TW202217195A - Energy-saving single runner hot-side bypass temperature control system and method which can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature when the organic waste gas is treated - Google Patents

Abstract

The present invention relates to an energy-saving single runner hot-side bypass temperature control system and method thereof, mainly used in an organic waste gas treatment system. The energy-saving single runner hot-side bypass temperature control system includes a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a first cold-side delivery pipe, an adsorption runner and a chimney. A hot-side forcible discharge pipe is disposed in the furnace of the direct-fired incinerator (TO). Further, the other end of the hot-side forcible discharge pipe is connected with 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 connected to any place of the outlets of the direct-fired incinerator (TO). Thus, when the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace of the direct-fired incinerator (TO) can be adjusted through the hot-side forcible discharge pipe so as to have the effect of adjusting the amount or concentration of heat recovery. When the organic waste gas is treated, it can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature and even leading to shutdown. The direct-fired incinerator includes a burner head and a furnace. The burner head and the furnace are connected with each other. The direct-fired incinerator has an inlet and an outlet. The inlet is disposed at the burner head and the outlet is disposed at the furnace. The first heat exchanger is disposed in the direct-fired incinerator and has a first cold-side pipe and a first hot-side pipe. The second heat exchanger is disposed in the direct-fired incinerator and has a second cold-side pipe and a second hot-side pipe. One end of the first cold-side delivery pipe is connected to the other end of the first cold-side pipe, and the other end of the first cold-side delivery pipe is connected to the inlet of the direct-fired incinerator.

Description

Energy-saving single runner hot side bypass temperature control system and method

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

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

However, in recent years, both the central government and the local governments have attached great importance to air pollution, so they have formulated relevant air quality standards in the emission standards of chimneys, and will review them periodically in accordance with the development of international control trends.

Therefore, in view of the above deficiencies, the present inventor hopes to propose an energy-saving single-runner hot-side bypass temperature control system and method thereof, which can improve the efficiency of organic waste gas treatment, so that users can easily operate and assemble. The system is designed to provide user convenience and the motivation of the inventor to develop the invention.

The main purpose of the present invention is to provide an energy-saving single runner hot side bypass temperature control system and method thereof, which are mainly used in organic waste gas treatment systems, and are provided with a direct-fired incinerator (TO), a first heat Exchanger, a second heat exchanger, a first cold side conveying pipeline, an adsorption runner and a chimney, and a hot side strong exhaust pipeline is provided through the furnace of the direct-fired incinerator (TO) , and the other end of the hot-side strong discharge pipe is connected with the second hot-side pipe of the second heat exchanger and the first hot-side pipe of the first heat exchanger, or with the direct 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 direct-fired incinerator ( The air volume of the furnace of TO) has the effect of adjusting the amount of heat recovery or concentration, so that when the organic waste gas is treated, it can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature, and even Situations that lead to downtime occur, thereby increasing overall utility.

Another object of the present invention is to provide an energy-saving single runner hot side bypass temperature control system and method thereof. The other end of the road is connected with the second hot side pipe of the second heat exchanger and the first hot side pipe of the first heat exchanger, or with the direct-fired incinerator (TO). Any one of the outlets is connected, so that when the concentration of volatile organic compounds (VOCs) becomes higher, the air volume of the furnace chamber of the direct-fired incinerator (TO) can be adjusted through the hot-side strong exhaust pipe, and the part of the outlet can be adjusted. The high temperature gas of the incineration is transported to the connection of the hot side pipes of different heat exchangers, so that the hot side strong exhaust pipe has the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be prevented from being directly discharged during the treatment. The combustion type incinerator (TO) will not overheat due to too high furnace temperature, or even lead to shutdown, thereby increasing the overall usability, thereby increasing the overall usability.

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

10: Direct-fired incinerator (TO)

101: Stove

102: Hearth

11: Entrance

12: Export

20: 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: Second cold side pipeline

32: Second hot side piping

60: Adsorption runner

601: Adsorption zone

602: Cooling Zone

603: Desorption zone

61: Exhaust gas intake line

611: Exhaust gas communication line

6111: Exhaust gas communication control valve

62: Clean air discharge pipeline

621: Clean air connection pipeline

6211: Clean air connection control valve

63: Cooling air intake line

64: Cooling gas delivery pipeline

65: Hot gas delivery pipeline

66: Desorption concentrated gas pipeline

661: Fan

80: Chimney

90: Hot side strong discharge pipeline

901: Adjust the damper

S100: Input the gas to be adsorbed

S200: Input the gas to be adsorbed

S110: adsorption by the adsorption runner

S210: adsorption by the adsorption runner

S120: Input cooling gas

S220: Input cooling gas

S130: Transporting hot gas for desorption

S230: Transporting hot gas for desorption

S140: Desorption enriched gas delivery

S240: Delivery of Desorbed Concentrated Gas

S150: Gas delivery after incineration

S250: Gas delivery after incineration

S160: Adjustment of hot side forced discharge pipeline

S260: Hot Side Forced Discharge Pipeline Adjustment

S300: Input the gas to be adsorbed

S400: Input the gas to be adsorbed

S310: adsorption by the adsorption runner

S410: adsorption by the adsorption runner

S320: Input cooling gas

S420: Input cooling gas

S330: Transporting hot gas for desorption

S430: Transporting hot gas for desorption

S340: Desorption Concentrated Gas Delivery

S440: Desorption Concentrated Gas Delivery

S350: Gas delivery after incineration

S450: Gas delivery after incineration

S360: Hot Side Forced Discharge Pipeline Adjustment

S460: Hot Side Forced Discharge Pipeline Adjustment

Fig. 1 is a schematic diagram of the system structure of the first embodiment of the present invention, in which the first heat exchanger is arranged on the right side of the second heat exchanger and has a hot-side strong discharge pipeline.

Fig. 2 is a schematic diagram of the system structure of the second embodiment of the present invention, in which the first heat exchanger is arranged on the right side of the second heat exchanger and has a hot-side strong discharge pipeline.

Fig. 3 is a schematic diagram of the system structure of the first embodiment of the present invention, in which the first heat exchanger is disposed on the left side of the second heat exchanger and has a hot-side strong discharge pipeline.

FIG. 4 is a schematic diagram of the system structure of the second embodiment of the present invention, in which the first heat exchanger is disposed on the left side of the second heat exchanger and has a hot-side strong discharge pipeline.

FIG. 5 is a flow chart of the main steps of the first embodiment of the present invention.

FIG. 6 is a flow chart of the main steps of the second embodiment of the present invention.

FIG. 7 is a flow chart of the main steps of the third embodiment of the present invention.

FIG. 8 is a flow chart of the main steps of the fourth embodiment of the present invention.

Please refer to FIGS. 1 to 8, which are schematic diagrams of embodiments of the present invention, and the best embodiments of the energy-saving single-wheel hot-side bypass temperature control system and method thereof of the present invention are used in the semiconductor industry, the optoelectronic industry or the Volatile organic waste gas treatment systems or similar equipment in chemical-related industries, mainly when the concentration of volatile organic compounds (VOCs) increases, can adjust the amount of heat recovery or The effect of concentration can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature during the treatment of organic waste gas, and even lead to shutdown.

The energy-saving single-wheel hot-side bypass temperature control system of the present invention mainly includes a direct-fired incinerator (TO) 10, a first heat exchanger 20, a second heat exchanger 30, a first heat exchanger The combined design of the cold side conveying pipeline 23, an adsorption runner 60 and a chimney 80 (as shown in Figures 1 to 4), wherein the first heat exchanger 20 is provided with a first cold side pipeline 21 and the first hot side pipeline 22 , the second heat exchanger 30 is provided with a second cold side pipeline 31 and a second hot side pipeline 32 . In addition, the direct-fired incinerator (TO) 10 is provided with a burner head 101 and a furnace chamber 102, the burner head 101 is communicated with the furnace chamber 102, and the first heat exchanger 20 and the second heat exchanger 30 are connected with each other. They are respectively installed in the direct-fired incinerator (TO) 10, and the direct-fired incinerator (TO) 10 is provided with an inlet 11 and an outlet 12 (as shown in Figures 1 to 4), 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 set at the furnace chamber 102, The outlet 12 is connected to the chimney 80 , thereby, the organic waste gas can enter the burner 101 through the inlet 11 for combustion, and the burned gas can pass through the hearth 102 and pass through the outlet 12 to be discharged to the chimney 80 for discharge, so as to have the effect of saving energy.

And the above-mentioned first heat exchanger 20 has two embodiments, wherein the first embodiment is to set the first heat exchanger 20 on the right side of the second heat exchanger 30 (as shown in FIG. 1 and FIG. 2 ). shown), so that the burner head 101 of the direct-fired incinerator (TO) 10 can firstly transport the incinerated high-temperature gas to one side of the second hot-side pipeline 32 of the second heat exchanger 30 for heat exchange, and then by the second heat exchanger 30 of the second hot side pipe The incinerated high temperature gas is transported to one side of the first hot side pipeline 22 of the first heat exchanger 20 for heat exchange, and finally the first hot side pipeline of the first heat exchanger 20 22 to be transported to the outlet 12 of the furnace 102 (as shown in Figures 1 and 2), and then transported to the chimney 80 from the outlet 12 of the furnace 102 to be discharged through the chimney 80.

Furthermore, another second embodiment is to set the first heat exchanger 20 on the left side of the third heat exchanger 40 (as shown in Fig. 3 and Fig. 4 ), so that the direct-fired incinerator (TO ) The burner 101 of 10 is capable of transporting the incinerated high-temperature gas to one side of the first hot-side pipeline 22 of the first heat exchanger 20 for heat exchange, and is passed through the first heat exchanger 20. The other side of the first hot side pipeline 22 is used to transport the incinerated high-temperature gas to one side of the second hot side pipeline 32 of the second heat exchanger 30 for heat exchange. The other side of the second hot-side pipeline 32 of the heat exchanger 30 is used to transport the incinerated high-temperature gas to the outlet 12 of the furnace 102 (as shown in Figures 3 and 4), and then the furnace 102 The outlet 12 is conveyed to the chimney 80 for discharge through the chimney 80 .

In addition, the adsorption runner 60 of the present invention is provided with an adsorption zone 601, a cooling zone 602 and a desorption zone 603, and the adsorption runner 60 is connected with an exhaust gas intake pipe 61, a clean air discharge pipe 62, and a cooling gas Intake pipeline 63, a cooling gas delivery pipeline 64, a hot gas delivery pipeline 65 and a desorption concentrated gas pipeline 66, (as shown in Figs. 1 to 4). The adsorption wheel 60 is a zeolite concentration wheel or a concentration wheel made of other materials.

One end of the exhaust gas intake pipeline 61 is connected to one side of the adsorption zone 601 of the adsorption rotor 60 , so that the exhaust gas intake pipeline 61 can transport the organic exhaust gas to the adsorption zone 601 of the adsorption rotor 60 . one side, and one end of the clean air discharge pipe 62 is connected to the The other side of the adsorption zone 601 of the adsorption wheel 60 is connected, the other end of the clean gas discharge pipeline 62 is connected to the chimney 80, and the clean gas discharge pipeline 62 is provided with a fan 621 (as shown in Fig. 2 and As shown in FIG. 4 ), through the fan 621 , the adsorbed gas in the clean air exhaust line 62 can be pushed and pulled into the chimney 80 for discharge.

In addition, one side of the cooling zone 602 of the adsorption wheel 60 is connected to the cooling gas inlet pipeline 63 for the gas to enter the cooling zone 602 of the adsorption wheel 60 for cooling (as shown in Figs. 1 to 4). shown), and the other side of the cooling zone 602 of the adsorption runner 60 is connected to one end of the cooling gas delivery pipeline 64, and the other end of the cooling gas delivery pipeline 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 runner 60 into the second heat exchanger 30 for heat exchange (as shown in FIG. 1 to FIG. 4 ). ), and further, one end of the hot gas conveying line 65 is connected to the other side of the desorption zone 603 of the adsorption wheel 60, and the other end of the hot gas conveying line 65 is connected to the second heat exchanger 30 The other end of the second cold side pipeline 31 is connected, so that the high-temperature hot gas for heat exchange through the second heat exchanger 30 can be transported to the desorption zone 603 of the adsorption runner 60 through the hot gas transport pipeline 65 for desorption.

The above-mentioned cooling zone 602 of the adsorption wheel 60 is provided with two embodiments. The first embodiment is that the cooling gas intake pipe 63 connected to one side of the cooling zone 602 of the adsorption wheel 60 is For the entry of fresh air or outside air (as shown in FIG. 1 ), the cooling zone 602 of the adsorption wheel 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 FIG. 2 and 4), so that the exhaust gas intake line 6 can pass through the exhaust gas communication line 611 The waste gas in 1 is sent to the cooling zone 602 of the adsorption runner 60 for cooling use. In addition, the waste gas communication line 611 is provided with an waste gas communication control valve 6111 to control the air volume of the waste gas communication line 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, wherein 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 side pipeline 23 is connected to one end of the first cold side pipeline 23. The other end of the side conveying pipeline 23 is connected to the inlet 11 of the direct-fired incinerator (TO) 10, so that the desorbed concentrated gas desorbed by the high temperature can pass through the desorbed concentrated gas pipeline 66. It is transported to one end of the first cold side pipeline 21 of the first heat exchanger 20, and is transported to the direct-fired incinerator from the other end of the first cold side pipeline 21 of the first heat exchanger 20 In the inlet 11 of the (TO) 10 (as shown in Figures 1 to 4), the burner head 101 of the direct-fired incinerator (TO) 10 can be pyrolyzed to reduce volatile organic compounds . In addition, the desorption concentrated gas pipeline 66 is provided with a fan 661 to push and pull the desorption concentrated gas into one end of the first cold side pipeline 21 of the first heat exchanger 20 .

Furthermore, the energy-saving single-wheel hot-side bypass temperature control system of the present invention mainly has two implementations, and in the two implementations, the direct-fired incinerator (TO) 10, the first The first heat exchanger 20, the second heat exchanger 30, the first cold side conveying pipeline 23, the adsorption runner 60 and the chimney 80 are of the same design. Therefore, the above-mentioned direct-fired incinerator (TO) 10, the first The content of the first heat exchanger 20 , the second heat exchanger 30 , the first cold side conveying pipeline 23 , the adsorption runner 60 and the chimney 80 will not be repeated, please refer to the above description.

The difference between the first implementation (as shown in Figures 1 and 3) is that The furnace chamber 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side strong exhaust pipe 90 , and one end of the hot-side strong exhaust pipe 90 is connected to the furnace chamber 102 of the direct-fired incinerator (TO) 10 connection, regardless of whether the first heat exchanger 20 is located to the right of the second heat exchanger 30 (as shown in FIG. 1 ) or the first heat exchanger 20 is located to the left of the second heat exchanger 30 (as shown in FIG. 1 ) 3), the other end of the hot-side strong discharge pipe 90 is connected to the second hot-side pipe 32 of the second heat exchanger 30 and the first hot-side pipe of the first heat exchanger 20 The pipes 22 are connected at the connection point, wherein the hot-side strong exhaust pipe 90 is provided with at least one damper 901, and two dampers (not shown) can also be provided in conjunction with the pipe to pass the damper 901. 901 to regulate the air volume of the hot side strong exhaust pipe 90, therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the direct-fired incinerator (TO) can be adjusted through the hot side strong exhaust pipe 90 10 and the air volume of the furnace chamber 102, and part of the incinerated high-temperature gas is transported between the second hot side pipeline 32 of the second heat exchanger 30 and the first hot side pipeline 22 of the first heat exchanger 20 At the connection, the hot-side strong exhaust pipe 90 has the effect of adjusting the amount of heat recovery or concentration, so that when the organic waste gas is treated, it can prevent the direct-fired incinerator (TO) 10 from occurring due to too high furnace temperature. The phenomenon of temperature, and even lead to downtime.

In addition, the difference of the second embodiment (as shown in FIG. 2 and FIG. 4 ) is that the furnace chamber 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side strong exhaust pipe 90 . One end of the side strong exhaust pipe 90 is connected with the furnace chamber 102 of the direct-fired incinerator (TO) 10, regardless of whether the first heat exchanger 20 is located on the right side of the second heat exchanger 30 (as shown in FIG. 2 ). shown) or when the first heat exchanger 20 is located on the left side of the second heat exchanger 30 (as shown in FIG. 4 ), the other end of the hot-side strong exhaust pipe 90 is connected to the direct-fired incinerator (TO) 10 is connected to the outlet 12, wherein the hot-side strong exhaust pipe 90 is provided with at least one regulating damper 901, which can also be matched with The pipeline is provided with two dampers (not shown), so that the air volume of the hot-side strong exhaust pipeline 90 can be regulated through the damper 901. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, The air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side strong exhaust pipe 90, and part of the incinerated high-temperature gas can be delivered to the outlet of the direct-fired incinerator (TO) 10 12, let the hot-side strong exhaust pipe 90 have the effect of adjusting the amount of heat recovery or concentration, so that when the organic waste gas is treated, it can prevent the direct-fired incinerator (TO) 10 from occurring due to too high furnace temperature. The phenomenon of temperature, and even lead to downtime.

The energy-saving single-wheel hot-side bypass temperature control method of the present invention is mainly used in an organic waste gas treatment system, and includes a direct-fired incinerator (TO) 10, a first heat exchanger 20, a first The combined design of two heat exchangers 30, a first cold side conveying pipeline 23, an adsorption runner 60 and a chimney 80 (as shown in Figs. 1 to 4), wherein the first heat exchanger 20 is a A first cold side pipeline 21 and a first hot side pipeline 22 are provided, and the second heat exchanger 30 is provided with a second cold side pipeline 31 and a second hot side pipeline 32, wherein the first cold side pipeline One end of the delivery pipeline 23 is connected to the other end of the first cold side pipeline 21 , and the other end of the first cold side delivery pipeline 23 is connected to the inlet 11 of the direct-fired incinerator (TO) 10 . In addition, the direct-fired incinerator (TO) 10 is provided with a burner head 101 and a furnace chamber 102, the burner head 101 is communicated with the furnace chamber 102, and the first heat exchanger 20 and the second heat exchanger 30 are connected with each other. They are respectively installed in the direct-fired incinerator (TO) 10, and the direct-fired incinerator (TO) 10 is provided with an inlet 11 and an outlet 12 (as shown in Figures 1 to 4), 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 set at the furnace chamber 102, And the outlet 12 is connected to the chimney 80 so that the organic waste gas can enter the burner 10 through the inlet 11 Combustion is carried out in 1, and then the burned gas can pass through the furnace 102 and be discharged from the outlet 12 to the chimney 80 for discharge, so as to have the effect of saving energy.

In addition, the adsorption runner 60 of the present invention is provided with an adsorption zone 601, a cooling zone 602 and a desorption zone 603, and the adsorption runner 60 is connected with an exhaust gas intake pipe 61, a clean air discharge pipe 62, and a cooling gas Intake pipeline 63, a cooling gas delivery pipeline 64, a hot gas delivery pipeline 65 and a desorption concentrated gas pipeline 66 (as shown in Figs. 1 to 4). The adsorption wheel 60 is a zeolite concentration wheel or a concentration wheel made of other materials.

The main steps of the control method (as shown in FIG. 5 ) include: step S100 inputting the gas to be adsorbed: passing the exhaust gas through the other end of the exhaust gas inlet pipe 61 and sending it into the adsorption area of the adsorption wheel 60 side of 601. After the above step S100 is completed, the next step S110 is performed.

In addition, in the next step S110, the adsorption wheel performs adsorption: after the adsorption is carried out through the adsorption zone 601 of the adsorption wheel 60, the gas after adsorption is passed through the other side of the adsorption zone 601 of the adsorption wheel 60 through the net The other end of the gas discharge line 62 is output. After the above step S110 is completed, the next step S120 is performed.

Wherein the other side of the adsorption area 601 of the adsorption wheel 60 in the above-mentioned step S110 is connected to the clean gas discharge pipeline 62 so as to be connected to the chimney 80 through the other end of the clean gas discharge pipeline 62, and the A fan 621 (as shown in Figures 2 and 4) is installed in the clean air discharge line 62, so that the adsorbed gas in the clean air discharge line 62 can be pushed and pulled to the chimney through the fan 621 80 for discharge.

In addition, the next step S120 is to input cooling gas: the cooling gas is sent to the cooling area 602 of the adsorption wheel 60 through the other end of the cooling gas inlet pipe 63 . After cooling, the cooling gas passing through the cooling zone 602 of the adsorption runner 60 is delivered to one end of the second cold side pipeline 31 of the second heat exchanger 30 through the other end of the cooling gas delivery pipeline 64 . After the above step S120 is completed, the next step S130 is performed.

The cooling area 602 of the adsorption wheel 60 in the above-mentioned step S120 has two implementations, wherein the first implementation is the cooling air intake pipe connected to one side of the cooling area 602 of the adsorption wheel 60 The passage 63 is for the entry of fresh air or outside air (as shown in FIG. 1 ), and the cooling zone 602 of the adsorption wheel 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 FIG. 2 and 4), so that the exhaust gas in the exhaust gas inlet pipe 61 can be transported to the cooling zone 602 of the adsorption runner 60 through the exhaust gas communication pipe 611 for cooling use, and the exhaust gas communication pipe 611 is provided with an exhaust gas communication control valve 6111 to control the air volume of the exhaust gas communication line 611 .

In addition, the next step S130 is to transport hot gas for desorption: the hot gas is transported to the adsorption runner 60 through the hot gas transport pipe 65 connected to the other end of the second cold side pipe 31 of the second heat exchanger 30 The desorption zone 603 is desorbed, and then the desorbed concentrated gas is sent to one end of the first cold side pipeline 21 of the first heat exchanger 20 through the other end of the desorbed concentrated gas pipeline 66 . After the above step S130 is completed, the next step S140 is performed.

The desorption concentrated gas pipeline 66 in the above-mentioned step S130 is provided with a fan 661 (as shown in FIG. 2 and FIG. 4 ), so that the desorption concentrated gas can be pushed and pulled into the first heat exchanger 20 . Inside the first cold side pipeline 21 .

In addition, in the next step S140, the desorbed and concentrated gas is transported: the desorbed and concentrated gas passes through the first cold-side transport pipeline 23 connected to the other end of the first cold-side pipeline 21 of the first heat exchanger 20. to be transported to the inlet 11 of the direct-fired incinerator (TO) 10 . After the above step S140 is completed, the next step S150 is performed.

In addition, in the next step S150, the gas delivery after incineration: the gas after incineration produced by the combustion of the burner head 101 of the direct-fired incinerator (TO) 10 is delivered to the second heat exchanger 30. One end of the second hot-side pipe 32 is then transported from the other end of the second hot-side pipe 32 of the second heat exchanger 30 to one end of the first hot-side pipe 22 of the first heat exchanger 20, and finally The other end of the first hot-side pipeline 22 of the first heat exchanger 20 is sent to the outlet 12 of the direct-fired incinerator (TO) 10 . After the above step S150 is completed, the next step S160 is performed.

The burner head 101 of the direct-fired incinerator (TO) 10 in the above-mentioned step S150 can transport the incinerated high-temperature gas to one side of the second hot-side pipeline 32 of the second heat exchanger 30 to Perform heat exchange (as shown in Figure 1), and then the incinerated high-temperature gas is sent to the first heat exchanger from the other side of the second hot side pipeline 32 of the second heat exchanger 30 One side of the first hot side pipeline 22 of the first heat exchanger 20 is used for heat exchange, and finally the other side of the first hot side pipeline 22 of the first heat exchanger 20 is transported to the outlet 12 of the furnace 102, and then sent to the outlet 12 of the furnace 102 by the other side. The outlet 12 of the furnace 102 is conveyed to the chimney 80 for discharge through the chimney 80 .

In addition, the next step S160 is to adjust the hot-side forced discharge pipeline: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced-discharge pipeline 90, and one end of the hot-side forced-discharge pipeline 90 is provided. It is connected with the furnace chamber 102 of the direct-fired incinerator (TO) 10, and the hot side is strongly discharged. The other end of the pipeline 90 is connected to the connection between the second hot side pipeline 32 of the second heat exchanger 30 and the first hot side pipeline 22 of the first heat exchanger 20, and the hot side is strongly discharged The pipeline 90 is provided with at least one regulating damper 901 to adjust the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 through the hot-side strong exhaust pipeline 90 .

In the above step S160, one end of the hot-side strong exhaust pipe 90 is connected to the furnace chamber 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side strong exhaust pipe 90 is connected to the second The second hot-side pipe 32 of the heat exchanger 30 is connected to the first hot-side pipe 22 of the first heat exchanger 20, wherein the hot-side strong discharge pipe 90 is provided with at least one damper 901, two dampers (not shown in the figure) can also be arranged in conjunction with the pipeline, so as to adjust the air volume of the hot-side strong exhaust pipeline 90 through the damper 901. Therefore, when volatile organic compounds (VOCs) When the concentration becomes high, the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side strong exhaust pipe 90, and part of the incinerated high-temperature gas can be sent to the second heat exchanger 30 The connection between the second hot-side pipeline 32 and the first hot-side pipeline 22 of the first heat exchanger 20 allows the hot-side strong discharge pipeline 90 to have the effect of adjusting the amount or concentration of heat recovery, so that the organic When the waste gas is treated, it can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, and even lead to shutdown.

Furthermore, the energy-saving single-wheel hot-side bypass temperature control method of the present invention mainly has four implementations, and the first implementation (as shown in FIG. 5 ) in step S100 inputs the input to be adsorbed The gas, step S110 adsorption runner for adsorption, S120 input cooling gas, step S130 delivery hot gas desorption, step S140 desorption concentrated gas delivery, step S150 gas delivery after incineration and step S160 hot side forced discharge pipeline adjustment, have been For the above description, please refer to the above description.

In the second embodiment (as shown in FIG. 6 ), the gas to be adsorbed is input in step S200 , the adsorption wheel is adsorbed in step S210 , the cooling gas is input in step S220 , the hot gas is conveyed for desorption in step S230 , and the desorption concentration in step S240 The gas delivery and the gas delivery after the incineration in step S250 are the same as the step S300 of the third embodiment (as shown in FIG. 7) to input the gas to be adsorbed, the step S310 to adsorb the runner for adsorption, the step S320 to input the cooling gas, and the step S330 delivers hot gas desorption, step S340 delivers desorbed concentrated gas, and step S350 delivers gas after incineration. In addition, in step S400 of the fourth embodiment (as shown in FIG. 8 ), the gas to be adsorbed is inputted in step S400, and the adsorbed gas is transferred in step S410. Carrying out adsorption, inputting cooling gas in S420, conveying hot gas desorption in step S430, conveying desorbed concentrated gas in step S440, and conveying gas after incineration in step S450, all of which are the same as those in the first embodiment (as shown in Fig. 5). The same design of step S100 inputting the gas to be adsorbed, step S110 adsorbing the runner for adsorption, S120 inputting cooling gas, step S130 conveying hot gas desorption, step S140 desorbing concentrated gas conveying, step S150 gas conveying after incineration, The only difference lies in the gas delivery after the incineration in step S150 and the content of the adjustment of the hot-side forced exhaust pipeline in step S160.

Therefore, the same content as the step S100 to input the gas to be adsorbed, the step S110 to adsorb the runner for adsorption, the S120 to input the cooling gas, the step S130 to convey the hot gas for desorption, and the step S140 to convey the desorbed concentrated gas will not be repeated. Please refer to the above. Description content. The following will focus on the second embodiment (as shown in Figure 6), the gas delivery after incineration in step S250 and the adjustment of the hot-side forced discharge pipeline in step S260, and the third embodiment (as shown in Figure 7) ) in step S350 of gas delivery after incineration and step S360 of hot-side forced discharge pipeline adjustment and step S450 in the fourth embodiment (as shown in FIG. 8 ) The gas transportation after incineration and the adjustment of the hot-side forced exhaust pipeline in step S460 will be described.

The difference of the second embodiment (as shown in FIG. 6 ) is the gas delivery after the incineration in step S250 : the incineration gas generated after the burner 101 of the direct-fired incinerator (TO) 10 is burned. The gas is sent to one end of the second hot side pipeline 32 of the second heat exchanger 30, and then sent to the first heat exchanger from the other end of the second hot side pipeline 32 of the second heat exchanger 30 One end of the first hot side pipeline 22 of the first heat exchanger 20 is finally transported to the outlet 12 of the direct-fired incinerator (TO) 10 from the other end of the first hot side pipeline 22 of the first heat exchanger 20 .

The burner head 101 of the direct-fired incinerator (TO) 10 in the above-mentioned step S250 can firstly transport the incinerated high-temperature gas to one side of the second hot-side pipeline 32 of the second heat exchanger 30 for Heat exchange (as shown in FIG. 2 ), and then the incinerated high temperature gas is sent to the first heat exchanger 20 from the other side of the second hot side pipeline 32 of the second heat exchanger 30 One side of the first hot-side pipeline 22 of the first heat exchanger 20 is used for heat exchange, and finally the other side of the first hot-side pipeline 22 of the first heat exchanger 20 is transported to the outlet 12 of the furnace 102, and then sent to the outlet 12 of the furnace 102 by the The outlet 12 of the furnace 102 is conveyed to the chimney 80 for discharge therethrough.

In step S260, the hot-side forced discharge pipeline is adjusted: the furnace chamber 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced-discharge pipeline 90, and one end of the hot-side forced-discharge pipeline 90 is connected to the direct-fired incinerator (TO) 10. The furnace chamber 102 of the type incinerator (TO) 10 is connected, and the other end of the hot side strong discharge pipeline 90 is connected with the outlet 12 of the direct-fired incinerator (TO) 10, and the hot side strong discharge pipeline 90 is provided with There is at least one regulating damper 901 for regulating the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 through the hot-side strong exhaust pipe 90 .

In the above step S260, one end of the hot-side strong discharge pipeline 90 is It is connected with the furnace chamber 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side strong discharge pipeline 90 is connected with the outlet 12 of the direct-fired incinerator (TO) 10, wherein the hot side is strong The exhaust pipe 90 is provided with at least one damper 901, and two dampers (not shown) can also be provided in conjunction with the pipe, so as to adjust the air volume of the hot-side strong exhaust pipe 90 through the damper 901 Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side strong exhaust pipe 90, and part of the incinerator can be The high-temperature gas is sent to the outlet 12 of the direct-fired incinerator (TO) 10, so that the hot-side strong exhaust pipe 90 has the effect of adjusting the amount of heat recovery or concentration, so that the organic waste gas can be treated to prevent direct-fired The incinerator (TO) 10 will not be overheated due to too high furnace temperature, or even lead to shutdown.

The difference of the third embodiment (as shown in FIG. 7 ) is the gas delivery after the incineration in step S350: the incineration gas generated after the burner 101 of the direct-fired incinerator (TO) 10 is burned. The gas is delivered to one end of the first hot side pipe 22 of the first heat exchanger 20, and is delivered to the second heat exchanger from the other end of the first hot side pipe 22 of the first heat exchanger 20 One end of the second hot side pipeline 32 of the second heat exchanger 30 is then transported to the outlet 12 of the direct-fired incinerator (TO) 10 from the other end of the second hot side pipeline 32 of the second heat exchanger 30 .

The burner head 101 of the direct-fired incinerator (TO) 10 in the above-mentioned step S350 can firstly transport the incinerated high-temperature gas to one side of the first hot-side pipeline 22 of the first heat exchanger 20 for processing. Heat exchange (as shown in FIG. 3 ), and the incinerated high temperature gas is transported to the second heat exchanger 30 from the other side of the first hot side pipeline 22 of the first heat exchanger 20 One side of the second hot-side pipeline 32 is used for heat exchange, and then the incinerated high-temperature gas is re-transported from the other side of the second hot-side pipeline 32 of the second heat exchanger 30 It is sent to the outlet 12 of the furnace 102, and then conveyed to the chimney 80 from the outlet 12 of the furnace 102, so as to be discharged through the chimney 80.

In step S360, the hot-side forced discharge pipeline is adjusted: the furnace chamber 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced-discharge pipeline 90, and one end of the hot-side forced-discharge pipeline 90 is connected to the direct-fired incinerator (TO) 10. The furnace chamber 102 of the type incinerator (TO) 10 is connected, and the other end of the hot side strong discharge pipe 90 is connected with the first hot side pipe 22 of the first heat exchanger 20 and the first hot side pipe 22 of the second heat exchanger 30 The two hot-side pipes 32 are connected at the connection point, and the hot-side forced exhaust pipe 90 is provided with at least one regulating damper 901 to adjust the direct-fired incinerator (TO) through the hot-side forced exhaust pipe 90 ) 10 of the air volume of the furnace 102.

In the above-mentioned step S360, one end of the hot-side strong exhaust pipe 90 is connected to the furnace chamber 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side strong exhaust pipe 90 is connected to the first The first hot-side pipeline 22 of the heat exchanger 20 is connected with the second hot-side pipeline 32 of the second heat exchanger 30, wherein the hot-side strong exhaust pipeline 90 is provided with at least one damper 901, two dampers (not shown in the figure) can also be arranged in conjunction with the pipeline, so as to adjust the air volume of the hot-side strong exhaust pipeline 90 through the damper 901. Therefore, when volatile organic compounds (VOCs) When the concentration becomes higher, the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side strong exhaust pipe 90, and part of the incinerated high-temperature gas can be sent to the first heat exchanger 20 The connection between the first hot-side pipe 22 and the second hot-side pipe 32 of the second heat exchanger 30 allows the hot-side strong discharge pipe 90 to have the effect of adjusting the amount of heat recovery or concentration, so that the organic When the waste gas is treated, it can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, and even lead to shutdown.

Furthermore, the difference of the fourth implementation form (as shown in FIG. 8 ) is step S 450 Gas delivery after incineration: The gas after incineration produced by the combustion of the burner 101 of the direct-fired incinerator (TO) 10 is delivered to the first hot side pipeline 22 of the first heat exchanger 20. one end of the first hot-side pipe 22 of the first heat exchanger 20 is transported to one end of the second hot-side pipe 32 of the second heat exchanger 30, and then passed through the second heat exchanger 30. The other end of the second hot side pipeline 32 of 30 is delivered to the outlet 12 of the direct-fired incinerator (TO) 10 .

The burner head 101 of the direct-fired incinerator (TO) 10 in the above-mentioned step S450 is capable of delivering the incinerated high-temperature gas to one side of the first hot-side pipeline 22 of the first heat exchanger 20 for processing. Heat exchange (as shown in FIG. 4 ), and the incinerated high temperature gas is transported to the second heat exchanger 30 from the other side of the first hot side pipeline 22 of the first heat exchanger 20 One side of the second hot side pipeline 32 is used for heat exchange, and then the incinerated high temperature gas is transported to the furnace 102 from the other side of the second hot side pipeline 32 of the second heat exchanger 30 The outlet 12 of the furnace 102 is then transported to the chimney 80 through the chimney 80 for discharge.

In step S460, the hot-side forced discharge pipeline is adjusted: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced-discharge pipeline 90, and one end of the hot-side forced-discharge pipeline 90 is connected to the direct-fired incinerator (TO) 10. The furnace chamber 102 of the type incinerator (TO) 10 is connected, and the other end of the hot side strong discharge pipeline 90 is connected with the outlet 12 of the direct-fired incinerator (TO) 10, and the hot side strong discharge pipeline 90 is provided with There is at least one regulating damper 901 for regulating the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 through the hot-side strong exhaust pipe 90 .

In the above step S460, one end of the hot-side strong exhaust pipe 90 is connected to the furnace chamber 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side strong exhaust pipe 90 is connected to the direct-fired incinerator (TO) 10. The outlet 12 of the type incinerator (TO) 10 is connected, wherein the hot side strong discharge line 9 The 0 series is provided with at least one damper 901, and two dampers (not shown) can also be provided in conjunction with the pipeline, so that the air volume of the hot-side strong exhaust pipeline 90 can be regulated through the damper 901. Therefore, When the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace chamber 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side strong exhaust line 90, and part of the incinerated high-temperature gas can be delivered To the outlet 12 of the direct-fired incinerator (TO) 10, the hot-side strong exhaust pipe 90 has the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be prevented from being treated by the direct-fired incinerator (TO). TO)10 will not overheat due to too high furnace temperature, or even lead to shutdown.

From the above detailed description, it can be understood by those skilled in the art that the present invention can indeed achieve the aforesaid object, and it is in compliance with the provisions of the Patent Law, and an application for a patent for invention can be filed.

However, the above are only the preferred embodiments of the present invention, and should not limit the scope of the present invention; therefore, any simple equivalent changes and modifications made according to the scope of the patent application of the present invention and the contents of the description of the invention , shall still fall within the scope covered by the patent of the present invention.

10: Direct-fired incinerator (TO)

101: Stove

102: Hearth

11: Entrance

12: Export

20: 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: Second cold side pipeline

32: Second hot side piping

60: Adsorption runner

601: Adsorption zone

602: Cooling Zone

603: Desorption zone

61: Exhaust gas intake line

62: Clean air discharge pipeline

63: Cooling air intake line

64: Cooling gas delivery pipeline

65: Hot gas delivery pipeline

66: Desorption concentrated gas pipeline

80: Chimney

90: Hot side strong discharge pipeline

901: Adjust the damper

Claims (16)

An energy-saving single runner hot side bypass temperature control system, comprising: A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a burner head and a hearth, the burner head is communicated with the hearth, and the direct-fired incinerator (TO) is provided with an inlet and a hearth. an outlet, the inlet being provided at the burner head, and the outlet being provided at the hearth; a first heat exchanger, the first heat exchanger is installed 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 installed 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 first cold-side conveying pipeline, one end of the first cold-side conveying pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side conveying pipeline is connected to the direct-fired type The inlet connection of the incinerator (TO); An adsorption runner. The adsorption runner system is provided with an adsorption area, a cooling area and a desorption area. 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 delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, one end of the exhaust gas inlet pipeline is connected to one side of the adsorption area of the adsorption runner, and the clean gas discharge pipeline has One end is connected with the other side of the adsorption area of the adsorption runner, one end of the cooling gas inlet pipeline is connected with one side of the cooling area 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 with one end of the second cold side pipeline of the second heat exchanger, and one end of the hot gas delivery pipeline is connected with the second cold side pipeline of the second heat exchanger. The other side of the desorption zone of the adsorption runner is connected, the other end of the hot gas conveying pipeline is connected with 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 tied to the One side of the desorption zone of the adsorption runner is connected, and the other end of the desorption concentrated gas pipeline is connected with one end of the first cold side pipeline of the first heat exchanger; a chimney to which the other end of the clean air discharge line is connected; and A hot-side forced-exhaust pipeline, one end of the hot-side forced-discharge pipeline is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced-discharge pipeline is connected to 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 strong discharge pipeline system is provided with at least one regulating damper. An energy-saving single runner hot side bypass temperature control system, comprising: A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a burner head and a hearth, the burner head is communicated with the hearth, and the direct-fired incinerator (TO) is provided with an inlet and a hearth. an outlet, the inlet being provided at the burner head, and the outlet being provided at the hearth; a first heat exchanger, the first heat exchanger is installed 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 installed 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 first cold-side conveying pipeline, one end of the first cold-side conveying pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side conveying pipeline is connected to the direct-fired type The inlet connection of the incinerator (TO); An adsorption runner. The adsorption runner system is provided with an adsorption area, a cooling area and a desorption area. 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 delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, one end of the exhaust gas inlet pipeline is connected to one side of the adsorption area of the adsorption runner, and the clean gas discharge pipeline has one end It is connected to the other side of the adsorption zone of the adsorption wheel, one end of the cooling gas inlet pipeline is connected to one side of the cooling zone of the adsorption wheel, and one end of the cooling gas delivery pipeline is connected to the adsorption The other side of the cooling zone of the 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 adsorption The other side of the desorption zone of the runner is connected, the other end of the hot gas conveying pipeline is connected with the other end of the second cold side pipeline of the second heat exchanger, and one end of the desorbed concentrated gas pipeline is connected is connected with one side of the desorption zone of the adsorption runner, and the other end of the desorption concentrated gas pipeline is connected with one end of the first cold side pipeline of the first heat exchanger; a chimney to which the other end of the clean air discharge line is connected; and A hot side strong discharge pipeline, one end of the hot side strong discharge pipeline is connected with the furnace of the direct-fired incinerator (TO), and the other end of the hot-side strong discharge pipeline is connected with the direct-fired incinerator The outlet of (TO) is connected, and the hot side strong exhaust pipe system is provided with at least one regulating damper. The energy-saving single-rotor hot-side bypass temperature control system described in claim 1 or 2, wherein the outlet of the direct-fired incinerator (TO) is further connected to the chimney. According to the energy-saving single runner hot side bypass temperature control system as described in claim 1 or 2, the cooling air intake pipe system is further provided for fresh air or outside air to enter. According to the energy-saving single runner hot-side bypass temperature control system described in claim 1 or 2, the exhaust gas intake pipe system is further provided with an exhaust gas communication pipe, and the exhaust gas communication pipe system is connected with the cooling The exhaust gas communication pipeline is further provided with an exhaust gas communication control valve to control the air volume of the exhaust gas communication pipeline. The energy-saving single-wheel hot-side bypass temperature control system described in claim 1 or 2, wherein the desorption and concentrated gas pipeline system is further provided with a fan. The energy-saving single runner hot side bypass temperature control system as described in claim 1 or 2, wherein the clean air discharge line system is further provided with a fan. An energy-saving single-runner hot-side bypass temperature control method is mainly used in an organic waste gas treatment system, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a The first cold side conveying pipeline, an adsorption runner and a chimney, the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner is communicated with the furnace, and the direct-fired incinerator ( TO) is provided with an inlet and an outlet, the inlet is set at the furnace head, the outlet is set at the furnace, and the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline , the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, one end of the first cold side delivery pipeline is connected with the other end of the first cold side pipeline, the first cold side pipeline The other end of the cold side conveying pipeline is connected to the inlet of the direct-fired incinerator (TO). The adsorption wheel train is provided with an adsorption zone, a cooling zone and a desorption zone. The adsorption wheel train is connected to an exhaust gas intake. pipeline, a clean gas discharge pipeline, a cooling gas intake pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, and the main steps of the control method include: Input the gas to be adsorbed: send the exhaust gas to one side of the adsorption zone of the adsorption runner through the other end of the exhaust gas inlet pipe; Adsorption by adsorption wheel: after adsorption is carried out through the adsorption zone of the adsorption wheel, the gas after adsorption is output through the other end of the clean gas discharge pipeline from the other side of the adsorption zone of the adsorption wheel; Input cooling gas: send cooling gas through the other end of the cooling gas inlet pipeline to the cooling area of the adsorption wheel for cooling, and then pass through the other end of the cooling gas delivery pipeline to cool the adsorption wheel The cooling gas from the zone is sent to the second cold side pipeline of the second heat exchanger. one end; Transporting hot gas for desorption: through the hot gas transport pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, the hot gas is transported to the desorption zone of the adsorption runner for desorption, and then passed through the desorption Attach the other end of the concentrated gas pipeline to deliver the desorbed concentrated gas to one end of the first cold side pipeline of the first heat exchanger; Delivery of desorption concentrated gas: the desorption concentrated gas is then transported to the direct-fired incinerator (TO ) entrance; Delivery of gas after incineration: The gas after combustion produced by the burner of the direct-fired incinerator (TO) is delivered to one end of the second hot-side pipeline of the second heat exchanger, and then sent to the end of the second hot side pipeline of the second heat exchanger. The other end of the second hot-side pipe of the second heat exchanger is transported to one end of the first hot-side pipe of the first heat exchanger, and finally sent to the other end of the first hot-side pipe of the first heat exchanger One end is delivered to the outlet of the direct-fired incinerator (TO); and Adjustment of hot-side forced discharge pipeline: The furnace of the direct-fired incinerator (TO) is provided with a hot-side forced-discharge pipeline, and one end of the hot-side forced-discharge pipeline is connected to the direct-fired incinerator (TO). The furnace is connected, and the other end of the hot-side strong discharge pipe is connected to the connection between the second hot-side pipe of the second heat exchanger and the first hot-side pipe of the first heat exchanger. The side strong exhaust pipe system is provided with at least one regulating damper to adjust the air volume of the furnace chamber of the direct-fired incinerator (TO) through the hot side strong exhaust pipe. An energy-saving single-runner hot-side bypass temperature control method is mainly used in an organic waste gas treatment system, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a The first cold side conveying pipeline, an adsorption runner and a chimney, the direct-fired incinerator (TO) is equipped with There is a burner head and a hearth, the burner head is communicated with the hearth, the direct-fired incinerator (TO) is provided with an inlet and an outlet, the inlet is arranged at the burner head, and the outlet is arranged at the hearth , the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, the first cold side pipeline One end of the side conveying pipeline is connected with the other end of the first cold side pipeline, and the other end of the first cold side conveying pipeline is connected with the inlet of the direct-fired incinerator (TO). The adsorption runner The system is provided with an adsorption zone, a cooling zone and a desorption zone. The adsorption runner is connected with an exhaust gas intake pipeline, a clean air discharge pipeline, a cooling gas intake pipeline, a cooling gas delivery pipeline, and a hot gas pipeline. The conveying pipeline and a desorption concentrated gas pipeline, and the main steps of the control method include: Input the gas to be adsorbed: send the exhaust gas to one side of the adsorption zone of the adsorption runner through the other end of the exhaust gas inlet pipe; Adsorption by adsorption wheel: after adsorption is carried out through the adsorption zone of the adsorption wheel, the gas after adsorption is output through the other end of the clean gas discharge pipeline from the other side of the adsorption zone of the adsorption wheel; Input cooling gas: send cooling gas through the other end of the cooling gas inlet pipeline to the cooling area of the adsorption wheel for cooling, and then pass through the other end of the cooling gas delivery pipeline to cool the adsorption wheel The cooling gas of the zone is delivered to one end of the second cold side pipeline of the second heat exchanger; Transporting hot gas for desorption: through the hot gas transport pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, the hot gas is transported to the desorption zone of the adsorption runner for desorption, and then passed through the desorption Attach the other end of the concentrated gas pipeline to deliver the desorbed concentrated gas to one end of the first cold side pipeline of the first heat exchanger; Delivery of desorption concentrated gas: the desorption concentrated gas is then transported to the direct-fired incinerator (TO ) entrance; Delivery of gas after incineration: The gas after combustion produced by the burner of the direct-fired incinerator (TO) is delivered to one end of the second hot-side pipeline of the second heat exchanger, and then sent to the end of the second hot side pipeline of the second heat exchanger. The other end of the second hot-side pipe of the second heat exchanger is transported to one end of the first hot-side pipe of the first heat exchanger, and finally sent to the other end of the first hot-side pipe of the first heat exchanger One end is delivered to the outlet of the direct-fired incinerator (TO); and Adjustment of hot-side forced discharge pipeline: The furnace of the direct-fired incinerator (TO) is provided with a hot-side forced-discharge pipeline, and one end of the hot-side forced-discharge pipeline is connected to the direct-fired incinerator (TO). The furnace is connected, and the other end of the hot-side forced exhaust pipe is connected to the outlet of the direct-fired incinerator (TO). A pipeline is used to adjust the air volume of the furnace chamber of the direct-fired incinerator (TO). An energy-saving single-runner hot-side bypass temperature control method is mainly used in an organic waste gas treatment system, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a The first cold side conveying pipeline, an adsorption runner and a chimney, the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner is communicated with the furnace, and the direct-fired incinerator ( TO) is provided with an inlet and an outlet, the inlet is set at the furnace head, the outlet is set at the furnace, and the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline , the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, one end of the first cold side delivery pipeline is connected with the other end of the first cold side pipeline, the first cold side pipeline The other end of the cold side conveying pipeline is connected to the inlet of the direct-fired incinerator (TO), and the adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone The adsorption runner is connected with an exhaust gas intake pipeline, a clean gas discharge pipeline, a cooling gas intake pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline , and the main steps of the control method include: Input the gas to be adsorbed: send the exhaust gas to one side of the adsorption zone of the adsorption runner through the other end of the exhaust gas inlet pipe; Adsorption by adsorption wheel: after adsorption is carried out through the adsorption zone of the adsorption wheel, the gas after adsorption is output through the other end of the clean gas discharge pipeline from the other side of the adsorption zone of the adsorption wheel; Input cooling gas: send cooling gas through the other end of the cooling gas inlet pipeline to the cooling area of the adsorption wheel for cooling, and then pass through the other end of the cooling gas delivery pipeline to cool the adsorption wheel The cooling gas of the zone is delivered to one end of the second cold side pipeline of the second heat exchanger; Transporting hot gas for desorption: through the hot gas transport pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, the hot gas is transported to the desorption zone of the adsorption runner for desorption, and then passed through the desorption Attach the other end of the concentrated gas pipeline to deliver the desorbed concentrated gas to one end of the first cold side pipeline of the first heat exchanger; Delivery of desorption concentrated gas: the desorption concentrated gas is then transported to the direct-fired incinerator (TO ) entrance; Delivery of gas after incineration: The gas after combustion generated by the burner of the direct-fired incinerator (TO) is delivered to one end of the first hot side pipeline of the first heat exchanger, and the The other end of the first hot side pipeline of the first heat exchanger is sent to the second hot side of the second heat exchanger One end of the pipeline is transported from the other end of the second hot side pipeline of the second heat exchanger to the outlet of the direct-fired incinerator (TO); and Adjustment of hot-side forced discharge pipeline: The furnace of the direct-fired incinerator (TO) is provided with a hot-side forced-discharge pipeline, and one end of the hot-side forced-discharge pipeline is connected to the direct-fired incinerator (TO). The furnace is connected, and the other end of the hot-side strong discharge pipe is connected to the connection between the first hot-side pipe of the first heat exchanger and the second hot-side pipe of the second heat exchanger. The side strong exhaust pipe system is provided with at least one regulating damper to adjust the air volume of the furnace chamber of the direct-fired incinerator (TO) through the hot side strong exhaust pipe. An energy-saving single-runner hot-side bypass temperature control method is mainly used in an organic waste gas treatment system, and is provided with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a The first cold side conveying pipeline, an adsorption runner and a chimney, the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner is communicated with the furnace, and the direct-fired incinerator ( TO) is provided with an inlet and an outlet, the inlet is set at the furnace head, the outlet is set at the furnace, and the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline , the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, one end of the first cold side delivery pipeline is connected with the other end of the first cold side pipeline, the first cold side pipeline The other end of the cold side conveying pipeline is connected to the inlet of the direct-fired incinerator (TO). The adsorption wheel train is provided with an adsorption zone, a cooling zone and a desorption zone. The adsorption wheel train is connected to an exhaust gas intake. pipeline, a clean gas discharge pipeline, a cooling gas intake pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, and the main steps of the control method include: Input the gas to be adsorbed: send the exhaust gas to one side of the adsorption zone of the adsorption runner through the other end of the exhaust gas inlet pipe; Adsorption by adsorption wheel: after adsorption is carried out through the adsorption zone of the adsorption wheel, the gas after adsorption is output through the other end of the clean gas discharge pipeline from the other side of the adsorption zone of the adsorption wheel; Input cooling gas: send cooling gas through the other end of the cooling gas inlet pipeline to the cooling area of the adsorption wheel for cooling, and then pass through the other end of the cooling gas delivery pipeline to cool the adsorption wheel The cooling gas of the zone is delivered to one end of the second cold side pipeline of the second heat exchanger; Transporting hot gas for desorption: through the hot gas transport pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, the hot gas is transported to the desorption zone of the adsorption runner for desorption, and then passed through the desorption Attach the other end of the concentrated gas pipeline to deliver the desorbed concentrated gas to one end of the first cold side pipeline of the first heat exchanger; Delivery of desorption concentrated gas: the desorption concentrated gas is then transported to the direct-fired incinerator (TO ) entrance; Delivery of gas after incineration: The gas after combustion generated by the burner of the direct-fired incinerator (TO) is delivered to one end of the first hot side pipeline of the first heat exchanger, and the The other end of the first hot side pipe of the first heat exchanger is transported to one end of the second hot side pipe of the second heat exchanger, and then sent to the other end of the second hot side pipe of the second heat exchanger. One end is delivered to the outlet of the direct-fired incinerator (TO); and Adjustment of hot-side forced discharge pipeline: The furnace of the direct-fired incinerator (TO) is provided with a hot-side forced-discharge pipeline, and one end of the hot-side forced-discharge pipeline is connected to the direct-fired incinerator (TO). The furnace is connected, and the other end of the hot side strong discharge pipeline is connected with the outlet of the direct-fired incinerator (TO). The pipeline system is provided with at least one regulating damper, so as to adjust the air volume of the furnace chamber of the direct-fired incinerator (TO) through the hot-side strong exhaust pipeline. The energy-saving single-rotor hot-side bypass temperature control method described in claim 8, 9, 10 or 11, wherein the outlet of the direct-fired incinerator (TO) is further connected to the chimney. According to the energy-saving single runner hot side bypass temperature control method described in claim 8, 9, 10 or 11, the cooling air intake pipe system is further provided for fresh air or outside air to enter. According to the energy-saving single runner hot side bypass temperature control method described in item 8, 9, 10 or 11 of the scope of application, wherein the exhaust gas intake pipe system is further provided with an exhaust gas communication pipe, and the exhaust gas communication pipe It 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. The energy-saving single runner hot-side bypass temperature control method described in claim 8, 9, 10 or 11, wherein the desorption concentrated gas pipeline system is further provided with a fan. According to the energy-saving single-runner hot-side bypass temperature control method described in item 8, 9, 10 or 11 of the patent application scope, the clean air discharge pipeline system is further provided with a fan.

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