CN215336385U - Runner system - Google Patents
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- CN215336385U CN215336385U CN202121367035.0U CN202121367035U CN215336385U CN 215336385 U CN215336385 U CN 215336385U CN 202121367035 U CN202121367035 U CN 202121367035U CN 215336385 U CN215336385 U CN 215336385U
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- 239000007789 gas Substances 0.000 claims abstract description 103
- 238000001704 evaporation Methods 0.000 claims abstract description 29
- 230000008020 evaporation Effects 0.000 claims abstract description 29
- 238000009833 condensation Methods 0.000 claims abstract description 28
- 230000005494 condensation Effects 0.000 claims abstract description 28
- 239000002912 waste gas Substances 0.000 claims abstract description 22
- 239000003507 refrigerant Substances 0.000 claims abstract description 8
- 238000001179 sorption measurement Methods 0.000 claims description 69
- 238000003795 desorption Methods 0.000 claims description 35
- 238000001816 cooling Methods 0.000 claims description 22
- 239000000112 cooling gas Substances 0.000 claims description 19
- 238000004891 communication Methods 0.000 claims description 10
- 239000010815 organic waste Substances 0.000 abstract description 5
- 238000012546 transfer Methods 0.000 description 9
- 238000002485 combustion reaction Methods 0.000 description 8
- 239000007788 liquid Substances 0.000 description 8
- 238000010586 diagram Methods 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 239000004065 semiconductor Substances 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 238000003915 air pollution 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
- 230000000694 effects Effects 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000011160 research Methods 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 runner system, which is mainly characterized in that a heat pipe is additionally arranged, the heat pipe is provided with an evaporation section and a condensation section, and a refrigerant is arranged in the heat pipe, wherein the evaporation section of the heat pipe is arranged in a hearth of a direct-fired incinerator, the condensation section of the heat pipe is arranged on a waste gas inlet pipeline, so that source waste gas can be heated and treated by the condensation section of the heat pipe, and incinerated gas can be treated by the evaporation section of the heat pipe and can be circulated back and forth through the evaporation section and the condensation section of the heat pipe, so that the treatment efficiency of organic waste gas is improved.
Description
Technical Field
The present invention relates to a rotary wheel system, and more particularly, to an organic waste gas treatment system or the like for improving the organic waste gas treatment efficiency and being suitable for the semiconductor industry, the photovoltaic industry, the chemical industry, or the like.
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 delivered to the incinerator for combustion, and the combusted gas is delivered to a chimney for emission.
Therefore, in view of the above-mentioned shortcomings, the present inventors have desired to provide a wheel system with improved organic waste gas treatment efficiency, which is easy to operate and assemble by users, and therefore, the present inventors have made extensive research and design efforts to provide convenience for users.
SUMMERY OF THE UTILITY MODEL
The present invention provides a rotary wheel system, which is mainly formed by adding a heat pipe having an evaporation section and a condensation section, and a refrigerant in the heat pipe, wherein the evaporation section of the heat pipe is disposed in a furnace chamber of a direct-fired incinerator (TO), and the condensation section of the heat pipe is disposed on the exhaust gas inlet pipeline, so that the source exhaust gas can be heated by the condensation section of the heat pipe, and the burned gas can be treated by the evaporation section of the heat pipe, and circulates back and forth through the evaporation section and the condensation section of the heat pipe, thereby improving the organic exhaust gas treatment efficiency, and further increasing the overall practicability.
Another object of the present invention is to provide a runner system, wherein the heat pipe is composed of the pipe shell and the wick, the liquid absorption core is tightly attached to the inner wall of the pipe shell, when a negative pressure state is formed in the pipe shell, a proper amount of refrigerant is loaded, so that the liquid absorption core tightly attached to the inner wall of the pipe shell can be filled with the refrigerant, when the incinerated gases in the direct-fired incinerator (TO) pass through the evaporator end of the heat pipe, the heat pipe will generate evaporation and vaporization to change liquid into vapor, and the vapor flows to the condensation section of the heat pipe under a slight pressure difference, the condensation phenomenon will be generated in the heat pipe to change the vapor into liquid and then flow back to the evaporation section of the heat pipe, so that the relative humidity of the source waste gas can be reduced by a circulation mode, so as to improve the adsorption efficiency of the adsorption zone entering the adsorption rotating wheel and further increase the whole adsorption property.
The second objective of the present invention is TO provide a runner system, the desorption zone passing through the adsorption runner needs TO be performed by hot gas, and the hot gas has two sources, the first is TO arrange a third heat exchanger in the direct-fired incinerator (TO), the third heat exchanger is arranged between the heat pipe and the first heat exchanger, and one end of the hot gas conveying pipeline is connected with the other side of the desorption zone of the adsorption runner, and the other end of the hot gas conveying pipeline is connected with the other end of the third cold side pipeline of the third heat exchanger, the second is TO arrange a heater, wherein the heater is any one of an air-TO-air heat exchanger, a liquid-TO-air heat exchanger, an electric heater and a gas heater, and the other end of the hot gas conveying pipeline is connected with the heater, and one end of the hot gas conveying pipeline is connected with the other side of the desorption zone of the adsorption runner, the desorption area of the adsorption rotating wheel can have the effect of high-temperature desorption, and the overall operability is further improved.
For a better understanding of the nature, features and aspects of the present invention, reference should be made to the following detailed description of the utility model, taken in conjunction with the accompanying drawings, which are provided for purposes of illustration and description only and are not intended to be limiting.
Drawings
Fig. 1 is a system architecture diagram of a main embodiment of the present invention.
Fig. 2 is another system architecture diagram of the main embodiment of the present invention.
FIG. 3 is a schematic view of a heat pipe according to the present invention.
Fig. 4 is a system architecture diagram according to another embodiment of the present invention.
FIG. 5 is a system architecture diagram according to another embodiment of the present invention.
Description of the reference numerals
10. Direct-fired incinerator (TO)
101. Furnace end
102. Hearth box
11. Inlet port
12. An outlet
20. First heat exchanger
21. First cold side pipeline
22. First hot side pipeline
30. Second heat exchanger
31. Second cold side pipeline
32. Second hot side pipeline
40. Third heat exchanger
41. Third cold side pipeline
42. Third hot side pipeline
50. Heating device
61. First cold side conveying pipeline
62. Second cold side transfer line
70. Adsorption rotating wheel
701. Adsorption zone
702. Cooling zone
703. Desorption zone
71. Waste gas inlet pipeline
711. Waste gas communicating pipeline
7111. Waste gas communicating control valve
712. Fan blower
72. Clean gas discharge pipeline
721. Fan blower
73. Cooling gas inlet pipeline
74. Cooling gas conveying pipeline
75. Hot gas conveying pipeline
76. Concentrated gas desorption pipeline
761. Fan blower
80. Chimney
90. Heat pipe
901. Evaporation section
902. Condensation section
91. Pipe shell
92. Liquid absorption core
Detailed Description
Referring to fig. 1 to 5, there are shown schematic diagrams illustrating an embodiment of the present invention, and a preferred embodiment of the wheel system of the present invention is applied to a voc emission treatment system or the like in the semiconductor industry, the photovoltaic industry or the chemical industry to improve the efficiency of the organic emission treatment.
The runner system of the present invention mainly includes a combination design of a direct-fired incinerator (TO)10, a first heat exchanger 20, a second heat exchanger 30, a third heat exchanger 40, a first cold-side delivery pipe 61, a second cold-side delivery pipe 62, an adsorption runner 70, a chimney 80 and a heat pipe 90 (as shown in fig. 1 TO 2), wherein the first heat exchanger 20 is provided with a first cold-side pipe 21 and a first hot-side pipe 22, the second heat exchanger 30 is provided with a second cold-side pipe 31 and a second hot-side pipe 32, and the third heat exchanger 40 is provided with a third cold-side pipe 41 and a third hot-side pipe 42. In addition, the direct-fired incinerator (TO)10 is provided with a furnace end 101 and a furnace chamber 102, the furnace end 101 is communicated with the furnace chamber 102, the first heat exchanger 20, the second heat exchanger 30 and the third heat exchanger 40 are respectively arranged in the furnace chamber 102 of the direct-fired incinerator (TO)10, the direct-fired incinerator (TO)10 is provided with an inlet 11 and an outlet 12, the inlet 11 is arranged at the furnace end 101, and the outlet 12 of the direct-fired incinerator (TO)10 is connected TO the chimney 80, so that organic waste gas can enter the furnace end 101 from the inlet 11 for combustion, and combusted gas can pass through the furnace chamber 102 and be discharged TO the chimney 80 from the outlet 11 for discharge, thereby having the efficiency of saving energy.
The adsorption rotor 70 of the present invention is further provided with an adsorption zone 701, a cooling zone 702 and a desorption zone 703, and the adsorption rotor 70 is connected to a waste gas inlet line 71, a clean gas discharge line 72, a cooling gas inlet line 73, a cooling gas delivery line 74, a hot gas delivery line 75 and a desorption concentrated gas line 76 (as shown in fig. 1 to 2). Wherein the adsorption wheel 70 is a zeolite concentration wheel or a concentration wheel made of other materials. One end of the waste gas inlet pipe 71 is connected to one side of the adsorption region 701 of the adsorption rotor 70, so that the waste gas inlet pipe 71 can deliver the source waste gas to one side of the adsorption region 701 of the adsorption rotor 70, one end of the clean gas discharge pipe 72 is connected to the other side of the adsorption region 701 of the adsorption rotor 70, the other end of the clean gas discharge pipe 72 is connected to the chimney 80, and the clean gas discharge pipe 72 is provided with a fan 721 (shown in fig. 2), so that the adsorbed gas in the clean gas discharge pipe 72 can be pushed and pulled into the chimney 80 by the fan 721 to be discharged.
In addition, one side of the cooling region 702 of the sorption rotor 70 is connected to the cooling gas inlet pipe 73 for allowing the gas to enter the cooling region 702 of the sorption rotor 70 for cooling, the other side of the cooling region 702 of the sorption rotor 70 is connected to one end of the cooling gas conveying pipe 74, and the other end of the cooling gas conveying pipe 74 is connected to one end of the third cold-side pipe 41 of the third heat exchanger 40 (as shown in fig. 1 to 2), so as to convey the gas entering the cooling region 702 of the sorption rotor 70 into the third heat exchanger 40 for heat exchange. Furthermore, one end of the hot gas conveying pipeline 75 is connected to the other side of the desorption region 703 of the adsorption rotor 70, and the other end of the hot gas conveying pipeline 75 is connected to the other end of the third cold-side pipeline 41 of the third heat exchanger 40, so that the high-temperature hot gas heat-exchanged by the third heat exchanger 40 can be conveyed to the desorption region 703 of the adsorption rotor 70 through the hot gas conveying pipeline 75 for desorption.
The cooling zone 702 of the sorption rotor 70 has two embodiments, wherein the first embodiment is that the cooling air inlet pipe 73 connected to one side of the cooling zone 702 of the sorption rotor 70 is used for introducing fresh air or external air (as shown in fig. 1), and the cooling zone 702 of the sorption rotor 70 is cooled by the fresh air or the external air. In the second embodiment, the exhaust gas inlet pipe 71 is provided with an exhaust gas communication pipe 711, and the other end of the exhaust gas communication pipe 711 is connected to the cooling gas inlet pipe 73 (as shown in fig. 2) so as to convey the source exhaust gas in the exhaust gas inlet pipe 71 to the cooling zone 702 of the sorption rotary wheel 70 for cooling through the exhaust gas communication pipe 711, and the exhaust gas communication pipe 711 is provided with an exhaust gas communication control valve 7111 (as shown in fig. 2) so as to control the air volume of the exhaust gas communication pipe 711.
In addition, one end of the desorption concentrated gas pipe 76 is connected TO one side of the desorption region 703 of the adsorption rotor 70, and the other end of the desorption concentrated gas pipe 76 is connected TO one end of the first cold-side pipe 21 of the first heat exchanger 20, wherein the other end of the first cold-side pipe 21 of the first heat exchanger 20 is connected TO one end of the first cold-side transfer pipe 61, the other end of the first cold-side transfer pipe 61 is connected TO one end of the second cold-side pipe 31 of the second heat exchanger 30, the other end of the second cold-side pipe 31 of the second heat exchanger 30 is connected TO one end of the second cold-side transfer pipe 62, and the other end of the second cold-side transfer pipe 62 is connected TO the inlet 11 of the direct-fired incinerator (TO)10 (as shown in fig. 1 TO 2), so that the desorption concentrated gas desorbed at a high temperature can be transferred into one end of the first cold-side pipe 21 of the first heat exchanger 20 through the desorption concentrated gas pipe 76, and is transferred from the other end of the first cold-side pipe 21 of the first heat exchanger 20 TO one end of the first cold-side transfer pipe 61, from the other end of the first cold-side transfer pipe 61 TO one end of the second cold-side pipe 31 of the second heat exchanger 30, from the other end of the second cold-side pipe 31 of the second heat exchanger 30 TO one end of the second cold-side transfer pipe 62, and finally from the other end of the second cold-side transfer pipe 62 TO the inlet 11 of the direct combustion type incinerator (TO)10, so that the burner 101 of the direct combustion type incinerator (TO)10 can be pyrolyzed TO reduce volatile organic compounds. The desorption concentrate gas line 76 is further provided with a blower 761 (as shown in fig. 2) for pushing and pulling the desorption concentrate gas into one end of the first cold-side line 21 of the first heat exchanger 20.
Furthermore, the present invention mainly adds a heat pipe 90, wherein the heat pipe 90 has an evaporation section 901 and a condensation section 902 (as shown in fig. 3), wherein the evaporation section 901 of the heat pipe 90 is disposed in the furnace 102 of the direct-fired incinerator (TO)10, one end of the evaporation section 901 of the heat pipe 90 is connected TO the other end of the second hot-side pipeline 32 of the second heat exchanger 30, the other end of the evaporation section 901 of the heat pipe 90 is connected TO one end of the third hot-side pipeline 42 of the third heat exchanger 40 (as shown in fig. 1 TO 2), the condensation section 902 of the heat pipe 90 is disposed on the exhaust gas inlet pipeline 71, the exhaust gas from the exhaust gas inlet pipeline 71 first enters one end of the condensation section 902 of the heat pipe 90, then is output from the other end of the condensation section 902 of the heat pipe 90, and is delivered TO one side of the adsorption region 701 of the adsorption rotor 70 through the exhaust gas inlet pipeline 71 (as shown in fig. 1 TO 2), the source exhaust gas can be heated by passing through the condensation section 902 of the heat pipe 90, and the incinerated gas can be treated by passing through the evaporation section 901 of the heat pipe 90. The exhaust gas inlet line 71 is further provided with a blower 712 (shown in fig. 2) to push and pull source exhaust gas into one end of the condenser section 902 of the heat pipe 90.
The heat pipe 90 is composed of the pipe shell 91 and the wick 92, the wick 92 is tightly attached to the inner wall of the pipe shell 91 (as shown in fig. 3), when a negative pressure state is formed in the pipe shell 91 and a proper amount of refrigerant is loaded, the liquid absorption core 92 tightly attached to the inner wall of the pipe shell 91 can be filled with the refrigerant, when the burned gas in the direct combustion incinerator (TO)10 passes through the evaporation section 901 of the heat pipe 90, evaporation and vaporization occur in the heat pipe 90 to change the liquid into vapor, and the vapor flows to the condensation section 902 of the heat pipe 90 under a slight pressure difference, and when the source exhaust gas passes through the condensation section 902 of the heat pipe 90, condensation occurs within the heat pipe 90 to change the vapor to a liquid, which then flows back to the evaporator end 901 of the heat pipe 90, and the evaporation section 901 and the condensation section 902 of the heat pipe 90 circulate back and forth, so that the relative humidity of the source exhaust gas is reduced, thereby enhancing the adsorption efficiency of the adsorption zone 701 entering the adsorption wheel 70.
The burner 101 of the direct combustion type incinerator (TO)10 can firstly deliver the burned gas TO one side of the second hot side pipeline 32 of the second heat exchanger 30 for heat exchange, then the burned gas is delivered TO the evaporation section 901 of the heat pipe 90 from the other side of the second hot side pipeline 32 of the second heat exchanger 30 (as shown in fig. 1 TO 2), and the burned gas passes through the evaporation section 901 of the heat pipe 90 and is delivered TO one side of the third hot side pipeline 42 of the third heat exchanger 40 for heat exchange, then the burned gas is delivered TO one side of the first hot side pipeline 22 of the first heat exchanger 20 for heat exchange from the other side of the third hot side pipeline 42 of the third heat exchanger 40 and is finally delivered TO the outlet 12 of the direct combustion type incinerator (TO)10 from the other side of the first hot side pipeline 22 of the first heat exchanger 20, and then delivered from the outlet 12 of the direct combustion incinerator (TO)10 TO a chimney 80 (shown in fig. 1 TO 2) TO be discharged through the chimney 80.
Further, another embodiment of the runner system of the present invention (as shown in fig. 4 TO 5) is provided, wherein the direct-fired incinerator (TO)10, the first heat exchanger 20, the second heat exchanger 30, the first cold-side delivery pipe 61, the second cold-side delivery pipe 62, the sorption runner 70, the chimney 80 and the heat pipe 90 are designed in the same manner as described above, and therefore, the contents of the direct-fired incinerator (TO)10, the first heat exchanger 20, the second heat exchanger 30, the first cold-side delivery pipe 61, the second cold-side delivery pipe 62, the sorption runner 70, the chimney 80 and the heat pipe 90 are not repeated.
The difference is that in another embodiment, the third heat exchanger 40 connected TO the other end of the hot gas conveying pipeline 75 and disposed inside the furnace chamber 102 of the direct-fired incinerator (TO)10 is removed, and the other end of the hot gas conveying pipeline 75 is connected TO a heater 50 (as shown in fig. 4 TO 5) disposed outside the furnace chamber 102 of the direct-fired incinerator (TO)10, wherein the heater 50 is any one of an air-TO-air heat exchanger, a liquid-TO-air heat exchanger, an electric heater, and a gas heater, the other end of the cooling gas conveying pipeline 74 connected TO the other side of the cooling zone 702 of the adsorption rotating wheel 70 is connected TO the heater 50 (as shown in fig. 1 TO 2), so as TO convey the gas after entering the cooling zone 702 of the adsorption rotating wheel 70 into the heater 50 for heating, and one end of the hot gas conveying pipeline 75 is connected TO the other side of the desorption zone 703 of the adsorption rotating wheel 70, and the other end of the hot gas conveying pipeline 75 is connected to the heater 50, so that the high-temperature hot gas heated by the heater 50 can be conveyed to the desorption region 703 of the adsorption rotor 70 through the hot gas conveying pipeline 75 for desorption.
From the foregoing detailed description, one skilled in the art will understand that the utility model does indeed achieve the foregoing objects, and that it has been submitted with the requirements of the patent laws, and that it is submitted with the claims that follow.
The above description is only a preferred embodiment of the present invention, and the protection scope of the present invention should not be limited thereby; all simple equivalent changes and modifications made within the claims and the specification of the present invention shall still fall within the protection scope of the present invention.
Claims (10)
1. A wheel system, comprising:
the direct-fired incinerator is provided with a furnace end and a hearth, the furnace end is communicated with the hearth, the direct-fired incinerator is provided with an inlet and an outlet, and the inlet is arranged at the furnace end;
the first heat exchanger is arranged in a hearth of the direct-fired incinerator and is provided with a first cold-side pipeline and a first hot-side pipeline;
the second heat exchanger is arranged in a hearth of the direct-fired incinerator and is provided with a second cold-side pipeline and a second hot-side pipeline;
the third heat exchanger is arranged in a hearth of the direct-fired incinerator and is provided with a third cold-side pipeline and a third hot-side pipeline;
the first cold side conveying pipeline is connected with one end of the first cold side pipeline, and the other end of the first cold side conveying pipeline is connected with one end of the second cold side pipeline;
one end of the second cold side conveying pipeline is connected with the other end of the second cold side pipeline, and the other end of the second cold side conveying pipeline is connected with an inlet of the direct-fired incinerator;
an adsorption rotating wheel, the adsorption rotating wheel is provided with an adsorption area, a cooling area and a desorption area, the adsorption rotating wheel is connected with a waste gas inlet pipeline, a clean gas discharge pipeline, a cooling gas inlet pipeline, a cooling gas conveying pipeline, a hot gas conveying pipeline and a desorption concentrated gas pipeline, one end of the waste gas inlet pipeline is connected to one side of the adsorption area of the adsorption rotating wheel, one end of the clean gas discharge pipeline is connected with the other side of the adsorption area of the adsorption rotating wheel, one end of the cooling gas inlet pipeline is connected with one side of the cooling area of the adsorption rotating wheel, one end of the cooling gas conveying pipeline is connected with the other side of the cooling area of the adsorption rotating wheel, the other end of the cooling gas conveying pipeline is connected with one end of a third cold side pipeline of a third heat exchanger, one end of the hot gas conveying pipeline is connected with the other side of the desorption area of the adsorption rotating wheel, and the other end of the hot gas conveying pipeline is connected with the other end of the third cold side pipeline of the third heat exchanger, one end of the desorption concentrated gas pipeline is connected with one side of the desorption area of the adsorption rotating wheel, and the other end of the desorption concentrated gas pipeline is connected with one end of the first cold side pipeline of the first heat exchanger;
the other end of the purified gas discharge pipeline is connected with the chimney; and
the heat pipe is provided with an evaporation section and a condensation section, the evaporation section of the heat pipe is arranged in the hearth of the direct-fired incinerator, one end of the evaporation section of the heat pipe is connected with the other end of the second hot side pipeline of the second heat exchanger, the other end of the evaporation section of the heat pipe is connected with one end of the third hot side pipeline of the third heat exchanger, the condensation section of the heat pipe is arranged on the waste gas inlet pipeline, and source waste gas of the waste gas inlet pipeline firstly enters one end of the condensation section of the heat pipe and then is output from the other end of the condensation section of the heat pipe, and is conveyed to one side of the adsorption area of the adsorption rotating wheel through the waste gas inlet pipeline.
2. A wheel system, comprising:
the direct-fired incinerator is provided with a furnace end and a hearth, the furnace end is communicated with the hearth, the direct-fired incinerator is provided with an inlet and an outlet, and the inlet is arranged at the furnace end;
the first heat exchanger is arranged in a hearth of the direct-fired incinerator and is provided with a first cold-side pipeline and a first hot-side pipeline;
the second heat exchanger is arranged in a hearth of the direct-fired incinerator and is provided with a second cold-side pipeline and a second hot-side pipeline;
the first cold side conveying pipeline is connected with one end of the first cold side pipeline, and the other end of the first cold side conveying pipeline is connected with one end of the second cold side pipeline;
one end of the second cold side conveying pipeline is connected with the other end of the second cold side pipeline, and the other end of the second cold side conveying pipeline is connected with an inlet of the direct-fired incinerator;
an adsorption runner, which is provided with an adsorption area, a cooling area and a desorption area, and is connected with a waste gas inlet pipeline, a purified gas discharge pipeline, a cooling gas inlet pipeline, a cooling gas conveying pipeline, a hot gas conveying pipeline and a desorption concentrated gas pipeline, one end of the waste gas inlet pipeline is connected to one side of the adsorption area of the adsorption rotating wheel, one end of the purified gas discharge pipeline is connected with the other side of the adsorption area of the adsorption rotating wheel, one end of the cooling gas inlet pipeline is connected with one side of the cooling area of the adsorption rotating wheel, one end of the cooling gas conveying pipeline is connected with the other side of the cooling area of the adsorption rotating wheel, one end of the hot gas conveying pipeline is connected with the other side of the desorption area of the adsorption rotating wheel, one end of the desorption concentrated gas pipeline is connected with one side of the desorption area of the adsorption rotating wheel, the other end of the desorption concentrated gas pipeline is connected with one end of a first cold side pipeline of the first heat exchanger;
the other end of the purified gas discharge pipeline is connected with the chimney; and
the heat pipe is provided with an evaporation section and a condensation section, the evaporation section of the heat pipe is arranged in the hearth of the direct-fired incinerator, one end of the evaporation section of the heat pipe is connected with the other end of the second hot side pipeline of the second heat exchanger, the other end of the evaporation section of the heat pipe is connected with one end of the first hot side pipeline of the first heat exchanger, the condensation section of the heat pipe is arranged on the waste gas inlet pipeline, and source waste gas of the waste gas inlet pipeline firstly enters one end of the condensation section of the heat pipe and then is output from the other end of the condensation section of the heat pipe, and is conveyed to one side of the adsorption area of the adsorption rotating wheel through the waste gas inlet pipeline.
3. The runner system of claim 1 or 2, wherein the outlet of the direct-fired incinerator is further connected to the chimney.
4. The runner system of claim 1 or claim 2, wherein the cooling air inlet duct is further accessible for fresh air or external air.
5. The rotary wheel system according to claim 1 or 2, wherein the exhaust gas inlet pipe is further provided with an exhaust gas communication pipe connected to the cooling gas inlet pipe, and the exhaust gas communication pipe is further provided with an exhaust gas communication control valve for controlling the air volume of the exhaust gas communication pipe.
6. The runner system of claim 1 or 2, wherein the desorption/concentration gas pipeline is further provided with a fan.
7. The runner system of claim 1 or 2, wherein the net gas discharge conduit is further provided with a fan.
8. The runner system of claim 1 or 2, wherein the exhaust gas inlet conduit is further provided with a fan.
9. The runner system of claim 2, wherein the other end of the cold air delivery pipeline is further connected to a heater, and the other end of the hot air delivery pipeline is further connected to the heater, wherein the heater is further any one of an air-to-air heat exchanger, a liquid-to-air heat exchanger, an electric heater, and a gas heater.
10. The runner system of claim 1 or 2, wherein the heat pipe further comprises a pipe shell and a wick, the wick is tightly attached to the inner wall of the pipe shell, and a proper amount of refrigerant is filled after a negative pressure state is formed in the pipe shell, so that the wick tightly attached to the inner wall of the pipe shell can be filled with the refrigerant.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| TW110205276U TWM620880U (en) | 2021-05-11 | 2021-05-11 | Rotation wheel system having heat source |
| TW110205276 | 2021-05-11 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN215336385U true CN215336385U (en) | 2021-12-28 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121367035.0U Active CN215336385U (en) | 2021-05-11 | 2021-06-18 | Runner system |
Country Status (2)
| Country | Link |
|---|---|
| CN (1) | CN215336385U (en) |
| TW (1) | TWM620880U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115325550A (en) * | 2021-05-11 | 2022-11-11 | 华懋科技股份有限公司 | Rotating wheel system with heat source and method thereof |
-
2021
- 2021-05-11 TW TW110205276U patent/TWM620880U/en unknown
- 2021-06-18 CN CN202121367035.0U patent/CN215336385U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115325550A (en) * | 2021-05-11 | 2022-11-11 | 华懋科技股份有限公司 | Rotating wheel system with heat source and method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| TWM620880U (en) | 2021-12-11 |
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