TWM606289U - Energy-saving type hot side bypass temperature control system with dual runners - Google Patents

Abstract

This creation is an energy-saving dual-rotor 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 exchanger, and a second heat exchange , A third heat exchanger, a first cold-side conveying pipeline, a first adsorption runner, a second adsorption runner and a chimney, and pass through the furnace system of the direct-fired incinerator (TO) A hot-side forced-exhaust pipeline is provided, and the other end of the hot-side forced-exhaust pipeline is between the third hot-side pipeline of the third heat exchanger and the second hot-side pipeline of the second heat exchanger Between the connection point, or the connection point between the second hot side pipe of the second heat exchanger and the first hot side pipe of the first heat exchanger, or the first heat pipe of the first heat exchanger The side pipe is connected to the third hot side pipe of the third heat exchanger, or connected to any one of the outlets of the direct-fired incinerator (TO), whereby when the volatile organic compounds When the concentration of (VOCs) becomes higher, the air volume in the furnace of the direct-fired incinerator (TO) can be adjusted through the hot side forced exhaust pipeline to have the effect of adjusting the heat recovery or concentration, so that the organic waste gas can be treated , 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 runner hot side passing temperature control system

This creation is about an energy-saving dual-wheel hot side-passing temperature control system, especially when the concentration of volatile organic compounds (VOCs) becomes high, it can adjust the heat recovery or concentration, so that the organic waste gas can be During the treatment, 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 treatment in the semiconductor industry, optoelectronic industry or chemical-related industries 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 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 dual-wheel hot-side passage temperature control system that can improve the efficiency of organic waste gas treatment, so that users can easily operate and assemble. , In order to provide user convenience, the creative motivation for the creators to develop.

The main purpose of this creation is to provide an energy-saving dual-rotor hot-side passing temperature control system, which is mainly used in organic waste gas treatment systems, and is equipped with a direct combustion incinerator (TO), a first heat exchanger, A second heat exchanger, a third heat exchanger, a first cold-side conveying pipeline, a first adsorption runner, a second adsorption runner and a chimney are passed through the direct-fired incinerator ( TO) the furnace is provided with a hot-side forced-exhaust pipeline, and the other end of the hot-side forced-exhaust pipeline is connected with the third hot-side pipeline of the third heat exchanger and the second heat exchanger The connection between the hot-side pipes, or the connection between the second hot-side pipe of the second heat exchanger and the first hot-side pipe of the first heat exchanger, or the first heat exchange The connection between the first hot-side pipeline of the heat exchanger and the third hot-side pipeline of the third heat exchanger, or any one of the outlets of the direct-fired incinerator (TO), thereby, When the concentration of volatile organic compounds (VOCs) becomes higher, the air volume of the direct-fired incinerator (TO) can be adjusted through the hot-side forced exhaust pipeline to have 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 shutdowns, thereby increasing the overall practicability.

Another purpose of this creation is to provide an energy-saving dual-rotor hot-side passing temperature control system, by arranging at least one regulating damper on the hot-side forced-exhaust pipeline, and the other One end is connected between 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 pipe of the second heat exchanger The connection between the first hot-side pipe of the first heat exchanger, or between the first hot-side pipe of the first heat exchanger and the third hot-side pipe of the third heat exchanger The connection point, or any one of the outlets of the direct-fired incinerator (TO), so that when the concentration of volatile organic compounds (VOCs) becomes high, the direct-fired exhaust pipe can be used to adjust the direct The amount of air in the furnace of the TO The burned high-temperature gas is transported to the connection of the hot-side pipelines of different heat exchangers, so that the hot-side forced exhaust pipeline has the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can prevent direct combustion during processing The type 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: burner

102: Hearth

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 delivery pipeline

30: second heat exchanger

31: The second cold side pipeline

32: The second hot side pipeline

40: third heat exchanger

41: The third cold side pipeline

42: The third hot side 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 connection pipeline

6211: The first clean air connection control valve

63: The first cooling air intake line

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 side forced exhaust pipeline

901: Adjust the damper

Figure 1 is a schematic diagram of a system architecture with a hot-side forced-exhaust pipeline in the first embodiment of the creation of the first heat exchanger installed beside the second heat exchanger.

Figure 2 is a schematic diagram of a system architecture with a hot-side forced-exhaust pipeline in the second embodiment of the creation of the first heat exchanger arranged beside the second heat exchanger.

Figure 3 is a schematic diagram of a system architecture with a hot-side forced-exhaust pipeline in a third embodiment in which the first heat exchanger is arranged beside the second heat exchanger.

Figure 4 is a schematic diagram of a system architecture with a hot-side forced-exhaust pipeline in the fourth embodiment of the creation of the first heat exchanger installed beside the third heat exchanger.

Figure 5 is a schematic diagram of the system architecture with the hot-side forced-exhaust pipeline in the first embodiment of the creation of the first heat exchanger installed beside the third heat exchanger.

Figure 6 is a schematic diagram of the system architecture with the hot-side forced-exhaust pipeline in the third embodiment of the creation of the first heat exchanger installed beside the third heat exchanger.

Please refer to Figures 1 to 6, which are schematic diagrams of this creative embodiment. The best implementation of the energy-saving dual-wheel hot-side passage 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 ( When the concentration of VOCs becomes higher, it can adjust the heat recovery amount 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 The situation that caused the downtime occurred.

And the energy-saving dual-wheel hot side pass temperature control system of the implementation framework of this creation mainly includes a direct-fired incinerator (TO) 10, a first heat exchanger 20, a second heat exchanger 30, The combined design of a third heat exchanger 40, a first cold side conveying pipeline 23, a first adsorption runner 60, a second adsorption runner 70 and a chimney 80 (as shown in Figures 1 to 6 Show), wherein the first heat exchanger 20 is provided with a first cold side pipeline 21 and a first hot side pipeline 22, and the second heat exchanger 30 is provided with a second cold side pipeline 31 and a second The 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 4) 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 the outlet 12 is 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 to It has the effect of saving energy.

And the above-mentioned first heat exchanger 20 has two embodiments. The first embodiment is to install the first heat exchanger 20 beside the second heat exchanger 30 (as shown in Figures 1 and 2). And shown in Figure 3), so that the burner head 101 of the direct-fired incinerator (TO) 10 can firstly deliver the high-temperature gas after incineration to the third hot-side pipe 42 of the third heat exchanger 40 One side is used for heat exchange, and the other side of the third hot side pipe 42 of the third heat exchanger 40 transports the incineration high temperature gas to the second hot side of the second heat exchanger 30 One side of the pipe 32 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 incineration high temperature gas to the first heat exchanger 20 One side of the first hot side pipe 22 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 (such as the first As shown in Figures, Figures 2 and 3), 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 Figure 4, Figure 5 and Figure 6), so that the direct combustion type The burner head 101 of the incinerator (TO) 10 is capable of transporting the incineration high-temperature gas to one side of the first hot-side pipe 22 of the first heat exchanger 20 for heat exchange, and the first heat The other side of the first hot-side pipe 22 of the heat exchanger 20 transports 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 is used to transport the incineration high-temperature gas to one side of the second hot-side pipe 32 of the second heat exchanger 30 for heating Exchange, and then the other side of the second hot side pipeline 32 of the second heat exchanger 30 will heat the incineration high temperature The gas is transported to the outlet 12 of the furnace 102 (as shown in FIGS. 4, 5 and 6), and then transported from the outlet 12 of the furnace 102 to the chimney 80 to be discharged 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. Road 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 6) 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 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 a zeolite concentration runner or a concentration runner 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 6). In addition, the other side of the adsorption zone 701 of the second adsorption rotor 70 is connected to the second clean air discharge pipeline 71 to pass the second clean air The other end of the exhaust pipe 71 is connected to the chimney 80, and the second clean air exhaust pipe 71 is provided with a fan 711 (as shown in Figures 2 and 3), which enables the fan 711 to The adsorbed gas in the second clean gas exhaust pipeline 71 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 gas to enter the cooling zone 602 of the first adsorption runner 60 for cooling purposes (such as 1 to 6), 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, 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 1 to 6), and further, one end of the first hot gas conveying pipe 65 is connected to the other side of the desorption zone 603 of the first adsorption rotor 60, and The other end of the first hot gas conveying pipe 65 is connected to the other end of the third cold side pipe 41 of the third heat exchanger 40, so that the high temperature hot gas that is heat exchanged through the third heat exchanger 40 can be transferred. It is transported to the desorption zone 603 of the first adsorption rotor 60 through the first hot gas transport pipeline 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 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. The path 63 is connected (as shown in Figs. 2 and 6), so that 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 pipe 611 For cooling use, the exhaust gas communication pipeline 611 is also 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 (such as 1 to 6), 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, 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 1 to 6). Furthermore, one end of the second hot gas conveying pipe 74 is connected to the other side of the desorption zone 703 of the second adsorption rotor 70, and The other end of the second hot gas 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 transfer the high temperature hot gas that undergoes heat exchange through the second heat exchanger 30 It is transported to the desorption zone 703 of the second adsorption rotor 70 through the second hot gas transport 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 gas discharge pipeline 62 is provided with a first clean gas communication pipeline 621, and the other end of the first clean gas communication pipeline 621 is connected to the second clean gas The cooling air intake pipe 72 is connected (as shown in Figures 2, 5, and 6), so that the first clean air can be discharged through the first clean air communication line 621. The gas is delivered to the cooling zone 702 of the second adsorption runner 70 for cooling. In addition, the first clean gas communication pipeline 621 is provided with a first clean gas communication control valve 6211 to control the first clean gas communication pipe The wind volume of road 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 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 1 to 6) to be able to remove the high temperature The attached desorbed concentrated gas can pass through the first desorbed concentrated gas pipe 66 to be transported to one end of the first cold side pipe 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 1 to 6), 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. Way, and the first embodiment is the second desorption concentrated gas pipeline The other end of 75 is connected to the exhaust gas inlet pipe 61 (as shown in Figure 1, Figure 2 and Figure 6), so that the concentrated gas can enter the first exhaust gas inlet pipe 61 through the exhaust gas inlet pipe 61. In the adsorption zone 601 of a adsorption wheel 60 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 3, 4 and 5) ), so that the concentrated gas can enter the cooling zone 602 of the first adsorption rotor 60 through the first cooling gas inlet pipe 63 for cooling. Furthermore, the second desorption concentrated gas pipeline 75 is provided with a fan 751 (as shown in Figs. 3 and 5) to push and pull the desorbed concentrated gas into 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 energy-saving dual-wheel hot side pass temperature control system of this creation mainly has four implementation modes. Among the four 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 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 incinerator (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 contents of the second adsorption runner 70 and chimney 80 are not repeated, please refer to the above description.

The difference in the first implementation (as shown in Figures 1 and 5) is that a hot-side forced exhaust pipe 90 is provided in the furnace 102 of the direct-fired incinerator (TO) 10, and the heat One end of the side forced exhaust pipe 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and No matter if the first heat exchanger 20 is arranged beside the second heat exchanger 30 (as shown in Figure 1) or the first heat exchanger 20 is arranged beside the third heat exchanger 40 (as shown in Figure 5) Shown), the other end of the hot-side forced exhaust pipe 90 is connected to the third hot-side pipe 42 of the third heat exchanger 40 and the second hot-side pipe 32 of the second heat exchanger 30 At least one regulating damper 901 is provided in the hot-side forced exhaust pipeline 90, and two regulating dampers (not shown in the figure) can also be provided in conjunction with the pipeline to control through the regulating damper 901 The air volume of the hot-side forced exhaust pipe 90, therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the furnace of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side forced exhaust pipe 90 102 air volume, and transport part of the high-temperature gas burned 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, Let the hot-side forced exhaust pipe 90 have the effect of adjusting the heat recovery amount or concentration, so that when the organic waste gas is processed, it can prevent the direct-fired incinerator (TO) 10 from overheating due to the high temperature of the furnace , And even lead to downtime.

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 equipped with a hot-side forced exhaust pipe 90, and the hot-side forced exhaust pipe 90 When one end of the pipe 90 is connected to the hearth 102 of the direct-fired incinerator (TO) 10, and the first heat exchanger 20 is arranged next to the second heat exchanger 30 (as shown in Figure 2), The other end of the hot-side forced exhaust pipe 90 is connected to the connection between the second hot-side pipe 32 of the second heat exchanger 30 and the first hot-side pipe 22 of the first heat exchanger 20, 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 forced exhaust through the regulating damper 901 The air volume of the pipe 90, therefore, when the concentration of volatile organic compounds (VOCs) becomes high, it can pass through the hot side for strong exhaust The pipeline 90 adjusts the air volume of the furnace 102 of the direct-fired incinerator (TO) 10, and delivers part of the incineration high-temperature gas to the second hot-side pipeline 32 of the second heat exchanger 30 and the first The connection between the first hot-side pipeline 22 of the heat exchanger 20 allows the hot-side forced exhaust pipeline 90 to have the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be prevented from the direct-fired incinerator during processing. (TO)10 will not over-temperature due to too high furnace temperature, and even cause shutdown.

In addition, the difference of the third implementation mode (as shown in Figures 3 and 6) is that the furnace 102 of the direct-fired incinerator (TO) 10 is equipped with a hot-side forced exhaust pipe 90. One end of the hot side forced exhaust pipe 90 is connected to the hearth 102 of the direct-fired incinerator (TO) 10, regardless of the first heat exchanger 20 being arranged next to the second heat exchanger 30 (as shown in Figure 3) Shown) or when the first heat exchanger 20 is arranged next to the third heat exchanger 40 (as shown in Figure 6), the other end of the hot side forced exhaust pipe 90 is connected to the direct combustion incinerator The outlet 12 of the furnace (TO) 10 is connected, in which the hot side forced exhaust pipe 90 is provided with at least one adjusting damper 901, or two adjusting damper (not shown) can be provided in conjunction with the pipe to pass the The damper 901 is adjusted to regulate the air volume of the hot side forced exhaust pipe 90. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the direct-fired incinerator can be adjusted through the hot side forced exhaust pipe 90 ( TO) 10 the air volume of the furnace 102, and transport part of the incineration high-temperature gas to the outlet 12 of the direct-fired incinerator (TO) 10, so that the hot side forced exhaust pipe 90 can adjust the heat recovery amount or concentration The efficiency of the organic waste gas treatment 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 fourth implementation mode (as shown in Figure 4) is that the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipe 90, and the hot-side forced exhaust pipe 90 One end of the pipeline 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and when the first When the heat exchanger 20 is arranged next to the third heat exchanger 40 (as shown in Figure 4), the other end of the hot side forced exhaust pipe 90 is connected to the first hot side of the first heat exchanger 20 The pipeline 22 is connected to the third hot-side pipeline 42 of the third heat exchanger 40, wherein the hot-side forced exhaust pipeline 90 is provided with at least one adjusting damper 901, which can also be used in conjunction with the pipeline Two regulating dampers (not shown) are provided to regulate the air volume of the hot side forced exhaust pipe 90 through the regulating dam 901. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the heat can be transmitted The side forced 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 first hot side pipe 22 and the first heat exchanger 20 of the first heat exchanger 20 The connection between the third hot-side pipes 42 of the third heat exchanger 40 allows the hot-side forced exhaust pipe 90 to adjust the heat recovery amount or concentration, so that the organic waste gas can prevent direct combustion during treatment The type incinerator (TO) 10 will not overheat due to the high temperature of the furnace, and even cause 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: burner

102: Hearth

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 delivery pipeline

30: second heat exchanger

31: The second cold side pipeline

32: The second hot side pipeline

40: third heat exchanger

41: The third cold side pipeline

42: The third hot side 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 line

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 side forced exhaust pipeline

901: Adjust the damper

Claims (14)

An energy-saving dual-rotor hot side passage 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, and the direct-fired incinerator (TO) has 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 provided 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 combustion type 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 first adsorption runner system is connected with an exhaust gas intake 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, one end of the first cooling gas delivery pipeline is connected to the other side of the cooling zone of the first adsorption runner, the first cooling gas delivery pipeline The other end of the third One end of the third cold side pipeline of the heat exchanger is connected, one end of the first hot gas delivery 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 delivery pipeline One end is connected to the other end of the third cold side pipeline of the third heat exchanger, and one end of the first desorption concentrated gas pipeline is connected to one side of the desorption zone of the first adsorption runner. 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 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 air discharge pipeline and a second cooling air intake 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 second adsorption runner On one side of the adsorption zone, 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 the second adsorption One side of the cooling zone of the runner is connected, one end of the second cooling gas delivery pipeline is connected with 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 with One end of the second cold side pipeline of the second heat exchanger is connected, one end of the second hot gas delivery pipeline is connected to the other side of the desorption zone of the second adsorption runner, the second hot gas delivery pipe The other end of the path 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 one side of the desorption zone of the second adsorption runner connection; A chimney, the other end of the second clean gas discharge pipeline is connected to the chimney; and A hot-side forced-exhaust pipeline, one end of the hot-side forced-exhaust pipeline is connected to the 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 with 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 dual-rotor hot side passage 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, and the direct-fired incinerator (TO) has 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 provided 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 combustion type 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 first adsorption runner system is connected with an exhaust gas intake 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, one end of the first cooling gas delivery pipeline is connected to the other side of the cooling zone of the first adsorption runner, the first cooling gas delivery pipeline The other end 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 is connected, the other end of the first hot gas conveying pipe is connected with the other end of the third cold side pipe of the third heat exchanger, and the first desorption One end of the concentrated gas pipeline is connected to one side of the desorption zone of the first adsorption rotor, and the other end of the first concentrated gas pipeline is connected to the first cold side tube of the first heat exchanger One end of the road 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 air discharge pipeline and a second cooling air intake 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 second adsorption runner On one side of the adsorption zone, 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 the second adsorption One side of the cooling zone of the runner is connected, one end of the second cooling gas delivery pipeline is connected with 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 with One end of the second cold side pipeline of the second heat exchanger is connected, one end of the second hot gas delivery pipeline is connected to the other side of the desorption zone of the second adsorption runner, the second hot gas delivery pipe The other end of the path 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 one side of the desorption zone of the second adsorption runner connection; A chimney, the other end of the second clean gas discharge pipeline is connected to the chimney; and A hot-side forced-exhaust pipeline, one end of the hot-side forced-exhaust pipeline is connected to the 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 with the first hot-side pipeline of the first heat exchanger, and the hot-side forced exhaust pipeline is provided with at least one air-regulating damper. An energy-saving dual-rotor hot side passage 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, and the direct-fired incinerator (TO) has 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 provided 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 combustion type 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 first adsorption runner system is connected with an exhaust gas intake 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, one end of the first cooling gas delivery pipeline is connected to the other side of the cooling zone of the first adsorption runner, the first cooling gas delivery pipeline The other end 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 other end of the first hot gas 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 to one side of the desorption zone of the first adsorption runner, and the first The other end of a 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 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 air discharge pipeline and a second cooling air intake 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 second adsorption runner On one side of the adsorption zone, 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 the second adsorption One side of the cooling zone of the runner is connected, one end of the second cooling gas delivery pipeline is connected with 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 with One end of the second cold side pipeline of the second heat exchanger is connected, one end of the second hot gas delivery pipeline is connected to the other side of the desorption zone of the second adsorption runner, the second hot gas delivery pipe The other end of the path 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 one side of the desorption zone of the second adsorption runner connection; A chimney, the other end of the second clean gas discharge pipeline is connected to the chimney; and A hot-side forced-exhaust pipeline, one end of the hot-side forced-exhaust pipeline is connected to the 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 equipped with at least one regulating damper. An energy-saving dual-rotor hot side passage 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, and the direct-fired incinerator (TO) has an entrance and Exit, the entrance Is located at the furnace head, and the outlet is located 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 provided 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 combustion type 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 first adsorption runner system is connected with an exhaust gas intake 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, one end of the first cooling gas delivery pipeline is connected to the other side of the cooling zone of the first adsorption runner, the first cooling gas delivery pipeline The other end 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 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 one end of the first desorption concentrated gas pipeline is connected to the desorption rotor of the first adsorption rotor. Attached to one side of the zone, the first desorption concentration The other end of the shrinking gas pipeline is connected with one end of the first cold side pipeline of the first heat exchanger; 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 air discharge pipeline and a second cooling air intake 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 second adsorption runner On one side of the adsorption zone, 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 the second adsorption One side of the cooling zone of the runner is connected, one end of the second cooling gas delivery pipeline is connected with 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 with One end of the second cold side pipeline of the second heat exchanger is connected, one end of the second hot gas delivery pipeline is connected to the other side of the desorption zone of the second adsorption runner, the second hot gas delivery pipe The other end of the path 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 one side of the desorption zone of the second adsorption runner connection; A chimney, the other end of the second clean gas discharge pipeline is connected to the chimney; and A hot-side forced-exhaust pipeline, one end of the hot-side forced-exhaust pipeline is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced exhaust pipeline is connected with the first heat exchanger The first hot-side pipeline is connected with the third hot-side pipeline of the third heat exchanger, and the hot-side forced exhaust pipeline is provided with at least one air regulating damper. As described in item 1, 2, 3 or 4 of the scope of patent application, the energy-saving dual runner 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, 3 or 4 of the scope of patent application, the energy-saving dual runner hot-side passing temperature control system, wherein the first cooling air intake pipe system is further supplied with 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-rotor hot-side passing temperature control system, wherein the second cooling air intake line is further supplied with fresh air or external air enter. As described in item 1, 2, 3, or 4 of the scope of patent application, the energy-saving dual runner hot side passage temperature control system, wherein the exhaust gas intake pipeline system is further provided with an exhaust gas communication pipeline, the exhaust gas communication pipeline It is connected with the first 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. For example, the energy-saving dual runner hot side pass temperature control system described in item 1, 2, 3 or 4 of the scope of patent application, wherein the first clean air discharge pipeline is further provided with a first clean air communication pipeline, The first clean gas communication pipeline is connected to the second cooling gas intake pipeline, and the first clean gas communication pipeline is further provided with a first clean gas communication control valve to control the first clean gas communication pipe The air volume of the road. As described in item 1, 2, 3 or 4 of the scope of patent application, the energy-saving dual runner hot side passing temperature control system, wherein the first desorption concentrated gas 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 runner hot side passing temperature control system, wherein the second desorption concentrated gas 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 runner hot side passing temperature control system, 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 runner hot-side passing temperature control system, wherein the other end of the second desorption concentrated gas pipeline is further connected to the exhaust gas inlet pipe Road phase connection. As described in item 1, 2, 3, or 4 of the scope of patent application, the energy-saving dual runner hot side passing temperature control system, wherein the other end of the second desorption concentrated gas pipeline is further connected with the first cooling gas The intake pipe is connected.

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