TWM619759U - Energy saving type single runner high concentration thermal side bypass over-temperature control system - Google Patents

Abstract

This creation is an energy-saving single-wheel high-concentration hot side-pass temperature control system, which is mainly used for organic waste gas treatment systems, and is equipped with a direct-fired incinerator (TO), a first heat exchanger, and a second The heat exchanger, a third heat exchanger, a first cold-side conveying pipeline, a third cold-side conveying pipeline, an adsorption runner and a chimney are passed through the direct-fired incinerator (TO) The furnace is provided 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 pipe of the second heat exchanger The connection between the roads, or the connection between the second hot-side pipeline of the second heat exchanger and the first hot-side pipeline of the first heat exchanger, or the direct-fired incinerator (TO ) Is connected to any one of the outlets, so that when the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the direct-fired incinerator (TO) can be adjusted through the hot side forced exhaust pipe , With the ability to adjust the heat recovery amount or concentration, the organic waste gas can be treated to prevent the direct-fired incinerator (TO) from overheating due to the high temperature of the furnace, and even causing shutdown.

Description

Energy-saving single-rotor high-concentration hot side pass temperature control system

This creation is about an energy-saving single-wheel high-concentration heat side-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 When the exhaust gas is processed, it can prevent the direct-fired incinerator (TO) from overheating due to the high temperature of the furnace, and even causing downtime. It is suitable for organic semiconductor industry, optoelectronic industry or chemical-related industries. Exhaust gas treatment 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 and 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 in 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 single-wheel high-concentration hot-side pass temperature control system that can improve the efficiency of organic waste gas treatment, so that users can easily operate and assemble. The organization system provides user convenience and is the creative motivation that the creator wants to develop.

The main purpose of this creation is to provide an energy-saving single-wheel high-concentration hot side-pass temperature control system, which is mainly used in organic waste gas treatment systems, and is equipped with a continuous combustion incinerator (TO), a first heat exchange Heat exchanger, a second heat exchanger, a third heat exchanger, a first cold-side conveying pipeline, a third cold-side conveying pipeline, an adsorption runner and a chimney, and through the direct-fired incineration The hearth of the furnace (TO) is provided with a hot-side forced-exhaust pipeline, and the other end of the hot-side forced-exhaust pipeline is connected to the third hot-side pipeline of the third heat exchanger and the second heat exchanger. The connection between the second hot-side pipeline, or the connection between the second hot-side pipeline of the second heat exchanger and the first hot-side pipeline of the first heat exchanger, or the direct combustion Connect any one of the outlets of the TO ) The air volume of the furnace has the effect of adjusting the heat recovery volume or concentration, so that when the organic waste gas is processed, it can prevent the direct-fired incinerator (TO) from overheating due to the high temperature of the furnace, and even cause The situation of downtime occurs, thereby increasing the overall practicability.

Another purpose of this creation is to provide an energy-saving single-wheel high-concentration hot-side passing temperature control system, by providing at least one regulating damper on the hot-side forced-exhaust pipeline, and the hot-side forced-exhaust pipeline The other end is connected to the third hot side pipe of the third heat exchanger and the second hot side pipe of the second heat exchanger, or with the second hot side of the second heat exchanger The connection between the pipeline and the first hot-side pipeline of the first heat exchanger, or any one of the outlets of the direct-fired incinerator (TO), to act as volatile organic compounds (VOCs) When the concentration becomes higher, the air volume of the furnace of the direct-fired incinerator (TO) can be adjusted through the hot-side forced exhaust pipeline, and part of the incineration high-temperature gas can be transported to the hot-side pipelines of different heat exchangers The connection point of the hot-side forced exhaust pipe has the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be treated to prevent direct combustion The incinerator (TO) will not overheat due to the high temperature of the furnace, and even cause the shutdown to occur, thereby increasing the overall usability.

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

43: The third cold side conveying pipeline

60: 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: Clean gas discharge pipeline

621: Clean air connection pipeline

6211: Net air connection control valve

63: Cooling gas intake pipe

64: Cooling gas delivery pipeline

65: Hot gas delivery pipeline

66: Desorption concentrated gas pipeline

661: Fan

80: Chimney

90: Hot side forced exhaust pipeline

901: Adjust the damper

Figure 1 is a schematic diagram of the system architecture with hot-side forced exhaust pipes in the first implementation of this creation.

Figure 2 is a schematic diagram of the system architecture with the hot-side forced-exhaust pipeline in the second implementation of this creation.

Figure 3 is a schematic diagram of the system architecture with the hot-side forced-exhaust pipeline in the third implementation of this creation.

Please refer to Figures 1 to 3, which are schematic diagrams of this creative embodiment. The best implementation of the energy-saving single-wheel high-concentration heat-side pass 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 When the concentration of the compound (VOCs) becomes higher, it can adjust the heat recovery amount or concentration, so that the organic waste gas can be treated to prevent the direct-fired incinerator (TO) from overheating due to the high temperature of the furnace , And even lead to downtime.

The energy-saving single-wheel high-concentration heat side-passing temperature control system of this creation mainly includes a direct-fired incinerator (TO) 10, a first heat exchanger 20, and a second heat exchange The combined design of the heat exchanger 30, a third heat exchanger 40, a first cold-side delivery pipeline 23, a third cold-side delivery pipeline 43, an adsorption runner 60 and a chimney 80 (as shown in Figures 1 to 3), wherein the first heat exchanger 20 is provided with a first cold side pipeline 21 and a first hot side pipeline 22, and the second heat exchanger 30 is provided with a second cold side pipeline 31 And the 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. 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 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 (as shown in Figures 1 to 3) Shown), and the inlet 11 is set at the furnace head 101, and the inlet 11 is connected to the other end of the third cold side pipeline 41 of the third heat exchanger 40, 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 the combusted gas can pass through The furnace 102 is discharged from the outlet 12 to the chimney 80 for discharge, so as to save energy.

The burner head 101 of the above-mentioned direct-fired incinerator (TO) 10 is capable of transporting the burned high-temperature gas to one side of the third hot-side pipe 42 of the third heat exchanger 40 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 one side of the second hot-side pipe 32 of the second heat exchanger 30. Perform heat exchange, and then the incineration high-temperature gas is transported to the first hot-side pipe of the first heat exchanger 20 from the other side of the second hot-side pipe 32 of the second heat exchanger 30 22 for heat exchange, and finally by the first hot side of the first heat exchanger 20 The other side of the pipeline 22 is transported to the outlet 12 of the furnace 102 (as shown in Figures 1 to 3), and then transported from the outlet 12 of the furnace 102 to the chimney 80 to pass through the chimney 80 emission.

In addition, the adsorption runner 60 of this creation is provided with an adsorption zone 601, a cooling zone 602, and a desorption zone 603. The adsorption runner 60 is connected with an exhaust gas inlet pipe 61, a clean gas discharge pipe 62, and a cooling gas The intake pipe 63, a cooling gas delivery pipe 64, a hot gas delivery pipe 65, and a desorption concentrated gas pipe 66 (as shown in Figs. 1 to 3). The adsorption runner 60 is a zeolite concentration runner or a concentration runner 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 adsorption rotor 60, so that the exhaust gas inlet pipeline 61 can transport organic waste gas to the adsorption zone 601 of the adsorption rotor 60 One end of the clean gas discharge pipeline 62 is connected to the other side of the adsorption zone 601 of the adsorption runner 60, and the other end of the clean gas discharge pipeline 62 is connected to the chimney 80, and the clean gas discharge pipeline 62 is connected to the chimney 80. The gas discharge pipeline 62 is provided with a fan 621 (as shown in Figure 3), which enables the gas after adsorption in the clean gas discharge pipeline 62 to be pushed and pulled into the chimney 80 for discharge through the fan 621 .

In addition, one side of the cooling zone 602 of the adsorption runner 60 is connected to the cooling gas inlet pipe 63 for air to enter the cooling zone 602 of the adsorption runner 60 for cooling purposes (as shown in Figures 1 to 3 Shown), and the other side of the cooling zone 602 of the adsorption runner 60 is connected to one end of the cooling gas conveying pipe 64, and the other end of the cooling gas conveying pipe 64 is connected to the second heat exchanger 30 One end of the second cold side pipeline 31 is connected to transport the gas after entering the cooling zone 602 of the adsorption rotor 60 to the second heat exchanger 30 for heat exchange (as shown in Figures 1 to 3 ), and furthermore, one end of the hot gas delivery pipe 65 is It is connected to the other side of the desorption zone 603 of the adsorption runner 60, and the other end of the hot gas conveying pipe 65 is connected to the other end of the second cold side pipe 31 of the second heat exchanger 30 to The high-temperature hot gas that undergoes heat exchange through the second heat exchanger 30 can be transported to the desorption zone 603 of the adsorption rotor 60 through the hot gas delivery pipe 65 for desorption use.

The cooling zone 602 of the adsorption runner 60 described above is provided with two implementations. The first implementation is that the cooling air inlet pipe 63 connected to one side of the cooling zone 602 of the adsorption runner 60 is Fresh air or outside air is provided (as shown in Figure 1), and the cooling zone 602 of the adsorption rotor 60 is provided for cooling 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 cooling gas intake pipe 63 (as shown in Figure 2 and As shown in Fig. 3), the exhaust gas in the exhaust gas intake pipe 61 can be transported to the cooling zone 602 of the 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 end of the desorption concentrated gas pipeline 66 is connected to one side of the desorption zone 603 of the adsorption rotor 60, and the other end of the desorption concentrated gas pipeline 66 is connected to the first heat exchanger 20. One end of the first cold-side pipeline 21 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 first cold The other end of the side conveying pipe 23 is connected to one end of the third cold side pipe 41 of the third heat exchanger 40 (as shown in Figs. 1 to 3). Furthermore, the other end of the third cold-side pipe 41 of the third heat exchanger 40 is connected to one end of the third cold-side conveying pipe 43, and the other end of the third cold-side conveying pipe 43 is With this direct-fired incinerator (TO) 10 The inlet 11 is connected to allow the desorption concentrated gas desorbed at high temperature to pass through the desorption concentrated gas pipeline 66 to one end of the first cold side pipeline 21 of the first heat exchanger 20 , And 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 pipeline 23 One end is transported to one end of the third cold-side pipeline 41 of the third heat exchanger 40, and then transported to the third cold-side pipeline 41 by the other end of the third cold-side pipeline 41 of the third heat exchanger 40 In one end of the side conveying pipe 43, the other end of the third cold side conveying pipe 43 is finally conveyed to the inlet 11 of the direct-fired incinerator (TO) 10 (as shown in Figs. 1 to 3) Show), so that 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 desorbed 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.

Furthermore, the energy-saving single-rotor high-concentration heat side pass temperature control system of this creation mainly has three implementation modes. Among the three implementation modes, the direct-fired incinerator (TO) 10 and the first The first heat exchanger 20, the second heat exchanger 30, the third heat exchanger 40, the first cold-side conveying pipe 23, the third cold-side conveying pipe 43, the adsorption runner 60 and the chimney 80 are of the same design. Therefore, the aforementioned direct-fired incinerator (TO) 10, the first heat exchanger 20, the second heat exchanger 30, the third heat exchanger 40, the first cold-side conveying pipeline 23, and the third cold-side conveying The contents of the pipeline 43, the adsorption runner 60 and the chimney 80 are not repeated, please refer to the above description.

The difference of the first implementation mode (as shown in Figure 1) is that the furnace 102 of the direct-fired incinerator (TO) 10 is equipped with a hot-side forced exhaust pipe 90, and the hot-side forced exhaust pipe One end of the road 90 is connected to the hearth 102 of the direct-fired incinerator (TO) 10, and the hot side is strong The other end of the exhaust pipe 90 is connected to the connection between the third hot side pipe 42 of the third heat exchanger 40 and the second hot side pipe 32 of the second heat exchanger 30, wherein the hot side The forced exhaust pipeline 90 is provided with at least one regulating damper 901, and two regulating dampers (not shown in the figure) can also be provided in conjunction with the pipeline to control the hot side forced exhaust pipeline 90 through the regulating damper 901 The air volume, 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 it can be incinerated The high-temperature gas is delivered to the connection between the third hot-side pipeline 42 of the third heat exchanger 40 and the second hot-side pipeline 32 of the second heat exchanger 30, so that the hot-side forced-exhaust pipeline 90 It has the ability to adjust 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 high temperature of the furnace, and 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 pipe 90, and the hot-side forced exhaust pipe 90 is One end of the 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 hot side pipe of the second heat exchanger 30 32 is connected to 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 adjusting damper 901, which can also be provided in conjunction with the pipeline Two regulating dampers (not shown in the figure) are used to regulate the air volume of the hot side forced exhaust pipe 90 through the regulating dam The exhaust pipe 90 adjusts the air volume of the furnace 102 of the direct-fired incinerator (TO) 10, and delivers part of the burned high-temperature gas to the second hot side pipe 32 of the second heat exchanger 30 and the first The connection 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 the organic waste gas can be treated to prevent direct combustion incineration furnace (TO)10 will not overheat due to too high furnace temperature, or even cause shutdown.

In addition, the difference of the third implementation mode (as shown in Figure 3) is that a hot-side forced exhaust pipe 90 is provided in the furnace 102 of the direct-fired incinerator (TO) 10. One end of the pipeline 90 is connected to the hearth 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side forced exhaust pipeline 90 is connected to the outlet 12 of the direct-fired incinerator (TO) 10 The hot side forced exhaust pipeline 90 is provided with at least one regulating damper 901, and two regulating dampers (not shown in the figure) can also be provided in conjunction with the pipeline to control the hot side intensity through the regulating damper 901 The air volume of the 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, Part of the incineration high temperature gas is delivered to the outlet 12 of the direct-fired incinerator (TO) 10, so that the hot side forced exhaust pipe 90 has the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be treated , It can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, and even causing shutdown.

Based on the above detailed description, those who are familiar with this art 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

43: The third cold side conveying pipeline

60: Adsorption wheel

601: Adsorption Zone

602: Cooling Zone

603: Desorption Zone

61: Exhaust gas intake pipe

62: Clean gas discharge pipeline

63: Cooling gas intake pipe

64: Cooling gas delivery pipeline

65: Hot gas delivery pipeline

66: Desorption concentrated gas pipeline

80: Chimney

90: Hot side forced exhaust pipeline

901: Adjust the damper

Claims (8)

An energy-saving single-rotor high-concentration hot side-passing 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 The 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 provided 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 third cold-side pipeline One end of the side pipeline is connected; A third cold-side delivery pipeline, one end of the third cold-side delivery pipeline is connected to the other end of the third cold-side pipeline, and the other end of the third cold-side delivery pipeline is connected to the direct-fired The entrance connection of the incinerator (TO); An adsorption runner, the adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone, the adsorption runner system is connected with an exhaust gas intake pipeline, a clean gas discharge pipeline, a cooling gas intake pipeline, A cooling gas conveying pipeline, a hot gas conveying pipeline and a desorption concentrated gas pipeline, one end of the exhaust gas inlet pipeline is connected to one side of the adsorption zone of the adsorption rotor, and the clean gas discharge pipeline One end is connected with the other side of the adsorption zone of the adsorption runner, and one end of the cooling gas inlet pipe is connected with One side of the cooling zone of the adsorption runner is connected, one end of the cooling gas conveying pipeline is connected with the other side of the cooling zone of the adsorption runner, and the other end of the cooling gas conveying pipeline is connected with the second heat One end of the second cold side pipeline of the exchanger is connected, one end of the hot gas delivery pipeline is connected with the other side of the desorption zone of the adsorption runner, and the other end of the hot gas delivery pipeline is connected with the second heat The other end of the second cold side pipeline of the exchanger is connected, one end of the desorption concentrated gas pipeline is connected with one side of the desorption zone of the adsorption rotor, and the other end of the desorption concentrated gas pipeline is connected with One end of the first cold side pipeline of the first heat exchanger is connected; A chimney, the other end of the 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 furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced-exhaust pipeline is connected with the third heat exchanger The third hot-side pipeline is connected to the second hot-side pipeline of the second heat exchanger, and the hot-side forced exhaust pipeline is provided with at least one air-regulating damper. An energy-saving single-rotor high-concentration hot side-passing 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 The 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 provided 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 third cold-side pipeline One end of the side pipeline is connected; A third cold-side delivery pipeline, one end of the third cold-side delivery pipeline is connected to the other end of the third cold-side pipeline, and the other end of the third cold-side delivery pipeline is connected to the direct-fired The entrance connection of the incinerator (TO); An adsorption runner, the adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone, the adsorption runner system is connected with an exhaust gas intake pipeline, a clean gas discharge pipeline, a cooling gas intake pipeline, A cooling gas conveying pipeline, a hot gas conveying pipeline and a desorption concentrated gas pipeline, one end of the exhaust gas inlet pipeline is connected to one side of the adsorption zone of the adsorption rotor, and the clean gas discharge pipeline One end is connected with the other side of the adsorption zone of the adsorption runner, one end of the cooling gas inlet pipe is connected with one side of the cooling zone of the adsorption runner, and one end of the cooling gas delivery pipeline is connected with the The other side of the cooling zone of the adsorption runner is connected, the other end of the cooling gas delivery pipeline is connected to one end of the second cold side pipeline of the second heat exchanger, and one end of the hot gas delivery pipeline is connected to the The other side of the desorption zone of the adsorption runner is connected, the other end of the 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 desorption concentrated gas pipeline Is connected to one side of the desorption zone of the adsorption runner, and the other end of the desorption concentrated gas pipeline is connected to one end of the first cold side pipeline of the first heat exchanger; A chimney, the other end of the 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 furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced-exhaust pipeline is connected with the second heat exchanger The second hot-side pipeline is connected to the first hot-side pipeline of the first heat exchanger, and the hot-side forced exhaust pipeline is At least one adjusting damper is provided. An energy-saving single-rotor high-concentration hot side-passing 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 The 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 provided 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 third cold-side pipeline One end of the side pipeline is connected; A third cold-side delivery pipeline, one end of the third cold-side delivery pipeline is connected to the other end of the third cold-side pipeline, and the other end of the third cold-side delivery pipeline is connected to the direct-fired The entrance connection of the incinerator (TO); An adsorption runner, the adsorption runner system is provided with an adsorption zone, a cooling zone and a desorption zone, the adsorption runner system is connected with an exhaust gas intake pipeline, a clean gas discharge pipeline, a cooling gas intake pipeline, A cooling gas conveying pipeline, a hot gas conveying pipeline and a desorption concentrated gas pipeline, one end of the exhaust gas inlet pipeline is connected to one side of the adsorption zone of the adsorption rotor, and the clean gas discharge pipeline One end is connected with the other side of the adsorption zone of the adsorption runner, and one end of the cooling gas inlet pipe is connected with One side of the cooling zone of the adsorption runner is connected, one end of the cooling gas conveying pipeline is connected with the other side of the cooling zone of the adsorption runner, and the other end of the cooling gas conveying pipeline is connected with the second heat One end of the second cold side pipeline of the exchanger is connected, one end of the hot gas delivery pipeline is connected with the other side of the desorption zone of the adsorption runner, and the other end of the hot gas delivery pipeline is connected with the second heat The other end of the second cold side pipeline of the exchanger is connected, one end of the desorption concentrated gas pipeline is connected with one side of the desorption zone of the adsorption rotor, and the other end of the desorption concentrated gas pipeline is connected with One end of the first cold side pipeline of the first heat exchanger is connected; A chimney, the other end of the 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 furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced-exhaust pipeline is connected with the direct-fired incinerator (TO) outlet connection, the hot side forced exhaust pipeline is provided with at least one regulating damper. As described in item 1, 2 or 3 of the scope of patent application, the energy-saving single-rotor high-concentration hot side-pass temperature control system, wherein the outlet of the direct-fired incinerator (TO) is further connected to the chimney. As described in item 1, 2 or 3 of the scope of patent application, the energy-saving single-rotor high-concentration hot side passage temperature control system, wherein the cooling air intake pipeline is further supplied with fresh air or external air . As described in item 1, 2 or 3 of the scope of patent application, the energy-saving single-rotor high-concentration hot side-pass temperature control system, wherein the exhaust gas intake pipeline system is further provided with an exhaust gas communication pipeline, the exhaust gas communication pipeline The system is connected with the cooling gas intake 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. As described in item 1, 2 or 3 of the scope of patent application, the energy-saving single-rotor high-concentration hot side-pass temperature control system, wherein the desorption concentrated gas pipeline system is further provided with a fan. As described in item 1, 2 or 3 of the scope of patent application, the energy-saving single-rotor high-concentration hot side pass temperature control system, wherein the clean air discharge pipeline is further provided with a fan.

Images