TW202243726A - Runner system with heat source and its method mainly designed by adding a heat pipe, which has an evaporation section and a condensation section to be circulated back and forth to improve the efficiency of organic waste gas treatment - Google Patents

Abstract

The present invention relates to a runner system with heat source and its method, which is mainly designed by adding a heat pipe. The heat pipe has an evaporation section and a condensation section, and there is refrigerant in the heat pipe. The evaporation section of the heat pipe is set in the hearth of the direct-fired thermal oxidizer (TO), and the condensation section of the heat pipe is set on the exhaust gas inlet pipe, such that the exhaust gas from the source can be heated through the condensation section of the heat pipe, and the gas after fired can be treated through the evaporation section of the heat pipe. Further, the evaporation section and the condensation section of the heat pipe are circulated back and forth to improve the efficiency of organic waste gas treatment.

Description

Rotor system with heat source and method thereof

The present invention relates to a rotary system with a heat source and its method, especially to an organic waste gas treatment system or similar equipment that can improve the efficiency of organic waste gas treatment and is suitable for semiconductor industry, photoelectric industry or chemical related industries.

Press, at present, volatile organic gases (VOC) are produced in the manufacturing process of the semiconductor industry or the optoelectronic industry. Therefore, processing equipment for processing volatile organic gases (VOC) will be installed in each factory area to avoid (VOC) directly into the air and cause air pollution. At present, most of the concentrated gas desorbed by the processing equipment is transported to the incinerator for combustion, and then the combusted gas is transported to the chimney for emission.

However, in recent years, the government has attached great importance to air pollution. Therefore, it has established relevant air quality standards for chimney emission standards. At the same time, it will be reviewed periodically in accordance with the development of international control trends.

Therefore, in view of the above deficiencies, the inventor hopes to propose a rotary system with a heat source and its method that can improve the efficiency of organic waste gas treatment, so that users can easily operate and assemble. User convenience is the motivation for the invention that the inventor wants to develop.

The main purpose of the present invention is to provide a runner system with a heat source and its method. Method, mainly through the design of adding a heat pipe, the heat pipe has an evaporation section and a condensation section, and there is a refrigerant in the heat pipe, wherein the evaporation section of the heat pipe is set in the furnace of the direct-fired incinerator (TO) and the condensing section of the heat pipe is set on the exhaust gas inlet pipe, so that the source exhaust gas can pass through the condensing section of the heat pipe for heat treatment, and the incinerated gas can be processed through the evaporating section of the heat pipe, and pass through the The evaporating section and the condensing section of the heat pipe circulate back and forth to improve the efficiency of organic waste gas treatment, thereby increasing the overall practicability.

Another object of the present invention is to provide a runner system with a heat source and its method, wherein the heat pipe is composed of the tube shell and a liquid-absorbing core, and the liquid-absorbing core is closely attached to the inner wall of the tube shell, When the negative pressure state is formed in the shell, there is an appropriate amount of refrigerant, so that the liquid-absorbing core close to the inner wall of the shell can be filled with refrigerant. When the incinerated gas in the direct-fired incinerator (TO) passes through the In the evaporation section of the heat pipe, evaporation and gasification will occur in the heat pipe to change the liquid into vapor, and the vapor will flow to the condensation section of the heat pipe under a small pressure difference. When the exhaust gas from the source passes through the condensation section of the heat pipe, the heat pipe will Condensation will occur in the interior to change the vapor into liquid, and then return to the evaporation section of the heat pipe, so that the relative humidity of the source exhaust gas can be reduced through circulation, so as to improve the adsorption efficiency of the adsorption area entering the adsorption wheel, and then Increase the overall adsorption.

The second object of the present invention is to provide a wheel system with a heat source and its method. The desorption zone of the adsorption wheel needs to be carried out through hot gas, and there are two sources of the hot gas. The first is the direct There is a third heat exchanger in the fired incinerator (TO), the third heat exchanger is set between the heat pipe and the first heat exchanger, and one end of the hot gas delivery pipeline is connected to the adsorption converter The other side of the desorption area of the wheel is connected, and the other end of the hot gas delivery pipeline is connected to the other end of the third cold side pipeline of the third heat exchanger, and the second type is provided with a heater, The heaters are air-to-air heat exchangers, liquid-to-air heat exchangers, electric heaters, and gas heaters. One of them, and the other end of the hot gas delivery pipeline is connected to the heater, and one end of the hot gas delivery pipeline is connected to the other side of the desorption area of the adsorption wheel, so that the adsorption wheel The desorption zone can have the effect of high temperature desorption, thereby increasing the overall operability.

In order to further understand the features, characteristics and technical content of the present invention, please refer to the following detailed description and drawings related to the present invention, but the attached drawings are only for reference and illustration, and are not intended to limit the present invention.

10: Direct fired incinerator (TO)

101: Stove head

102: Furnace

11: Entrance

12: Export

20: First heat exchanger

21: The first cold side pipeline

22: The first hot side pipeline

30: Second heat exchanger

31: Second cold side pipeline

32: Second hot side pipeline

40: The third heat exchanger

41: The third cold side pipeline

42: The third hot side pipeline

50: heater

61: The first cold side delivery pipeline

62: Second cold side delivery pipeline

70: Adsorption Wheel

701: adsorption area

702: cooling zone

703: Desorption area

71: Exhaust gas intake pipe

711: Exhaust gas communication pipeline

7111: Exhaust gas connection control valve

712: fan

72: Net gas discharge pipeline

721: fan

73: Cooling air intake pipe

74: Cooling air delivery pipeline

75: Hot gas delivery pipeline

76: Desorption concentrated gas pipeline

761: fan

80: chimney

90: heat pipe

901: evaporation section

902: condensation section

91: shell

92: Liquid absorbent core

S100: Source exhaust gas for transportation

S200: Source exhaust gas for transportation

S110: source exhaust gas through the heat pipe

S210: source exhaust gas through heat pipe

S120: Adsorption by the adsorption wheel

S220: Adsorption by the adsorption wheel

S130: Input the cooling air in the cooling zone

S230: Input the cooling air in the cooling zone

S140: Desorption in the desorption area

S240: Desorption in the desorption area

S150: Desorption concentrated gas delivery

S250: Desorption Concentrated Gas Delivery

S160: Transportation of incinerated gas

S260: Transportation of incinerated gas

S170: The gas after incineration passes through the pipe body

S270: The gas after incineration passes through the pipe body

S180: Gas outlet output after incineration

S280: Gas outlet output after incineration

Figure 1 is a schematic diagram of the system architecture of the main implementation of the present invention.

FIG. 2 is a schematic diagram of another system architecture of the main implementation aspect of the present invention.

Figure 3 is a schematic diagram of the heat pipe of the present invention.

FIG. 4 is a schematic diagram of the system architecture of another embodiment of the present invention.

FIG. 5 is a schematic diagram of the system architecture of another embodiment of the present invention.

Fig. 6 is a flow chart of the main steps of the main implementation of the present invention.

Fig. 7 is a flow chart of main steps of another embodiment of the present invention.

Please refer to Figures 1 to 7, which are schematic diagrams of embodiments of the present invention, and the best implementation of the runner system with a heat source and its method of the present invention is to apply to volatile organic compounds in the semiconductor industry, optoelectronic industry or chemical related industries Waste gas treatment system or similar equipment to improve the efficiency of organic waste gas treatment.

And the runner system of the tool heat source of the present invention mainly comprises direct fired incinerator (TO) 10, a first heat exchanger 20, a second heat exchanger 30, a third heat exchanger 4 0. Combination design of a first cold-side delivery pipeline 61, a second cold-side delivery pipeline 62, an adsorption runner 70, a chimney 80 and a heat pipe 90 (as shown in Figures 1 to 2) , wherein the first heat exchanger 20 is provided with a first cold side pipeline 21 and a first hot side pipeline 22, and the second heat exchanger 30 is provided with a second cold side pipeline 31 and a second hot side pipeline Pipeline 32 , the third heat exchanger 40 is provided with a third cold side pipeline 41 and a third hot side pipeline 42 . In addition, this direct-fired incinerator (TO) 10 is provided with a burner 101 and a furnace 102, and the burner 101 is communicated with the furnace 102, and the first heat exchanger 20, the second heat exchanger 30 and the The third heat exchanger 40 is respectively located in the furnace 102 of the direct-fired incinerator (TO) 10, and the direct-fired incinerator (TO) 10 is provided with an inlet 11 and an outlet 12, and the inlet 11 is Located at the burner 101, and the outlet 12 of the direct-fired incinerator (TO) 10 is connected to the chimney 80, whereby organic waste gas can enter the burner 101 from the inlet 11 for combustion, Then let the combusted gas pass through the furnace 102 and be discharged from the outlet 11 to the chimney 80 for emission, so as to save energy.

In addition, the adsorption runner 70 of the present invention is provided with an adsorption zone 701, a cooling zone 702 and a desorption zone 703. The adsorption runner 70 is connected with a waste gas inlet pipeline 71, a clean gas discharge pipeline 72, a cooling gas Air intake pipeline 73, a cooling gas delivery pipeline 74, a hot gas delivery pipeline 75 and a desorbed concentrated gas pipeline 76 (as shown in Figures 1 to 2). Wherein the adsorption runner 70 is a zeolite concentration runner or a concentration runner made of other materials. And one end of the exhaust gas inlet pipeline 71 is connected to one side of the adsorption zone 701 of the adsorption runner 70, so that the exhaust gas inlet pipeline 71 can deliver the source exhaust gas to the adsorption zone 701 of the adsorption runner 70. One side, and one end of the clean gas discharge pipeline 72 is connected with the other side of the adsorption zone 701 of the adsorption runner 70, and the other end of the clean gas discharge pipeline 72 is connected with the chimney 80, And this clean gas discharge pipeline 72 is provided with a fan 721 (as shown in Figure 2), so that the gas after adsorption in the clean gas discharge pipeline 72 can be pushed and pulled into the chimney 80 through the fan 721 to discharge.

In addition, one side of the cooling zone 702 of the adsorption runner 70 is connected to the cooling gas inlet pipeline 73, so that the gas enters the cooling zone 702 of the adsorption runner 70 for cooling, and the cooling of the adsorption runner 70 The other side of the zone 702 is connected to one end of the cooling air delivery pipeline 74, and the other end of the cooling air delivery pipeline 74 is connected to one end of the third cold side pipeline 41 of the third heat exchanger 40 (such as 1 to 2), to transport the gas entering the cooling zone 702 of the adsorption wheel 70 to the third heat exchanger 40 for heat exchange. Furthermore, one end of the hot gas delivery pipeline 75 is connected to the other side of the desorption zone 703 of the adsorption wheel 70, and the other end of the hot gas delivery pipeline 75 is connected to the third heat exchanger 40. The other end of the three cold side pipelines 41 is connected so that the high-temperature hot gas exchanged through the third heat exchanger 40 can be transported to the desorption zone 703 of the adsorption runner 70 through the hot gas delivery pipeline 75 Detach and use.

The above-mentioned cooling zone 702 of the adsorption runner 70 is provided with two implementations, wherein the first implementation is that the cooling air intake pipeline 73 connected to one side of the cooling zone 702 of the adsorption runner 70 is For fresh air or external air to enter (as shown in Figure 1), the cooling zone 702 of the adsorption runner 70 is provided for cooling through the fresh air or external air. Another second embodiment is that the exhaust gas inlet pipeline 71 is provided with an exhaust gas communication pipeline 711, and the other end of the exhaust gas communication pipeline 711 is connected with the cooling air inlet pipeline 73 (as shown in FIG. 2 ). shown), so that the source exhaust gas in the exhaust gas intake pipeline 71 can be transported to the cooling zone 702 of the adsorption runner 70 through the exhaust gas communication pipeline 711 for use in cooling, and the exhaust gas The communication pipeline 711 is provided with an exhaust gas communication control valve 7111 (as shown in FIG. 2 ) to control the air volume of the exhaust gas communication pipeline 711 .

In addition, one end of the desorption concentrated gas pipeline 76 is connected to one side of the desorption zone 703 of the adsorption wheel 70, and the other end of the desorption concentrated gas pipeline 76 is connected to the first heat exchanger 20. One end of the first cold side pipeline 21 is connected, wherein the other end of the first cold side pipeline 21 of the first heat exchanger 20 is connected with one end of the first cold side delivery pipeline 61, the first cold side The other end of the delivery pipeline 61 is connected to one end of the second cold side pipeline 31 of the second heat exchanger 30, and the other end of the second cold side pipeline 31 of the second heat exchanger 30 is connected to the second heat exchanger 30. One end of the second cold-side delivery pipeline 62 is connected, and the other end of the second cold-side delivery pipeline 62 is connected with the inlet 11 of the direct-fired incinerator (TO) 10 (as shown in Figure 1 to Figure 2 shown), so that the desorbed concentrated gas desorbed at high temperature can be transported to one end of the first cold side pipeline 21 of the first heat exchanger 20 through the desorbed concentrated gas pipeline 76, And from the other end of the first cold side pipeline 21 of the first heat exchanger 20 to be transported into one end of the first cold side delivery pipeline 61, and from the other end of the first cold side delivery pipeline 61 to be transported to one end of the second cold side pipeline 31 of the second heat exchanger 30, and then transported to the second cold side by the other end of the second cold side pipeline 31 of the second heat exchanger 30 One end of the delivery pipeline 62, and finally transported to the inlet 11 of the direct-fired incinerator (TO) 10 by the other end of the second cold-side delivery pipeline 62, so that the direct-fired incinerator (TO) TO) 10 furnace head 101 to carry out pyrolysis, to reduce volatile organic compounds. In addition, the desorption concentrated gas pipeline 76 is provided with a fan 761 (as shown in Figure 2), so that the desorbed concentrated gas can be pushed and pulled into one end of the first cold side pipeline 21 of the first heat exchanger 20 Inside.

Furthermore, the present invention is mainly through the design of adding a heat pipe 90, the heat pipe 9 O has an evaporation section 901 and a condensation section 902 (as shown in Figure 3), wherein the evaporation section 901 of the heat pipe 90 is set in the furnace 102 of the direct-fired incinerator (TO) 10, and the heat pipe One end of the evaporation section 901 of the heat pipe 90 is connected to the other end of the second heat side pipeline 32 of the second heat exchanger 30, and the other end of the evaporation section 901 of the heat pipe 90 is connected to the third heat exchanger 40. One end of the third hot side pipeline 42 is connected (as shown in the first figure to the second figure), and the condensation section 902 of the heat pipe 90 is arranged on the exhaust gas inlet pipeline 71, and the exhaust gas inlet pipeline 71 The source exhaust gas 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 transported to the adsorption area 701 of the adsorption runner 70 through the exhaust gas inlet pipeline 71 One side (as shown in FIG. 1 to FIG. 2 ) allows source exhaust gas to pass through the condensation section 902 of the heat pipe 90 for heat treatment, and the incinerated gas can pass through the evaporation section 901 of the heat pipe 90 for processing. In addition, the waste gas intake pipeline 71 is provided with a fan 712 (as shown in FIG. 2 ), so as to push and pull the source waste gas into one end of the condensation section 902 of the heat pipe 90 .

And above-mentioned heat pipe 90 is made up of this pipe shell 91 and liquid-absorbing core 92, and this liquid-absorbing core 92 is close on this pipe shell 91 inner wall (as shown in the 3rd figure), when this pipe shell 91 After forming a negative pressure state, an appropriate amount of refrigerant is installed, so that the liquid-absorbing core 92 close to the inner wall of the tube shell 91 can be filled with refrigerant. When the incinerated gas in the direct-fired incinerator (TO) 10 passes through the heat pipe 90 When the evaporating section 901 is in the heat pipe 90, evaporation and gasification will occur in the heat pipe 90 to change the liquid into vapor, and the vapor will flow to the condensation section 902 of the heat pipe 90 under a small pressure difference. At 902, condensation will occur in the heat pipe 90 to change the vapor into liquid, and then flow back to the evaporation section 901 of the heat pipe 90, and circulate back and forth through the evaporation section 901 and the condensation section 902 of the heat pipe 90, so that the exhaust gas from the source The relative humidity decreases, To have the effect of improving the adsorption into the adsorption zone 701 of the adsorption runner 70 .

The burner head 101 of the above-mentioned direct-fired incinerator (TO) 10 is able to transport the burned gas to one side of the second heat side pipeline 32 of the second heat exchanger 30 for heat exchange. Then the other side of the second heat side pipeline 32 of the second heat exchanger 30 will transport the burned gas to the evaporation section 901 of the heat pipe 90 (as shown in Figure 1 to Figure 2 ), and the incinerated gas passes through the evaporation section 901 of the heat pipe 90, and then transported to one side of the third heat side pipeline 42 of the third heat exchanger 40 for heat exchange, and then the third heat The other side of the third heat-side pipeline 42 of the exchanger 40 is used to transport the gas after incineration to one side of the first heat-side pipeline 22 of the first heat exchanger 20 for heat exchange, finally by The other side of the first hot side pipeline 22 of the first heat exchanger 20 is transported to the outlet 12 of the direct-fired incinerator (TO) 10, and then from the outlet of the direct-fired incinerator (TO) 10 12 to the chimney 80 (as shown in Figures 1 to 2), to be discharged through the chimney 80.

Furthermore, another embodiment of the rotary system with a heat source of the present invention (as shown in Figures 4 to 5), wherein the direct-fired incinerator (TO) 10, the first heat exchanger 20 , the second heat exchanger 30, the first cold side delivery pipeline 61, the second cold side delivery pipeline 62, the adsorption runner 70, the chimney 80 and the heat pipe 90 are to adopt the same design as above, therefore, the above-mentioned direct combustion Type incinerator (TO) 10, first heat exchanger 20, second heat exchanger 30, first cold side delivery pipeline 61, second cold side delivery pipeline 62, adsorption runner 70, chimney 80 and heat pipe 90 The content is not repeated, please refer to the above description.

The above-mentioned difference is that in another embodiment, the other end of the original hot gas delivery pipeline 75 is connected to the furnace 102 of the direct-fired incinerator (TO) 10. The third heat exchanger 40 is removed, and the other end of the hot gas delivery pipeline 75 is changed to connect a heater 50 (as shown in Fig. 4 to Fig. 5), 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, so that the cooling zone 702 of the adsorption runner 70 The other end of the cooling air conveying pipeline 74 connected to the other side of the other side is connected with the heater 50 (as shown in the first figure to the second figure), so that after entering the cooling zone 702 of the adsorption runner 70 The gas is transported into the heater 50 for heating, and one end of the hot gas delivery pipeline 75 is connected to the other side of the desorption zone 703 of the adsorption wheel 70, and the other end of the hot gas delivery pipeline 75 is connected to the other end of the hot gas delivery pipeline 75. The heater 50 is connected so that the high-temperature hot gas heated by the heater 50 can be transported to the desorption area 703 of the adsorption wheel 70 through the hot gas delivery pipeline 75 for desorption.

And the runner method of tool heat source of the present invention mainly comprises direct combustion type incinerator (TO) 10, a first heat exchanger 20, a second heat exchanger 30, a 3rd heat exchanger 40, a first A combined design of a cold-side delivery pipeline 61, a second cold-side delivery pipeline 62, an adsorption runner 70, a chimney 80 and a heat pipe 90 (as shown in Figures 1 to 2), wherein the first A heat exchanger 20 is provided with a first cold side pipeline 21 and a first hot side pipeline 22, and the second heat exchanger 30 is provided with a second cold side pipeline 31 and a second hot side pipeline 32, The third heat exchanger 40 is provided with a third cold-side pipeline 41 and a third hot-side pipeline 42, and one end of the first cold-side delivery pipeline 61 is connected to the other end of the first cold-side pipeline 21 The other end of the first cold-side delivery pipeline 61 is connected to one end of the second cold-side pipeline 31, and one end of the second cold-side delivery pipeline 62 is connected to the other end of the second cold-side pipeline 31. One end is connected, and the other end of the second cold-side delivery pipeline 62 is connected with the inlet 11 of the direct-fired incinerator (TO) 10 . Another should be straight Combustion type incinerator (TO) 10 is provided with a furnace head 101 and a furnace 102, and this furnace head 101 is communicated with this furnace 102 system, and the first heat exchanger 20, the second heat exchanger 30 and the third heat exchanger The exchanger 40 is arranged in the hearth 102 of the direct-fired incinerator (TO) respectively (as shown in Fig. 1 to Fig. 2), and the direct-fired incinerator (TO) 10 is provided with an inlet 11 and Outlet 12, and the inlet 11 is located at the burner 101, and the outlet 12 of the direct-fired incinerator (TO) 10 is connected to the chimney 80, and the heat pipe 90 has an evaporation section 901 and a condensation Section 902 (as shown in Figure 3), and the evaporation section 901 of the heat pipe 90 is set in the furnace 102 of the direct-fired incinerator (TO) 10, and the condensation section 902 of the heat pipe 90 is set in the exhaust gas On the air intake pipeline 71 (as shown in Figure 1 to Figure 2), whereby the organic waste gas can enter the burner 101 from the inlet 11 for combustion, and then the gas after combustion can pass through Pass through the furnace 102 and discharge to the chimney 80 through the outlet 12 to save energy.

In addition, the adsorption runner 70 of the present invention is provided with an adsorption zone 701, a cooling zone 702 and a desorption zone 703. The adsorption runner 70 is connected with a waste gas inlet pipeline 71, a clean gas discharge pipeline 72, a cooling gas Air intake pipeline 73, a cooling gas delivery pipeline 74, a hot gas delivery pipeline 75 and a desorbed concentrated gas pipeline 76 (as shown in Figures 1 to 2). Wherein the adsorption runner 70 is a zeolite concentration runner or a concentration runner made of other materials.

The method steps of the main implementation mode (as shown in FIG. 6 ) include: step S100 source exhaust gas is transported: the source exhaust gas is transported to one end of the condensation section 902 of the heat pipe 90 through the exhaust gas inlet pipeline 71 . After the above step S100 is completed, the next step S110 is performed.

In addition, in the next step S110, the source exhaust gas passes through the heat pipe: the source After the waste gas passes through the condensation section 902 of the heat pipe 90 , it is output from the other end of the condensation section 903 of the heat pipe 90 , and is transported to one side of the adsorption area 701 of the adsorption wheel 70 through the exhaust gas inlet pipe 71 . After the above step S110 is completed, the next step S120 is performed.

Wherein the heat pipe 90 in the above step S100 and step S110 has an evaporation section 901 and a condensation section 902 (as shown in Figure 3), wherein the condensation section 902 of the heat pipe 90 is arranged on the exhaust gas intake pipeline 71 Above, the source exhaust gas of the exhaust gas intake pipeline 71 first enters one end of the condensation section 902 of the heat pipe 90, and then outputs from the other end of the condensation section 902 of the heat pipe 90 (as shown in Figures 1 to 2) , and transported to the side of the adsorption area 701 of the adsorption wheel 70 through the exhaust gas inlet pipeline 71, so that the source exhaust gas can pass through the condensation section 902 of the heat pipe 90 for heat treatment. In addition, the waste gas intake pipeline 71 is provided with a fan 712 (as shown in FIG. 2 ), so as to push and pull the source waste gas into one end of the condensation section 902 of the heat pipe 90 .

In addition, the step S120 carried out in the next step is adsorption by the adsorption wheel: after the adsorption is carried out through the adsorption area 701 of the adsorption wheel 70, the gas after adsorption is passed through the net from the other side of the adsorption area 701 of the adsorption wheel 70. The other end of the gas discharge pipeline 72 is output. After the above step S120 is completed, the next step S130 is performed.

Wherein in the above-mentioned step S120, one end of the clean gas discharge pipeline 72 is connected with the other side of the adsorption area 701 of the adsorption runner 70, and the other end of the clean gas discharge pipeline 72 is connected with the chimney 80 (as 1 to 2), and the net gas discharge pipeline 72 is provided with a fan 721 (as shown in Figure 2), so that the air in the net gas discharge pipeline 72 can be discharged through the fan 721 The adsorbed gas is pushed and pulled into the chimney 80 for discharge.

In addition, in the next step S130, the cooling air is input into the cooling zone: through the other end of the cooling air inlet pipeline 73, the cooling air is delivered to the cooling zone 702 of the adsorption runner 70 for cooling, and then through the cooling air delivery pipe The other end of the road 74 is used to deliver the cooling air passing through the cooling zone 702 of the adsorption wheel 70 to one end of the third cold side pipeline 41 of the third heat exchanger 40 . After the above step S130 is completed, the next step S140 is performed.

Wherein the side of the cooling zone 702 of the adsorption runner 70 in the above-mentioned step S130 is connected to the cooling gas inlet pipeline 73, for the gas to enter the cooling zone 702 of the adsorption runner 70 for cooling, and the adsorption The other side of the cooling zone 702 of the runner 70 is connected to one end of the cooling air delivery pipeline 74 (as shown in Figure 1 to Figure 2), and the other end of the cooling air delivery pipeline 74 is connected to the third cooling air delivery pipeline 74. One end of the third cold side pipeline 41 of the heat exchanger 40 is connected to transport the gas entering the cooling zone 702 of the adsorption wheel 70 to the third heat exchanger 40 for heat exchange.

And the cooling zone 702 of the above-mentioned adsorption runner 70 is provided with two kinds of implementation modes, wherein the first kind of implementation mode is that the cooling air intake pipeline 73 connected to one side of the cooling zone 702 of the adsorption rotor 70 is for supplying Fresh air or external air enters (as shown in FIG. 1 ), and the cooling zone 702 of the adsorption runner 70 is provided for cooling through the fresh air or external air. Another second embodiment is that the exhaust gas intake pipeline 71 is provided with an exhaust gas communication pipeline 711 (as shown in Figure 2), and the other end of the exhaust gas communication pipeline 711 is connected to the cooling air intake pipeline. 73 connection, so that the source exhaust gas in the exhaust gas inlet pipeline 71 can be transported to the cooling zone 702 of the adsorption runner 70 through the exhaust gas communication pipeline 711 for cooling use, and the exhaust gas communication pipeline 711 is set There is an exhaust gas communication control valve 7111 (as shown in FIG. 2 ) to control the air volume of the exhaust gas communication pipeline 711 .

In addition, in the next step S140, the desorption area performs desorption: through the hot gas delivery pipeline 75 connected to the other end of the third cold side pipeline 41 of the third heat exchanger 40, the hot gas is delivered to the adsorption rotor. The desorption zone 703 of the wheel 70 is desorbed, and then the desorbed concentrated gas is delivered to one end of the first cold side pipeline 21 of the first heat exchanger 20 through the other end of the desorbed concentrated gas pipeline 76 . After the above step S140 is completed, the next step S150 is performed.

One end of the hot gas delivery pipeline 75 in the above step S140 is connected to the other side of the desorption zone 703 of the adsorption wheel 70, and the other end of the hot gas delivery pipeline 75 is connected to the third heat exchanger The other end of the third cold-side pipeline 41 of 40 is connected (as shown in the first figure to the second figure), so that the high-temperature hot gas that is heat-exchanged through the third heat exchanger 40 can pass through the hot gas delivery pipeline 75 to be transported to the desorption zone 703 of the adsorption wheel 70 for desorption.

In addition, the next step S150 is to transport the desorbed concentrated gas: the desorbed concentrated gas passes through the first cold side delivery pipeline 61 connected to the other end of the first cold side pipeline 21 of the first heat exchanger 20 to be transported to one end of the second cold side pipeline 31 of the second heat exchanger 30, and then transported through the second cold side connected to the other end of the second cold side pipeline 31 of the second heat exchanger 30 The pipeline 62 is delivered to the inlet 11 of the direct fired incinerator (TO) 10 . After the above step S150 is completed, the next step S160 is performed.

The other end of the first cold-side pipeline 21 of the first heat exchanger 20 in the above-mentioned step S150 is connected to one end of the first cold-side delivery pipeline 61, and the other end of the first cold-side delivery pipeline 61 Then it is connected with one end of the second cold side pipeline 31 of the second heat exchanger 30, and the other end of the second cold side pipeline 31 of the second heat exchanger 30 is connected with the second One end of the cold-side delivery pipeline 62 is connected, and the other end of the second cold-side delivery pipeline 62 is connected with the inlet 11 of the direct-fired incinerator (TO) 10 (as shown in Figure 1 to Figure 2 ), so that the desorbed concentrated gas desorbed through the high temperature can be transported to one end of the first cold side pipeline 21 of the first heat exchanger 20 through the desorbed concentrated gas pipeline 76, and by The other end of the first cold-side pipeline 21 of the first heat exchanger 20 is delivered to one end of the first cold-side delivery pipeline 61, and is delivered by the other end of the first cold-side delivery pipeline 61. to one end of the second cold side pipeline 31 of the second heat exchanger 30, and then transported to the second cold side delivery pipe by the other end of the second cold side pipeline 31 of the second heat exchanger 30 One end of the road 62, and finally transported to the inlet 11 of the direct-fired incinerator (TO) 10 by the other end of the second cold-side delivery pipeline 62, so that the direct-fired incinerator (TO) 10 furnace heads 101 for pyrolysis to reduce volatile organic compounds. In addition, the desorption concentrated gas pipeline 76 is provided with a fan 761 (as shown in Figure 2), so that the desorbed concentrated gas can be pushed and pulled into one end of the first cold side pipeline 21 of the first heat exchanger 20 Inside.

In addition, in the next step S160, the incinerated gas is transported: the incinerated gas produced by burning the burner 101 of the direct-fired incinerator (TO) 10 is transported to the second heat exchanger 30 One end of the second hot-side pipeline 32 is transported from the other end of the second heat-side pipeline 32 of the second heat exchanger 30 to one end of the evaporation section 901 of the heat pipe 90 . After the above step S160 is completed, the next step S170 is performed.

Wherein the above step S160, the heat pipe 90 has an evaporation section 901 and a condensation section 902 (as shown in Figure 3), wherein the evaporation section 901 of the heat pipe 90 is located in the direct-fired incinerator (TO) 10 In the furnace 102 of the heat pipe 90, one end of the evaporation section 901 of the heat pipe 90 is connected to the other end of the second heat side pipeline 32 of the second heat exchanger 30 (As shown in Figures 1 to 2), and the other end of the evaporation section 901 of the heat pipe 90 is connected to one end of the third heat side pipeline 32 of the third heat exchanger 30, and the gas after incineration It can be processed through the evaporation section 901 of the heat pipe 90 .

In addition, in the next step S170, the incinerated gas passes through the heat pipe: after the incinerated gas passes through the evaporation section 901 of the heat pipe 90, it is output from the other end of the evaporation section 901 of the heat pipe 90 to the third heat exchanger 40 One end of the third hot side pipeline 42. After the above step S170 is completed, the next step S180 is performed.

Wherein the heat pipe 90 in the above-mentioned step S170 is made up of the pipe shell 91 and the liquid-absorbing core 92, and the liquid-absorbing core 92 is closely attached to the inner wall of the pipe shell 91 (as shown in Figure 3), when the pipe After forming a negative pressure state in the shell 91, an appropriate amount of refrigerant is installed, so that the liquid-absorbing core 92 close to the inner wall of the tube shell 91 can be filled with refrigerant. When the incinerated gas in the direct-fired incinerator (TO) 10 passes through In the evaporation section 901 of the heat pipe 90, evaporation and gasification will occur in the heat pipe 90 to change the liquid into vapor, and the vapor will flow to the condensation section 902 of the heat pipe 90 under a small pressure difference. When the exhaust gas from the source passes through the heat pipe 90 In the condensation section 902 of the heat pipe 90, condensation will occur in the heat pipe 90 to turn the vapor into a liquid, and then flow back to the evaporation section 901 of the heat pipe 90, and circulate back and forth through the evaporation section 901 and the condensation section 902 of the heat pipe 90, so that The relative humidity of the source exhaust gas is reduced to enhance the adsorption efficiency of the adsorption area 701 entering the adsorption wheel 70 .

In addition, the output of the incinerated gas outlet in the next step S180: the incinerated gas is transported to the first heat exchanger 20 by the other end of the third heat side pipeline 42 of the third heat exchanger 40 One end of the first hot-side pipeline 22 is finally delivered to the outlet of the direct-fired incinerator (TO) 10 by the other end of the first hot-side pipeline 22 of the first heat exchanger 20 Mouth 12.

Wherein the furnace head 101 of the direct-fired incinerator (TO) 10 can deliver the burned gas to one side of the second heat side pipeline 32 of the second heat exchanger 30 for heat exchange (such as Figures 1 to 2), and then through the other side of the second heat side pipeline 32 of the second heat exchanger 30, the gas after incineration is transported to the evaporation section 901 of the heat pipe 90 , and the incinerated gas passes through the evaporation section 901 of the heat pipe 90, and then is transported to one side of the third heat side pipeline 42 of the third heat exchanger 40 for heat exchange, and then the third heat exchange The other side of the third hot side pipeline 42 of the device 40 is used to transport the incinerated gas to one side of the first heat side pipeline 22 of the first heat exchanger 20 for heat exchange, and finally the The other side of the first heat side pipeline 22 of the first heat exchanger 20 is transported to the outlet 12 of the direct-fired incinerator (TO) 10, and then from the outlet 12 of the direct-fired incinerator (TO) 10 To transport to the chimney 80 (as shown in Figure 1 to Figure 2), to be discharged through the chimney 80.

Furthermore, in the runner method with heat source of the present invention, the main implementation aspect (as shown in Figure 6) is step S100 source exhaust gas is transported, step S110 source exhaust gas is adsorbed through heat pipe, S120 adsorption runner, and step S130 is input for cooling District cooling gas, step S140 desorption area for desorption, step S150 desorption concentrated gas transportation, step S160 incineration gas transportation, step S170 incineration gas through the heat pipe and step S180 gas outlet output after incineration, has been in For the above explanation, please refer to the above explanation content.

In another implementation mode (as shown in Figure 7), the source exhaust gas in step S200 is transported, the source exhaust gas in step S210 is absorbed through the heat pipe, and S220 is absorbed by the adsorption runner. Attachment, step S250 desorbed concentrated gas delivery and step S260 gas after incineration are transported by using the source exhaust gas of step S100 in the main implementation mode (as shown in Figure 6) for delivery, and step S110 source exhaust gas passing through the heat pipe, S120 Adsorption by the adsorption wheel, Step S150 Desorption Condensed gas delivery and Step S160 The same design of incineration gas delivery, the only difference is that step S130 input cooling gas in the cooling zone, step S140 desorption in the desorption zone, step S170 The incinerated gas is output through the heat pipe and the incinerated gas outlet in step S180.

Therefore, the same contents as those of step S200 for transporting the source exhaust gas, step S210 for the source exhaust gas to be adsorbed through the heat pipe, S220 for the adsorption runner, step S250 for the desorption and concentrated gas transport, and step S260 for the incineration gas transport are not repeated, please refer to The content of the above description. The following will input the cooling gas in the cooling zone for step S230 in another implementation mode (as shown in Figure 7), desorb in the desorption zone in step S240, desorb the gas after step S270 incineration, and pass the gas after incineration in step S280 Export the output for illustration.

And the difference of another embodiment is that step S230 imports the cooling air of the cooling zone: through the other end of the cooling air inlet pipeline 73, the cooling air is delivered to the cooling zone 702 of the adsorption runner 70 for cooling, and then passes through the The other end of the cooling air delivery pipeline 74 is used to output the cooling air passing through the cooling zone 702 of the adsorption rotor 70 . After the above step S230 is completed, the next step S240 is performed.

In addition, the step S240 that is carried out in the next step is desorbed in the desorption area: one end of the hot gas delivery pipeline 75 is connected with the desorption area 703 of the adsorption wheel 70, and is carried out by the desorption area 703 of the adsorption wheel 70. desorption, and then through the desorption concentrated gas pipeline 76 to The desorbed concentrated gas is delivered to one end of the first cold side pipeline 21 of the first heat exchanger 20 .

Wherein the above-mentioned step S230 and step S240 in the hot gas conveying pipeline 75 system, the third heat exchanger 40 that the original other end is connected and is located in the hearth 102 of this direct-fired incinerator (TO) 10 is removed, and let the The other end of the hot gas delivery pipeline 75 is connected to a heater 50 (as shown in Fig. 4 to Fig. 5 ) outside the furnace 102 of the direct-fired incinerator (TO) 10, wherein the heater 50 It is any one of air-to-air heat exchanger, liquid-to-air heat exchanger, electric heater, and gas heater, so that the cooling gas delivery pipeline connected to the other side of the cooling zone 702 of the adsorption runner 70 The other end of 74 is connected with the heater 50, so that the gas that enters the cooling zone 702 of the adsorption wheel 70 is delivered to the heater 50 for heating (as shown in Figures 4 to 5), and One end of the hot gas delivery pipeline 75 is connected with the other side of the desorption zone 703 of the adsorption wheel 70, and the other end of the hot gas delivery pipeline 75 is connected with the heater 50, so that The high-temperature hot gas heated by the device 50 is transported to the desorption area of the adsorption wheel 70 through the hot gas delivery pipeline 75 to be desorbed 703 for use.

Furthermore, the incinerated gas in step S270 passes through the heat pipe: after the incinerated gas passes through the evaporation section 901 of the heat pipe 90, it is output from the other end of the evaporation section 901 of the heat pipe 90 to the first part of the first heat exchanger 20. One end of the hot side pipeline 22. After the above step S270 is completed, the next step S280 is performed.

In addition, the output of the gas outlet after the incineration of the step S280 carried out in the next step: the gas after the incineration is finally transported to the direct-fired incinerator (TO )10 exit 12.

Wherein the above-mentioned step S270 and step S280 in the direct-fired incineration The furnace head 101 of the furnace (TO) 10 is able to transport the burned gas to one side of the second heat side pipeline 32 of the second heat exchanger 30 for heat exchange, and then the second heat exchange The other side of the second hot side pipeline 32 of the device 30 is used to transport the incinerated gas to the evaporation section 901 of the heat pipe 90, and the incinerated gas passes through the evaporation section 901 of the heat pipe 90, and then transported To one side of the first heat side pipeline 22 of the first heat exchanger 20 to perform heat exchange (as shown in Fig. 4 to Fig. 5), and finally from the first heat side of the first heat exchanger 20 The other side of the pipeline 22 is transported to the outlet 12 of the direct-fired incinerator (TO) 10, and then transported to the chimney 80 through the outlet 12 of the direct-fired incinerator (TO) 10 to pass through the chimney 80 to discharge.

From the above detailed description, those who are familiar with this art can understand that the present invention can indeed achieve the aforementioned purpose, and have actually met the provisions of the Patent Law, so they should file an application for a patent for invention.

But the above-mentioned ones are only preferred embodiments of the present invention, and should not limit the scope of the present invention; therefore, all simple equivalent changes and modifications made according to the patent scope of the present invention and the contents of the description of the invention , should still fall within the scope covered by the patent of the present invention.

10: Direct fired incinerator (TO)

101: Stove head

102: Furnace

11: Entrance

12: Export

20: First heat exchanger

21: The first cold side pipeline

22: The first hot side pipeline

30: Second heat exchanger

31: Second cold side pipeline

32: Second hot side pipeline

40: The third heat exchanger

41: The third cold side pipeline

42: The third hot side pipeline

61: The first cold side delivery pipeline

62: Second cold side delivery pipeline

70: Adsorption runner

701: adsorption area

702: cooling zone

703: Desorption area

71: Exhaust gas intake pipe

72: Net gas discharge pipeline

73: Cooling air intake pipe

74: Cooling air delivery pipeline

75: Hot gas delivery pipeline

76: Desorption concentrated gas pipeline

80: chimney

90: heat pipe

91: shell

92: Liquid absorbent core

Claims (20)

A wheel system with a heat source, comprising: A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner is connected to the furnace, the direct-fired incinerator (TO) is provided with an entrance and an outlet, the inlet being at the burner; A first heat exchanger, the first heat exchanger is set in the furnace of the direct-fired incinerator (TO), the first heat exchanger is provided with a first cold side pipeline and a first hot side pipe road; A second heat exchanger, the second heat exchanger is set in the furnace of the direct-fired incinerator (TO), the second heat exchanger is provided with a second cold side pipeline and a second hot side pipe road; A third heat exchanger, the third heat exchanger is installed in the furnace of the direct-fired incinerator (TO), the third heat exchanger is provided with a third cold side pipeline and a third hot side pipe road; A first cold-side delivery pipeline, one end of the first cold-side delivery pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side delivery pipeline is connected to the second cold-side delivery pipeline. One end connection of the side pipe; A second cold-side delivery pipeline, one end of the second cold-side delivery pipeline is connected to the other end of the second cold-side pipeline, and the other end of the second cold-side delivery pipeline is connected to the direct-fired The inlet connection of the incinerator (TO); An adsorption runner, the adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, the adsorption runner is connected with a waste gas inlet pipeline, a clean gas discharge pipeline, a cooling gas inlet pipeline, A cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, one end of the exhaust gas inlet pipeline is connected to one side of the adsorption area of the adsorption runner, and the clean gas discharge pipeline is One end is connected to the other side of the adsorption area of the adsorption runner, and one end of the cooling air inlet pipeline is connected to the One side of the cooling zone of the adsorption runner is connected, one end of the cooling gas delivery pipeline is connected to the other side of the cooling zone of the adsorption runner, and the other end of the cooling gas delivery pipeline is connected to the third heating One end of the third cold side pipeline of the exchanger is connected, one end of the hot gas delivery pipeline is connected with the other side of the desorption area of the adsorption wheel, and the other end of the hot gas delivery pipeline is connected with the third hot gas delivery pipeline. The other end of the third cold side pipeline of the exchanger is connected, one end of the desorption concentrated gas pipeline is connected with one side of the desorption area of the adsorption 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 is connected; a chimney to which the other end of the clean gas discharge line is connected; and A heat pipe, the heat pipe has an evaporating section and a condensing section, the evaporating section of the heat pipe is arranged in the furnace of the direct-fired incinerator (TO), and one end of the evaporating section of the heat pipe is exchanged with the second heat The other end of the second hot side pipeline of the heat pipe is connected, the other end of the evaporation section of the heat pipe is connected with one end of the third heat side pipeline of the third heat exchanger, and the condensation section of the heat pipe is set at the waste gas On the intake pipeline, the exhaust gas from the exhaust gas intake pipeline first 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 transported to the adsorption converter through the exhaust gas intake pipeline. One side of the adsorption area of the wheel. A wheel system with a heat source, comprising: A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner is connected to the furnace, the direct-fired incinerator (TO) is provided with an entrance and an outlet, the inlet being at the burner; A first heat exchanger, the first heat exchanger is set in the furnace of the direct-fired incinerator (TO), the first heat exchanger is provided with a first cold side pipeline and a first hot side pipe road; A second heat exchanger, the second heat exchanger is located in the hearth of the direct-fired incinerator (TO) Inside, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline; A first cold-side delivery pipeline, one end of the first cold-side delivery pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side delivery pipeline is connected to the second cold-side delivery pipeline. One end connection of the side pipe; A second cold-side delivery pipeline, one end of the second cold-side delivery pipeline is connected to the other end of the second cold-side pipeline, and the other end of the second cold-side delivery pipeline is connected to the direct-fired The inlet connection of the incinerator (TO); An adsorption runner, the adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, the adsorption runner is connected with a waste gas inlet pipeline, a clean gas discharge pipeline, a cooling gas inlet pipeline, A cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, one end of the exhaust gas inlet pipeline is connected to one side of the adsorption area of the adsorption runner, and the clean gas discharge pipeline is One end is connected to the other side of the adsorption zone of the adsorption runner, one end of the cooling air inlet pipeline is connected to one side of the cooling zone of the adsorption runner, and one end of the cooling gas delivery pipeline is connected to the The other side of the cooling zone of the adsorption wheel is connected, one end of the hot gas delivery pipeline is connected to the other side of the desorption area of the adsorption wheel, and one end of the desorption concentrated gas pipeline is connected to the adsorption wheel One side of the desorption zone is connected, 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; a chimney to which the other end of the clean gas discharge line is connected; and A heat pipe, the heat pipe has an evaporating section and a condensing section, the evaporating section of the heat pipe is arranged in the furnace of the direct-fired incinerator (TO), and one end of the evaporating section of the heat pipe is exchanged with the second heat The other end of the second hot side pipeline of the heat pipe is connected, the other end of the evaporation section of the heat pipe is connected with one end of the first heat side pipeline of the first heat exchanger, and the condensation section of the heat pipe is set at the waste gas Enter On the gas pipeline, the exhaust gas from the exhaust gas inlet pipeline first 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 transported to the adsorption runner through the exhaust gas inlet pipeline. side of the adsorption area. The rotary system with heat source as described in item 1 or 2 of the scope of the patent application, wherein the outlet of the direct-fired incinerator (TO) is further connected to the chimney. As the runner system with heat source as described in item 1 or 2 of the scope of application, the cooling air intake pipeline is further used for fresh air or external air to enter. The runner system with a heat source as described in item 1 or 2 of the scope of the patent application, wherein the exhaust gas intake pipeline is further provided with an exhaust gas communication pipeline, and the exhaust gas communication pipeline is connected to the cooling air intake pipeline , the exhaust gas communication pipeline is further provided with an exhaust gas communication control valve to control the air volume of the exhaust gas communication pipeline. As the runner system with heat source described in item 1 or 2 of the scope of the patent application, the desorption concentrated gas pipeline is further equipped with a fan. As the runner system with heat source described in item 1 or 2 of the scope of application, the clean air discharge pipeline is further provided with a fan. The runner system with a heat source as described in item 1 or 2 of the scope of the patent application, wherein the waste gas inlet pipeline is further provided with a fan. The wheel system with heat source as described in item 2 of the scope of the patent application, 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. The wheel system with heat source as described in item 1 or 2 of the scope of the patent application, wherein the heat pipe It is further composed of a shell and a liquid-absorbing core. The liquid-absorbing core is closely attached to the inner wall of the shell. When a negative pressure is formed in the shell, an appropriate amount of refrigerant is installed to make it close to the shell The liquid-absorbing core of wall can be filled with refrigerant. A rotary method with a heat source, mainly equipped with a direct fired incinerator (TO), a first heat exchanger, a second heat exchanger, a third heat exchanger, and a first cold side delivery pipeline , a second cold-side delivery pipeline, an adsorption runner, a chimney and a heat pipe, the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner communicates with the furnace, the direct The combustion type incinerator (TO) is provided with an inlet and an outlet, the inlet is located at the burner, the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline, and the second The heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, the third heat exchanger is provided with a third cold side pipeline and a third hot side pipeline, and the first cold side delivery pipeline One end of the first cold side pipeline is connected to the other end of the first cold side pipeline, the other end of the first cold side delivery pipeline is connected to one end of the second cold side pipeline, and one end of the second cold side delivery pipeline It is connected to the other end of the second cold-side pipeline, and the other end of the second cold-side delivery pipeline is connected to the inlet of the direct-fired incinerator (TO). The adsorption wheel is provided with an adsorption area, Cooling zone and desorption zone, the adsorption runner is connected with a waste gas intake pipeline, a clean gas discharge pipeline, a cooling gas intake pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption Attached to the concentrated gas pipeline, the heat pipe has an evaporation section and a condensation section, the evaporation section of the heat pipe is set in the furnace of the direct-fired incinerator (TO), and the condensation section of the heat pipe is set in the waste gas inlet The main steps of the method include: Conveyance of source exhaust gas: transport the source exhaust gas through the exhaust gas inlet pipeline to one end of the condensation section of the heat pipe; The exhaust gas from the source passes through the heat pipe: after the exhaust gas from the source passes through the condensation section of the heat pipe, it is The other end of the condensation section is output, and is transported to one side of the adsorption area of the adsorption wheel through the exhaust gas inlet pipeline; Adsorption by the adsorption wheel: after adsorption through the adsorption area of the adsorption wheel, the adsorbed gas is output from the other side of the adsorption area of the adsorption wheel through the other end of the clean gas discharge pipeline; Cooling air input into the cooling area: through the other end of the cooling air inlet pipeline, the cooling air is sent to the cooling area of the adsorption runner for cooling, and then passed through the adsorption runner through the other end of the cooling air delivery pipeline The cooling air in the cooling zone is delivered to one end of the third cold side pipeline of the third heat exchanger; Desorption in the desorption zone: through the hot gas delivery pipeline connected to the other end of the third cold side pipeline of the third heat exchanger, the hot gas is transported to the desorption zone of the adsorption runner for desorption, and then through The other end of the desorbed concentrated gas pipeline is used to transport the desorbed concentrated gas to one end of the first cold side pipeline of the first heat exchanger; Delivery of desorbed concentrated gas: the desorbed concentrated gas is sent to the first cold side pipeline connected to the other end of the first cold side pipeline of the first heat exchanger to the second heat exchanger One end of the second cold-side pipeline, and then transported to the direct-fired incinerator (TO) through the second cold-side delivery pipeline connected to the other end of the second cold-side pipeline of the second heat exchanger Entrance; Delivery of the incinerated gas: the incinerated gas produced by burning the burner of the direct-fired incinerator (TO) is delivered to one end of the second heat side pipeline of the second heat exchanger, and The other end of the second heat side pipeline of the second heat exchanger is delivered to one end of the evaporation section of the heat pipe; The incinerated gas passes through the heat pipe: after the incinerated gas passes through the evaporation section of the heat pipe, it is output from the other end of the evaporation section of the heat pipe to one of the third heat side pipelines of the third heat exchanger terminal; and The output of the incinerated gas outlet: the incinerated gas is transported from the other end of the third heat side pipeline of the third heat exchanger to one end of the first heat side pipeline of the first heat exchanger, and finally sent to the first heat side pipeline of the first heat exchanger. The other end of the first hot side pipeline of the first heat exchanger is delivered to the outlet of the direct fired incinerator (TO). A rotary method with a heat source, mainly equipped with a direct fired incinerator (TO), a first heat exchanger, a second heat exchanger, a first cold-side delivery pipeline, and a second cold-side delivery Pipeline, an adsorption runner, a chimney and a heat pipe, the direct-fired incinerator (TO) is equipped with a burner and a furnace, the burner is connected to the furnace, the direct-fired incinerator (TO) An inlet and an outlet are provided, the inlet is provided at the burner, the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline, and the second heat exchanger is provided with a second Two cold-side pipelines and the second hot-side pipeline, one end of the first cold-side delivery pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side delivery pipeline is connected to the One end of the second cold-side pipeline is connected, one end of the second cold-side delivery pipeline is connected to the other end of the second cold-side pipeline, and the other end of the second cold-side delivery pipeline is connected to the direct-fired The inlet of the type incinerator (TO) is connected. The adsorption wheel is equipped with an adsorption area, a cooling area and a desorption area. The adsorption wheel is connected with a waste gas inlet pipeline, a clean gas discharge pipeline, and a cooling gas Intake pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorbed concentrated gas pipeline, the heat pipe system has an evaporation section and a condensation section, the evaporation section of the heat pipe is set in the direct-fired In the hearth of the incinerator (TO), the condensing section of the heat pipe is arranged on the exhaust gas inlet pipeline, and the main steps of the method include: Conveyance of source exhaust gas: transport the source exhaust gas through the exhaust gas inlet pipeline to one end of the condensation section of the heat pipe; The source exhaust gas passes through the heat pipe: after the source exhaust gas passes through the condensation section of the heat pipe, it is output from the other end of the condensation section of the heat pipe, and is transported to the side of the adsorption area of the adsorption wheel through the exhaust gas inlet pipeline; Adsorption by the adsorption wheel: after adsorption through the adsorption area of the adsorption wheel, the adsorbed gas is output from the other side of the adsorption area of the adsorption wheel through the other end of the clean gas discharge pipeline; Cooling air input into the cooling area: through the other end of the cooling air inlet pipeline, the cooling air is sent to the cooling area of the adsorption runner for cooling, and then passed through the adsorption runner through the other end of the cooling air delivery pipeline The cooling air output of the cooling zone; Desorption in the desorption area: one end of the hot gas delivery pipeline is connected to the desorption area of the adsorption wheel, and the desorption is performed from the desorption area of the adsorption wheel, and then through the desorption concentrated gas pipeline. transporting the desorbed concentrated gas to one end of the first cold side pipeline of the first heat exchanger; Delivery of desorbed concentrated gas: the desorbed concentrated gas is sent to the first cold side pipeline connected to the other end of the first cold side pipeline of the first heat exchanger to the second heat exchanger One end of the second cold-side pipeline, and then transported to the direct-fired incinerator (TO) through the second cold-side delivery pipeline connected to the other end of the second cold-side pipeline of the second heat exchanger Entrance; Delivery of the incinerated gas: the incinerated gas produced by burning the burner of the direct-fired incinerator (TO) is delivered to one end of the second heat side pipeline of the second heat exchanger, and The other end of the second heat side pipeline of the second heat exchanger is delivered to one end of the evaporation section of the heat pipe; The incinerated gas passes through the heat pipe: after the incinerated gas passes through the evaporation section of the heat pipe, it is output from the other end of the evaporation section of the heat pipe to one end of the first heat side pipeline of the first heat exchanger; and Output of incinerated gas outlet: the incinerated gas is finally transported from the other end of the first heat side pipeline of the first heat exchanger to the outlet of the direct-fired incinerator (TO). The rotary wheel method with heat source as described in item 11 or 12 of the scope of application, wherein the outlet of the direct-fired incinerator (TO) is further connected to the chimney. As the method of turning wheels with a heat source as described in item 11 or 12 of the scope of the patent application, the cooling air intake pipeline is further used for fresh air or external air to enter. The runner method with a heat source as described in item 11 or 12 of the scope of the patent application, wherein the exhaust gas intake pipeline is further provided with an exhaust gas communication pipeline, and the exhaust gas communication pipeline is connected to the cooling air intake pipeline , the exhaust gas communication pipeline is further provided with an exhaust gas communication control valve to control the air volume of the exhaust gas communication pipeline. The rotary method with a heat source as described in item 11 or 12 of the scope of the patent application, wherein the desorption concentrated gas pipeline is further provided with a fan. As the method of turning a wheel with a heat source as described in item 11 or 12 of the scope of application, the clean air discharge pipeline is further provided with a fan. As the method of turning a wheel with a heat source as described in item 11 or 12 of the scope of the patent application, wherein the waste gas inlet pipeline is further provided with a fan. The method of turning wheels with heat sources as described in item 12 of the scope of the patent application, 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. The wheel method with a heat source as described in item 11 or 12 of the scope of patent application, wherein the The heat pipe system is further composed of a tube shell and a liquid-absorbing core. The liquid-absorbing core is closely attached to the inner wall of the tube shell. The liquid-absorbing core on the inner wall can be filled with refrigerant.

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