TWI823027B - Energy-saving dual-runner hot side pass temperature control system and method thereof - Google Patents

Abstract

The invention is an energy-saving dual-runner hot side pass temperature control system and a method thereof. It is mainly used in an organic waste gas treatment system and is provided with a direct-fired incinerator (TO), a first heat exchanger, a first Two heat exchangers, a third heat exchanger, a first cold-side conveying pipeline, a first adsorption wheel, a second adsorption wheel and a chimney, and pass through the direct-fired incinerator (TO) The furnace is equipped with a hot side forced exhaust pipe, and the other end of the hot side forced exhaust pipe is connected with the third hot side pipe of the third heat exchanger and the second hot side of the second heat exchanger. The connection between the pipes, or the connection between the second hot side pipe of the second heat exchanger and the first hot side pipe of the first heat exchanger, or the connection between the second heat side pipe of the second heat exchanger and the first hot side pipe of the first heat exchanger. The connection between the first hot side pipeline and the third hot side pipeline of the third heat exchanger or any one of the outlet of the direct-fired incinerator (TO), whereby when volatilization When the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace of the direct-fired incinerator (TO) can be adjusted through the hot side forced exhaust pipe, so as to have the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas During processing, it can prevent the direct-fired incinerator (TO) from overheating due to the furnace temperature being too high, or even causing shutdown.

Description

Energy-saving dual-runner hot side pass temperature control system and method thereof

The present invention relates to an energy-saving dual-runner hot side pass temperature control system and a method thereof. In particular, it relates to an energy-saving dual-runner hot side pass temperature control system and a method thereof, and particularly refers to a system that can adjust the amount or concentration of heat recovery when the concentration of volatile organic compounds (VOCs) becomes high, so that When treating organic waste gas, it can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature, or even causing shutdown. It is suitable for the semiconductor industry, optoelectronic industry or chemical-related industries. Organic waste gas treatment system or similar equipment.

According to the current situation, volatile organic gases (VOC) are generated in the manufacturing and production process of the semiconductor industry or optoelectronic industry. Therefore, processing equipment for processing volatile organic gases (VOC) will be installed in each factory area to avoid the occurrence of volatile organic gases. (VOC) are directly discharged into the air causing air pollution. At present, most of the concentrated gas desorbed by the treatment equipment is transported to the incinerator for combustion, and then the burned gas is transported to the chimney for discharge.

However, in recent years, both the central government and local governments have attached great importance to air pollution, and therefore have set relevant air quality standards for chimney emission standards. At the same time, they will be reviewed periodically in accordance with the development of international regulatory trends.

Therefore, in view of the above shortcomings, the inventor hopes to propose an energy-saving dual-runner thermal side pass temperature control system and method that can improve the organic waste gas treatment efficiency, so that the user can easily operate and assemble it, and has devoted himself to research and development. Designing the assembly to provide user convenience is the motive behind the invention that the inventor intends to develop.

The main purpose of the present invention is to provide an energy-saving dual-runner hot-side bypass temperature control system and method thereof, which is mainly used in organic waste gas treatment systems and is provided with a direct-fired incinerator (TO), a first thermal exchanger, a second heat exchanger, a third heat exchanger, a first cold side conveying pipeline, a first adsorption wheel, a second adsorption wheel and a chimney, and through the direct-fired The furnace of the incinerator (TO) is equipped with a hot side forced exhaust pipe, and the other end of the hot side forced exhaust pipe is connected to the third hot side pipe of the third heat exchanger and the second heat exchanger The connection point between the second hot side pipeline of the second heat exchanger, or the connection point between the second hot side pipeline of the second heat exchanger and the first hot side pipeline of the first heat exchanger, or the connection point with the second hot side pipeline of the second heat exchanger. The connection between the first hot side pipe of a heat exchanger and the third hot side pipe of the third heat exchanger, or any connection with the outlet of the direct-fired incinerator (TO), In this way, when the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace of the direct-fired incinerator (TO) can be adjusted through the hot side forced exhaust pipe, so as to have the ability to adjust the heat recovery amount or concentration. The efficiency prevents the direct-fired incinerator (TO) from overheating due to too high furnace temperature when treating organic waste gas, and even causes shutdown, thereby increasing the overall practicality.

Another object of the present invention is to provide an energy-saving dual-runner hot-side bypass temperature control system and method thereof, by providing at least one damper on the hot-side forced exhaust pipe, and the hot-side forced exhaust pipe The other end of the path is the connection point between the third hot side pipeline of the third heat exchanger and the second hot side pipeline of the second heat exchanger, or with the second heat side pipeline of the second heat exchanger. The connection point between the side pipe and the first hot side pipe of the first heat exchanger, or between the first hot side pipe of the first heat exchanger and the third hot side pipe of the third heat exchanger The connection between the pipelines, or any connection with the outlet of the direct-fired incinerator (TO), so that when the concentration of volatile organic compounds (VOCs) becomes high, it can be discharged through the hot side forced exhaust pipeline. Adjust the air volume of the furnace of the direct-fired incinerator (TO), and Partially incinerated high-temperature gases are transported to the connection points of the hot-side pipes of different heat exchangers, so that the hot-side forced exhaust pipes have the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be treated This prevents the direct-fired incinerator (TO) from overheating due to too high furnace temperature, which may even lead to shutdown, thereby increasing the overall usability.

In order to further understand the features, characteristics and technical content of the present invention, please refer to the following detailed description and drawings of the present invention. However, 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

102:furnace

11: Entrance

12:Export

20:First heat exchanger

21: First cold side pipeline

22:First hot side pipe

23: First cold side delivery pipeline

30: Second heat exchanger

31: Second cold side pipeline

32:Second hot side pipe

40:Third heat exchanger

41:Third cold side pipeline

42:Third hot side pipe

60: The first adsorption wheel

601: Adsorption area

602: Cooling area

603:Desorption zone

61:Exhaust gas intake pipe

611:Exhaust gas connecting pipe

6111: Exhaust gas connection control valve

62: First clean gas discharge pipe

621: The first clean gas connecting pipe

6211: The first clean gas connection control valve

63: First cooling air intake pipe

64: First cooling air delivery pipeline

65: The first hot gas delivery pipeline

66: First desorption concentrated gas pipeline

661:Fan

70: Second adsorption wheel

701: Adsorption area

702: Cooling area

703:Desorption zone

71: Second clean gas discharge pipe

711:Fan

72:Second cooling air intake pipe

73: Second cooling air delivery pipeline

74: Second hot gas delivery pipeline

75: Second desorption concentrated gas pipeline

751:Fan

80:Chimney

90: Hot side forced exhaust pipe

901: Adjust damper

S100: Input the gas to be adsorbed

S200: Input the gas to be adsorbed

S110: First adsorption wheel adsorption

S210: First adsorption wheel adsorption

S120: Input the first cooling gas

S220: Input the first cooling gas

S130: Deliver the first hot gas for desorption

S230: Deliver the first hot gas for desorption

S140: Desorption concentrated gas transportation

S240: Desorption concentrated gas transportation

S150: Gas transportation after incineration

S250: Gas transportation after incineration

S160: Second adsorption wheel adsorption

S260: Second adsorption wheel adsorption

S170: Input the second cooling gas

S270: Input the second cooling gas

S180: Transport the second hot gas for desorption

S280: Transport the second hot gas for desorption

S190: Hot side forced exhaust pipeline adjustment

S290: Hot side forced exhaust pipe adjustment

S300: Input the gas to be adsorbed

S400: Input the gas to be adsorbed

S310: First adsorption wheel adsorption

S410: First adsorption wheel adsorption

S320: Input the first cooling gas

S420: Input the first cooling gas

S330: Deliver the first hot gas for desorption

S430: Deliver the first hot gas for desorption

S340: Desorption concentrated gas transportation

S440: Desorption concentrated gas transportation

S350: Gas transportation after incineration

S450: Gas transportation after incineration

S360: Second adsorption wheel adsorption

S460: Second adsorption wheel adsorption

S370: Input the second cooling gas

S470: Input the second cooling gas

S380: Deliver the second hot gas for desorption

S480: Deliver the second hot gas for desorption

S390: Hot side forced exhaust pipeline adjustment

S490: Hot side forced exhaust pipe adjustment

S500: Input the gas to be adsorbed

S600: Input the gas to be adsorbed

S510: First adsorption wheel adsorption

S610: First adsorption wheel adsorption

S520: Input the first cooling gas

S620: Input the first cooling gas

S530: Deliver the first hot gas for desorption

S630: Deliver the first hot gas for desorption

S540: Desorption concentrated gas transportation

S640: Desorption concentrated gas transportation

S550: Gas transportation after incineration

S650: Gas transportation after incineration

S560: Second adsorption wheel adsorption

S660: Second adsorption wheel adsorption

S570: Input the second cooling gas

S670: Input the second cooling gas

S580: Deliver the second hot gas for desorption

S680: Deliver the second hot gas for desorption

S590: Hot side forced exhaust pipeline adjustment

S690: Hot side forced exhaust pipeline adjustment

Figure 1 is a schematic diagram of the system architecture with a hot-side forced exhaust pipeline in a first embodiment of the present invention in which the first heat exchanger is located next to the second heat exchanger.

Figure 2 is a schematic diagram of the system architecture with a hot-side forced exhaust pipeline in a second embodiment of the present invention in which the first heat exchanger is located next to the second heat exchanger.

Figure 3 is a schematic diagram of the system architecture with a hot-side forced exhaust pipeline in a third embodiment of the present invention in which the first heat exchanger is located next to the second heat exchanger.

Figure 4 is a schematic diagram of the system architecture with a hot-side forced exhaust pipeline according to the fourth embodiment of the present invention in which the first heat exchanger is located next to the third heat exchanger.

Figure 5 is a schematic diagram of the system architecture with a hot-side forced exhaust pipeline in a first embodiment of the present invention in which the first heat exchanger is located next to the third heat exchanger.

Figure 6 is a schematic diagram of the system architecture with a hot-side forced exhaust pipeline in a third embodiment of the present invention in which the first heat exchanger is located next to the third heat exchanger.

Figure 7 is a flow chart of the main steps of the first implementation aspect of the present invention.

Figure 8 is a flow chart of the main steps of the second implementation aspect of the present invention.

Figure 9 is a flow chart of the main steps of the third implementation aspect of the present invention.

Figure 10 is a flow chart of the main steps of the fourth implementation aspect of the present invention.

Figure 11 is a main step flow chart of the fifth implementation aspect of the present invention.

Figure 12 is a flow chart of the main steps of the sixth implementation aspect of the present invention.

Please refer to Figures 1 to 12, which are schematic diagrams of embodiments of the present invention. The best implementation mode of the energy-saving dual-runner hot side pass temperature control system and method of the present invention is applied to the semiconductor industry, optoelectronic industry or Volatile organic waste gas treatment systems or similar equipment in chemical-related industries are mainly capable of adjusting the heat recovery amount or concentration when the concentration of volatile organic compounds (VOCs) becomes high, so that direct combustion of organic waste gas can be prevented during treatment. The incinerator (TO) will not overheat due to the furnace temperature being too high, or even cause shutdown.

The energy-saving double-runner hot side pass temperature control system of the present invention mainly includes a direct-fired incinerator (TO) 10, a first heat exchanger 20, a second heat exchanger 30, and a third heat exchanger. The combined design of the heat exchanger 40, a first cold-side delivery pipe 23, a first adsorption wheel 60, a second adsorption wheel 70 and a chimney 80 (as shown in Figures 1 to 6), The first heat exchanger 20 is provided with a first cold side pipe 21 and a first hot side pipe 22, and the second heat exchanger 30 is provided with a second cold side pipe 31 and a second hot side pipe. Path 32, the third heat exchanger 40 is provided with a third cold side pipeline 41 and a third hot side pipeline 42. In addition, the direct-fired incinerator (TO) 10 is provided with a burner 101 and a furnace 102. The burner 101 is connected with the furnace 102, and the first heat exchanger 20, the second heat exchanger 30 and The third heat exchangers 40 are respectively provided in the direct-fired incinerator (TO) 10, and the direct-fired incinerator (TO) 10 The incinerator (TO) 10 is provided with an inlet 11 and an outlet 12 (as shown in Figures 1 to 4), and the inlet 11 is located at the burner head 101, and the inlet 11 is connected to the first heat The other end of the first cold side pipe 21 of the exchanger 20 is connected. Furthermore, the outlet 12 is located at the furnace 102, and the outlet 12 is connected to the chimney 80, thereby allowing the organic waste gas to pass through The inlet 11 enters the burner 101 for combustion, and then allows the burned gas to pass through the furnace 102 and be discharged from the outlet 12 to the chimney 80 for discharge, thereby saving energy.

And the above-mentioned first heat exchanger 20 has two embodiments. The first embodiment is to dispose the first heat exchanger 20 next to the second heat exchanger 30 (as shown in Figure 1 and Figure 2 and shown in Figure 3), so that the burner head 101 of the direct-fired incinerator (TO) 10 can deliver the high-temperature gas after incineration to the third hot side pipe 42 of the third heat exchanger 40 first. One side is used for heat exchange, and the other side of the third hot side pipe 42 of the third heat exchanger 40 transports the incinerated high-temperature gas to the second hot side of the second heat exchanger 30 One side of the pipeline 32 is used for heat exchange, and then the other side of the second hot side pipeline 32 of the second heat exchanger 30 transports the incinerated high-temperature gas to the first heat exchanger 20 One side of the first hot side pipeline 22 is used for heat exchange, and finally the other side of the first hot side pipeline 22 of the first heat exchanger 20 is transported to the outlet 12 of the furnace 102 (such as the first 2 and 3), and then transported to the chimney 80 through the outlet 12 of the furnace 102, so as to be discharged through the chimney 80.

Furthermore, another second embodiment is to dispose the first heat exchanger 20 next to the third heat exchanger 40 (as shown in Figures 4, 5 and 6), so that the direct-fired The burner head 101 of the incinerator (TO) 10 can deliver the incinerated high-temperature gas to the first heat exchanger first. One side of the first hot side pipe 22 of the first heat exchanger 20 is used for heat exchange, and the other side of the first hot side pipe 22 of the first heat exchanger 20 is used to transport the incinerated high-temperature gas to One side of the third hot side pipe 42 of the third heat exchanger 40 is used for heat exchange, and then the other side of the third hot side pipe 42 of the third heat exchanger 40 is used to transfer the high-temperature incineration The gas is then transported to one side of the second hot-side pipe 32 of the second heat exchanger 30 for heat exchange, and then comes from the other side of the second hot-side pipe 32 of the second heat exchanger 30 The incinerated high-temperature gas is then transported to the outlet 12 of the furnace 102 (as shown in Figures 4, 5 and 6), and then transported to the chimney 80 through the outlet 12 of the furnace 102 to pass through the chimney. 80 for emissions.

In addition, the first adsorption wheel 60 of the present invention is provided with an adsorption area 601, a cooling area 602 and a desorption area 603. The first adsorption wheel 60 is connected to an exhaust gas inlet pipe 61 and a first clean gas discharge pipe. 62, a first cooling gas inlet pipeline 63, a first cooling gas delivery pipeline 64, a first hot gas delivery pipeline 65 and a first desorption concentrated gas pipeline 66, (as shown in Figure 1 to (shown in Figure 6) and the second adsorption wheel 70 is provided with an adsorption zone 701, a cooling zone 702 and a desorption zone 703. The second adsorption wheel 70 is connected to a second clean gas discharge pipe 71, a A second cooling gas inlet pipeline 72 , a second cooling gas delivery pipeline 73 , a second hot gas delivery pipeline 74 and a second desorption concentrated gas pipeline 75 . The first adsorption rotor 60 and the second adsorption rotor 70 are respectively zeolite concentration rotors or concentration rotors made of other materials.

One end of the waste gas inlet pipe 61 is connected to one side of the adsorption area 601 of the first adsorption rotor 60 so that the waste gas inlet pipe 61 can transport organic waste gas to the first adsorption rotor 60 . One side of the adsorption zone 601, and the first clean gas discharge pipe 62 One end of the first clean gas discharge pipe 62 is connected to the other side of the adsorption area 601 of the first adsorption wheel 60 , and one end of the first clean gas discharge pipe 62 is connected to one side of the adsorption area 701 of the second adsorption wheel 70 , so that the organic waste gas can adsorb organic matter through the adsorption zone 601 of the first adsorption wheel 60 and then be transported to the adsorption zone 701 of the second adsorption wheel 70 through the first clean gas discharge pipe 62 ( As shown in Figures 1 to 6). In addition, the other side of the adsorption area 701 of the second adsorption wheel 70 is connected to the second clean gas discharge pipe 71 to be connected to the chimney 80 through the other end of the second clean gas discharge pipe 71. And the second clean air discharge pipe 71 is equipped with a fan 711 (as shown in Figures 2 and 3), so that the air in the second clean air discharge pipe 71 can be adsorbed through the fan 711 The gas is pushed and pulled into the chimney 80 for discharge.

In addition, one side of the cooling zone 602 of the first adsorption wheel 60 is connected to the first cooling gas inlet pipe 63, so that the gas can enter the cooling zone 602 of the first adsorption wheel 60 for cooling (such as 1 to 6), and the other side of the cooling zone 602 of the first adsorption wheel 60 is connected to one end of the first cooling air delivery pipeline 64, and the first cooling air delivery pipeline 64 The other end is connected to one end of the third cold side pipe 41 of the third heat exchanger 40 to transport the gas entering the cooling zone 602 of the first adsorption rotor 60 to the third heat exchanger 40 Heat exchange is performed (as shown in Figures 1 to 6). Furthermore, one end of the first hot gas delivery pipe 65 is connected to the other side of the desorption zone 603 of the first adsorption rotor 60, and The other end of the first hot gas transport pipeline 65 is connected to the other end of the third cold side pipeline 41 of the third heat exchanger 40 to transfer the high-temperature hot gas that is heat exchanged through the third heat exchanger 40 The hot gas is transported to the desorption area 603 of the first adsorption rotor 60 through the first hot gas delivery pipe 65 for desorption use.

The cooling zone 602 of the first adsorption wheel 60 is provided with two implementation modes. The first implementation mode is a first cooling air inlet connected to one side of the cooling zone 602 of the first adsorption wheel 60. The air pipeline 63 is for fresh air or outside air to enter (as shown in Figure 1), and the cooling zone 602 of the first adsorption rotor 60 is provided with cooling through the fresh air or outside air. Another second embodiment is that the exhaust gas inlet pipe 61 is provided with an exhaust gas connecting pipe 611, and the other end of the exhaust gas connecting pipe 611 is connected to the first cooling air inlet pipe 63 (such as the second 6), the exhaust gas in the exhaust gas inlet pipe 61 can be transported to the cooling zone 602 of the first adsorption rotor 60 for cooling through the exhaust gas communication pipe 611, and the The exhaust gas communication pipeline 611 is provided with an exhaust gas communication control valve 6111 to control the air volume of the exhaust gas communication pipeline 611.

In addition, one side of the cooling zone 702 of the second adsorption wheel 70 is connected to the second cooling gas inlet pipe 72 so that the gas can enter the cooling zone 702 of the second adsorption wheel 70 for cooling (such as 1 to 6), and the other side of the cooling zone 702 of the second adsorption wheel 70 is connected to one end of the second cooling air delivery pipeline 73, and the second cooling air delivery pipeline 73 The other end is connected to one end of the second cold side pipe 31 of the second heat exchanger 30 to transport the gas entering the cooling zone 702 of the second adsorption rotor 70 to the second heat exchanger 30 Heat exchange is performed (as shown in Figures 1 to 6). Furthermore, one end of the second hot gas delivery pipeline 74 is connected to the other side of the desorption zone 703 of the second adsorption rotor 70, and The other end of the second hot gas transport pipeline 74 is connected to the other end of the second cold side pipeline 31 of the second heat exchanger 30 to transfer the high-temperature hot gas that is heat exchanged through the second heat exchanger 30 The hot gas is transported to the desorption area 703 of the second adsorption rotor 70 through the second hot gas delivery pipeline 74 for desorption use.

The cooling zone 702 of the second adsorption wheel 70 is provided with two embodiments. The first implementation mode is a second cooling air inlet connected to one side of the cooling zone 702 of the second adsorption wheel 70 . The air pipeline 72 is for fresh air or outside air to enter (as shown in Figure 1), and the cooling zone 702 of the second adsorption rotor 70 is provided with cooling through the fresh air or outside air. Another second embodiment is that the first clean gas discharge pipe 62 is provided with a first clean gas communication pipe 621, and the other end of the first clean gas communication pipe 621 is connected to the second cooling air inlet. The pipeline 72 is connected (as shown in Figures 2, 5 and 6), so that the gas in the first clean gas discharge pipeline 62 can be transported to the first clean gas communication pipeline 621. The cooling zone 702 of the second adsorption wheel 70 is used for cooling. In addition, the first clean gas communication pipe 621 is provided with a first clean gas communication control valve 6211 to control the air volume of the first clean gas communication pipe 621 .

In addition, one end of the first desorbed concentrated gas pipeline 66 is connected to one side of the desorption zone 603 of the first adsorption rotor 60, and the other end of the first desorbed concentrated gas pipeline 66 is connected to the third One end of the first cold side pipeline 21 of a heat exchanger 20 is connected, and the other end of the first cold side pipeline 21 of the first heat exchanger 20 is connected to one end of the first cold side delivery pipeline 23 , and the other end of the first cold-side conveying pipeline 23 is connected to the inlet 11 of the direct-fired incinerator (TO) 10 (as shown in Figures 1 to 6), so that the high-temperature degassed The attached desorbed concentrated gas can be transported to one end of the first cold side pipeline 21 of the first heat exchanger 20 through the first desorbed concentrated gas pipeline 66, and is transported from the first heat exchanger 20 to The other end of the first cold side pipeline 21 is transported to one end of the first cold side transportation pipeline 23, and the other end of the first cold side transportation pipeline 23 is transported to the direct-fired incinerator. Inside the entrance 11 of (TO) 10 (as shown in Figures 1 to 6), the direct-fired incinerator (TO) 10 burners 101 are used to perform high temperature cracking to reduce volatile organic compounds. In addition, the first desorbed concentrated gas pipeline 66 is provided with a fan 661 to push and pull the desorbed concentrated gas into one end of the first cold side pipeline 21 of the first heat exchanger 20 .

In addition, one end of the second desorbed concentrated gas pipeline 75 is connected to one side of the desorption zone 703 of the second adsorption rotor 70 , and the other end of the second desorbed concentrated gas pipeline 75 can be implemented in two ways. way, and the first implementation mode is that the other end of the second desorbed concentrated gas pipeline 75 is connected to the exhaust gas inlet pipeline 61 (as shown in Figure 1, Figure 2 and Figure 6) , so that the concentrated gas can enter the adsorption zone 601 of the first adsorption rotor 60 through the exhaust gas inlet pipe 61 for re-adsorption. Another second embodiment is that the other end of the second desorbed concentrated gas pipeline 75 is connected to the first cooling gas inlet pipeline 63 (as shown in Figures 3, 4 and 5 ), so that the concentrated gas can enter the cooling zone 602 of the first adsorption rotor 60 through the first cooling gas inlet pipe 63 for cooling. Furthermore, the second desorbed concentrated gas pipeline 75 is provided with a fan 751 (as shown in Figures 3 and 5) to push and pull the desorbed concentrated gas into the exhaust gas inlet pipeline 61 or the exhaust gas inlet pipeline 61. The first cooling air enters the air pipeline 63 . The desorption gas generated through the desorption zone 703 of the second adsorption wheel 70 can enter the adsorption zone 601 of the first adsorption wheel 60 or the cooling zone 602 of the first adsorption wheel 60 for recycling. In order to improve the treatment efficiency of organic waste gas.

Furthermore, the energy-saving double-runner hot side pass temperature control system of the present invention mainly has four implementation modes, and among the four implementation modes, the direct-fired incinerator (TO) 10, The first heat exchanger 20, the second heat exchanger 30, the third heat exchanger 40, the first cold side delivery pipe 23, the first adsorption wheel 60, the second adsorption wheel 70 and the chimney 80 adopt the same design. Design, therefore, the above-mentioned direct-fired incinerator (TO) 10, first heat exchanger 20, second heat exchanger 30, third heat exchanger 40, first cold-side transfer pipeline 23, first adsorption rotor The contents of the wheel 60, the second adsorption runner 70 and the chimney 80 are not repeated, please refer to the above description.

The difference between the first implementation mode (as shown in Figures 1 and 5) is that the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipe 90. One end of the side forced exhaust pipe 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, regardless of whether the first heat exchanger 20 is located next to the second heat exchanger 30 (as shown in Figure 1 (shown in Figure 5) or when the first heat exchanger 20 is located next to the third heat exchanger 40 (as shown in Figure 5), the other end of the hot side forced exhaust pipe 90 is connected to the third heat exchanger The connection point between the third hot side pipe 42 of 40 and the second hot side pipe 32 of the second heat exchanger 30 is connected, wherein the hot side forced exhaust pipe 90 is provided with at least one damper 901, and Two dampers (not shown) can be provided in conjunction with the pipeline to control the air volume of the hot-side forced exhaust pipeline 90 through the damper 901. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, At this time, the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot side forced exhaust pipe 90, and part of the high-temperature gas of the incineration can be transported to the third heat exchanger 40. The connection between the hot side pipeline 42 and the second hot side pipeline 32 of the second heat exchanger 30 allows the hot side forced exhaust pipeline 90 to have the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be processed At this time, it can prevent the direct-fired incinerator (TO) 10 from overheating due to the furnace temperature being too high, or even causing shutdown.

In addition, the difference of the second implementation mode (as shown in Figure 2) is that the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipeline 90. One end of the pipeline 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the first heat When the exchanger 20 is located next to the second heat exchanger 30 (as shown in Figure 2), the other end of the hot side forced exhaust pipe 90 is connected to the second hot side pipe of the second heat exchanger 30. 32 is connected to the connection point between the first hot side pipeline 22 of the first heat exchanger 20, wherein the hot side forced exhaust pipeline 90 is provided with at least one damper 901, which can also be provided in conjunction with the pipeline. Two dampers (not shown) are used to control the air volume of the hot-side forced exhaust pipe 90 through the damper 901. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the hot-side strong exhaust pipe can be The exhaust pipe 90 is used to adjust the air volume of the furnace 102 of the direct-fired incinerator (TO) 10, and transport part of the high-temperature gas of combustion to the second hot side pipe 32 of the second heat exchanger 30 and the second heat exchanger 30. The connection point between the first hot side pipes 22 of a heat exchanger 20 allows the hot side forced exhaust pipe 90 to have the effect of adjusting the heat recovery amount or concentration, so that direct combustion incineration can be prevented during the treatment of organic waste gas. Furnace (TO) 10 will not overheat due to the furnace temperature being too high, or even cause shutdown.

In addition, the difference between the third implementation mode (as shown in Figures 3 and 6) is that the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipe 90. One end of the hot side forced exhaust pipe 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, regardless of whether the first heat exchanger 20 is located next to the second heat exchanger 30 (as shown in Figure 3 (as shown in Figure 6) or when the first heat exchanger 20 is located next to the third heat exchanger 40 (as shown in Figure 6), the other end of the hot side forced exhaust pipe 90 is connected to the direct-fired incineration The outlet 12 of the furnace (TO) 10 is connected. The hot side forced exhaust pipe 90 is provided with at least one damper 901. Two dampers (not shown) can also be provided with the pipe to pass through the pipe. The damper 901 is used to regulate the air volume of the hot-side forced exhaust pipe 90. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the direct-fired incinerator can be adjusted through the hot-side forced exhaust pipe 90 ( The air volume of the furnace 102 of the TO) 10 is transferred to the outlet of the direct-fired incinerator (TO) 10. At the port 12, the hot side forced exhaust pipe 90 has the effect of adjusting the heat recovery amount or concentration, so that when the organic waste gas is processed, it can prevent the direct-fired incinerator (TO) 10 from being caused by the furnace temperature being too high. The phenomenon of over-temperature may even lead to shutdown.

In addition, the difference of the fourth implementation mode (as shown in Figure 4) is that the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipeline 90. One end of the pipeline 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and when the first heat exchanger 20 is located next to the third heat exchanger 40 (as shown in Figure 4) When The hot side forced exhaust pipe 90 is provided with at least one damper 901, and two dampers (not shown) can also be provided in conjunction with the pipeline to control the hot side through the damper 901. The air volume of the forced exhaust pipe 90, therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot side forced exhaust pipe 90 , and transport part of the burned high-temperature gas to the connection between the first hot side pipe 22 of the first heat exchanger 20 and the third hot side pipe 42 of the third heat exchanger 40, so that the heat The side forced exhaust pipe 90 has the effect of adjusting the heat recovery amount or concentration, so that when the organic waste gas is processed, it can prevent the direct-fired incinerator (TO) 10 from overheating due to the furnace temperature being too high, and even causing A shutdown situation occurs.

The energy-saving dual-runner hot side pass temperature control method of the present invention is mainly used in an organic waste gas treatment system, and includes a direct-fired incinerator (TO) 10, a first heat exchanger 20, a first The combined device of two heat exchangers 30, a third heat exchanger 40, a first cold-side conveying pipeline 23, a first adsorption wheel 60, a second adsorption wheel 70 and a chimney 80 Design (as shown in Figures 1 to 6), in which 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 There is 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, wherein the first cold side conveys One end of the pipeline 23 is connected to the other end of the first cold-side pipeline 21 , and the other end of the first cold-side delivery pipeline 23 is connected to the inlet 11 of the direct-fired incinerator (TO) 10 . In addition, the direct-fired incinerator (TO) 10 is provided with a burner 101 and a furnace 102. The burner 101 is connected with the furnace 102, and the first heat exchanger 20, the second heat exchanger 30 and The third heat exchangers 40 are respectively installed in the direct-fired incinerator (TO) 10, and the direct-fired incinerator (TO) 10 is provided with an inlet 11 and an outlet 12 (as shown in Figures 1 to 6 as shown in the figure), and the inlet 11 is located at the furnace head 101, and the inlet 11 is connected to the other end of the first cold side delivery pipe 23, and furthermore, the outlet 12 is located in the furnace 102 , and the outlet 12 is connected to the chimney 80, thereby allowing the organic waste gas to enter the burner 101 through the inlet 11 for combustion, and then allow the burned gas to pass through the furnace 102 and pass through the furnace 102. The outlet 12 discharges to the chimney 80 for energy saving.

In addition, the first adsorption wheel 60 of the present invention is provided with an adsorption area 601, a cooling area 602 and a desorption area 603. The first adsorption wheel 60 is connected to an exhaust gas inlet pipe 61 and a first clean gas discharge pipe. 62, a first cooling gas inlet pipeline 63, a first cooling gas delivery pipeline 64, a first hot gas delivery pipeline 65 and a first desorption concentrated gas pipeline 66 (as shown in Figure 1 to Figure 1 6), and the second adsorption runner 70 is provided with an adsorption zone 701, a cooling zone 702 and a desorption zone 703. The second adsorption runner 70 is connected to a second clean gas discharge pipe 71, a A second cooling air inlet pipe 72 and a second cooling air delivery pipe 73. A second hot gas delivery pipeline 74 and a second desorption concentrated gas pipeline 75 (as shown in Figures 1 to 6). The first adsorption rotor 60 and the second adsorption rotor 70 are respectively zeolite concentration rotors or concentration rotors made of other materials.

The main steps of the control method (as shown in Figure 7) include: Step S100: input the gas to be adsorbed: send the waste gas into the first adsorption wheel 60 through the other end of the waste gas inlet pipe 61 One side of the adsorption area 601. After completing the above step S100, the next step S110 is performed.

In addition, the next step is step S110: first adsorption wheel adsorption: after adsorption through the adsorption area 601 of the first adsorption wheel 60, the adsorbed material is adsorbed from the other side of the adsorption area 601 of the first adsorption wheel 60. The gas is output to the adsorption area 701 of the second adsorption rotor 70 through the other end of the first clean gas discharge pipe 62 . After completing the above step S110, the next step S120 is performed.

In the above-mentioned step S110, the other side of the adsorption area 701 of the second adsorption rotor 70 is connected to the second clean gas discharge pipe 71, so as to communicate with the second clean gas discharge pipe 71 through the other end of the second clean gas discharge pipe 71. The chimney 80 is connected, and the second clean air discharge pipe 71 is provided with a fan 711 (as shown in Figures 2 and 3), so that the second clean air discharge pipe 71 can be discharged through the fan 711. The adsorbed gas is pushed and pulled into the chimney 80 for discharge.

In addition, the next step S120 is to input the first cooling gas: transport the cooling gas through the other end of the first cooling gas inlet pipe 63 to the cooling zone 602 of the first adsorption wheel 60 for cooling, and then through the The other end of the first cooling air delivery pipeline 64 is used to deliver the cooling air passing through the cooling zone 602 of the first adsorption rotor 60 to the third heat exchanger. One end of the third cold side pipeline 41 of 40. After completing the above step S120, the next step S130 is performed.

The cooling zone 602 of the first adsorption wheel 60 in the above-mentioned step S120 is provided with two implementation modes, wherein the first implementation mode is connected to one side of the cooling zone 602 of the first adsorption wheel 60 . A cooling air inlet pipe 63 is for fresh air or outside air to enter (as shown in Figure 1), and the fresh air or outside air is used to cool down the cooling zone 602 of the first adsorption rotor 60. Another second embodiment is that the exhaust gas inlet pipe 61 is provided with an exhaust gas connecting pipe 611, and the other end of the exhaust gas connecting pipe 611 is connected to the first cooling air inlet pipe 63 (such as the second 6), the exhaust gas in the exhaust gas inlet pipe 61 can be transported to the cooling zone 602 of the first adsorption rotor 60 for cooling through the exhaust gas communication pipe 611, and the The exhaust gas communication pipeline 611 is provided with an exhaust gas communication control valve 6111 to control the air volume of the exhaust gas communication pipeline 611.

In addition, the next step S130 is to transport the first hot gas for desorption: transport the hot gas to the third heat exchanger 40 through the first hot gas transport pipeline 65 connected to the other end of the third cold side pipeline 41. The desorption zone 603 of the first adsorption wheel 60 performs desorption, and then the desorption concentrated gas is transported to the first cold side tube of the first heat exchanger 20 through the other end of the first desorption concentrated gas pipeline 66 One end of Road 21. After completing the above step S130, the next step S140 is performed.

The first desorbed concentrated gas pipeline 66 in the above-mentioned step S130 is provided with a fan 661 (as shown in Figures 2 and 3) to push and pull the desorbed concentrated gas into the first heat exchanger. In the first cold side pipeline 21 of 20.

In addition, the next step S140 is desorption and concentrated gas transportation: the desorption The concentrated gas is then transported to the inlet 11 of the direct-fired incinerator (TO) 10 through the first cold-side delivery pipe 23 connected to the other end of the first cold-side pipe 21 of the first heat exchanger 20 . After completing the above step S140, the next step S150 is performed.

In addition, the next step S150 is to transport the incinerated gas: transport the incinerated gas generated by the burner head 101 of the direct-fired incinerator (TO) 10 to the third heat exchanger 40 One end of the three hot side pipes 42 is transported from the other end of the third hot side pipe 42 of the third heat exchanger 40 to one end of the second hot side pipe 32 of the second heat exchanger 30, and then It is transported from the other end of the second hot side pipe 32 of the second heat exchanger 30 to one end of the first hot side pipe 22 of the first heat exchanger 20, and finally from the first heat side pipe 20 of the first heat exchanger 20. The other end of a hot side pipeline 22 is delivered to the outlet 12 of the direct-fired incinerator (TO) 10 . After completing the above step S150, the next step S160 is performed.

In addition, the next step S160 is adsorption by the second adsorption wheel: transporting the adsorbed gas in the first clean gas discharge pipe 62 to one side of the adsorption area 701 of the second adsorption wheel 70 for adsorption, and then The gas after the second adsorption is transported to the chimney 80 for discharge through the second clean gas discharge pipe 71 . After completing the above step S160, the next step S170 is performed.

In addition, the next step S170 is to input the second cooling gas: transport the cooling gas through the other end of the second cooling gas inlet pipe 72 to the cooling zone 702 of the second adsorption wheel 70 for cooling, and then through the The other end of the second cooling air delivery pipe 73 is used to deliver the cooling air passing through the cooling zone 702 of the second adsorption rotor 70 to one end of the second cold side pipe 31 of the second heat exchanger 30 . After completing the above step S170, the next step S180 is performed.

The cooling zone 702 of the second adsorption wheel 70 in the above-mentioned step S170 is provided with two implementation modes, wherein the first implementation mode is the second cooling zone connected to one side of the cooling zone 702 of the second adsorption wheel 70 . The second cooling air inlet pipe 72 is for fresh air or outside air to enter (as shown in Figure 1), and the fresh air or outside air is used to cool down the cooling zone 702 of the second adsorption rotor 70. Another second embodiment is that the first clean gas discharge pipe 62 is provided with a first clean gas communication pipe 621, and the other end of the first clean gas communication pipe 621 is connected to the second cooling air inlet. The pipeline 72 is connected (as shown in Figures 5 and 6), so that the gas in the first clean gas discharge pipeline 62 can be transported to the second adsorption rotor through the first clean gas communication pipeline 621. The cooling zone 702 of the wheel 70 is used for cooling, and the first clean air communication pipe 621 is provided with a first clean gas communication control valve 6211 to control the air volume of the first clean gas communication pipe 621.

In addition, the next step S180 is to transport the second hot gas for desorption: transport the hot gas to the second hot gas transport pipeline 74 through the second hot gas transport pipeline 74 connected to the other end of the second cold side pipeline 31 of the second heat exchanger 30 . The desorption zone 703 of the second adsorption wheel 70 performs desorption and is output through the other end of the second desorption concentrated gas pipeline 75 . After completing the above step S180, the next step S190 is performed.

There are two implementation methods for the other end of the second desorbed concentrated gas pipeline 75 in the above-mentioned step S180, and the first embodiment is that the other end of the second desorbed concentrated gas pipeline 75 is connected to the second end of the second desorbed concentrated gas pipeline 75. The exhaust gas inlet pipe 61 is connected (as shown in Figure 1, Figure 2 and Figure 6), so that the concentrated gas can enter the adsorption of the first adsorption wheel 60 through the exhaust gas inlet pipe 61. in area 601 for re-adsorption. Another second embodiment is that the other end of the second desorbed concentrated gas pipeline 75 is connected to the first cooling gas inlet pipeline 63 connected (as shown in Figures 3, 4 and 5), so that the concentrated gas can enter the cooling zone 602 of the first adsorption rotor 60 through the first cooling gas inlet pipe 63 , for cooling. Furthermore, the second desorbed concentrated gas pipeline 75 is provided with a fan 751 to push and pull the desorbed concentrated gas into the exhaust gas inlet pipeline 61 or the first cooling gas inlet pipeline 63 . The desorption gas generated through the desorption zone 703 of the second adsorption wheel 70 can enter the adsorption zone 601 of the first adsorption wheel 60 or the cooling zone 602 of the first adsorption wheel 60 for recycling. In order to improve the treatment efficiency of organic waste gas.

In addition, the next step S190 is to adjust the hot side forced exhaust pipeline: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot side forced exhaust pipeline 90, and one end of the hot side forced exhaust pipeline 90 It is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot side forced exhaust pipe 90 is connected to the third hot side pipe 42 of the third heat exchanger 40 and the second heat pipe. The second hot side pipes 32 of the exchanger 30 are connected at the joints. The hot side forced exhaust pipe 90 is provided with at least one regulating damper 901 to adjust the direct combustion through the hot side forced exhaust pipe 90. The air volume of the furnace 102 of the type incinerator (TO) 10.

In the above-mentioned step S190, one end of the hot side forced exhaust pipe 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot side forced exhaust pipe 90 is connected to the third The third hot side pipe 42 of the heat exchanger 40 is connected to the second hot side pipe 32 of the second heat exchanger 30 (as shown in Figure 1), wherein the hot side forced exhaust pipe System 90 is provided with at least one damper 901 to control the air volume of the hot side forced exhaust pipe 90 through the damper 901. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, it can pass through the hot side strong exhaust pipe 90. The exhaust pipe 90 is used to adjust the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 and transport part of the high-temperature gas burned to the third hot side of the third heat exchanger 40 The connection between the pipeline 42 and the second hot side pipeline 32 of the second heat exchanger 30 allows the hot side forced exhaust pipeline 90 to have the effect of adjusting the heat recovery amount or concentration, so that when the organic waste gas is treated, It can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, or even causing shutdown.

Furthermore, the energy-saving double-runner hot side pass temperature control method of the present invention mainly has six implementation modes, and the step S100 of the first implementation mode (as shown in Figure 7) inputs the input to be adsorbed. Gas, step S110 is adsorbed by the first adsorption wheel, step S120 is inputting the first cooling gas, step S130 is transporting the first hot gas for desorption, step S140 is transporting the desorbed concentrated gas, step S150 is transporting the gas after incineration, and step S160 is the second adsorption wheel. Wheel adsorption, input of the second cooling gas in step S170, delivery of the second hot gas for desorption in step S180, and adjustment of the hot side forced exhaust pipeline in step S190 have been explained above. Please refer to the above explanation.

In another second implementation mode (as shown in Figure 8), step S200 inputs the gas to be adsorbed, step S210 adsorbs the first adsorption wheel, inputs the first cooling gas in step S220, and transports the first hot gas for desorption in step S230. Step S240 desorption concentrated gas transportation, step S250 gas transportation after incineration, step S260 second adsorption wheel adsorption, step S270 inputting the second cooling gas and step S280 transporting the second hot gas for desorption, are the same as the third implementation mode ( As shown in Figure 9), step S300 inputs the gas to be adsorbed, step S310 adsorbs the first adsorption wheel, S320 inputs the first cooling gas, step S330 transports the first hot gas for desorption, step S340 transports the desorbed concentrated gas, Step S350 is to transport the gas after incineration, step S360 is to adsorb the second adsorption wheel, step S370 is to input the second cooling gas and step S380 is to transport the second hot gas for desorption, and the fourth implementation mode (as shown in Figure 10 (shown) in step S400 to input the gas to be adsorbed, step S410 to adsorb by the first adsorption wheel, S420 to input the first cooling gas, step S430 to transport the first hot gas for desorption, step S440 to transport the desorbed concentrated gas, and step S450 to incinerate. Gas transport, step S460 adsorption by the second adsorption wheel, step S470 input of the second cooling gas and step S480 transport of the second hot gas for desorption, and the input of step S500 in the fifth implementation mode (as shown in Figure 11) is pending. Adsorbed gas, step S510 first adsorption wheel adsorption, step S520 input of the first cooling gas, step S530 transport of the first hot gas for desorption, step S540 desorption of concentrated gas transport, step S550 gas transport after incineration, step S560 second adsorption Rotor adsorption, step S570 inputting the second cooling gas and step S580 transporting the second hot gas for desorption, and step S600 in the sixth implementation mode (as shown in Figure 12) inputting the gas to be adsorbed, step S610 first adsorption Rotor adsorption, S620 input of the first cooling gas, step S630 transport of the first hot gas for desorption, step S640 transport of desorbed concentrated gas, step S650 gas transport after incineration, step S660 second adsorption wheel adsorption, step S670 input of the second The cooling gas and step S680 of transporting the second hot gas for desorption are all the same as in the first implementation mode (as shown in Figure 7). Step S100 of inputting the gas to be adsorbed, step S110 of first adsorption rotor adsorption, S120 Input the first cooling gas, step S130 to transport the first hot gas for desorption, step S140 to transport the desorbed concentrated gas, step S150 to transport the gas after incineration, step S160 to adsorb the second adsorption wheel, step S170 to input the second cooling gas, step S180 The design of transporting the second hot gas for desorption is the same. The only difference lies in the gas transport after incineration in step S150 and the adjustment of the hot side forced exhaust pipeline in step S190.

Therefore, the above and step S100 input the gas to be adsorbed, step S110 the first adsorption wheel adsorption, S120 input the first cooling gas, step S130 transport the first The same contents include hot gas desorption, step S140 desorption and concentrated gas transportation, step S150 gas transportation after incineration, step S160 second adsorption wheel adsorption, step S170 input of the second cooling gas, and step S180 transportation of the second hot gas for desorption. No need to repeat, please refer to the above explanation. The following will focus on step S250 gas transportation after incineration and step S290 hot side forced exhaust pipeline adjustment in the second implementation mode (as shown in Figure 8), and the third implementation mode (as shown in Figure 9 ) in step S350 gas transportation after incineration and step S390 hot side forced exhaust pipeline adjustment, step S450 gas transportation after incineration and step S490 hot side exhaust pipe adjustment in the fourth implementation mode (as shown in Figure 10) Exhaust pipeline adjustment, step S550 of gas transportation after incineration in the fifth implementation mode (as shown in Figure 11) and step S590 hot side forced exhaust pipeline adjustment and the sixth implementation mode (as shown in Figure 12 As shown in the figure), step S650 of gas transportation after incineration and step S690 of hot side forced exhaust pipeline adjustment will be explained.

The difference between the second implementation mode (as shown in Figure 8) is the gas transportation after incineration in step S250: the incinerated gas generated by burning the burner head 101 of the direct-fired incinerator (TO) 10 The gas is transported to one end of the third hot side pipeline 42 of the third heat exchanger 40, and is transported to the second heat exchanger from the other end of the third hot side pipeline 42 of the third heat exchanger 40. One end of the second hot side pipeline 32 of the second heat exchanger 30 is then transported to the first hot side pipeline 22 of the first heat exchanger 20 from the other end of the second hot side pipeline 32 of the second heat exchanger 30 One end is finally transported to the outlet 12 of the direct-fired incinerator (TO) 10 by the other end of the first hot side pipe 22 of the first heat exchanger 20 .

In the above-mentioned step S250, the burner head 101 of the direct-fired incinerator (TO) 10 can first transport the incinerated high-temperature gas to one side of the third hot side pipe 42 of the third heat exchanger 40 for processing. heat exchange, and then through the third hot side tube of the third heat exchanger 40 The incinerated high-temperature gas is then transported to one side of the second hot side pipe 32 of the second heat exchanger 30 from the other side of the path 42 for heat exchange, and then through the second heat exchanger 30 The other side of the second hot-side pipeline 32 transports the incinerated high-temperature gas to one side of the first hot-side pipeline 22 of the first heat exchanger 20 for heat exchange. Finally, the first heat The other side of the first hot side pipe 22 of the exchanger 20 is transported to the outlet 12 of the furnace 102 (as shown in Figures 1, 2 and 3), and then from the outlet 12 of the furnace 102. It is transported to the chimney 80 for discharge through the chimney 80 .

Step S290 hot side forced exhaust pipeline adjustment: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipeline 90, and one end of the hot-side forced exhaust pipeline 90 is connected to the direct-fired incinerator (TO) 10. The furnace 102 of the type incinerator (TO) 10 is connected, and the other end of the hot side forced exhaust pipe 90 is connected with the second hot side pipe 32 of the second heat exchanger 30 and the first heat exchanger 20 The hot side pipelines 22 are connected at the joints. The hot side forced exhaust pipeline 90 is provided with at least one damper 901 to adjust the direct-fired incinerator (TO) through the hot side forced exhaust pipeline 90. )10 air volume of the furnace 102.

In the above-mentioned step S290, one end of the hot side forced exhaust pipe 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot side forced exhaust pipe 90 is connected to the second The second hot side pipe 32 of the heat exchanger 30 is connected to the first hot side pipe 22 of the first heat exchanger 20 (as shown in Figure 2), wherein the hot side forced exhaust pipe The 90 series is provided with at least one damper 901, and can also be equipped with two dampers (not shown) in conjunction with the pipeline to control the air volume of the hot side forced exhaust pipeline 90 through the damper 901. Therefore, When the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot side forced exhaust pipe 90, and part of the incinerator can be The burned high-temperature gas is transported to the connection between the second hot side pipe 32 of the second heat exchanger 30 and the first hot side pipe 22 of the first heat exchanger 20, so that the hot side forced exhaust pipe 90 has the ability to adjust the heat recovery amount or concentration, so that when organic waste gas is being processed, it can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, or even causing shutdown.

The difference in the third implementation mode (as shown in Figure 9) is the gas transportation after incineration in step S350: the incinerated gas generated by burning the burner head 101 of the direct-fired incinerator (TO) 10 The gas is transported to one end of the third hot side pipeline 42 of the third heat exchanger 40, and is transported to the second heat exchanger from the other end of the third hot side pipeline 42 of the third heat exchanger 40. One end of the second hot side pipeline 32 of the second heat exchanger 30 is then transported to the first hot side pipeline 22 of the first heat exchanger 20 from the other end of the second hot side pipeline 32 of the second heat exchanger 30 One end is finally transported to the outlet 12 of the direct-fired incinerator (TO) 10 by the other end of the first hot side pipe 22 of the first heat exchanger 20 .

In the above-mentioned step S350, the burner head 101 of the direct-fired incinerator (TO) 10 can first transport the incinerated high-temperature gas to one side of the third hot side pipe 42 of the third heat exchanger 40 for processing. Heat exchange, and then the incinerated high-temperature gas is transported to the second hot side pipeline 32 of the second heat exchanger 30 from the other side of the third hot side pipe 42 of the third heat exchanger 40 One side is for heat exchange, and then the other side of the second hot side pipe 32 of the second heat exchanger 30 transports the incinerated high-temperature gas to the first heat of the first heat exchanger 20 One side of the side pipe 22 is used for heat exchange, and finally the other side of the first hot side pipe 22 of the first heat exchanger 20 is transported to the outlet 12 of the furnace 102 (as shown in Figure 1, Figure 2 3), and then transported to the chimney 80 through the outlet 12 of the furnace 102, so as to be discharged through the chimney 80.

Step S390 hot side forced exhaust pipeline adjustment: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipeline 90, and one end of the hot-side forced exhaust pipeline 90 is connected to the direct-fired incinerator (TO) 10. The furnace 102 of the direct-fired incinerator (TO) 10 is connected. The other end of the hot-side forced exhaust pipe 90 is connected to the outlet 12 of the direct-fired incinerator (TO) 10. The hot-side forced exhaust pipe 90 is equipped with There is at least one damper 901 for adjusting the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 through the hot side forced exhaust pipe 90 .

In the above-mentioned step S390, one end of the hot-side forced exhaust pipe 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side forced exhaust pipe 90 is connected to the direct-fired incinerator (TO) 10. The outlet 12 of the type incinerator (TO) 10 is connected (as shown in Figure 3). The hot side forced exhaust pipe 90 is provided with at least one regulating damper 901, and two regulating dampers can also be provided in conjunction with the pipe. A damper (not shown) is used to adjust the air volume of the hot side forced exhaust pipe 90 through the adjusting damper 901. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, it can pass through the hot side forced exhaust pipe. 90 to adjust the air volume of the furnace 102 of the direct-fired incinerator (TO) 10, and transport part of the high-temperature combustion gas to the outlet 12 of the direct-fired incinerator (TO) 10, so that the hot side can be discharged The pipeline 90 has the function of adjusting the heat recovery amount or concentration, so that when the organic waste gas is processed, it can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, or even causing shutdown. happen.

The difference of the fourth implementation mode (as shown in Figure 10) is the gas transportation after incineration in step S450: the incinerated gas generated by burning the burner head 101 of the direct-fired incinerator (TO) 10 The gas is transported to one end of the first hot side pipeline 22 of the first heat exchanger 20, and is transported to the third heat exchanger from the other end of the first hot side pipeline 22 of the first heat exchanger 20. One end of the third hot side pipe 42 of the third heat exchanger 40 The other end of the third hot side pipe 42 is transported to one end of the second hot side pipe 32 of the second heat exchanger 30 , and finally from the other end of the second hot side pipe 32 of the second heat exchanger 30 Transported to the outlet 12 of the direct-fired incinerator (TO) 10.

In the above-mentioned step S450, the burner head 101 of the direct-fired incinerator (TO) 10 can first transport the incinerated high-temperature gas to one side of the first hot side pipe 22 of the first heat exchanger 20 for processing. Heat exchange, and then the incinerated high-temperature gas is transported to the third hot side pipe 42 of the third heat exchanger 40 from the other side of the first hot side pipe 22 of the first heat exchanger 20 One side is used for heat exchange, and then the other side of the third hot side pipe 42 of the third heat exchanger 40 transports the incinerated high-temperature gas to the second heat of the second heat exchanger 30 One side of the side pipe 32 is used for heat exchange, and finally the other side of the second hot side pipe 32 of the second heat exchanger 30 is transported to the outlet 12 of the furnace 102 (as shown in Figure 4, Figure 5 and 6), and then transported to the chimney 80 through the outlet 12 of the furnace 102, so as to be discharged through the chimney 80.

Step S490 hot side forced exhaust pipeline adjustment: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipeline 90, and one end of the hot-side forced exhaust pipeline 90 is connected to the direct-fired incinerator (TO) 10. The furnace 102 of the type incinerator (TO) 10 is connected, and the other end of the hot side forced exhaust pipe 90 is connected to the first hot side pipe 22 of the first heat exchanger 20 and the third heat exchanger 40 The three hot-side pipelines 42 are connected at the joints. The hot-side forced exhaust pipeline 90 is provided with at least one regulating damper 901 to adjust the direct-fired incinerator (TO) through the hot-side forced exhaust pipeline 90. )10 air volume of the furnace 102.

In the above-mentioned step S490, one end of the hot side forced exhaust pipe 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot side forced exhaust pipe 90 One end is connected to the connection between the first hot side pipe 22 of the first heat exchanger 20 and the third hot side pipe 42 of the third heat exchanger 40 (as shown in Figure 4), wherein the The hot-side forced exhaust pipeline 90 is provided with at least one regulating damper 901. The pipeline may also be provided with two regulating dampers (not shown) to control the hot-side forced exhaust pipeline through the adjusting damper 901. The air volume is 90%. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot side forced exhaust pipe 90, and the partial air volume can be adjusted. A portion of the burned high-temperature gas is transported to the connection between the first hot side pipe 22 of the first heat exchanger 20 and the third hot side pipe 42 of the third heat exchanger 40, so that the hot side forced exhaust pipe Road 90 has the function of adjusting the heat recovery amount or concentration, so that when organic waste gas is processed, it can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, or even causing shutdown. .

The difference of the fifth implementation mode (as shown in Figure 11) is the gas transportation after incineration in step S550: the incinerated gas generated by burning the burner head 101 of the direct-fired incinerator (TO) 10 The gas is transported to one end of the first hot side pipeline 22 of the first heat exchanger 20, and is transported to the third heat exchanger from the other end of the first hot side pipeline 22 of the first heat exchanger 20. One end of the third hot side pipeline 42 of the third heat exchanger 40 is then transported to the second hot side pipeline 32 of the second heat exchanger 30 from the other end of the third hot side pipeline 42 of the third heat exchanger 40 One end is finally transported to the outlet 12 of the direct-fired incinerator (TO) 10 by the other end of the second hot side pipe 32 of the second heat exchanger 30 .

In the above-mentioned step S550, the burner head 101 of the direct-fired incinerator (TO) 10 can first transport the incinerated high-temperature gas to one side of the first hot side pipe 22 of the first heat exchanger 20 for processing. heat exchange, and then transport the incinerated high-temperature gas to the third heat exchanger 40 through the other side of the first hot side pipe 22 of the first heat exchanger 20 One side of the third hot-side pipeline 42 is used for heat exchange, and then the incinerated high-temperature gas is transported to the second side through the other side of the third hot-side pipeline 42 of the third heat exchanger 40 One side of the second hot side pipe 32 of the heat exchanger 30 is used for heat exchange, and finally the other side of the second hot side pipe 32 of the second heat exchanger 30 is transported to the outlet 12 of the furnace 102 (As shown in Figures 4, 5 and 6), it is then transported to the chimney 80 through the outlet 12 of the furnace 102 for discharge through the chimney 80.

Step S590 hot side forced exhaust pipeline adjustment: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipeline 90, and one end of the hot-side forced exhaust pipeline 90 is connected to the direct-fired incinerator (TO) 10. The furnace 102 of the type incinerator (TO) 10 is connected, and the other end of the hot side forced exhaust pipe 90 is connected to the third hot side pipe 42 of the third heat exchanger 40 and the third hot side pipe 42 of the second heat exchanger 30. The two hot-side pipelines 32 are connected at the junction. The hot-side forced exhaust pipeline 90 is provided with at least one damper 901 to adjust the direct-fired incinerator (TO) through the hot-side forced exhaust pipeline 90. )10 air volume of the furnace 102.

In the above-mentioned step S590, one end of the hot side forced exhaust pipe 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot side forced exhaust pipe 90 is connected to the third The third hot side pipe 42 of the heat exchanger 40 is connected to the second hot side pipe 32 of the second heat exchanger 30 (as shown in Figure 5), wherein the hot side forced exhaust pipe The 90 series is provided with at least one damper 901, and can also be equipped with two dampers (not shown) in conjunction with the pipeline to control the air volume of the hot side forced exhaust pipeline 90 through the damper 901. Therefore, When the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot side forced exhaust pipe 90, and part of the high-temperature gas of the incineration can be transported The third hot side pipe 42 to the third heat exchanger 40 and the second heat side The connection between the second hot-side pipes 32 of the exchanger 30 allows the hot-side forced exhaust pipe 90 to adjust the heat recovery amount or concentration, so that the direct-fired incinerator ( TO)10 will not cause overheating or even shutdown due to too high furnace temperature.

The difference of the sixth implementation mode (as shown in Figure 12) is the post-incineration gas transportation in step S650: the post-incineration gas generated by burning the burner head 101 of the direct-fired incinerator (TO) 10 The gas is transported to one end of the first hot side pipeline 22 of the first heat exchanger 20, and is transported to the third heat exchanger from the other end of the first hot side pipeline 22 of the first heat exchanger 20. One end of the third hot side pipeline 42 of the third heat exchanger 40 is then transported to the second hot side pipeline 32 of the second heat exchanger 30 from the other end of the third hot side pipeline 42 of the third heat exchanger 40 One end is finally transported to the outlet 12 of the direct-fired incinerator (TO) 10 by the other end of the second hot side pipe 32 of the second heat exchanger 30 .

In the above-mentioned step S650, the burner head 101 of the direct-fired incinerator (TO) 10 can first transport the incinerated high-temperature gas to one side of the first hot side pipe 22 of the first heat exchanger 20 for heating. exchange, and then transport the incinerated high-temperature gas to one side of the third hot-side pipeline 42 of the third heat exchanger 40 from the other side of the first hot side pipeline 22 of the first heat exchanger 20 side for heat exchange, and then the incinerated high-temperature gas is transported to the second hot side of the second heat exchanger 30 through the other side of the third hot side pipe 42 of the third heat exchanger 40 One side of the pipe 32 is used for heat exchange, and finally the other side of the second hot side pipe 32 of the second heat exchanger 30 is transported to the outlet 12 of the furnace 102 (as shown in Figures 4 and 5 and shown in Figure 6), and then transported to the chimney 80 through the outlet 12 of the furnace 102, so as to be discharged through the chimney 80.

And step S690 hot side forced exhaust pipeline adjustment: the direct-fired incinerator (TO) The furnace 102 of 10 is provided with a hot side forced exhaust pipeline 90. One end of the hot side forced exhaust pipeline 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10. The hot side forced exhaust pipeline 90 The other end is connected to the outlet 12 of the direct-fired incinerator (TO) 10. The hot side forced exhaust pipe 90 is provided with at least one regulating damper 901 for adjustment through the hot side forced exhaust pipe 90. The air volume of the furnace 102 of the direct-fired incinerator (TO) 10.

In the above-mentioned step S690, one end of the hot-side forced exhaust pipe 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side forced exhaust pipe 90 is connected to the direct-fired incinerator (TO) 10. The outlet 12 of the type incinerator (TO) 10 is connected (as shown in Figure 6), in which the hot side forced exhaust pipe 90 is provided with at least one regulating damper 901, and can also be provided with two regulating dampers in conjunction with the pipe. A damper (not shown) is used to adjust the air volume of the hot side forced exhaust pipe 90 through the adjusting damper 901. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, it can pass through the hot side forced exhaust pipe. 90 to adjust the air volume of the furnace 102 of the direct-fired incinerator (TO) 10, and transport part of the high-temperature combustion gas to the outlet 12 of the direct-fired incinerator (TO) 10, so that the hot side can be discharged The pipeline 90 has the function of adjusting the heat recovery amount or concentration, so that when the organic waste gas is processed, it can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, or even causing shutdown. happen.

From the above detailed description, those who are familiar with this art can understand that the present invention can indeed achieve the aforementioned objectives, and has complied with the provisions of the patent law, and is ready to file an invention patent application.

However, the above are only preferred embodiments of the present invention, and should not be used to limit the scope of the present invention; therefore, any simple equivalent changes and modifications made based on the patent scope of the present invention and the content of the invention description , should still fall within the scope covered by the patent of this invention.

10: Direct-fired incinerator (TO)

101:Stove

102:furnace

11: Entrance

12:Export

20:First heat exchanger

21: First cold side pipeline

22:First hot side pipe

23: First cold side delivery pipeline

30: Second heat exchanger

31: Second cold side pipeline

32:Second hot side pipe

40:Third heat exchanger

41:Third cold side pipeline

42:Third hot side pipe

60: The first adsorption wheel

601: Adsorption area

602: Cooling area

603:Desorption zone

61:Exhaust gas intake pipe

62: First clean gas discharge pipe

63: First cooling air intake pipe

64: First cooling air delivery pipeline

65: The first hot gas delivery pipeline

66: First desorption concentrated gas pipeline

70: Second adsorption wheel

701: Adsorption area

702: Cooling area

703:Desorption zone

71: Second clean gas discharge pipe

72:Second cooling air intake pipe

73: Second cooling air delivery pipeline

74: Second hot gas delivery pipeline

75: Second desorption concentrated gas pipeline

80:Chimney

90: Hot side forced exhaust pipe

901: Adjust damper

Claims (30)

An energy-saving double-runner hot side pass temperature control system includes: a direct-fired incinerator (TO). The direct-fired incinerator (TO) is equipped with a burner head and a furnace. The burner head and the furnace are are connected, the direct-fired incinerator (TO) is provided with an inlet and an outlet, the inlet is located at the burner head, and the outlet is located at the furnace; a first heat exchanger, the first heat exchanger The device is located in the direct-fired incinerator (TO), and the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline; a second heat exchanger, the second heat exchanger is The device is located in the direct-fired incinerator (TO), and the second heat exchanger is provided with a second cold-side pipeline and a second hot-side pipeline; a third heat exchanger, the third heat exchanger is The device is located in the direct-fired incinerator (TO), and the third heat exchanger is provided with a third cold-side pipeline and a third hot-side pipeline; a first cold-side delivery pipeline, the first One end of the 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 inlet of the direct-fired incinerator (TO); a first Adsorption runner, the first adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, and the first adsorption runner is connected to a waste gas inlet pipeline, a first clean gas discharge pipeline, a first Cooling gas inlet pipeline, a first cooling gas delivery pipeline, a first hot gas delivery pipeline and a first desorption concentrated gas pipeline, one end of the waste gas intake pipeline is connected to the first adsorption rotor On one side of the adsorption area of the wheel, one end of the first clean gas discharge pipe is connected to the other side of the adsorption area of the first adsorption wheel, and one end of the first cooling air inlet pipe is connected to the third One side of the cooling zone of an adsorption rotor is connected, one end of the first cooling gas delivery pipe is connected to the other side of the cooling zone of the first adsorption rotor, and the other end of the first cooling gas delivery pipe related to the third One end of the third cold side pipeline of the heat exchanger is connected, one end of the first hot gas transport pipeline is connected to the other side of the desorption zone of the first adsorption rotor, and the other end of the first hot gas transport pipeline One end is connected to the other end of the third cold side pipeline of the third heat exchanger, and one end of the first desorption concentrated gas pipeline is connected to one side of the desorption zone of the first adsorption rotor. The other end of the first desorbed concentrated gas pipeline is connected to one end of the first cold side pipeline of the first heat exchanger; a second adsorption wheel, the second adsorption wheel is provided with an adsorption area, cooling zone and desorption zone, the second adsorption rotor is connected to a second clean gas discharge pipeline, a second cooling gas inlet pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and A second desorption concentrated gas pipeline, one end of the first clean gas discharge pipeline is connected to one side of the adsorption area of the second adsorption rotor, and one end of the second clean gas discharge pipeline is connected to the third The other side of the adsorption area of the two adsorption rollers is connected. One end of the second cooling air inlet pipe is connected to one side of the cooling area of the second adsorption roller. One end of the second cooling air delivery pipeline is connected to the other side of the cooling zone of the second adsorption rotor, and the other end of the second cooling gas delivery pipeline is connected to one end of the second cold side pipeline of the second heat exchanger. One end of the hot gas delivery pipeline is connected to the other side of the desorption zone of the second adsorption rotor, and the other end of the second hot gas delivery pipeline is connected to the second cold side pipeline of the second heat exchanger. The other end is connected, one end of the second desorption concentrated gas pipeline is connected to one side of the desorption area of the second adsorption rotor; a chimney, the other end of the second clean gas discharge pipeline is connected to the chimney connection; and a hot side forced exhaust pipeline, one end of the hot side forced exhaust pipeline is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot side forced exhaust pipeline is connected to the third The connection point between the third hot side pipeline of the heat exchanger and the second hot side pipeline of the second heat exchanger is connected. The hot side forced exhaust pipeline is provided with at least one damper to pass through the hot side Forced exhaust pipeline to regulate the direct-fired incinerator (TO) the air volume of the furnace, and transports part of the burned high-temperature gas to the connection between the third hot side pipe of the third heat exchanger and the second hot side pipe of the second heat exchanger, Let the hot side forced exhaust pipeline have the ability to adjust the heat recovery amount or concentration. An energy-saving double-runner hot side pass temperature control system includes: a direct-fired incinerator (TO). The direct-fired incinerator (TO) is equipped with a burner head and a furnace. The burner head and the furnace are are connected, the direct-fired incinerator (TO) is provided with an inlet and an outlet, the inlet is located at the burner head, and the outlet is located at the furnace; a first heat exchanger, the first heat exchanger The device is located in the direct-fired incinerator (TO), and the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline; a second heat exchanger, the second heat exchanger is The device is located in the direct-fired incinerator (TO), and the second heat exchanger is provided with a second cold-side pipeline and a second hot-side pipeline; a third heat exchanger, the third heat exchanger is The device is located in the direct-fired incinerator (TO), and the third heat exchanger is provided with a third cold-side pipeline and a third hot-side pipeline; a first cold-side delivery pipeline, the first One end of the 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 inlet of the direct-fired incinerator (TO); a first Adsorption runner, the first adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, and the first adsorption runner is connected to a waste gas inlet pipeline, a first clean gas discharge pipeline, a first Cooling gas inlet pipeline, a first cooling gas delivery pipeline, a first hot gas delivery pipeline and a first desorption concentrated gas pipeline, one end of the waste gas intake pipeline is connected to the first adsorption rotor On one side of the adsorption area of the wheel, one end of the first clean gas discharge pipe is connected to the other side of the adsorption area of the first adsorption wheel, and one end of the first cooling air inlet pipe is connected to the third A suction wheel One side of the cooling zone is connected, one end of the first cooling gas delivery pipeline is connected to the other side of the cooling zone of the first adsorption rotor, and the other end of the first cooling gas delivery pipeline is connected to the third cooling zone. One end of the third cold side pipeline of the three heat exchangers is connected, and one end of the first hot gas transport pipeline is connected to the other side of the desorption zone of the first adsorption rotor. The other end is connected to the other end of the third cold side pipeline of the third heat exchanger, and one end of the first desorption concentrated gas pipeline is connected to one side of the desorption zone of the first adsorption rotor, The other end of the first desorbed concentrated gas pipeline is connected to one end of the first cold side pipeline of the first heat exchanger; a second adsorption wheel, the second adsorption wheel is provided with an adsorption zone, In the cooling zone and the desorption zone, the second adsorption rotor is connected to a second clean gas discharge pipeline, a second cooling gas inlet pipeline, a second cooling gas transport pipeline, and a second hot gas transport pipeline. and a second desorption concentrated gas pipeline, one end of the first clean gas discharge pipeline is connected to one side of the adsorption area of the second adsorption rotor, and one end of the second clean gas discharge pipeline is connected to the The other side of the adsorption zone of the second adsorption rotor is connected. One end of the second cooling gas inlet pipe is connected with one side of the cooling zone of the second adsorption rotor. The second cooling gas delivery pipe One end is connected to the other side of the cooling zone of the second adsorption rotor, and the other end of the second cooling gas delivery pipeline is connected to one end of the second cold side pipeline of the second heat exchanger. One end of the two hot gas delivery pipelines is connected to the other side of the desorption zone of the second adsorption rotor, and the other end of the second hot gas delivery pipeline is connected to the second cold side pipeline of the second heat exchanger. The other end of the second desorption concentrated gas pipeline is connected to one side of the desorption area of the second adsorption rotor; a chimney, and the other end of the second clean gas discharge pipeline is connected to the Chimney connection; and a hot side forced exhaust pipe, one end of the hot side forced exhaust pipe is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot side forced exhaust pipe is connected to the third The second hot side pipe of the second heat exchanger Connected to the connection point of the first hot-side pipe of the first heat exchanger, the hot-side forced exhaust pipe is provided with at least one regulating damper to adjust the direct-fired exhaust pipe through the hot-side forced exhaust pipe. The air volume of the furnace of the incinerator (TO) is used to transport part of the burned high-temperature gas to the second hot side pipe of the second heat exchanger and the first hot side pipe of the first heat exchanger. location, so that the hot side forced exhaust pipe can adjust the heat recovery amount or concentration. An energy-saving double-runner hot side pass temperature control system includes: a direct-fired incinerator (TO). The direct-fired incinerator (TO) is equipped with a burner head and a furnace. The burner head and the furnace are are connected, the direct-fired incinerator (TO) is provided with an inlet and an outlet, the inlet is located at the burner head, and the outlet is located at the furnace; a first heat exchanger, the first heat exchanger The device is located in the direct-fired incinerator (TO), and the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline; a second heat exchanger, the second heat exchanger is The device is located in the direct-fired incinerator (TO), and the second heat exchanger is provided with a second cold-side pipeline and a second hot-side pipeline; a third heat exchanger, the third heat exchanger is The device is located in the direct-fired incinerator (TO), and the third heat exchanger is provided with a third cold-side pipeline and a third hot-side pipeline; a first cold-side delivery pipeline, the first One end of the 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 inlet of the direct-fired incinerator (TO); a first Adsorption runner, the first adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, and the first adsorption runner is connected to a waste gas inlet pipeline, a first clean gas discharge pipeline, a first Cooling gas inlet pipeline, a first cooling gas delivery pipeline, a first hot gas delivery pipeline and a first desorption concentrated gas pipeline, one end of the waste gas intake pipeline is connected to the first adsorption rotor wheel On one side of the adsorption zone, one end of the first clean gas discharge pipe is connected to the other side of the adsorption zone of the first adsorption rotor, and one end of the first cooling gas inlet pipe is connected to the first One side of the cooling zone of the adsorption rotor is connected, one end of the first cooling gas delivery pipe is connected to the other side of the cooling zone of the first adsorption rotor, and the other end of the first cooling gas delivery pipe is Connected to one end of the third cold side pipeline of the third heat exchanger, one end of the first hot gas transport pipeline is connected to the other side of the desorption zone of the first adsorption rotor, and the first hot gas transport pipeline The other end of the pipeline is connected to the other end of the third cold side pipeline of the third heat exchanger, and one end of the first desorption concentrated gas pipeline is connected to an end of the desorption zone of the first adsorption rotor. side connection, the other end of the first desorption concentrated gas pipeline is connected to one end of the first cold side pipeline of the first heat exchanger; a second adsorption runner, the second adsorption runner is provided with In the adsorption zone, the cooling zone and the desorption zone, the second adsorption rotor is connected to a second clean gas discharge pipeline, a second cooling gas inlet pipeline, a second cooling gas delivery pipeline, and a second hot gas A transport pipeline and a second desorbed concentrated gas pipeline. One end of the first clean gas discharge pipeline is connected to one side of the adsorption area of the second adsorption rotor. One end of the second clean gas discharge pipeline It is connected to the other side of the adsorption area of the second adsorption rotor. One end of the second cooling air inlet pipe is connected to one side of the cooling area of the second adsorption rotor. The second cooling air is transported One end of the pipeline is connected to the other side of the cooling zone of the second adsorption rotor, and the other end of the second cooling gas delivery pipeline is connected to one end of the second cold side pipeline of the second heat exchanger. , one end of the second hot gas delivery pipeline is connected to the other side of the desorption zone of the second adsorption rotor, and the other end of the second hot gas delivery pipeline is connected to the second cold side of the second heat exchanger. The other end of the side pipe is connected, and one end of the second desorption concentrated gas pipe is connected to one side of the desorption area of the second adsorption rotor; a chimney, the other end of the second clean gas discharge pipe connected to the chimney; and A hot side forced exhaust pipeline, one end of the hot side forced exhaust pipeline is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced exhaust pipeline is connected to the direct-fired incinerator (TO) outlet connection, the hot side forced exhaust pipe is equipped with at least one damper to adjust the air volume of the furnace of the direct-fired incinerator (TO) through the hot side forced exhaust pipe, and partially The high-temperature gas burned in part is transported to the outlet of the direct-fired incinerator (TO), so that the hot side forced exhaust pipe can adjust the heat recovery amount or concentration. An energy-saving double-runner hot side pass temperature control system includes: a direct-fired incinerator (TO). The direct-fired incinerator (TO) is equipped with a burner head and a furnace. The burner head and the furnace are are connected, the direct-fired incinerator (TO) is provided with an inlet and an outlet, the inlet is located at the burner head, and the outlet is located at the furnace; a first heat exchanger, the first heat exchanger The device is located in the direct-fired incinerator (TO), and the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline; a second heat exchanger, the second heat exchanger is The device is located in the direct-fired incinerator (TO), and the second heat exchanger is provided with a second cold-side pipeline and a second hot-side pipeline; a third heat exchanger, the third heat exchanger is The device is located in the direct-fired incinerator (TO), and the third heat exchanger is provided with a third cold-side pipeline and a third hot-side pipeline; a first cold-side delivery pipeline, the first One end of the 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 inlet of the direct-fired incinerator (TO); a first Adsorption runner, the first adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, and the first adsorption runner is connected to a waste gas inlet pipeline, a first clean gas discharge pipeline, a first A cooling air inlet pipeline, a first cooling air delivery pipeline, a first hot gas delivery pipeline and a first A desorption concentrated gas pipeline, one end of the exhaust gas inlet pipeline is connected to one side of the adsorption area of the first adsorption roller, and one end of the first clean gas discharge pipeline is connected to the first adsorption roller The other side of the adsorption zone is connected, one end of the first cooling gas inlet pipe is connected to one side of the cooling zone of the first adsorption rotor, and one end of the first cooling gas delivery pipe is connected to the third The other side of the cooling zone of an adsorption rotor is connected. The other end of the first cooling gas delivery pipeline is connected to one end of the third cold side pipeline of the third heat exchanger. The first hot gas delivery pipeline One end is connected to the other side of the desorption zone of the first adsorption rotor, and the other end of the first hot gas transport pipeline is connected to the other end of the third cold side pipeline of the third heat exchanger, One end of the first desorbed concentrated gas pipeline is connected to one side of the desorption zone of the first adsorption rotor, and the other end of the first desorbed concentrated gas pipeline is connected to the third side of the first heat exchanger. One end of a cold side pipeline is connected; a second adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, and the second adsorption runner is connected to a second clean gas discharge pipe pipeline, a second cooling gas inlet pipeline, a second cooling gas transport pipeline, a second hot gas transport pipeline and a second desorbed concentrated gas pipeline, one end of the first clean gas discharge pipeline is Connected to one side of the adsorption area of the second adsorption rotor, one end of the second clean gas discharge pipe is connected to the other side of the adsorption area of the second adsorption rotor, and the second cooling air inlet pipe One end of the pipeline is connected to one side of the cooling zone of the second adsorption rotor, and one end of the second cooling gas delivery pipe is connected to the other side of the cooling zone of the second adsorption rotor. The other end of the gas delivery pipeline is connected to one end of the second cold side pipeline of the second heat exchanger, and one end of the second hot gas delivery pipeline is connected to the other end of the desorption zone of the second adsorption rotor. side connection, the other end of the second hot gas transport pipeline is connected to the other end of the second cold side pipeline of the second heat exchanger, and one end of the second desorption concentrated gas pipeline is connected to the second adsorption One side of the desorption zone of the runner is connected; A chimney, the other end of the second clean gas discharge pipeline is connected to the chimney; and a hot side forced exhaust pipeline, one end of the hot side forced exhaust pipeline is connected to the direct-fired incinerator (TO) The furnace is connected, and the other end of the hot side forced exhaust pipe is connected to the connection between the first hot side pipe of the first heat exchanger and the third hot side pipe of the third heat exchanger. The side forced exhaust pipe is equipped with at least one damper to adjust the air volume of the furnace of the direct-fired incinerator (TO) through the hot side forced exhaust pipe and transport part of the high-temperature gas burned to the third The connection point between the first hot side pipe of a heat exchanger and the third hot side pipe of the third heat exchanger allows the hot side forced exhaust pipe to adjust the heat recovery amount or concentration. For example, in the energy-saving double-runner hot-side bypass temperature control system described in items 1, 2, 3 or 4 of the patent application, the outlet of the direct-fired incinerator (TO) is further connected to the chimney. For example, in the energy-saving double-runner hot-side bypass temperature control system described in Item 1, 2, 3 or 4 of the patent application, the first cooling air inlet pipeline is further used to supply fresh air or outside air. Enter. For example, in the energy-saving double-runner hot-side bypass temperature control system described in Item 1, 2, 3 or 4 of the patent application, the second cooling air inlet pipeline is further used to supply fresh air or outside air. Enter. For example, in the energy-saving dual-runner hot-side bypass temperature control system described in Item 1, 2, 3 or 4 of the patent application, the exhaust gas inlet pipeline is further provided with an exhaust gas connecting pipeline, and the exhaust gas connecting pipeline It is connected to the first cooling air inlet pipeline, and 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. For example, in the energy-saving dual-runner hot-side bypass temperature control system described in Item 1, 2, 3 or 4 of the patent application, the first clean gas discharge pipeline is further provided with a first clean gas connecting pipe. line, the first clean gas communication pipeline is connected to the second cooling air inlet pipeline, and the first clean gas communication pipeline is further provided with a first clean gas communication control valve to control the first clean gas The air volume of the connecting pipe. For example, in the energy-saving double-runner hot-side bypass temperature control system described in items 1, 2, 3 or 4 of the patent application, the first desorption concentrated gas pipeline is further equipped with a fan. For example, in the energy-saving double-runner hot-side bypass temperature control system described in items 1, 2, 3 or 4 of the patent application, the second desorbed concentrated gas pipeline is further equipped with a fan. For example, in the energy-saving dual-runner hot-side bypass temperature control system described in items 1, 2, 3 or 4 of the patent application, the second clean air discharge pipeline is further equipped with a fan. For example, in the energy-saving dual-runner hot-side bypass temperature control system described in items 1, 2, 3 or 4 of the patent application, the other end of the second desorbed concentrated gas pipeline is further connected to the exhaust gas inlet pipe. Roads connect. In the energy-saving dual-runner hot side bypass temperature control system described in items 1, 2, 3 or 4 of the patent application, the other end of the second desorbed concentrated gas pipeline is further connected with the first cooling gas. Connect the air intake pipe. An energy-saving dual-runner hot side pass temperature control method, mainly used in organic waste gas treatment systems, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a A third heat exchanger, a first cold-side conveying pipe, a first adsorption wheel, a second adsorption wheel and a chimney. The direct-fired incinerator (TO) is provided with a burner head and a furnace. The burner is connected to the furnace, and the direct-fired incinerator (TO) is provided with an inlet and an outlet. The inlet is located at the furnace, and the outlet is located at the furnace. The first heat exchanger The second 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 cold side pipeline and a second hot side pipeline. side pipeline, the third heat exchanger is provided with a third cold side pipeline and a third hot side pipeline, one end of the first cold side delivery pipeline is connected to the other end of the first cold side pipeline, The other end of the first cold-side conveying pipeline is connected to the inlet of the direct-fired incinerator (TO). The first adsorption rotor is provided with an adsorption zone, a cooling zone and a desorption zone. The first adsorption rotor is The gear train is connected with an exhaust gas inlet pipeline, a first clean air discharge pipeline, a first cooling air intake pipeline, a first cooling air delivery pipeline, a first hot gas delivery pipeline and a first degassing pipeline. With a concentrated gas pipeline, the second adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone. The second adsorption runner is connected to a second clean gas discharge pipe and a second cooling gas inlet pipe. pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and a second desorption concentrated gas pipeline, and the main steps of the control method include: inputting the gas to be adsorbed: passing the waste gas through the waste gas The other end of the air inlet pipe is fed into one side of the adsorption area of the first adsorption rotor; the first adsorption rotor adsorption: after adsorption through the adsorption area of the first adsorption rotor, the first adsorption rotor The other side of the adsorption zone of the wheel outputs the adsorbed gas to the adsorption zone of the second adsorption wheel through the other end of the first clean gas discharge pipe; input the first cooling gas: enter through the first cooling gas The other end of the air pipeline is used to transport cooling air to the cooling zone of the first adsorption rotor for cooling, and then the cooling air passing through the cooling zone of the first adsorption rotor is cooled through the other end of the first cooling air delivery pipe. The gas is transported to one end of the third cold side pipeline of the third heat exchanger; the first hot gas is transported for desorption: the first hot gas is transported through the first hot gas connected to the other end of the third cold side pipeline of the third heat exchanger. The pipeline transports the hot gas to the desorption zone of the first adsorption rotor for desorption, and then transports the desorbed concentrated gas through the other end of the first desorbed concentrated gas pipeline. to one end of the first cold side pipeline of the first heat exchanger; desorption concentrated gas transportation: the desorption concentrated gas then passes through the first gas connected to the other end of the first cold side pipeline of the first heat exchanger. The cold side transport pipeline is used to transport the inlet of the direct-fired incinerator (TO); the post-incineration gas transportation: the post-incineration gas generated by the burner head of the direct-fired incinerator (TO) is transported to one end of the third hot side pipe of the third heat exchanger, and from the other end of the third hot side pipe of the third heat exchanger to the second hot side pipe of the second heat exchanger One end of the second hot side pipeline of the second heat exchanger is then transported to one end of the first hot side pipeline of the first heat exchanger, and finally the first heat side pipeline of the first heat exchanger is transported to one end of the first hot side pipeline of the first heat exchanger. The other end of the hot side pipeline is transported to the outlet of the direct-fired incinerator (TO); the second adsorption wheel adsorption: transports the adsorbed gas in the first clean gas discharge pipe to the second adsorption wheel Adsorption is carried out on one side of the adsorption zone, and then the gas after the second adsorption is transported to the chimney for discharge through the second clean gas discharge pipe; the second cooling gas is input: through the other side of the second cooling gas inlet pipe One end is used to transport cooling air to the cooling zone of the second adsorption rotor for cooling, and the other end of the second cooling air delivery pipeline is used to transport the cooling air passing through the cooling zone of the second adsorption rotor to the third One end of the second cold side pipeline of the second heat exchanger; transporting the second hot gas for desorption: the hot gas is transported through the second hot gas delivery pipeline connected to the other end of the second cold side pipeline of the second heat exchanger. It is transported to the desorption zone of the second adsorption wheel for desorption, and then output through the other end of the second desorption concentrated gas pipeline; and the hot side forced exhaust pipeline adjustment: the direct-fired incinerator (TO ) is equipped with a hot-side forced exhaust pipe, and one end of the hot-side forced exhaust pipe is connected to the furnace of the direct-fired incinerator (TO). The other end of the side forced exhaust pipeline is connected to the connection between the third hot side pipeline of the third heat exchanger and the second hot side pipeline of the second heat exchanger. The hot side forced exhaust pipeline It is equipped with at least one damper to adjust the air volume of the furnace of the direct-fired incinerator (TO) through the hot-side forced exhaust pipe, and transport part of the high-temperature gas burned to the third heat exchanger The connection point between the third hot side pipeline and the second hot side pipeline of the second heat exchanger allows the hot side forced exhaust pipeline to adjust the heat recovery amount or concentration. An energy-saving dual-runner hot side pass temperature control method, mainly used in organic waste gas treatment systems, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a A third heat exchanger, a first cold-side conveying pipe, a first adsorption wheel, a second adsorption wheel and a chimney. The direct-fired incinerator (TO) is provided with a burner head and a furnace. The burner is connected to the furnace, and the direct-fired incinerator (TO) is provided with an inlet and an outlet. The inlet is located at the furnace, and the outlet is located at the furnace. The first heat exchanger The system is provided with a first cold side pipeline and a first hot side pipeline, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, and the third heat exchanger is provided with a third There are three cold-side pipelines and a third 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 inlet of the direct-fired incinerator (TO) is connected. The first adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone. The first adsorption runner is connected to a waste gas inlet pipe and a first A clean gas discharge pipeline, a first cooling gas inlet pipeline, a first cooling gas transport pipeline, a first hot gas transport pipeline and a first desorption concentrated gas pipeline, the second adsorption runner system It is provided with an adsorption area, a cooling area and a desorption area. The second adsorption rotor system is connected to a second clean air discharge pipeline, a second cooling air inlet pipeline, a second cooling air delivery pipeline, and a first two hot gas delivery pipelines and a second desorption concentrated gas pipeline, and the main steps of the control method The system includes: inputting the gas to be adsorbed: sending the waste gas into one side of the adsorption area of the first adsorption rotor through the other end of the waste gas inlet pipe; adsorption by the first adsorption rotor: through the first adsorption rotor After the adsorption zone of the wheel is adsorbed, the adsorbed gas is output from the other side of the adsorption zone of the first adsorption wheel to the adsorption zone of the second adsorption wheel through the other end of the first clean gas discharge pipe. ; Input the first cooling gas: transport the cooling gas through the other end of the first cooling gas inlet pipe to the cooling zone of the first adsorption wheel for cooling, and then through the other end of the first cooling gas delivery pipe To transport the cooling air passing through the cooling zone of the first adsorption wheel to one end of the third cold side pipeline of the third heat exchanger; transport the first hot gas for desorption: through the third heat exchanger The first hot gas transport pipeline connected to the other end of the cold side pipeline transports the hot gas to the desorption zone of the first adsorption rotor for desorption, and then passes through the other end of the first desorption concentrated gas pipeline. The desorbed concentrated gas is transported to one end of the first cold side pipeline of the first heat exchanger; the desorbed concentrated gas is transported: the desorbed concentrated gas then passes through the other end of the first cold side pipeline of the first heat exchanger. The first cold-side transport pipeline connected at one end is transported to the inlet of the direct-fired incinerator (TO); the gas transportation after incineration: produced by burning the burner head of the direct-fired incinerator (TO) The incinerated gas is transported to one end of the third hot side pipeline of the third heat exchanger, and is transported to the second heat exchanger from the other end of the third hot side pipeline of the third heat exchanger. One end of the second hot side pipe is then transported from the other end of the second hot side pipe of the second heat exchanger to one end of the first hot side pipe of the first heat exchanger, and finally from the first The first hot side of the heat exchanger The other end of the pipeline is transported to the outlet of the direct-fired incinerator (TO); the second adsorption wheel adsorption: transports the adsorbed gas in the first clean gas discharge pipe to the adsorption area of the second adsorption wheel Adsorption is performed on one side of the air, and then the gas after the second adsorption is transported to the chimney for discharge through the second clean gas discharge pipe; the second cooling gas is input: through the other end of the second cooling gas inlet pipe Transport the cooling air to the cooling zone of the second adsorption wheel for cooling, and then deliver the cooling air passing through the cooling zone of the second adsorption wheel to the second heat through the other end of the second cooling air delivery pipeline. One end of the second cold side pipeline of the exchanger; transporting the second hot gas for desorption: transporting the hot gas to The desorption zone of the second adsorption wheel performs desorption, and then outputs it through the other end of the second desorption concentrated gas pipeline; and the hot side forced exhaust pipeline adjustment: the direct-fired incinerator (TO) The furnace is equipped with a hot-side forced exhaust pipeline. One end of the hot-side forced exhaust pipeline is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced exhaust pipeline is connected to the second The second hot side pipe of the heat exchanger is connected to the first hot side pipe of the first heat exchanger. The hot side forced exhaust pipe is provided with at least one damper to pass through the hot side. The forced exhaust pipeline is used to adjust the air volume of the furnace of the direct-fired incinerator (TO), and transport part of the high-temperature gas of combustion to the second hot side pipeline of the second heat exchanger to exchange with the first heat exchanger. The connection point between the first hot side pipeline of the device allows the hot side forced exhaust pipeline to adjust the heat recovery amount or concentration. An energy-saving dual-runner hot side pass temperature control method, mainly used in organic waste gas treatment systems, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a A third heat exchanger, a first cold side delivery pipe, a first adsorption rotor, a second An adsorption runner and a chimney. The direct-fired incinerator (TO) is provided with a burner head and a furnace. The burner head is connected with the furnace. The direct-fired incinerator (TO) is provided with an inlet and an outlet. The inlet is located at the furnace head, the outlet is located at the furnace, 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 There is 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. One end of the first cold side delivery pipeline is connected to The other end of the first cold-side pipeline is connected, the other end of the first cold-side delivery pipeline is connected with the inlet of the direct-fired incinerator (TO), the first adsorption rotor is provided with an adsorption area, In the cooling zone and the desorption zone, the first adsorption rotor is connected to a waste gas inlet pipeline, a first clean gas discharge pipeline, a first cooling air inlet pipeline, a first cooling gas delivery pipeline, A first hot gas delivery pipeline and a first desorption concentrated gas pipeline. The second adsorption rotor is provided with an adsorption zone, a cooling zone and a desorption zone. The second adsorption rotor is connected to a second clean gas A discharge pipeline, a second cooling gas inlet pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and a second desorption concentrated gas pipeline, and the main steps of the control method include : Input the gas to be adsorbed: send the waste gas into one side of the adsorption area of the first adsorption wheel through the other end of the waste gas inlet pipe; adsorption by the first adsorption wheel: through the first adsorption wheel After adsorption in the adsorption zone, the adsorbed gas is output from the other side of the adsorption zone of the first adsorption wheel through the other end of the first clean gas discharge pipe to the adsorption zone of the second adsorption wheel; input First cooling gas: The cooling gas is transported to the cooling zone of the first adsorption wheel through the other end of the first cooling gas inlet pipe for cooling, and then the cooling gas is transported through the other end of the first cooling gas transportation pipe. The cooling air passing through the cooling zone of the first adsorption wheel is transported to the third heat exchanger One end of the third cold side pipeline of the exchanger; transporting the first hot gas for desorption: transporting the hot gas to The desorption zone of the first adsorption wheel performs desorption, and then the desorption concentrated gas is transported to one end of the first cold side pipeline of the first heat exchanger through the other end of the first desorption concentrated gas pipeline. ; Desorption concentrated gas transportation: The desorption concentrated gas is then transported to the direct-fired incinerator ( The inlet of TO); the gas transportation after incineration: the incineration gas generated by the combustion of the burner head of the direct-fired incinerator (TO) is transported to the third hot side pipe of the third heat exchanger One end is transported from the other end of the third hot side pipe of the third heat exchanger to one end of the second hot side pipe of the second heat exchanger, and then the second heat pipe of the second heat exchanger is The other end of the side pipeline is transported to one end of the first hot side pipeline of the first heat exchanger, and finally the other end of the first hot side pipeline of the first heat exchanger is transported to the direct-fired incinerator. (TO) outlet; second adsorption wheel adsorption: transport the adsorbed gas in the first clean gas discharge pipe to one side of the adsorption area of the second adsorption wheel for adsorption, and then adsorb the gas after the second adsorption The gas is transported to the chimney for discharge through the second clean gas discharge pipe; the second cooling gas is input: the cooling gas is transported to the cooling area of the second adsorption rotor through the other end of the second cooling gas inlet pipe. Cooling is carried out, and then the cooling air passing through the cooling zone of the second adsorption rotor is transported to one end of the second cold side pipeline of the second heat exchanger through the other end of the second cooling gas transport pipeline; transporting Second hot gas desorption: through the other end of the second cold side pipe connected to the second heat exchanger The second hot gas delivery pipeline is connected to transport the hot gas to the desorption zone of the second adsorption rotor for desorption, and then output through the other end of the second desorption concentrated gas pipeline; and a hot side forced exhaust pipe Road adjustment: The furnace of the direct-fired incinerator (TO) is equipped with a hot-side forced exhaust pipe. One end of the hot-side forced exhaust pipe is connected to the furnace of the direct-fired incinerator (TO). The other end of the side forced exhaust pipe is connected to the outlet of the direct-fired incinerator (TO). The hot side forced exhaust pipe is equipped with at least one regulating damper to adjust through the hot side forced exhaust pipe. The air volume of the furnace of the direct-fired incinerator (TO) is transferred to the outlet of the direct-fired incinerator (TO), so that the hot-side forced exhaust pipe can adjust the heat recovery amount. or concentration. An energy-saving dual-runner hot side pass temperature control method, mainly used in organic waste gas treatment systems, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a A third heat exchanger, a first cold-side conveying pipe, a first adsorption wheel, a second adsorption wheel and a chimney. The direct-fired incinerator (TO) is provided with a burner head and a furnace. The burner is connected to the furnace, and the direct-fired incinerator (TO) is provided with an inlet and an outlet. The inlet is located at the furnace, and the outlet is located at the furnace. The first heat exchanger The system is provided with a first cold side pipeline and a first hot side pipeline, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, and the third heat exchanger is provided with a third There are three cold-side pipelines and a third 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 other end of the first cold-side delivery pipeline. The inlet of the direct-fired incinerator (TO) is connected. The first adsorption runner is equipped with an adsorption zone, a cooling zone and a desorption zone. The first adsorption runner is connected to a waste gas inlet pipeline and a first purifier. gas discharge pipeline, a first cooling gas inlet pipeline, a first cooling gas transport pipeline, a first hot gas transport pipeline and a first desorption concentrated gas pipeline, the second adsorption rotor is equipped with There is an adsorption zone, a cooling zone and a desorption zone, and the second adsorption rotor system is connected to a second clean gas discharge pipeline, a second cooling gas inlet pipeline, a second cooling gas delivery pipeline, a second hot gas transport pipeline and a second desorption concentrated gas pipeline, and the main steps of the control method are Including: inputting the gas to be adsorbed: sending the waste gas into one side of the adsorption area of the first adsorption wheel through the other end of the waste gas inlet pipe; adsorption by the first adsorption wheel: passing through the first adsorption wheel After adsorption in the adsorption zone, the adsorbed gas is output from the other side of the adsorption zone of the first adsorption wheel to the adsorption zone of the second adsorption wheel through the other end of the first clean gas discharge pipe; Input the first cooling gas: transport the cooling gas through the other end of the first cooling gas inlet pipe to the cooling zone of the first adsorption rotor for cooling, and then through the other end of the first cooling gas delivery pipe. The cooling air passing through the cooling zone of the first adsorption wheel is transported to one end of the third cold side pipe of the third heat exchanger; the first hot gas is transported for desorption: through the third cold side of the third heat exchanger The first hot gas delivery pipeline connected to the other end of the side pipeline transports the hot gas to the desorption zone of the first adsorption rotor for desorption, and then passes through the other end of the first desorption concentrated gas pipeline to The desorbed concentrated gas is transported to one end of the first cold side pipeline of the first heat exchanger; the desorbed concentrated gas is transported: the desorbed concentrated gas then passes through the other end of the first cold side pipeline of the first heat exchanger The connected first cold-side transport pipeline is transported to the inlet of the direct-fired incinerator (TO); gas transportation after incineration: generated by burning the burner head of the direct-fired incinerator (TO) The burned gas is transported to one end of the first hot side pipeline of the first heat exchanger, and is transported to the third heat side pipeline of the third heat exchanger from the other end of the first hot side pipeline of the first heat exchanger. Three hot sides One end of the pipeline is then transported from the other end of the third hot side pipeline of the third heat exchanger to one end of the second hot side pipeline of the second heat exchanger, and finally from the second heat side pipeline of the second heat exchanger. The other end of the second hot side pipeline is transported to the outlet of the direct-fired incinerator (TO); the second adsorption rotor adsorbs: transports the adsorbed gas in the first clean gas discharge pipe to the second adsorption rotor Adsorption is carried out on one side of the adsorption area of the wheel, and then the gas after the second adsorption is transported to the chimney for discharge through the second clean gas discharge pipe; the second cooling gas is input: through the second cooling gas inlet pipe The other end of the second cooling air delivery pipe is used to transport cooling air to the cooling zone of the second adsorption rotor for cooling, and then the cooling air passing through the cooling zone of the second adsorption rotor is delivered to the other end of the second cooling air delivery pipeline. One end of the second cold side pipeline of the second heat exchanger; transports the second hot gas for desorption: through the second hot gas delivery pipeline connected to the other end of the second cold side pipeline of the second heat exchanger. The hot gas is transported to the desorption zone of the second adsorption wheel for desorption, and then output through the other end of the second desorption concentrated gas pipeline; and the hot side forced exhaust pipeline adjustment: the direct-fired incinerator The furnace of (TO) is equipped with a hot-side forced exhaust pipe. One end of the hot-side forced exhaust pipe is connected to the furnace of the direct-fired incinerator (TO). The other end of the hot-side forced exhaust pipe is connected to the furnace of the direct-fired incinerator (TO). Connected to the connection point between the first hot side pipe of the first heat exchanger and the third hot side pipe of the third heat exchanger, the hot side forced exhaust pipe is provided with at least one damper to The air volume of the furnace of the direct-fired incinerator (TO) is adjusted through the hot-side forced exhaust pipe, and part of the high-temperature gas burned is transported to the first hot-side pipe of the first heat exchanger and the first heat-side pipe. The connection between the third hot side pipes of the third heat exchanger allows the hot side forced exhaust pipe to adjust the heat recovery amount or concentration. An energy-saving dual-runner hot side pass temperature control method, mainly used for organic waste gas treatment management system, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a third heat exchanger, a first cold side conveying pipeline, a first adsorption transfer wheel, a second adsorption runner and a chimney. The direct-fired incinerator (TO) is provided with a burner head and a furnace. The burner head is connected with the furnace. The direct-fired incinerator (TO) is equipped with There is an inlet and an outlet. The inlet is located at the burner head. The outlet is located at the furnace. The first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline. The second heat exchanger is provided with a first cold side pipeline and a first hot side pipeline. 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 a 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 the inlet of the direct-fired incinerator (TO), and the first adsorption wheel is equipped with There is an adsorption area, a cooling area and a desorption area. The first adsorption rotor system is connected with a waste gas inlet pipeline, a first clean gas discharge pipeline, a first cooling air inlet pipeline, and a first cooling air A conveying pipeline, a first hot gas conveying pipeline and a first desorbed concentrated gas pipeline. The second adsorption rotor is provided with an adsorption zone, a cooling zone and a desorption zone. The second adsorption rotor is connected to a a second clean gas discharge pipeline, a second cooling gas inlet pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and a second desorption concentrated gas pipeline, and the control method The main steps include: inputting the gas to be adsorbed: sending the waste gas into one side of the adsorption area of the first adsorption wheel through the other end of the waste gas inlet pipe; adsorption by the first adsorption wheel: passing through the first After the adsorption zone of the adsorption wheel is adsorbed, the adsorbed gas is output from the other side of the adsorption zone of the first adsorption wheel to the second adsorption wheel through the other end of the first clean gas discharge pipe. Adsorption zone; input the first cooling gas: deliver the cooling gas through the other end of the first cooling gas inlet pipe to the cooling zone of the first adsorption rotor for cooling, and then transport the cooling air passing through the cooling zone of the first adsorption rotor to the third heat exchanger through the other end of the first cooling air delivery pipeline One end of the third cold-side pipeline; transporting the first hot gas for desorption: transporting the hot gas to the first hot gas through the first hot gas transport pipeline connected to the other end of the third cold-side pipeline of the third heat exchanger Desorption is carried out in the desorption zone of the adsorption rotor, and then the desorption concentrated gas is transported to one end of the first cold side pipeline of the first heat exchanger through the other end of the first desorption concentrated gas pipeline; desorption Concentrated gas transportation: The desorbed concentrated gas is then transported to the direct-fired incinerator (TO) through the first cold-side transportation pipeline connected to the other end of the first cold-side pipeline of the first heat exchanger. Inlet; gas transportation after incineration: the incinerated gas produced by the burner of the direct-fired incinerator (TO) is transported to one end of the first hot side pipe of the first heat exchanger, and It is transported from the other end of the first hot side pipeline of the first heat exchanger to one end of the third hot side pipeline of the third heat exchanger, and then from the third hot side pipeline of the third heat exchanger. The other end of the second hot side pipeline of the second heat exchanger is transported to one end of the second hot side pipeline of the second heat exchanger, and finally the other end of the second hot side pipeline of the second heat exchanger is transported to the direct-fired incinerator (TO) outlet; second adsorption wheel adsorption: transport the adsorbed gas in the first clean gas discharge pipe to one side of the adsorption area of the second adsorption wheel for adsorption, and then pass the second adsorbed gas through The second clean gas discharge pipeline is transported to the chimney for discharge; the second cooling gas is input: the cooling gas is transported through the other end of the second cooling gas inlet pipeline to the cooling zone of the second adsorption transfer for cooling. The cooling air passing through the cooling zone of the second adsorption rotor is then delivered to the second heat exchanger through the other end of the second cooling air delivery pipeline. One end of the second cold side pipeline of the second heat exchanger; transporting the second hot gas for desorption: transporting the hot gas to The desorption zone of the second adsorption wheel performs desorption, and then outputs it through the other end of the second desorption concentrated gas pipeline; and the hot side forced exhaust pipeline adjustment: the direct-fired incinerator (TO) The furnace is equipped with a hot-side forced exhaust pipeline. One end of the hot-side forced exhaust pipeline is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced exhaust pipeline is connected to the third The connection point between the third hot side pipeline of the heat exchanger and the second hot side pipeline of the second heat exchanger is connected. The hot side forced exhaust pipeline is provided with at least one damper to pass through the hot side The forced exhaust pipe is used to adjust the air volume of the furnace of the direct-fired incinerator (TO), and transport part of the high-temperature gas of combustion to the third hot side pipe of the third heat exchanger to exchange with the second heat The connection point between the second hot side pipe of the device allows the hot side forced exhaust pipe to adjust the heat recovery amount or concentration. An energy-saving dual-runner hot side pass temperature control method, mainly used in organic waste gas treatment systems, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a A third heat exchanger, a first cold-side conveying pipe, a first adsorption wheel, a second adsorption wheel and a chimney. The direct-fired incinerator (TO) is provided with a burner head and a furnace. The burner is connected to the furnace, and the direct-fired incinerator (TO) is provided with an inlet and an outlet. The inlet is located at the furnace, and the outlet is located at the furnace. The first heat exchanger The system is provided with a first cold side pipeline and a first hot side pipeline, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, and the third heat exchanger is provided with a third There are three cold-side pipelines and a third 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 other end of the first cold-side delivery pipeline. The inlet connection of the direct-fired incinerator (TO), the first adsorption runner system It is provided with an adsorption area, a cooling area and a desorption area. The first adsorption rotor system is connected to a waste gas inlet pipeline, a first clean gas discharge pipeline, a first cooling gas inlet pipeline, and a first cooling gas transportation pipeline, a first hot gas transportation pipeline and a first desorption concentrated gas pipeline. The second adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone. The second adsorption runner is connected to There is a second clean gas discharge pipeline, a second cooling gas inlet pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and a second desorption concentrated gas pipeline, and the control method The main steps include: inputting the gas to be adsorbed: sending the waste gas into one side of the adsorption area of the first adsorption wheel through the other end of the waste gas inlet pipe; adsorption by the first adsorption wheel: passing through the third After the adsorption zone of an adsorption wheel is adsorbed, the adsorbed gas is output from the other side of the adsorption zone of the first adsorption wheel to the second adsorption wheel through the other end of the first clean gas discharge pipe. The adsorption zone; input the first cooling gas: transport the cooling gas through the other end of the first cooling gas inlet pipe to the cooling zone of the first adsorption wheel for cooling, and then pass the first cooling gas delivery pipe The other end is used to transport the cooling air passing through the cooling zone of the first adsorption wheel to one end of the third cold side pipeline of the third heat exchanger; transporting the first hot gas for desorption: through and the third heat exchanger The first hot gas transport pipeline connected to the other end of the third cold side pipeline transports the hot gas to the desorption zone of the first adsorption rotor for desorption, and then passes through the first desorption concentrated gas pipeline. The other end is used to transport the desorbed concentrated gas to one end of the first cold side pipe of the first heat exchanger; the desorbed concentrated gas is transported: the desorbed concentrated gas then passes through the first cold side pipe of the first heat exchanger. The first cold side delivery pipeline connected to the other end of the road is delivered to the direct-fired incinerator (TO) Inlet; gas transportation after incineration: the incineration gas generated by the combustion of the burner head of the direct-fired incinerator (TO) is transported to one end of the first hot side pipe of the first heat exchanger, The other end of the first hot side pipe of the first heat exchanger is transported to one end of the third hot side pipe of the third heat exchanger, and then from the third hot side pipe of the third heat exchanger. The other end of the pipeline is transported to one end of the second hot side pipeline of the second heat exchanger, and finally the other end of the second hot side pipeline of the second heat exchanger is transported to the direct-fired incinerator (TO ); second adsorption wheel adsorption: transport the adsorbed gas in the first clean gas discharge pipe to one side of the adsorption area of the second adsorption wheel for adsorption, and then transport the second adsorbed gas It is transported to the chimney for discharge through the second clean air discharge pipeline; the second cooling gas is input: the cooling gas is transported through the other end of the second cooling air inlet pipeline to the cooling zone of the second adsorption rotor for cooling. , and then transport the cooling air passing through the cooling zone of the second adsorption wheel to one end of the second cold side pipeline of the second heat exchanger through the other end of the second cooling air transport pipeline; transport the second Hot gas desorption: The hot gas is transported to the desorption area of the second adsorption rotor for desorption through the second hot gas transport pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, and then Output through the other end of the second desorbed concentrated gas pipeline; and hot side forced exhaust pipeline adjustment: the furnace of the direct-fired incinerator (TO) is equipped with a hot side forced exhaust pipeline, which One end of the exhaust pipe is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced exhaust pipe is connected to the outlet of the direct-fired incinerator (TO). The hot-side forced exhaust The pipeline system is equipped with at least one damper to adjust the air volume of the furnace of the direct-fired incinerator (TO) through the hot-side forced exhaust pipeline, and transport part of the high-temperature gas burned to the direct-fired incinerator (TO). At the outlet of the incinerator (TO), the hot side forced exhaust pipe has the ability to adjust the heat recovery amount or concentration. For example, in the energy-saving dual-runner hot side pass temperature control method described in Item 15, 16, 17, 18, 19 or 20 of the patent application, the outlet of the direct-fired incinerator (TO) is further connected to the chimney. For example, in the energy-saving dual-runner hot side pass temperature control method described in Item 15, 16, 17, 18, 19 or 20 of the patent application, the first cooling air inlet pipeline is further used to supply fresh air or It's the outside air that comes in. For example, in the energy-saving dual-runner hot side pass temperature control method described in Item 15, 16, 17, 18, 19 or 20 of the patent application, the second cooling air inlet pipeline is further used to supply fresh air or It's the outside air that comes in. For example, in the energy-saving dual-runner hot side pass temperature control method described in Item 15, 16, 17, 18, 19 or 20 of the patent application, the exhaust gas inlet pipeline is further provided with an exhaust gas connecting pipeline, The exhaust gas communication pipeline is connected to the first cooling air inlet 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. For example, in the energy-saving dual-runner hot side pass temperature control method described in Item 15, 16, 17, 18, 19 or 20 of the patent application, the first clean gas discharge pipeline is further provided with a first clean gas The first clean air connection pipe is connected to the second cooling air inlet pipe, and the first clean air connection pipe is further provided with a first clean air connection control valve to control the first The air volume of the clean air connecting pipe. For example, in the energy-saving dual-runner hot side pass temperature control method described in Item 15, 16, 17, 18, 19 or 20 of the patent application, the first desorption concentrated gas pipeline is A fan is further provided. For example, in the energy-saving dual-runner hot side pass temperature control method described in Item 15, 16, 17, 18, 19 or 20 of the patent application, the second desorbed concentrated gas pipeline is further equipped with a fan. For example, in the energy-saving dual-runner hot side pass temperature control method described in Item 15, 16, 17, 18, 19 or 20 of the patent application, the second clean air discharge pipeline is further equipped with a fan. The energy-saving double-runner hot side pass temperature control method described in item 15, 16, 17, 18, 19 or 20 of the patent application, wherein the second desorption concentration in the step of delivering the second hot gas for desorption The other end of the gas pipeline is further connected to the exhaust gas inlet pipeline. The energy-saving double-runner hot side pass temperature control method described in item 15, 16, 17, 18, 19 or 20 of the patent application, wherein the second desorption concentration in the step of delivering the second hot gas for desorption The other end of the gas pipeline is further connected to the first cooling gas inlet pipeline.

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