch control valve
Detailed Description
Please refer to fig. 1 to 4, which are schematic diagrams illustrating an embodiment of the disclosure. The best mode of the double-rotary high-concentration organic waste gas treatment system is applied to organic waste gas treatment systems or similar equipment in the semiconductor industry, the photoelectric industry or the chemical related industry, mainly can improve the efficiency of organic waste gas treatment, and has the effects of saving energy and reducing emission.
The dual-rotary high-concentration organic waste gas treatment system in the embodiment of the present disclosure mainly includes a combined design of an incineration apparatus 10, a heat exchanger 20, a first adsorption rotary 30, a second adsorption rotary 50 and a chimney 70 (as shown in fig. 1 to 4). The heat exchanger 20 has a cold side channel 201 and a hot side channel 202, and the heat exchanger 20 has a hot side conveying pipe 21 and a hot side exhaust pipe 22, one end of the hot side conveying pipe 21 is connected to the incineration apparatus 10, and the other end of the hot side conveying pipe 21 is connected to one end of the hot side channel 202, and in addition, one end of the hot side exhaust pipe 22 is connected to the other end of the hot side channel 202, and the other end of the hot side exhaust pipe 22 is connected to the chimney 70 (as shown in fig. 1 to fig. 4). In addition, the incineration apparatus 10 is provided with an inlet 101 and an outlet 102, the outlet 102 of the incineration apparatus 10 is connected TO the chimney 70, the incineration apparatus 10 is provided with a combustion chamber 11, the combustion chamber 11 is communicated with one end of the hot-side conveying pipeline 21 (as shown in fig. 1 TO 4), and the incineration apparatus 10 is a direct-fired incinerator (TO), a catalytic incinerator or a Regenerative Thermal Oxidizer (RTO). The incineration apparatus 10 is provided with a combustion heater or an electric heater.
In addition, the first adsorption rotor 30 of the present disclosure is provided with an adsorption region 301, a cooling region 302 and a desorption region 303, and the first adsorption rotor 30 is connected to an exhaust gas inlet line 31, a first purified gas discharge line 32, a first cooling gas delivery line 33, a first hot gas delivery line 34 and a first desorption concentrated gas line 35 (as shown in fig. 1 to 4). The second adsorption rotor 50 is provided with an adsorption zone 501, a cooling zone 502 and a desorption zone, and the second adsorption rotor 50 is connected to a second purified gas discharge pipeline 51, a second cooling gas inlet pipeline 52, a second cooling gas delivery pipeline 53, a second hot gas delivery pipeline 54 and a second desorption concentrated gas pipeline 55 (as shown in fig. 1 to 4). Wherein the first adsorption rotor 30 and the second adsorption rotor 50 are zeolite concentration rotors or concentration rotors made of other materials, respectively.
Wherein one end of the waste gas inlet pipeline 31 is connected to one side of the adsorption region 301 of the first adsorption rotor 30, so that the waste gas inlet pipeline 31 can convey the organic waste gas into the adsorption region 301 of the first adsorption rotor 30, one end of the first net gas discharge pipeline 32 is connected to the other side of the adsorption region 301 of the first adsorption rotor 30, and one end of the first net gas discharge pipeline 32 is connected to one side of the adsorption region 501 of the second adsorption rotor 50, so that the organic waste gas can be conveyed into the adsorption region 501 of the second adsorption rotor 50 by the first net gas discharge pipeline 32 after adsorbing organic matters through the adsorption region 301 of the first adsorption rotor 30. In addition, the other side of the adsorption region 501 of the second adsorption rotor 50 is connected to the second purified gas discharge pipeline 51, and can be connected to the chimney 70 through the other end of the second purified gas discharge pipeline 51 (as shown in fig. 1 and 2), and the second purified gas discharge pipeline 51 is provided with a fan 511 (as shown in fig. 3 and 4), and the gas adsorbed in the second purified gas discharge pipeline 51 is pushed and pulled into the chimney 70 by the fan 511 for discharge.
In addition, the other side of the cooling area 302 of the first adsorption rotor 30 is connected to one end of the first cooling air conveying pipe 33, the other end of the first cooling air conveying pipe 33 is connected to one end of the cold side channel 201 of the heat exchanger 20, and the gas entering the cooling area 302 of the first adsorption rotor 30 can be conveyed into the heat exchanger 20 for heat exchange (as shown in fig. 1 to 4). In addition, the other side of the desorption region 303 of the first adsorption rotor 30 is connected with one end of the first hot gas conveying pipe 34, the hot gas can be conveyed to the desorption region 303 of the first adsorption rotor 30 through the first hot gas conveying pipe 34 for desorption, in addition, one side of the desorption region 303 of the first adsorption rotor 30 is connected with one end of the first desorption concentrated gas pipeline 35, the other end of the first desorption concentrated gas pipeline 35 is connected with the inlet 101 of the incineration device 10 (as shown in fig. 1 to 4), the desorption concentrated gas subjected to high-temperature desorption can be conveyed to the inlet 101 of the incineration device 10 through the first desorption concentrated gas pipeline 35, and the combustion chamber 11 of the incineration device 10 is subjected to high-temperature cracking to reduce volatile organic compounds. The first desorption concentrated gas pipeline 35 is provided with a fan 351 (as shown in fig. 3 and 4) for pushing and pulling the desorption concentrated gas into the inlet 101 of the incineration apparatus 10.
A first cooling gas bypass line 40 (as shown in fig. 2 to 4) is disposed between the first cooling gas delivery line 33 and the first hot gas delivery line 34, one end of the first cooling gas bypass line 40 is connected to the first cooling gas delivery line 33, and the other end of the first cooling gas bypass line 40 is connected to the first hot gas delivery line 34, so that the first cooling gas delivery line 33 branches to deliver a part of the cooled gas into the first hot gas delivery line 34 through the first cooling gas bypass line 40, thereby increasing the temperature of the hot gas in the first hot gas delivery line 34, and in addition, the first cooling gas bypass line 40 is provided with a first cooling gas bypass control valve 401 (as shown in fig. 3 and 4) for controlling the air volume of the first cooling gas bypass line 40. In addition, the first cooling air delivery pipe 33 is provided with a first cooling air delivery control valve 331, which can control the air volume of the first cooling air delivery pipe 33 (as shown in fig. 3), and a proportional damper is formed by the first cooling air bypass control valve 401 and the first cooling air delivery control valve 331. In addition, a first hot gas delivery control valve 341 (as shown in fig. 4) may be disposed on the first hot gas delivery pipeline 34, so as to control the air volume of the first hot gas delivery pipeline 34, and a proportional damper is formed by the first cooling gas bypass control valve 401 and the first hot gas delivery control valve 341. Therefore, the temperature of the hot gas delivered to the desorption region 303 of the first adsorption rotor 30 by the first hot gas delivery line 34 can be adjusted to have the effect of increasing the control temperature.
In addition, the other end of the second cooling gas inlet pipe 52 is connected to one side of the cooling region 502 of the second adsorption rotor 50, so that the gas can enter the cooling region 502 of the second adsorption rotor 50 for cooling, the other side of the cooling region 502 of the second adsorption rotor 50 is connected to one end of the second cooling gas delivery pipe 53, the other end of the second cooling gas delivery pipe 53 is connected to one end of the cold side channel 201 of the heat exchanger 20, so that the gas entering the cooling region 502 of the second adsorption rotor 50 can be delivered into the heat exchanger 20 for heat exchange (as shown in fig. 1 to 4). In addition, the other side of the desorption region 503 of the second adsorption rotor 50 is connected to one end of the second hot gas conveying pipeline 54, and the other end of the second hot gas conveying pipeline 54 is connected to the other end of the cold side channel 201 of the heat exchanger 20, so that the high-temperature hot gas after heat exchange by the heat exchanger 20 can be conveyed into the desorption region 503 of the second adsorption rotor 50 through the second hot gas conveying pipeline 54 for desorption, wherein the second hot gas conveying pipeline 54 is branched and connected to the other end of the first hot gas conveying pipeline 34 (as shown in fig. 1 to 4), so that the high-temperature hot gas after heat exchange by the heat exchanger 20 is branched and conveyed into the desorption region 303 of the first adsorption rotor 30 through the first hot gas conveying pipeline 34 for desorption.
The cooling area 502 of the second sorption rotor 50 has two embodiments, wherein in the first embodiment, one end of the second cooling air inlet pipe 52 connected to one side of the cooling area 502 of the second sorption rotor 50 is used for allowing fresh air or outside air to enter (as shown in fig. 1 and fig. 2), and the cooling area 502 of the second sorption rotor 50 is cooled by the fresh air or the outside air. In the second embodiment, the first net gas discharge pipeline 32 is provided with a first net gas bypass pipeline 80 (as shown in fig. 3 and 4), one end of the first net gas bypass pipeline 80 is connected to the first net gas discharge pipeline 32, the other end of the first net gas bypass pipeline 80 is connected to one end of the second cooling gas inlet pipeline 52, the gas in the first net gas discharge pipeline 32 can be branched and conveyed to the cooling zone 502 of the second adsorption rotating wheel 50 for cooling through the first net gas bypass pipeline 80, in addition, the first net gas bypass pipeline 80 is provided with a first net gas bypass control valve 801 (as shown in fig. 3 and 4), and the air volume of the first net gas bypass pipeline 80 can be controlled.
A second cooling gas bypass line 60 (as shown in fig. 2 to 3) is disposed between the second cooling gas delivery line 53 and the second hot gas delivery line 54, one end of the second cooling gas bypass line 60 is connected to the second cooling gas delivery line 53, the other end of the second cooling gas bypass line 60 is connected to the second hot gas delivery line 54, so that the second cooling gas delivery line 53 branches to deliver the partially cooled gas into the second hot gas delivery line 54 through the second cooling gas bypass line 60, thereby increasing the temperature of the hot gas in the second hot gas delivery line 54, and the second cooling gas bypass line 60 is disposed with a second cooling gas bypass control valve 601 (as shown in fig. 3 and 4) for controlling the air volume of the second cooling gas bypass line 60. In addition, the second cooling air delivery pipe 53 is provided with a second cooling air delivery control valve 531 (as shown in fig. 3), which can control the air volume of the second cooling air delivery pipe 53, and a proportional damper is formed by the second cooling air bypass control valve 601 and the second cooling air delivery control valve 531. In addition, a second hot gas delivery control valve 541 (as shown in fig. 4) may be disposed on the second hot gas delivery pipeline 54, so as to control the air volume of the second hot gas delivery pipeline 54, and a proportional damper is formed by the second cooling gas bypass control valve 601 and the second hot gas delivery control valve 541, so that the temperature of the hot gas delivered to the desorption region 503 of the second adsorption rotor 50 by the second hot gas delivery pipeline 54 can be adjusted, so as to have the function of raising the control temperature.
In addition, one side of the desorption region 503 of the second adsorption rotor 50 is connected to the other end of the second desorption concentrated gas pipeline 55, one end of the second desorption concentrated gas pipeline 55 is connected to one side of the cooling region 302 of the first adsorption rotor 30 (as shown in fig. 1 to 4), so that the desorption concentrated gas desorbed at a high temperature can be conveyed into the cooling region 302 of the first adsorption rotor 30 through the second desorption concentrated gas pipeline 55 for cooling the cooling region 302 of the first adsorption rotor 30, and the second desorption concentrated gas pipeline 55 is provided with a fan 551 (as shown in fig. 3 and 4), so that the desorption concentrated gas can be pushed into the cooling region 302 of the first adsorption rotor 30.
A first purified gas branch line 90 (as shown in fig. 2 to 4) is disposed between the second desorption concentrated gas line 55 and the first purified gas discharge line 32, one end of the first purified gas branch line 90 is connected to the first purified gas discharge line 32, the other end of the first purified gas branch line 90 is connected to the second desorption concentrated gas line 55, so that the gas branch after adsorption in the first purified gas discharge line 32 is delivered into the second desorption concentrated gas line 55 through the first purified gas branch line 90, the temperature of the desorption concentrated gas delivered to the cooling region 302 of the first adsorption rotor 30 through the second desorption concentrated gas line 55 can be adjusted, the temperature of the gas entering the cooling region 302 of the first adsorption rotor 30 is reduced, and the effect of cooling the cooling region 302 of the first adsorption rotor 30 is achieved, and the first purified gas branch line 90 is provided with a first purified gas branch control valve 901 (as shown in fig. 3 and 4) The air volume of the first clean air branch line 90 can be controlled. In addition, the exhaust gas inlet pipeline 31 is provided with a blower 311 (as shown in fig. 3 and 4) for pushing the source gas (organic exhaust gas) in the exhaust gas inlet pipeline 31 into the adsorption region 301 of the first adsorption rotor 30.
Based on the above detailed description, those skilled in the art can understand that the present disclosure can achieve the aforementioned objects, and that the present disclosure meets the requirements of patent laws, and thus, a new and useful patent application is proposed.
Although the present disclosure has been described with reference to the above embodiments, the embodiments are merely preferred embodiments of the disclosure, and the scope of the disclosure is not limited thereto. All simple equivalent changes and modifications made in accordance with the claims and the contents of the specification of the present disclosure are intended to be included within the protection of the present disclosure.
Claims (16)
1. A double-rotary high-concentration organic waste gas treatment system is characterized by comprising:
a chimney;
the incineration equipment is provided with an inlet and an outlet, and the outlet of the incineration equipment is connected with the chimney;
the heat exchanger is provided with a cold side channel and a hot side channel, the heat exchanger is provided with a hot side conveying pipeline and a hot side discharging pipeline, one end of the hot side conveying pipeline is connected with the incineration equipment, the other end of the hot side conveying pipeline is connected with one end of the hot side channel, one end of the hot side discharging pipeline is connected with the other end of the hot side channel, and the other end of the hot side discharging pipeline is connected with the chimney;
a first adsorption rotating wheel, the first adsorption rotating wheel is provided with an adsorption area, a cooling area and a desorption area, the first adsorption rotating wheel is connected with a waste gas inlet pipeline, a first purified gas discharge pipeline, a first cooling gas conveying pipeline, a first hot gas conveying pipeline and a first desorption concentrated gas pipeline, one end of the waste gas inlet pipeline is connected to one side of the adsorption area of the first adsorption rotating wheel, one end of the first purified gas discharge pipeline is connected with the other side of the adsorption area of the first adsorption rotating wheel, one end of the first cooling gas conveying pipeline is connected with the other side of the cooling area of the first adsorption rotating wheel, the other end of the first cooling gas conveying pipeline is connected with one end of a cold side channel of the heat exchanger, one end of the first hot gas conveying pipeline is connected with the other side of the desorption area of the first adsorption rotating wheel, one end of the first desorption concentrated gas pipeline is connected with one side of the desorption area of the first adsorption rotating wheel, the other end of the first desorption concentrated gas pipeline is connected with an inlet of the incineration equipment;
a second adsorption rotating wheel, which is provided with an adsorption zone, a cooling zone and a desorption zone, the second adsorption rotating wheel is connected with a second purified gas discharge pipeline, a second cooling gas inlet pipeline, a second cooling gas conveying pipeline, a second hot gas conveying pipeline and a second desorption concentrated gas pipeline, the other end of the first purified gas discharge pipeline is connected to one side of the adsorption zone of the second adsorption rotating wheel, one end of the second purified gas discharge pipeline is connected with the other side of the adsorption zone of the second adsorption rotating wheel, the other end of the second purified gas discharge pipeline is connected with the chimney, the other end of the second cooling gas inlet pipeline is connected with one side of the cooling zone of the second adsorption rotating wheel, one end of the second cooling gas conveying pipeline is connected with the other side of the cooling zone of the second adsorption rotating wheel, the other end of the second cooling gas conveying pipeline is connected with one end of the cold side channel of the heat exchanger, one end of the second hot gas conveying pipeline is connected with the other side of the desorption area of the second adsorption rotating wheel, the other end of the second hot gas conveying pipeline is connected with the other end of the cold side channel of the heat exchanger, the branch of the second hot gas conveying pipeline is connected with the other end of the first hot gas conveying pipeline, the other end of the second desorption concentrated gas pipeline is connected with one side of the desorption area of the second adsorption rotating wheel, and one end of the second desorption concentrated gas pipeline is connected with one side of the cooling area of the first adsorption rotating wheel; and
and one end of the first purified gas branch pipeline is connected with the first purified gas discharge pipeline, and the other end of the first purified gas branch pipeline is connected with the second desorption concentrated gas pipeline.
2. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein the incineration facility is provided with a combustion chamber, and the combustion chamber is communicated with one end of the hot-side conveying pipeline.
3. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein the incineration equipment is a direct-fired incinerator, a catalytic incinerator or a regenerative incinerator.
4. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein one end of the second cooling gas inlet pipeline is used for fresh air or external gas to enter.
5. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein the first net gas discharge pipeline is provided with a first net gas bypass pipeline, one end of the first net gas bypass pipeline is connected with the first net gas discharge pipeline, the other end of the first net gas bypass pipeline is connected with one end of the second cooling gas inlet pipeline, and the first net gas bypass pipeline is not provided with a first net gas bypass control valve so as to control the air volume of the first net gas bypass pipeline.
6. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein a first cooling gas bypass line is disposed between the first cooling gas delivery line and the first hot gas delivery line, one end of the first cooling gas bypass line is connected to the first cooling gas delivery line, the other end of the first cooling gas bypass line is connected to the first hot gas delivery line, and the first cooling gas bypass line is provided with a first cooling gas bypass control valve for controlling the air volume of the first cooling gas bypass line.
7. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein the first cooling gas delivery line is provided with a first cooling gas delivery control valve for controlling the air volume of the first cooling gas delivery line.
8. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein the first hot gas delivery line is provided with a first hot gas delivery control valve for controlling the air volume of the first hot gas delivery line.
9. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein a second cooling gas bypass line is disposed between the second cooling gas delivery line and the second hot gas delivery line, one end of the second cooling gas bypass line is connected to the second cooling gas delivery line, the other end of the second cooling gas bypass line is connected to the second hot gas delivery line, and the second cooling gas bypass line is provided with a second cooling gas bypass control valve for controlling the air volume of the second cooling gas bypass line.
10. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein the second cooling gas delivery line is provided with a second cooling gas delivery control valve for controlling the air volume of the second cooling gas delivery line.
11. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein the second hot gas delivery line is provided with a second hot gas delivery control valve for controlling the air volume of the second hot gas delivery line.
12. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein the first net gas branch line is provided with a first net gas branch control valve for controlling the air volume of the first net gas branch line.
13. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein the first desorption concentrated gas pipeline is provided with a fan.
14. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein the second desorption concentrated gas pipeline is provided with a fan.
15. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein the second net gas discharge line is provided with a fan.
16. The dual-rotor high-concentration organic waste gas treatment system of claim 1, wherein the waste gas inlet line is provided with a fan.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW109216046U TWM609215U (en) | 2020-12-04 | 2020-12-04 | Dual-wheel high-concentration organic waste gas treatment system |
| TW109216046 | 2020-12-04 |
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| CN214552358U true CN214552358U (en) | 2021-11-02 |
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| CN202120219077.3U Active CN214552358U (en) | 2020-12-04 | 2021-01-26 | Double-rotary-wheel high-concentration organic waste gas treatment system |
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| TW (1) | TWM609215U (en) |
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| TWI826752B (en) * | 2020-12-04 | 2023-12-21 | 華懋科技股份有限公司 | Double-runner high-concentration organic waste gas treatment system and method thereof |
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2020
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