TWM608581U - Energy-saving dual-wheel high-concentration heat-bypass temperature control system - Google Patents

Abstract

This creation is an energy-saving dual-wheel high-concentration heat bypass temperature control system, mainly used in organic waste gas treatment systems, and through the direct-fired incinerator (TO) with a heat bypass channel, when When the concentration of volatile organic compounds (VOCs) becomes higher, the heat bypass channel can be used to adjust the air volume in the furnace of the direct-fired incinerator (TO) to have the effect of adjusting the heat recovery volume or concentration, so that the organic waste gas can be During processing, it can prevent the direct-fired incinerator (TO) from overheating due to the high temperature of the furnace, and even causing shutdown.

Description

Energy-saving dual-wheel high-concentration heat bypass temperature control system

This creation is about an energy-saving dual-wheel high-concentration heat-by-pass temperature control system, especially when the concentration of volatile organic compounds (VOCs) becomes high, it can adjust the heat recovery or concentration, so that organic waste gas During processing, it can prevent the direct-fired incinerator (TO) from overheating due to the high temperature of the furnace, and even causing shutdowns. It is suitable for organic waste gas in the semiconductor industry, optoelectronic industry or chemical-related industries. Processing system or similar equipment.

At present, volatile organic gas (VOC) is generated in the manufacturing process of the semiconductor industry or the optoelectronic industry. Therefore, processing equipment for processing volatile organic gas (VOC) will be installed in each plant area to avoid volatile organic gas (VOC). ) Directly discharged into the air to cause air pollution.

However, in recent years, both the central government and local governments have attached great importance to air pollution. Therefore, relevant air quality standards have been set on the emission standards of chimneys. At the same time, they will be reviewed in accordance with the development of international control trends.

Therefore, in view of the above-mentioned deficiencies, the author expects to propose an energy-saving dual-wheel high-concentration heat bypass temperature control system that can improve the efficiency of organic waste gas treatment, so that users can easily operate and assemble. System to provide user convenience and the creative motivation for the creator’s research and development.

The main purpose of this creation is to provide an energy-saving dual-wheel high-concentration heat-bypass temperature control system, which is mainly used in organic waste gas treatment systems, and through the direct-fired incinerator (TO) with a thermal bypass channel By this, when the concentration of volatile organic compounds (VOCs) becomes higher, the heat bypass channel can be used to adjust the air volume of the direct-fired incinerator (TO) to have the effect of adjusting the heat recovery amount or concentration , Which can prevent the direct-fired incinerator (TO) from overheating due to the high temperature of the furnace during the treatment of organic waste gas, and even cause shutdowns, thereby increasing the overall practicability.

Another purpose of this creation is to provide an energy-saving dual-wheel high-concentration heat-bypass temperature control system, which is provided with a first heat exchanger and a second heat exchanger in the direct-fired incinerator (TO). , The design of the third heat exchanger and the fourth heat exchanger, and the bottom or side of the first heat exchanger, the bottom or the side of the second heat exchanger, and the bottom of the third heat exchanger Or there is a thermal bypass channel on the side and below or on the side of the fourth heat exchanger, and when the concentration of volatile organic compounds (VOCs) becomes high, the direct-fired type can be adjusted through the thermal bypass channel The air volume in the furnace of the incinerator (TO) allows the heat bypass channel to have the effect of adjusting the heat recovery or concentration, so that the organic waste gas can be processed to prevent the direct-fired incinerator (TO) from being too high due to the furnace temperature. The occurrence of overheating may even lead to shutdowns, thereby increasing the overall usability.

One purpose of this creation is to provide an energy-saving dual-wheel high-concentration heat-bypass temperature control system, in which the direct-fired incinerator (TO) is correspondingly provided with a first heat exchanger and a second heat exchanger And the design of the third heat exchanger, and the bottom or side of the first heat exchanger, the bottom or side of the second heat exchanger, and the bottom or side of the third heat exchanger are provided with Thermal bypass channel, and when the concentration of volatile organic compounds (VOCs) becomes high, it can pass through the thermal bypass Through passage to adjust the air volume of the furnace of the direct-fired incinerator (TO), so that the heat bypass passage has the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can prevent the direct-fired incinerator (TO) from being processed. ) The furnace temperature will not be too high to cause overheating, and even cause downtime, thereby increasing the overall convenience.

In order to further understand the features, characteristics and technical content of this creation, please refer to the following detailed description and drawings of this creation. However, the attached drawings are only for reference and explanation, and are not intended to limit this creation.

10: Direct-fired incinerator (TO)

101: stove top

102: Furnace

11: entrance

12: Exit

20: The first heat exchanger

21: The first cold side pipeline

22: The first hot side pipeline

23: The first cold side conveying pipeline

30: second heat exchanger

31: The second cold side pipeline

32: The second hot side pipeline

40: The third heat exchanger

41: The third cold side pipeline

42: The third hot side pipeline

50: The fourth heat exchanger

51: Fourth cold side pipeline

52: The fourth hot side pipeline

53: The fourth cold side conveying pipeline

60: The first adsorption wheel

601: Adsorption Zone

602: Cooling Zone

603: Desorption Zone

61: Exhaust gas intake pipe

611: Exhaust gas connection pipeline

6111: Exhaust gas connection control valve

62: The first clean gas discharge pipeline

621: The first clean air connecting pipeline

6211: The first clean air connection control valve

63: The first cooling air intake pipe

64: The first cooling gas delivery pipeline

65: The first hot gas delivery pipeline

66: The first desorption concentrated gas pipeline

661: Fan

70: The second adsorption wheel

701: Adsorption Zone

702: Cooling Zone

703: Desorption Zone

71: The second clean gas discharge pipeline

711: Fan

72: The second cooling air intake line

73: The second cooling gas delivery pipeline

74: The second hot gas delivery pipeline

75: The second desorption concentrated gas pipeline

751: Fan

80: Chimney

90: Hot Bypass Channel

Figure 1 is a schematic diagram of the system architecture with a thermal bypass channel in the first design of this creation.

Figure 2 is a schematic diagram of the system architecture with a thermal bypass channel in the first design of this creation.

Figure 3 is a schematic diagram of the system architecture with a thermal bypass channel in the first design of this creation.

Figure 4 is a schematic diagram of the system architecture with a thermal bypass channel in the first design of this creation.

Figure 5 is a schematic diagram of the system architecture with a thermal bypass channel in the second design of this creation.

Figure 6 is a schematic diagram of the system architecture with a thermal bypass channel in the second design of this creation.

Figure 7 is a schematic diagram of the system architecture with a thermal bypass channel in the second design of this creation.

Figure 8 is a schematic diagram of the system architecture with a thermal bypass channel in the second design of this creation.

Please refer to Figures 1 to 8, which are schematic diagrams of this creative embodiment. The best implementation of the energy-saving dual-wheel high-concentration heat bypass temperature control system in this creation is applied to the volatile organic waste gas treatment system or similar equipment in the semiconductor industry, optoelectronic industry or chemical-related industries, mainly volatile organic compounds (VOCs) When the concentration becomes higher, it can adjust the amount of heat recovery or The efficiency of the concentration can prevent the direct-fired incinerator (TO) from overheating due to the high temperature of the direct-fired incinerator (TO) during the treatment of the organic waste gas, and even causing the shutdown.

The energy-saving dual-wheel high-concentration heat-bypass temperature control system of the implementation framework of this creation mainly has two designs. The first design is that the direct-fired incinerator (TO) 10 is equipped with a The contents of the first heat exchanger 20, a second heat exchanger 30, a third heat exchanger 40, and a fourth heat exchanger 50 (as shown in Figures 1 to 4), and the following is for the first Kind of design to illustrate.

The first design system includes a straight-fired incinerator (TO) 10, a first heat exchanger 20, a second heat exchanger 30, a third heat exchanger 40, and a fourth heat exchanger 50. , A first cold-side delivery pipeline 23, a fourth cold-side delivery pipeline 53, a first adsorption runner 60, a second adsorption runner 70 and a chimney 80 combined design (as shown in Figures 1 to 4), 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 a second cold side pipeline 31 And the second hot side pipe 32, the third heat exchanger 40 is provided with a third cold side pipe 41 and a third hot side pipe 42, and the fourth heat exchanger 50 is provided with a fourth cold side pipe Road 51 and the fourth hot side pipeline 52. In addition, the direct-fired incinerator (TO) 10 is provided with a furnace head 101 and a furnace 102, the furnace head 101 is in communication with the furnace 102, and the first heat exchanger 20, the second heat exchanger 30, The third heat exchanger 40 and the fourth heat exchanger 50 are respectively arranged in the direct-fired incinerator (TO) 10, and the direct-fired incinerator (TO) 10 is provided with an inlet 11 and an outlet 12 (such as 1 to 4), and the inlet 11 is provided at the furnace head 101, and the inlet 11 is connected to the other end of the fourth cold side pipeline 51 of the fourth heat exchanger 50, Furthermore, the outlet 12 is provided at the furnace 102, and the outlet 12 is connected to the chimney 80, Thereby, the organic waste gas can enter the furnace head 101 through the inlet 11 for combustion, and the combusted gas can pass through the furnace 102 and be discharged from the outlet 12 to the chimney 80 for discharge. It has the effect of saving energy.

The burner head 101 of the above-mentioned direct-fired incinerator (TO) 10 can firstly deliver the burned high-temperature gas to one side of the fourth hot-side pipe 52 of the fourth heat exchanger 50 for heat exchange. And from the other side of the fourth hot-side pipeline 52 of the fourth heat exchanger 50, the incineration high-temperature gas is transported to one side of the third hot-side pipeline 42 of the third heat exchanger 40. Perform heat exchange, and then the incineration high-temperature gas is transported to the second hot-side pipe 32 of the second heat exchanger 30 from the other side of the third hot-side pipe 42 of the third heat exchanger 40 Heat exchange on one side of the second heat exchanger 30, and then the other side of the second hot side pipe 32 of the second heat exchanger 30 transports the burned high-temperature gas to the first heat exchanger 20 One side of the hot 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 Figures 1 to 4), the outlet 12 of the furnace 102 is transported to the chimney 80 for discharge through the chimney 80.

In addition, the first adsorption runner 60 of this creation is provided with an adsorption zone 601, a cooling zone 602 and a desorption zone 603. The first adsorption runner 60 is connected with an exhaust gas inlet pipe 61 and a first clean gas discharge pipe. Path 62, a first cooling gas inlet pipe 63, a first cooling gas delivery pipe 64, a first hot gas delivery pipe 65 and a first desorption concentrated gas pipe 66, (as shown in Figure 1 to As shown in Figure 4) and the second adsorption runner 70 is provided with an adsorption zone 701, a cooling zone 702 and a desorption zone 703, and the second adsorption runner 70 is connected with a second clean gas discharge pipeline 71, a The second cooling gas intake pipe 72, a second cooling gas delivery pipe 73. A second hot gas delivery pipeline 74 and a second desorption concentrated gas pipeline 75. The first adsorption runner 60 and the second adsorption runner 70 are respectively zeolite concentration runners or concentration runners made of other materials.

One end of the exhaust gas inlet pipe 61 is connected to one side of the adsorption zone 601 of the first adsorption rotor 60, so that the exhaust gas inlet pipe 61 can transport organic waste gas to the first adsorption rotor 60 One side of the adsorption zone 601, and one end of the first clean gas discharge pipeline 62 is connected to the other side of the adsorption zone 601 of the first adsorption rotor 60, and one end of the first clean gas discharge pipeline 62 Is connected to one side of the adsorption zone 701 of the second adsorption runner 70, so that the organic waste gas can adsorb organic matter through the adsorption zone 601 of the first adsorption runner 60 and then pass through the first clean gas discharge pipeline 62 to be transported to the adsorption zone 701 of the second adsorption rotor 70 (as shown in Figures 1 to 4). In addition, the other side of the adsorption zone 701 of the second adsorption rotor 70 is connected to the second clean gas discharge pipeline 71, so as to connect to the chimney 80 through the other end of the second clean gas discharge pipeline 71, And the second clean air discharge pipeline 71 is provided with a fan 711 (as shown in Figures 3 and 4), so that the fan 711 can be used to absorb the air in the second clean air discharge pipeline 71 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 runner 60 is connected to the first cooling gas inlet pipe 63 for air to enter the cooling zone 602 of the first adsorption runner 60 for cooling purposes (e.g. 1 to 4), and the other side of the cooling zone 602 of the first adsorption runner 60 is connected to one end of the first cooling gas delivery pipe 64, and the first cooling gas delivery pipe 64 The other end is connected to one end of the third cold-side pipeline 41 of the third heat exchanger 40 to transport the gas that has entered the cooling zone 602 of the first adsorption runner 60 It is sent to the third heat exchanger 40 for heat exchange (as shown in Figures 1 to 4). Furthermore, one end of the first hot gas conveying pipe 65 is connected to the first adsorption rotor 60. The other side of the attached area 603 is connected, and the other end of the first hot gas conveying pipe 65 is connected to the other end of the third cold side pipe 41 of the third heat exchanger 40, so as to be able to pass through the third heat exchanger 40. The high-temperature hot gas exchanged by the heat exchanger 40 passes through the first hot gas delivery pipe 65 to be transported to the desorption zone 603 of the first adsorption rotor 60 for desorption use.

The cooling zone 602 of the first adsorption runner 60 is provided with two embodiments. The first implementation is that the first cooling air is connected to one side of the cooling zone 602 of the first adsorption runner 60. The air 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 provide the cooling zone 602 of the first adsorption rotor 60 for cooling. Another second embodiment is that the exhaust gas intake pipe 61 is provided with an exhaust gas communication pipe 611, and the other end of the exhaust gas communication pipe 611 is connected to the first cooling gas intake pipe 63 (such as the third As shown in the figure), the exhaust gas in the exhaust gas intake pipe 61 can be transported to the cooling zone 602 of the first adsorption runner 60 through the exhaust gas communication pipeline 611 for cooling use, and 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 runner 70 is connected to the second cooling gas inlet pipe 72 for gas to enter the cooling zone 702 of the second adsorption runner 70 for cooling use (e.g. 1 to 4), and the other side of the cooling zone 702 of the second adsorption runner 70 is connected to one end of the second cooling gas delivery pipe 73, and the second cooling gas delivery pipe 73 The other end is connected to one end of the second cold side pipeline 31 of the second heat exchanger 30 to transport the gas that has entered the cooling zone 702 of the second adsorption rotor 70 It is sent to the second heat exchanger 30 for heat exchange (as shown in Figures 1 to 4). Furthermore, one end of the second hot gas conveying pipe 74 is connected to the second adsorption rotor 70. The other side of the attached area 703 is connected, and the other end of the second hot gas conveying pipe 74 is connected to the other end of the second cold side pipe 31 of the second heat exchanger 30, so as to be able to pass through the second The high-temperature hot gas exchanged by the heat exchanger 30 passes through the second hot gas delivery pipe 74 to be transported to the desorption zone 703 of the second adsorption rotor 70 for desorption use.

The cooling zone 702 of the second adsorption runner 70 is provided with two embodiments. The first implementation is that the second cooling air is connected to one side of the cooling zone 702 of the second adsorption runner 70. The air 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 provide the cooling zone 702 of the second adsorption rotor 70 for cooling. Another second embodiment is that the first clean air discharge pipeline 62 is provided with a first clean air communication pipeline 621, and the other end of the first clean air communication pipeline 621 is connected to the second cooling air inlet. The pipeline 72 is connected (as shown in Figures 3 and 4), so that the gas in the first clean gas discharge pipeline 62 can be transported to the second adsorption converter 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 pipeline 621 is provided with a first clean air communication control valve 6211 to control the air volume of the first clean air communication pipeline 621.

In addition, one end of the first desorption 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 desorption concentrated gas pipeline 66 is connected to the second 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 conveying pipeline 23 , And the other end of the first cold-side conveying pipe 23 is connected to the fourth heat exchanger One end of the fourth cold-side pipeline 51 of 50 is connected (as shown in Figures 1 to 4). Furthermore, the other end of the fourth cold-side pipe 51 of the fourth heat exchanger 50 is connected to one end of the fourth cold-side conveying pipe 53, and the other end of the fourth cold-side conveying pipe 53 is Connected to the inlet 11 of the direct-fired incinerator (TO) 10, so that the desorbed concentrated gas desorbed at high temperature can be transported to the first heat exchange through the first desorbed concentrated gas pipeline 66 Inside one end of the first cold-side pipeline 21 of the heat exchanger 20, and transported from the other end of the first cold-side pipeline 21 of the first heat exchanger 20 to one end of the first cold-side conveying pipeline 23, And from the other end of the first cold-side conveying pipe 23 to one end of the fourth cold-side pipe 51 of the fourth heat exchanger 50, and then from the fourth cold-side pipe of the fourth heat exchanger 50 The other end of the pipeline 51 is delivered to one end of the fourth cold-side delivery pipeline 53, and finally the other end of the fourth cold-side delivery pipeline 53 is delivered to the direct-fired incinerator (TO) 10 In the inlet 11 (as shown in Figs. 1 to 4), the furnace head 101 of the direct-fired incinerator (TO) 10 can be subjected to high-temperature cracking to reduce volatile organic compounds. In addition, the first desorption concentrated gas pipeline 66 is equipped 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 desorption 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 desorption concentrated gas pipeline 75 has two implementations. In the first embodiment, the other end of the second desorption concentrated gas pipeline 75 is connected to the exhaust gas inlet pipeline 61 (as shown in Figures 1 and 3), so that the concentrated gas The gas can then 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 desorption concentrated gas pipeline 75 is connected to the first cooling gas inlet pipeline 63 (such as the second As shown in Figures and Figure 4), the concentrated gas can enter the cooling zone 602 of the first adsorption runner 60 through the first cooling gas inlet pipe 63 for cooling. Furthermore, the second desorption concentrated gas pipeline 75 is provided with a fan 751 (as shown in Figs. 3 and 4) to push and pull the desorbed concentrated gas into the exhaust gas inlet pipe 61 or the exhaust gas inlet pipe 61 or the In the first cooling air intake pipe 63. The desorption gas generated through the desorption zone 703 of the second adsorption runner 70 can enter the adsorption zone 601 of the first adsorption runner 60 or the cooling zone 602 of the first adsorption runner 60 for recycling. So that the treatment efficiency of organic waste gas can be improved.

Furthermore, the first design of this creation mainly has two implementation modes, and the direct-fired incinerator (TO) 10, the first heat exchanger 20, and the second heat exchanger in the two implementation modes The exchanger 30, the third heat exchanger 40, the fourth heat exchanger 50, the first cold side conveying pipe 23, the fourth cold side conveying pipe 53, the first adsorption runner 60, the second adsorption runner 70 and The chimney 80 is of the same design. Therefore, the above-mentioned direct-fired incinerator (TO) 10, the first heat exchanger 20, the second heat exchanger 30, the third heat exchanger 40, and the fourth heat exchanger 50, The contents of the first cold-side conveying pipeline 23, the fourth cold-side conveying pipeline 53, the first adsorption runner 60, the second adsorption runner 70 and the chimney 80 are not repeated, please refer to the above description.

Among them, the difference of the first embodiment is that in the direct-fired incinerator (TO) 10 under the first heat exchanger 20, under the second heat exchanger 30, and under the third heat exchanger 40 A heat bypass passage 90 is provided below the fourth heat exchanger 50, and this part of the incineration high-temperature gas can pass through the third heat exchanger through the heat bypass passage 90 below the fourth heat exchanger 50 The heat bypass channel 90 below the second heat exchanger 30 passes through the heat bypass channel 90 below the second heat exchanger 30 and the heat bypass channel 90 below the first heat exchanger 20. Therefore, when the volatile organic When the compound (VOCs) concentration becomes higher, it can pass through the thermal bypass Channel 90 to adjust the air volume of the furnace 102 of the direct-fired incinerator (TO) 10, so that part of the incineration high-temperature gas can be transported through the thermal bypass channel 90, so that the thermal bypass channel 90 has a regulated heat The efficiency of the recovery amount or concentration can prevent the direct-fired incinerator (TO) 10 from overheating due to the high temperature of the furnace during the treatment of organic waste gas, and even causing shutdown.

In addition, the difference of the second embodiment is that the side of the first heat exchanger 20, the side of the second heat exchanger 30, and the side of the third heat exchanger in the direct-fired incinerator (TO) 10 A heat bypass passage 90 is provided on the side of the fourth heat exchanger 50 and the side of the fourth heat exchanger 50. The high-temperature incineration gas in this part can pass through the heat bypass passage 90 under the fourth heat exchanger 50. The heat bypass channel 90 under the third heat exchanger 40 passes through the heat bypass channel 90 under the second heat exchanger 30 and the heat bypass channel 90 under the first heat exchanger 20, so When the concentration of volatile organic compounds (VOCs) becomes higher, the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 can be adjusted through the thermal bypass channel 90, so that part of the high-temperature gas of incineration can be borrowed It is transported by the heat bypass channel 90, so that the heat bypass channel 90 has the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be treated to prevent the direct-fired incinerator (TO) 10 from being affected by the furnace temperature. If it is too high, it will overheat and even cause downtime.

The second design of this creation is that the direct-fired incinerator (TO) 10 is equipped with a first heat exchanger 20, a second heat exchanger 30, and a third heat exchanger 40 (such as Figures 5 to 8), and the following is an explanation of the second design.

The second design system includes a straight-fired incinerator (TO) 10, a first heat exchanger 20, a second heat exchanger 30, a third heat exchanger 40, and a first cold-side delivery pipe The combined design of road 23, a first adsorption runner 60, a second adsorption runner 70 and a chimney 80 (as shown in Figures 5 to 8), wherein the first heat exchanger 20 is provided with a first A cold side pipeline 21 and a first hot side pipeline 22, the second heat exchanger 30 is provided with a second cold side pipeline 31 and a second hot side pipeline 32, and the third heat exchanger 40 is provided with There are 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 furnace head 101 and a furnace 102, the furnace head 101 is in communication with the furnace 102, and the first heat exchanger 20, the second heat exchanger 30 and The third heat exchanger 40 is respectively provided 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 5 to 8 Shown), and the inlet 11 is set at the furnace head 101, and the inlet 11 is connected to the other end of the first cold side pipeline 21 of the first heat exchanger 20, and further, the outlet 12 is It is located at the furnace 102, and the outlet 12 is connected to the chimney 80, so that the organic waste gas can enter the furnace head 101 through the inlet 11 for combustion, and then the gas after combustion can pass through The furnace 102 is discharged from the outlet 12 to the chimney 80 for discharge, so as to save energy.

And the above-mentioned first heat exchanger 20 has two embodiments. The first embodiment is to arrange the first heat exchanger 20 beside the second heat exchanger 30 (as shown in Figures 5 and 6). (Shown), so that the burner head 101 of the direct-fired incinerator (TO) 10 can firstly deliver the burned high-temperature gas to one side of the third hot-side pipe 42 of the third heat exchanger 40 for processing For heat exchange, the other side of the third hot-side pipe 42 of the third heat exchanger 40 transports the incineration high-temperature gas to the second hot-side pipe 32 of the second heat exchanger 30 One side is used for heat exchange, and then the other side of the second hot side pipe 32 of the second heat exchanger 30 transports the burned 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 Figs. 5 and 6 Figure (Shown), the outlet 12 of the furnace 102 is transported to the chimney 80 for discharge through the chimney 80.

Furthermore, another second embodiment is to install the first heat exchanger 20 next to the third heat exchanger 40 (as shown in Figures 7 and 8), so that the direct-fired incinerator (TO ) The furnace head 101 of 10 is capable of transporting the burned high-temperature gas to one side of the first hot-side pipe 22 of the first heat exchanger 20 for heat exchange. The other side of the first hot-side pipe 22 is used to transport the incineration high-temperature gas to one side of the third hot-side pipe 42 of the third heat exchanger 40 for heat exchange, and then the third heat The other side of the third hot side pipe 42 of the heat exchanger 40 transports the burned high-temperature gas to one side of the second hot side pipe 32 of the second heat exchanger 30 for heat exchange, and then From the other side of the second hot side pipeline 32 of the second heat exchanger 30, the incineration high-temperature gas is transported to the outlet 12 of the furnace 102 (as shown in Figs. 7 and 8), and then The outlet 12 of the furnace 102 is conveyed to the chimney 80 for discharge through the chimney 80.

In addition, the first adsorption runner 60 of this creation is provided with an adsorption zone 601, a cooling zone 602 and a desorption zone 603. The first adsorption runner 60 is connected with an exhaust gas inlet pipe 61 and a first clean gas discharge pipe. Path 62, a first cooling gas inlet pipe 63, a first cooling gas delivery pipe 64, a first hot gas delivery pipe 65, and a first desorption concentrated gas pipe 66, (as shown in Figures 5 to (Shown in Figure 8) 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 with a second clean gas discharge pipeline 71, a The second cooling gas intake 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 runner 60 and the second adsorption runner 70 are respectively zeolite concentration runners or other Concentrated runner of material.

One end of the exhaust gas inlet pipe 61 is connected to one side of the adsorption zone 601 of the first adsorption rotor 60, so that the exhaust gas inlet pipe 61 can transport organic waste gas to the first adsorption rotor 60 One side of the adsorption zone 601, and one end of the first clean gas discharge pipeline 62 is connected to the other side of the adsorption zone 601 of the first adsorption rotor 60, and one end of the first clean gas discharge pipeline 62 Is connected to one side of the adsorption zone 701 of the second adsorption runner 70, so that the organic waste gas can adsorb organic matter through the adsorption zone 601 of the first adsorption runner 60 and then pass through the first clean gas discharge pipeline 62 to be transported to the adsorption zone 701 of the second adsorption rotor 70 (as shown in Figures 5 to 8). In addition, the other side of the adsorption zone 701 of the second adsorption rotor 70 is connected to the second clean gas discharge pipeline 71, so as to connect to the chimney 80 through the other end of the second clean gas discharge pipeline 71, And the second clean air discharge pipeline 71 is provided with a fan 711 (as shown in Figures 6 and 8), so that the fan 711 can be used to absorb the air in the second clean air discharge pipeline 71. 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 runner 60 is connected to the first cooling gas inlet pipe 63 for air to enter the cooling zone 602 of the first adsorption runner 60 for cooling purposes (e.g. 5 to 8), and the other side of the cooling zone 602 of the first adsorption runner 60 is connected to one end of the first cooling gas delivery pipe 64, and the first cooling gas delivery pipe 64 The other end is connected to one end of the third cold-side pipeline 41 of the third heat exchanger 40 to transport the gas entering the cooling zone 602 of the first adsorption rotor 60 into the third heat exchanger 40 Perform heat exchange (as shown in Figures 5 to 8). Furthermore, one end of the first hot gas conveying pipe 65 is connected to the desorption zone 603 of the first adsorption rotor 60 The other side is connected, and the other end of the first hot gas conveying pipe 65 is connected to the other end of the third cold side pipe 41 of the third heat exchanger 40 so as to be able to pass through the third heat exchanger 40 The high-temperature hot gas undergoing heat exchange is transported to the desorption zone 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 runner 60 is provided with two embodiments. The first implementation is that the first cooling air is connected to one side of the cooling zone 602 of the first adsorption runner 60. The air pipe 63 is for fresh air or outside air to enter (as shown in FIG. 5), and the fresh air or outside air is used to provide the cooling zone 602 of the first adsorption rotor 60 to cool down through the fresh air or outside air. Another second embodiment is that the exhaust gas intake pipe 61 is provided with an exhaust gas communication pipe 611, and the other end of the exhaust gas communication pipe 611 is connected to the first cooling gas intake pipe 63 (e.g., No. 6 As shown in the figure), the exhaust gas in the exhaust gas intake pipe 61 can be transported to the cooling zone 602 of the first adsorption runner 60 through the exhaust gas communication pipeline 611 for cooling use, and 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 runner 70 is connected to the second cooling gas inlet pipe 72 for gas to enter the cooling zone 702 of the second adsorption runner 70 for cooling use (e.g. 5 to 8), and the other side of the cooling zone 702 of the second adsorption rotor 70 is connected to one end of the second cooling gas delivery pipe 73, and the second cooling gas delivery pipe 73 The other end is connected to one end of the second cold-side pipeline 31 of the second heat exchanger 30 to transport the gas entering the cooling zone 702 of the second adsorption rotor 70 into the second heat exchanger 30 Perform heat exchange (as shown in Figures 5 to 8). Furthermore, one end of the second hot gas conveying pipe 74 is connected to the desorption zone 703 of the second adsorption rotor 70 The other side is connected, and the other end of the second hot gas conveying pipe 74 is connected with the other end of the second cold side pipe 31 of the second heat exchanger 30 so as to be able to pass through the second heat exchanger 30 The high-temperature hot gas undergoing heat exchange is transported to the desorption zone 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 runner 70 is provided with two embodiments. The first implementation is that the second cooling air is connected to one side of the cooling zone 702 of the second adsorption runner 70. The air 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 provide the cooling zone 702 of the second adsorption rotor 70 for cooling. Another second embodiment is that the first clean air discharge pipeline 62 is provided with a first clean air communication pipeline 621, and the other end of the first clean air communication pipeline 621 is connected to the second cooling air inlet. The pipeline 72 is connected (as shown in Figure 6), so that the gas in the first clean gas discharge pipeline 62 can be transported to the second adsorption runner 70 for cooling through the first clean gas communication pipeline 621 The area 702 is used for cooling, and the first clean air communication pipeline 621 is provided with a first clean air communication control valve 6211 to control the air volume of the first clean air communication pipeline 621.

In addition, one end of the first desorption 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 desorption concentrated gas pipeline 66 is connected to the second 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 conveying 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 5 to 8) to be able to remove the high temperature The attached desorbed concentrated gas can pass through the first desorbed concentrated gas pipeline 66 to be transported to one end of the first cold side pipeline 21 of the first heat exchanger 20, and is transferred by the first heat exchanger 20 The other end of the first cold-side pipeline 21 is delivered to one end of the first cold-side delivery pipeline 23, and the other end of the first cold-side delivery pipeline 23 is delivered to the direct-fired incinerator In the entrance 11 of (TO) 10 (as shown in Figures 5 to 8), the furnace head 101 of the direct-fired incinerator (TO) 10 can be subjected to high temperature cracking to reduce volatile organic compounds . In addition, the first desorption concentrated gas pipeline 66 is equipped 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 desorption 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 desorption concentrated gas pipeline 75 has two implementations. In the first embodiment, the other end of the second desorption concentrated gas pipeline 75 is connected to the exhaust gas inlet pipeline 61 (as shown in Figures 5 and 6), so that the concentrated gas The gas can then 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 desorption concentrated gas pipeline 75 is connected to the first cooling gas inlet pipeline 63 (as shown in Figures 7 and 8), so that the The concentrated gas can then enter the cooling zone 602 of the first adsorption runner 60 through the first cooling gas inlet pipe 63 for cooling. Furthermore, the second desorption concentrated gas pipeline 75 is provided with a fan 751 (as shown in Figs. 6 and 8) to push and pull the desorbed concentrated gas into the exhaust gas inlet pipe 61 or the exhaust gas inlet pipe 61 or the In the first cooling air intake pipe 63. The desorption gas generated through the desorption zone 703 of the second adsorption runner 70 can enter the adsorption zone 601 of the first adsorption runner 60 or the cooling zone 602 of the first adsorption runner 60 for recycling. So that the treatment efficiency of organic waste gas can be improved.

Furthermore, the second design of this creation mainly has two implementation modes, and in the two implementation modes, the direct-fired incinerator (TO) 10, the first heat exchanger 20, and the second heat exchanger cross The converter 30, the third heat exchanger 40, the first cold-side conveying pipeline 23, the first adsorption runner 60, the second adsorption runner 70, and the chimney 80 are of the same design. Therefore, the above-mentioned direct-fired incineration The furnace (TO) 10, the first heat exchanger 20, the second heat exchanger 30, the third heat exchanger 40, the first cold side conveying pipe 23, the first adsorption runner 60, the second adsorption runner 70 and The content of Chimney 80 is not repeated, please refer to the above description.

The difference in the first implementation aspect is in the direct-fired incinerator (TO) 10 under the first heat exchanger 20, under the second heat exchanger 30, and under the third heat exchanger 40 A heat bypass passage 90 is provided, regardless of whether the first heat exchanger 20 is located beside the second heat exchanger 30 (as shown in FIGS. 5 and 6) or the first heat exchanger 20 is located When next to the third heat exchanger 40 (as shown in Figs. 7 and 8), the part of the incineration high temperature gas can pass through the heat bypass passage 90 under the third heat exchanger 40 The heat bypass channel 90 under the second heat exchanger 30 and the heat bypass channel 90 under the first heat exchanger 20, or the part of the incineration high-temperature gas can pass through the first heat exchange The heat bypass channel 90 under the heat exchanger 20 passes through the heat bypass channel 90 under the third heat exchanger 40 and the heat bypass channel 90 under the second heat exchanger 30. Therefore, when the volatile organic When the concentration of compounds (VOCs) becomes higher, the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 can be adjusted through the thermal bypass channel 90, so that part of the high-temperature gas of incineration can be bypassed by the heat The heat bypass channel 90 has the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be treated to prevent the direct-fired incinerator (TO) 10 from being caused by too high furnace temperature. The phenomenon of warmth may even lead to downtime.

In addition, the difference of the second embodiment is the side of the first heat exchanger 20, the side of the second heat exchanger 30, and the third heat exchanger in the direct-fired incinerator (TO) 10 A heat bypass passage 90 is provided on the side of 40, regardless of whether the first heat exchanger 20 is arranged beside the second heat exchanger 30 (as shown in FIGS. 5 and 6) or the first heat exchange When the device 20 is installed beside the third heat exchanger 40 (as shown in Figs. 7 and 8), the part of the incineration high temperature gas can pass through the heat bypass on the side of the third heat exchanger 40 The passage 90 passes through the heat bypass passage 90 on the side of the second heat exchanger 30 and the heat bypass passage 90 on the side of the first heat exchanger 20, or the part of the high-temperature incineration gas Can pass through the heat bypass channel 90 on the side of the third heat exchanger 40 and the heat bypass on the side of the second heat exchanger 30 via the heat bypass channel 90 on the side of the first heat exchanger 20 Through the passage 90, when the concentration of volatile organic compounds (VOCs) becomes high, the heat bypass passage 90 can be used to adjust the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 to make part of the incineration The high-temperature gas can be transported through the thermal bypass channel 90, so that the thermal bypass channel 90 has the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be prevented from the direct-fired incinerator (TO) 10 when the organic waste gas is processed. There will be no overheating due to too high furnace temperature, or even shutdown.

Based on the above detailed description, those who are familiar with this technique can understand that this creation can indeed achieve the aforementioned purpose, and that it has actually complied with the provisions of the Patent Law, and filed a patent application.

However, the above are only the preferred embodiments of this creation, and should not be used to limit the scope of implementation of this creation; therefore, all simple equivalent changes and modifications made in accordance with the scope of the patent application for this creation and the content of the creation specification , Should still be within the scope of this creation patent.

10: Direct-fired incinerator (TO)

101: stove top

102: Furnace

11: entrance

12: Exit

20: The first heat exchanger

21: The first cold side pipeline

22: The first hot side pipeline

23: The first cold side conveying pipeline

30: second heat exchanger

31: The second cold side pipeline

32: The second hot side pipeline

40: The third heat exchanger

41: The third cold side pipeline

42: The third hot side pipeline

50: The fourth heat exchanger

51: Fourth cold side pipeline

52: The fourth hot side pipeline

53: The fourth cold side conveying pipeline

60: The first adsorption wheel

601: Adsorption Zone

602: Cooling Zone

603: Desorption Zone

61: Exhaust gas intake pipe

62: The first clean gas discharge pipeline

63: The first cooling air intake pipe

64: The first cooling gas delivery pipeline

65: The first hot gas delivery pipeline

66: The first desorption concentrated gas pipeline

70: The second adsorption wheel

701: Adsorption Zone

702: Cooling Zone

703: Desorption Zone

71: The second clean gas discharge pipeline

72: The second cooling air intake line

73: The second cooling gas delivery pipeline

74: The second hot gas delivery pipeline

75: The second desorption concentrated gas pipeline

80: Chimney

90: Hot Bypass Channel

Claims (14)

An energy-saving dual-wheel high-concentration heat-bypass temperature control system, which includes: A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a furnace head and a furnace, the furnace head is in communication with the furnace, the direct-fired incinerator (TO) is provided with an entrance and Outlet, the inlet is set at the furnace head, and the outlet is set at the furnace; A first heat exchanger, the first heat exchanger is arranged 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 arranged 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 arranged 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 fourth heat exchanger, the fourth heat exchanger is arranged in the direct-fired incinerator (TO), and the fourth heat exchanger is provided with a fourth cold side pipeline and a fourth hot side pipeline; A first cold-side delivery pipeline, one end of the first cold-side delivery pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side delivery pipeline is connected to the fourth cold-side pipeline One end of the side pipeline is connected; A fourth cold-side delivery pipeline, one end of the fourth cold-side delivery pipeline is connected to the other end of the fourth cold-side pipeline, and the other end of the fourth cold-side delivery pipeline is connected to the direct-fired The entrance connection of the incinerator (TO); A first adsorption runner, the first adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone, and the first adsorption runner system is connected with an exhaust gas inlet pipeline, a first clean gas discharge pipeline, A first cooling gas intake pipeline, a first cooling gas 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 zone of the first adsorption runner, and one end of the first clean gas discharge pipeline is connected to the first adsorption runner The other side of the adsorption zone is connected, one end of the first cooling gas inlet pipeline is connected to one side of the cooling zone of the first adsorption runner, and one end of the first cooling gas delivery pipeline is connected to the first cooling zone. The other side of the cooling zone of an adsorption runner 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, and the first hot gas delivery pipeline One end of is connected to the other side of the desorption zone of the first adsorption runner, the other end of the first hot gas conveying pipeline is connected to the other end of the third cold side pipeline of the third heat exchanger, One end of the first desorption concentrated gas pipeline is connected with one side of the desorption zone of the first adsorption rotor, and the other end of the first desorption concentrated gas pipeline is connected with the first heat exchanger. One end of a cold side pipeline is connected; a second adsorption runner, the second adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone, and the second adsorption runner system is connected with a second clean air discharge pipe 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 Connected to one side of the adsorption zone of the second adsorption runner, one end of the second clean air discharge pipeline is connected to the other side of the adsorption zone of the second adsorption runner, and the second cooling gas inlet pipe One end of the path is connected to one side of the cooling zone of the second adsorption runner, and one end of the second cooling gas delivery pipeline is connected to the other side of the cooling zone of the second adsorption runner. The second cooling 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 delivery 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 At least one heat bypass passage, the heat bypass passage is arranged below the first heat exchanger, below the second heat exchanger, below the third heat exchanger, and below the fourth heat exchanger. An energy-saving dual-wheel high-concentration heat-bypass temperature control system, which includes: A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a furnace head and a furnace, the furnace head is in communication with the furnace, the direct-fired incinerator (TO) is provided with an entrance and Outlet, the inlet is set at the furnace head, and the outlet is set at the furnace; A first heat exchanger, the first heat exchanger is arranged 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 arranged 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 arranged 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 fourth heat exchanger, the fourth heat exchanger is arranged in the direct-fired incinerator (TO), and the fourth heat exchanger is provided with a fourth cold side pipeline and a fourth hot side pipeline; A first cold-side delivery pipeline, one end of the first cold-side delivery pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side delivery pipeline is connected to the fourth cold-side pipeline One end of the side pipeline is connected; A fourth cold-side delivery pipeline, one end of the fourth cold-side delivery pipeline is connected to the other end of the fourth cold-side pipeline, and the other end of the fourth cold-side delivery pipeline is connected to the direct-fired The entrance connection of the incinerator (TO); A first adsorption runner, the first adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone, the The first adsorption runner system is connected with an exhaust gas intake pipeline, a first clean gas discharge pipeline, a first cooling gas intake pipeline, a first cooling gas delivery pipeline, a first hot gas delivery pipeline, and A first desorption concentrated gas pipeline, one end of the exhaust gas inlet pipeline is connected to one side of the adsorption zone of the first adsorption rotor, and one end of the first clean gas discharge pipeline is connected to the first adsorption The other side of the adsorption zone of the runner is connected, one end of the first cooling gas inlet pipe is connected with one side of the cooling zone of the first adsorption runner, and one end of the first cooling gas delivery pipeline is connected with The other side of the cooling zone of the first adsorption runner 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, and the first hot gas delivery One end of the pipeline is connected to the other side of the desorption zone of the first adsorption runner, and the other end of the first hot gas conveying pipeline is connected to the other end of the third cold side pipeline of the third heat exchanger Connected, one end of the first desorption concentrated gas pipeline is connected with one side of the desorption zone of the first adsorption rotor, and the other end of the first desorption concentrated gas pipeline is connected with the first heat exchanger One end of the first cold side pipeline is connected; a second adsorption runner, the second adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, and the second adsorption runner is connected with a second clean air The discharge pipeline, a second cooling gas intake pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and a second desorption concentrated gas pipeline, the first clean gas discharge pipeline One end is connected to one side of the adsorption zone of the second adsorption runner, one end of the second clean air discharge pipeline is connected to the other side of the adsorption zone of the second adsorption runner, and the second cooling air enters One end of the gas pipeline is connected to one side of the cooling zone of the second adsorption runner, and one end of the second cooling gas delivery pipeline is connected to the other side of the cooling zone of the second adsorption runner. The other end of the two cooling gas delivery pipelines 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 desorption zone of the second adsorption runner Connected to the other side, and the other end of the second hot gas delivery pipeline is connected to the second hot gas The other end of the second cold side pipeline of the exchanger is connected, and one end of the second desorption concentrated gas pipeline is connected to one side of the desorption zone of the second adsorption runner; A chimney, the other end of the second clean gas discharge pipeline is connected to the chimney; and At least one heat bypass channel, the heat bypass channel is arranged on the side of the first heat exchanger, the side of the second heat exchanger, the side of the third heat exchanger, and the side of the fourth heat exchanger side. An energy-saving dual-wheel high-concentration heat-bypass temperature control system, which includes: A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a furnace head and a furnace, the furnace head is in communication with the furnace, the direct-fired incinerator (TO) is provided with an entrance and Outlet, the inlet is set at the furnace head, and the outlet is set at the furnace; A first heat exchanger, the first heat exchanger is arranged 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 arranged 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 arranged 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, 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 direct-fired The entrance connection of the incinerator (TO); A first adsorption runner, the first adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone, and the first adsorption runner system is connected with an exhaust 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 exhaust gas inlet pipeline is connected to the first An adsorption wheel One side of the adsorption zone, one end of the first clean air discharge pipeline is connected to the other side of the adsorption zone of the first adsorption runner, and one end of the first cooling gas inlet pipeline is connected to the first One side of the cooling zone of the adsorption runner is connected, one end of the first cooling gas delivery pipeline is connected with the other side of the cooling zone of the first adsorption runner, and the other end of the first cooling gas delivery pipeline is connected It is connected to one end of the third cold side pipeline of the third heat exchanger, and one end of the first hot gas conveying pipeline is connected to the other side of the desorption zone of the first adsorption runner. The first hot gas conveys 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 a desorption zone of the first adsorption runner 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 Adsorption zone, cooling zone and desorption zone, the second adsorption runner system is connected with a second clean gas discharge pipeline, a second cooling gas inlet pipeline, a second cooling gas delivery pipeline, and 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 zone of the second adsorption runner, and one end of the second clean gas discharge pipeline Is connected to the other side of the adsorption zone of the second adsorption runner, one end of the second cooling air inlet pipe is connected to one side of the cooling zone of the second adsorption runner, and the second cooling air is conveyed One end of the pipeline is connected to the other side of the cooling zone of the second adsorption runner, 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 conveying 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 conveying pipeline is connected to the second cold of the second heat exchanger. The other end of the side pipeline is connected, and one end of the second desorption concentrated gas pipeline is connected to one side of the desorption zone of the second adsorption runner; A chimney, the other end of the second clean gas discharge pipeline is connected to the chimney; and At least one heat bypass channel is provided below the first heat exchanger, below the second heat exchanger, and below the third heat exchanger. An energy-saving dual-wheel high-concentration heat-bypass temperature control system, which includes: A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a furnace head and a furnace, the furnace head is in communication with the furnace, the direct-fired incinerator (TO) is provided with an entrance and Outlet, the inlet is set at the furnace head, and the outlet is set at the furnace; A first heat exchanger, the first heat exchanger is arranged 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 arranged 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 arranged 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, 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 direct-fired The entrance connection of the incinerator (TO); A first adsorption runner, the first adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone, and the first adsorption runner system is connected with an exhaust 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 exhaust gas inlet pipeline is connected to the first One side of the adsorption zone of an adsorption runner, one end of the first clean air discharge pipeline is connected to the other side of the adsorption zone of the first adsorption runner, and one end of the first cooling gas inlet pipeline Connected to one side of the cooling zone of the first adsorption runner, and one end of the first cooling gas delivery pipeline is connected to the first adsorption runner The other side of the cooling zone of the wheel 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, and one end of the first hot gas delivery pipeline is connected Connected to the other side of the desorption zone of the first adsorption runner, the other end of the first hot gas conveying pipeline is connected to the other end of the third cold side pipeline of the third heat exchanger, and the first One end of the desorption concentrated gas pipeline is connected to one side of the desorption zone of the first adsorption rotor, and the other end of the first desorption concentrated gas pipeline is connected to the first cold side of the first heat exchanger One end of the pipeline is connected; a second adsorption runner, the second adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone, the second adsorption runner system is connected with a second clean gas discharge pipeline, a The 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 the One side of the adsorption zone of the second adsorption runner, one end of the second clean air discharge pipeline is connected to the other side of the adsorption zone of the second adsorption runner, and one end of the second cooling gas inlet pipeline Is connected to one side of the cooling zone of the second adsorption runner, one end of the second cooling gas conveying pipe is connected to the other side of the cooling zone of the second adsorption runner, the second cooling gas conveying pipe The other end of the circuit is connected to one end of the second cold side pipeline of the second heat exchanger, and one end of the second hot gas conveying pipeline is connected to the other side of the desorption zone of the second adsorption runner, The other end of the second hot gas conveying 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 runner One side of the desorption zone is connected; A chimney, the other end of the second clean gas discharge pipeline is connected to the chimney; and At least one heat bypass channel, the heat bypass channel is arranged on the side of the first heat exchanger, the side of the second heat exchanger, and the side of the third heat exchanger. Energy-saving dual-wheel high-concentration heat bypass as described in item 1, 2, 3 or 4 of the scope of patent application The over-temperature control system, wherein the outlet of the direct-fired incinerator (TO) is further connected to the chimney. The energy-saving dual-wheel high-concentration heat-bypass temperature control system described in item 1, 2, 3, or 4 of the scope of patent application, wherein the first cooling air intake pipeline is further provided for fresh air or external air Come and enter. The energy-saving dual-wheel high-concentration heat-bypass temperature control system described in item 1, 2, 3, or 4 of the scope of patent application, wherein the second cooling air intake pipeline is further provided for fresh air or external air Come and enter. As described in item 1, 2, 3 or 4 of the scope of patent application, the energy-saving dual-wheel high-concentration heat-by-pass temperature control system, wherein the exhaust gas intake pipe system is further provided with an exhaust gas communication pipe, the exhaust gas communication pipe The circuit is connected with the first cooling gas intake pipeline, and the exhaust gas communication pipeline system is further provided with an exhaust gas communication control valve to control the air volume of the exhaust gas communication pipeline. The energy-saving dual-rotor high-concentration heat-bypass temperature control system as described in item 1, 2, 3 or 4 of the scope of patent application, wherein the first clean gas discharge pipeline is further provided with a first clean gas communication pipeline , The first clean air communication pipeline is connected with the second cooling air intake pipeline, and the first clean air communication pipeline is further provided with a first clean air communication control valve to control the first clean air communication The air volume of the pipeline. The energy-saving dual-rotor high-concentration heat-bypass temperature control system described in item 1, 2, 3, or 4 of the scope of patent application, wherein the first desorption concentrated gas pipeline system is further provided with a fan. For example, the energy-saving double-rotor high-concentration heat-bypass temperature control system described in item 1, 2, 3 or 4 of the scope of patent application, wherein the second desorption concentrated gas pipeline system is further provided with a wind machine. The energy-saving dual-rotor high-concentration heat-bypass temperature control system described in item 1, 2, 3 or 4 of the scope of patent application, wherein the second clean air discharge pipeline is further provided with a fan. As described in item 1, 2, 3 or 4 of the scope of patent application, the energy-saving dual-wheel high-concentration heat-by-pass temperature control system, wherein the other end of the second desorption concentrated gas pipeline is further connected to the exhaust gas inlet The pipelines are connected. The energy-saving dual-rotor high-concentration heat-bypass temperature control system described in item 1, 2, 3 or 4 of the scope of patent application, wherein the other end of the second desorption concentrated gas pipeline is further connected with the first cooling Connect the gas and intake pipes.

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