TWI788715B - Energy-saving dual-rotor high-concentration hot side bypass temperature control system and method - Google Patents

Abstract

The present invention is an energy-saving double-runner high-concentration hot side bypass temperature control system and its method, which are mainly used in organic waste gas treatment systems, and are equipped with a direct-fired incinerator (TO), a first heat exchanger, A second heat exchanger, a third heat exchanger, a fourth heat exchanger, a first cold side delivery pipeline, a fourth cold side delivery pipeline, a first adsorption rotor, a second adsorption rotor Wheel and a chimney, and through the furnace 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 connected to the fourth heat exchanger. The connection between the four heat side pipelines and the third heat side pipeline of the third heat exchanger, or the connection between the third heat side pipeline of the third heat exchanger and the second heat pipe of the second heat exchanger The connection between the side pipes, or the connection between the second heat side pipe of the second heat exchanger and the first heat side pipe of the first heat exchanger, or the connection with the direct-fired incinerator One of the outlets of (TO) is connected, so that when the concentration of volatile organic compounds (VOCs) becomes high, the furnace of the direct-fired incinerator (TO) can be adjusted through the hot-side forced exhaust pipeline The air volume can be used to adjust the heat recovery amount or concentration, so that when the organic waste gas is processed, it can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature, and even cause shutdown. occur.

Description

Energy-saving dual-rotor high-concentration hot side bypass temperature control system and method

The present invention relates to an energy-saving double-rotor high-concentration hot side bypass temperature control system and its method, especially a kind of performance that can adjust the heat recovery amount or concentration when the concentration of volatile organic compounds (VOCs) becomes high , so that when the organic waste gas is processed, it can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature, and even cause shutdown. It is suitable for the semiconductor industry, optoelectronic industry or chemical related industries. Industrial organic waste gas treatment system or similar equipment.

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

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

Therefore, in view of the above deficiencies, the inventors hope to propose an energy-saving double-rotor high-concentration hot-side bypass temperature control system and its method that can improve the efficiency of organic waste gas treatment, so that users can easily operate and assemble. Thinking, design and organization to provide user convenience, Motivation for the invention that the inventor intends to develop.

The main purpose of the present invention is to provide an energy-saving double-runner high-concentration heat side bypass temperature control system and its method, which are mainly used in organic waste gas treatment systems, and are equipped with a direct-fired incinerator (TO), a first A heat exchanger, a second heat exchanger, a third heat exchanger, a fourth heat exchanger, a first cold-side delivery pipeline, a fourth cold-side delivery pipeline, a first adsorption runner, A second adsorption runner and a chimney, and through the furnace 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 connected to the fourth The connection between the fourth heat side pipeline of the heat exchanger and the third heat side pipeline of the third heat exchanger, or the third heat side pipeline of the third heat exchanger and the second heat exchange The connection between the second heat side pipeline of the heat exchanger, or the connection between the second heat side pipeline of the second heat exchanger and the first heat side pipeline of the first heat exchanger, or the connection between the second heat side pipeline of the first heat exchanger One of the outlets of the direct-fired incinerator (TO) is connected, so that when the concentration of volatile organic compounds (VOCs) becomes high, the direct-fired incinerator can be adjusted through the hot-side forced exhaust pipeline The air volume of the furnace (TO) has the effect of adjusting the amount of heat recovery or concentration, so that when the organic waste gas is processed, it can prevent the direct-fired incinerator (TO) from overheating due to too high furnace temperature. It may even lead to downtime, thereby increasing the overall practicality.

Another object of the present invention is to provide an energy-saving dual-rotor high-concentration hot side bypass temperature control system and its method. By setting at least one damper on the hot side forced exhaust pipeline, the hot side forced The other end of the row pipeline is connected to the fourth heat side pipeline of the fourth heat exchanger and the third heat side pipeline of the third heat exchanger, or connected to the third heat side pipeline of the third heat exchanger. The connection between the three heat side pipelines and the second heat side pipeline of the second heat exchanger, or the connection between the second heat side pipeline of the second heat exchanger and the first heat pipe of the first heat exchanger The connection between the side pipes, or with the One of the outlets of the direct-fired incinerator (TO) is connected so that when the concentration of volatile organic compounds (VOCs) becomes high, the direct-fired incinerator (TO) can be adjusted through the hot-side forced exhaust pipeline. ) of the furnace, and transport part of the incinerated high-temperature gas to the joints of the hot-side pipelines of different heat exchangers, so that the hot-side forced exhaust pipeline has the effect of adjusting the amount or concentration of heat recovery, so that 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 cause shutdown, thereby increasing the overall usability.

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

10: Direct fired incinerator (TO)

101: Stove head

102: Furnace

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 pipeline

40: The third heat exchanger

41: The third cold side pipeline

42: The third hot side pipeline

50: The fourth heat exchanger

51: The fourth cold side pipeline

52: The fourth hot side pipeline

53: The fourth cold side delivery pipeline

60: The first adsorption runner

601: adsorption area

602: cooling zone

603: Desorption area

61: Exhaust gas intake pipe

611: Exhaust gas communication pipeline

6111: Exhaust gas connection control valve

62: The first net gas discharge pipeline

621: The first clean gas communication pipeline

6211: The first net gas connection control valve

63: The first cooling air intake pipeline

64: The first cooling air delivery pipeline

65: The first hot gas delivery pipeline

66: The first desorption concentrated gas pipeline

661: fan

70:Second Adsorption Runner

701: adsorption area

702: cooling zone

703: Desorption area

71: The second net gas discharge pipeline

711: fan

72: The second cooling air intake pipe

73: The second cooling air delivery pipeline

74: The second hot gas delivery pipeline

75: The second desorption concentrated gas pipeline

751: fan

80: chimney

90:Hot side forced discharge pipeline

901: adjust damper

S100: Input the gas to be adsorbed

S200: Input the gas to be adsorbed

S110: Adsorption by the first adsorption runner

S210: Adsorption by the first adsorption runner

S120: Input the first cooling gas

S220: input the first cooling gas

S130: Transporting the first hot gas for desorption

S230: transporting the first hot gas for desorption

S140: Desorption concentrated gas delivery

S240: Desorption concentrated gas delivery

S150: Gas delivery after incineration

S250: Gas delivery after incineration

S160: Adsorption by the second adsorption runner

S260: Adsorption by the second adsorption runner

S170: Input the second cooling gas

S270: Input the second cooling gas

S180: Transporting the second hot gas for desorption

S280: transporting the second hot gas for desorption

S190: Adjustment of hot side forced discharge pipeline

S290: Adjustment of hot side forced discharge pipeline

S300: Input the gas to be adsorbed

S400: Input the gas to be adsorbed

S310: Adsorption by the first adsorption runner

S410: Adsorption by the first adsorption runner

S320: Input the first cooling gas

S420: Input the first cooling gas

S330: transporting the first hot gas for desorption

S430: transporting the first hot gas for desorption

S340: Desorption Concentrated Gas Delivery

S440: Desorption Concentrated Gas Delivery

S350: Gas delivery after incineration

S450: Gas delivery after incineration

S380: Adsorption by the second adsorption runner

S460: Adsorption by the second adsorption runner

S370: Input the second cooling gas

S470: Input the second cooling gas

S380: transporting the second hot gas for desorption

S480: transporting the second hot gas for desorption

S390: Adjustment of hot side forced exhaust pipeline

S490: Adjustment of hot side forced discharge pipeline

Fig. 1 is a schematic diagram of the system architecture with hot-side forced exhaust pipelines according to the first embodiment of the present invention.

Fig. 2 is a schematic diagram of the system architecture with hot-side forced exhaust pipelines according to the second embodiment of the present invention.

Fig. 3 is a schematic diagram of the system architecture with hot-side forced exhaust pipelines according to the third embodiment of the present invention.

Fig. 4 is a schematic diagram of the system architecture with hot-side forced exhaust pipelines according to the fourth embodiment of the present invention.

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 Figures 1 to 8, which are schematic diagrams of embodiments of the present invention, and the best implementation of the energy-saving double-rotor high-concentration heat side bypass temperature control system and method of the present invention is applied to the semiconductor industry, optoelectronics Volatile organic waste gas treatment systems or similar equipment in industrial or chemical-related industries mainly have the effect of adjusting the amount or concentration of heat recovery when the concentration of volatile organic compounds (VOCs) becomes high, so that organic waste gas can be treated without direct discharge. Combustion type incinerator (TO) will not overheat due to too high furnace temperature, or even cause shutdown.

And the energy-saving double-runner high-concentration heat 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 A third heat exchanger 40 , a fourth heat exchanger 50 , a first cold-side delivery pipeline 23 , a fourth cold-side delivery pipeline 53 , a first adsorption runner 60 , and a second adsorption runner 70 and a combined design of 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 a first hot side pipeline 22, the second The heat exchanger 30 is provided with a second cold-side pipeline 31 and a second hot-side pipeline 32, and the third heat exchanger 40 is provided with a third cold-side pipeline 41 and a third hot-side pipeline 42. The fourth heat exchanger 50 is provided with a fourth cold-side pipeline 51 and a fourth hot-side pipeline 52 . In addition, this direct-fired incinerator (TO) 10 is provided with a burner 101 and a furnace 102, the burner 101 communicates with the furnace 102, and the first heat exchanger 20, the second heat exchanger 30, The third heat exchanger 40 and the fourth heat exchanger 50 are respectively located in the direct-fired incinerator (TO) 10, and the direct-fired incinerator (TO) 10 is provided with an inlet 11 and an outlet 12 (such as 1 to 4), and the inlet 11 is located at the burner 101, and the inlet 11 is connected to the fourth heat exchanger 50 The other end of the fourth cold side pipeline 51 is connected, moreover, the outlet 12 is located at the furnace 102, and the outlet 12 is connected to the chimney 80, whereby the organic waste gas can come from the inlet 11 Enter the burner 101 for combustion, and then allow the burned gas to pass through the furnace 102 and be discharged to the chimney 80 through the outlet 12, so as to save energy.

And the burner head 101 of the above-mentioned direct-fired incinerator (TO) 10 is able to transport the high-temperature gas through incineration to one side of the fourth heat side pipeline 52 of the fourth heat exchanger 50 for heat exchange, And from the other side of the fourth heat side pipeline 52 of the fourth heat exchanger 50, the high-temperature gas through incineration is sent to one side of the third heat side pipeline 42 of the third heat exchanger 40 to Perform heat exchange, and then transport the incinerated high-temperature gas to the second heat side pipeline 32 of the second heat exchanger 30 from the other side of the third heat side pipeline 42 of the third heat exchanger 40 One side of the second heat exchanger 30 is used for heat exchange, and then the other side of the second heat side pipeline 32 of the second heat exchanger 30 is used to transport the burned high-temperature gas to the first heat exchanger 20 of the first heat exchanger 20. One side of the hot-side pipeline 22 is used for heat exchange, and finally the other side of the first heat-side pipeline 22 of the first heat exchanger 20 is transported to the outlet 12 of the furnace 102 (as shown in Fig. 1 to No. 4), and then transported to the chimney 80 by the outlet 12 of the furnace 102, so as to discharge through the chimney 80.

In addition, the first adsorption runner 60 of the present invention 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 pipeline 61 and a first clean gas discharge pipe. Road 62, a first cooling gas intake pipeline 63, a first cooling gas delivery pipeline 64, a first hot gas delivery pipeline 65 and a first desorption concentrated gas pipeline 66, (as shown in Fig. 1 to As shown in Fig. 4) and the second adsorption runner 70 is provided with an adsorption area 70 1. Cooling zone 702 and desorption zone 703, the second adsorption runner 70 is connected with a second clean gas discharge pipeline 71, a second cooling gas intake pipeline 72, and a second cooling gas delivery pipeline 73 . A second hot gas delivery pipeline 74 and a second desorption concentrated gas pipeline 75 . Wherein the first adsorption runner 60 and the second adsorption runner 70 are respectively zeolite concentration runners or concentration runners made of other materials.

One end of the exhaust gas inlet pipeline 61 is connected to one side of the adsorption area 601 of the first adsorption runner 60, so that the exhaust gas inlet pipeline 61 can transport organic waste gas to the first adsorption runner 60. One side of the adsorption zone 601, and one end of the first clean gas discharge pipeline 62 is connected with the other side of the adsorption zone 601 of the first adsorption runner 60, and one end of the first clean gas discharge pipeline 62 It is connected to one side of the adsorption area 701 of the second adsorption wheel 70, so that the organic waste gas can absorb organic matter through the adsorption area 601 of the first adsorption wheel 60 and then be discharged from the first clean gas pipeline 62 to transport to the adsorption area 701 of the second adsorption wheel 70 (as shown in Figures 1 to 4). In addition, the other side of the adsorption area 701 of the second adsorption runner 70 is connected to the second clean gas discharge pipeline 71, so as to be connected with the chimney 80 through the other end of the second clean gas discharge pipeline 71, And this second clean air discharge pipeline 71 is provided with a blower fan 711 (as shown in the 3rd figure and the 4th figure), so that after the adsorption process in the second clean gas discharge pipeline 71 can be made through the blower fan 711 The gas is pushed and pulled into the chimney 80 for discharge.

In addition, one side of the cooling zone 602 of the first adsorption runner 60 is connected to the first cooling air inlet pipeline 63, so that the gas enters the cooling zone 602 of the first adsorption runner 60 for cooling (as shown in the first 1 to 4), and the other side of the cooling zone 602 of the first adsorption runner 60 is connected to one end of the first cooling air delivery pipeline 64, the first The other end of the cooling gas delivery pipeline 64 is connected to one end of the third cold side pipeline 41 of the third heat exchanger 40, so as to deliver the gas entering the cooling zone 602 of the first adsorption runner 60 to the third heat exchanger 40. Heat exchange is carried out in the third heat exchanger 40 (as shown in the first figure to the fourth figure), moreover, one end of the first hot gas delivery pipeline 65 is connected to the desorption zone 603 of the first adsorption runner 60 and the other end of the first hot gas delivery pipeline 65 is connected with the other end of the third cold-side pipeline 41 of the third heat exchanger 40, so as to pass through the third heat exchanger 40. The high-temperature hot gas for heat exchange is transported to the desorption area 603 of the first adsorption wheel 60 through the first hot gas delivery pipeline 65 for desorption.

The above-mentioned cooling zone 602 of the first adsorption runner 60 is provided with two implementations, wherein the first implementation is the first cooling gas inlet connected to one side of the cooling zone 602 of the first adsorption runner 60. The air pipeline 63 is for the entry of fresh air or external air (as shown in FIG. 1 ), through which the cooling zone 602 of the first adsorption runner 60 is provided for cooling. Another second embodiment is that the exhaust gas inlet pipeline 61 is provided with an exhaust gas communication pipeline 611, and the other end of the exhaust gas communication pipeline 611 is connected with the first cooling air inlet pipeline 63 (as in the third As shown in the figure), the exhaust gas in the exhaust gas inlet pipeline 61 can be transported to the cooling zone 602 of the first adsorption runner 60 through the exhaust gas communication pipeline 611 for cooling use, and the exhaust gas communication pipeline 611 is provided with an exhaust gas communication control valve 6111 to control the air volume of the exhaust gas communication pipeline 611 .

In addition, one side of the cooling zone 702 of the second adsorption runner 70 is connected to the second cooling air inlet pipeline 72, so that the gas enters the cooling zone 702 of the second adsorption runner 70 for cooling (as in the second 1 to 4), and the other side of the cooling zone 702 of the second adsorption runner 70 is connected to one end of the second cooling air delivery pipeline 73, the second The other end of the cooling air delivery pipeline 73 is connected to one end of the second cold side pipeline 31 of the second heat exchanger 30, so as to deliver the gas entering the cooling zone 702 of the second adsorption runner 70 to the second heat exchanger 30. Heat exchange is carried out in the second heat exchanger 30 (as shown in the first figure to the fourth figure), moreover, one end of the second hot gas delivery pipeline 74 is connected to the desorption zone 703 of the second adsorption runner 70 and the other end of the second hot gas delivery pipeline 74 is connected with the other end of the second cold side pipeline 31 of the second heat exchanger 30, so as to pass through the second heat exchanger 30. The high-temperature hot gas for heat exchange is transported to the desorption zone 703 of the second adsorption wheel 70 through the second hot gas delivery pipeline 74 for desorption and use.

The above-mentioned cooling zone 702 of the second adsorption runner 70 is provided with two implementations, wherein the first implementation is the second cooling air inlet connected to one side of the cooling zone 702 of the second adsorption runner 70. The air pipeline 72 is for the entry of fresh air or external air (as shown in FIG. 1 ), through which the cooling zone 702 of the second adsorption runner 70 is provided 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 with the second cooling air inlet Pipeline 72 is connected (as shown in Figure 3 and Figure 4), so that the gas in the first clean gas discharge pipeline 62 can be delivered to the second adsorption rotor through the first clean gas communication pipeline 621. The cooling zone 702 of the wheel 70 is used for cooling down, and the first clean air communication pipeline 621 is provided with a first clean air communication control valve 6211 to control the air volume of the first clean air communication pipeline 621.

In addition, one end of the first desorption concentrated gas pipeline 66 is connected to one side of the desorption zone 603 of the first adsorption wheel 60, and the other end of the first desorption concentrated gas pipeline 66 is connected to the first desorption and concentrated gas pipeline 66. One end of the first cold side pipeline 21 of a heat exchanger 20 is connected, wherein the first The other end of the first cold side pipeline 21 of a heat exchanger 20 is connected with one end of the first cold side delivery pipeline 23, and the other end of the first cold side delivery pipeline 23 is connected with the fourth heat transfer pipeline 23. One end of the fourth cold-side pipeline 51 of the exchanger 50 is connected (as shown in FIG. 1 to FIG. 4 ). Furthermore, the other end of the fourth cold-side pipeline 51 of the fourth heat exchanger 50 is connected to one end of the fourth cold-side delivery pipeline 53, and the other end of the fourth cold-side delivery pipeline 53 is It is connected to the inlet 11 of the direct-fired incinerator (TO) 10, so that the desorbed concentrated gas desorbed at high temperature can be transported to the first heat exchange through the first desorbed concentrated gas pipeline 66 One end of the first cold-side pipeline 21 of the heat exchanger 20, and transported to one end of the first cold-side delivery pipeline 23 by the other end of the first cold-side pipeline 21 of the first heat exchanger 20, And the other end of the first cold side delivery pipeline 23 is transported to one end of the fourth cold side pipeline 51 of the fourth heat exchanger 50, and then the fourth cold side of the fourth heat exchanger 50 The other end of the pipeline 51 is delivered to one end of the fourth cold-side delivery pipeline 53, and finally the other end of the fourth cold-side delivery pipeline 53 is delivered to the direct-fired incinerator (TO) 10 In the inlet 11 (as shown in Fig. 1 to Fig. 4), the burner 101 of the direct-fired incinerator (TO) 10 is allowed to perform pyrolysis to reduce volatile organic compounds. In addition, the first desorbed concentrated gas pipeline 66 is provided with a fan 661 to push and pull the desorbed concentrated gas into one end of the first cold side pipeline 21 of the first heat exchanger 20 .

In addition, one end of the second desorption concentrated gas pipeline 75 is connected to one side of the desorption area 703 of the second adsorption wheel 70, wherein the other end of the second desorption concentrated gas pipeline 75 has two implementations: way, and the first implementation is that the other end of the second desorption-enriched gas pipeline 75 is connected with the exhaust gas inlet pipeline 61 (as shown in the first figure and the third figure), so that the concentrated The gas can then enter the first adsorption runner 60 through the exhaust gas inlet pipeline 61 In the adsorption zone 601 for re-adsorption. Another second kind of embodiment is that the other end of the second desorption concentrated gas pipeline 75 is connected with the first cooling gas inlet pipeline 63 (as shown in Fig. 2 and Fig. 4), so that the The concentrated gas can enter the cooling zone 602 of the first adsorption runner 60 through the first cooling gas inlet pipeline 63 for cooling. Furthermore, the second desorbed concentrated gas pipeline 75 is provided with a fan 751 (as shown in Fig. 3 and Fig. 4), so that the desorbed concentrated gas can be pushed and pulled into the waste gas inlet pipeline 61 or the The first cooling air enters the pipeline 63 . The desorption gas generated by the desorption area 703 of the second adsorption wheel 70 can enter the adsorption area 601 of the first adsorption wheel 60 or the cooling area 602 of the first adsorption wheel 60 for recycling, In order to improve the treatment efficiency of organic waste gas.

Furthermore, the energy-saving double-rotor high-concentration hot side bypass temperature control system of the present invention mainly has four implementation forms, and the direct-fired incinerator (TO) 10 in the four implementation forms , the first heat exchanger 20, the second heat exchanger 30, the third heat exchanger 40, the fourth heat exchanger 50, the first cold side delivery pipeline 23, the fourth cold side delivery pipeline 53, the first adsorption The 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 The contents of the exchanger 40, the fourth heat exchanger 50, the first cold side delivery pipeline 23, the fourth cold side delivery pipeline 53, the first adsorption runner 60, the second adsorption runner 70 and the chimney 80 are not repeated, please Refer to the description above.

Wherein the difference of the first kind of implementation pattern (as shown in Fig. 1) is that the furnace 102 of this direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipeline 90, and the hot-side forced exhaust pipe One end of the road 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side forced exhaust pipeline 90 is connected to the fourth heat-side pipeline 52 of the fourth heat exchanger 50 with the The connection between the third hot side pipelines 42 of the three heat exchangers 40 is connected, wherein the hot side forced exhaust pipeline 90 is provided with at least one damper 901, and two dampers can also be provided in conjunction with the pipeline. (not shown in the figure), to regulate the air volume of the hot-side forced-exhaust pipeline 90 through the damper 901, so when the concentration of volatile organic compounds (VOCs) becomes high, it can pass through the hot-side forced-exhaust pipeline 90 To adjust the air volume of the furnace 102 of the direct-fired incinerator (TO) 10, and deliver the partially incinerated high-temperature gas to the fourth heat side pipeline 52 of the fourth heat exchanger 50 and the third heat exchanger The connection between the third hot-side pipeline 42 of 40 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 treated without direct-fired incinerator (TO) 10 There will be no overheating phenomenon due to too high furnace temperature, or even shutdown.

In addition, the difference of the second implementation pattern (as shown in Fig. 2) is that a hot-side forced exhaust pipeline 90 is arranged in the furnace 102 of the direct-fired incinerator (TO) 10, and the hot-side forced exhaust One end of the pipeline 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot side exhaust pipeline 90 is connected to the third heat side pipeline of the third heat exchanger 40 42 is connected to the connection between 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, which can also be provided in conjunction with the pipeline Two dampers (not shown in the figure) are used to regulate the air volume of the hot-side forced exhaust pipeline 90 through the damper 901. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the hot-side forced Arrange the pipeline 90 to adjust the air volume of the furnace 102 of the direct-fired incinerator (TO) 10, and deliver the partially incinerated high-temperature gas to the third heat side pipeline 42 of the third heat exchanger 40 and the second heat exchanger 40. The connection between the second hot-side pipeline 32 of the second heat exchanger 30 allows the hot-side forced exhaust pipeline 90 to have the effect of adjusting the heat recovery amount or concentration, so that the organic waste gas can be treated without direct combustion. Furnace (TO) 10 will not be overheated due to too high furnace temperature, or even shut down.

In addition, the difference of the third implementation pattern (as shown in Fig. 3 ) is that the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipeline 90, and the hot-side forced exhaust One end of the pipeline 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot side exhaust pipeline 90 is connected to the second heat side pipeline of the second heat exchanger 30 32 is connected to the connection between the first hot-side pipeline 22 of the first heat exchanger 20, wherein the hot-side forced exhaust pipeline 90 is provided with at least one damper 901, which can also be provided in conjunction with the pipeline Two dampers (not shown in the figure) are used to regulate the air volume of the hot-side forced exhaust pipeline 90 through the damper 901. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the hot-side forced Arrange the pipeline 90 to adjust the air volume of the furnace 102 of the direct-fired incinerator (TO) 10, and deliver the partially incinerated high-temperature gas to the second heat side pipeline 32 of the second heat exchanger 30 and the second heat exchanger 30. The connection between the first hot-side pipeline 22 of a 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 treated without direct combustion Furnace (TO) 10 will not be overheated due to too high furnace temperature, or even shut down.

In addition, the difference of the fourth implementation pattern (as shown in Fig. 4) is that the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipeline 90, and the hot-side forced exhaust One end of the pipeline 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot side exhaust pipeline 90 is connected to the outlet 12 of the direct-fired incinerator (TO) 10 , wherein the hot-side forced discharge pipeline 90 is provided with at least one damper 901, or two dampers (not shown) may be provided in conjunction with the pipeline, so as to regulate the hot-side forced discharge through the damper 901. Therefore, when the concentration of volatile organic compounds (VOCs) becomes high, the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot side exhaust pipeline 90, And partly burnt high-temperature gas is sent to the outlet 12 of the direct-fired incinerator (TO) 10 Let the hot-side forced exhaust pipeline 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 too high furnace temperature phenomenon, and even lead to downtime.

And the energy-saving double-runner high-concentration heat side bypass temperature control method of the present invention is mainly used in organic waste gas treatment systems, and includes a direct-fired incinerator (TO) 10, a first heat exchanger 20, A second heat exchanger 30, a third heat exchanger 40, a fourth heat exchanger 50, a first cold side delivery pipeline 23, a fourth cold side delivery pipeline 53, a first adsorption runner 60, A combined design of a second adsorption runner 70 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 a first hot side pipeline 22, the second heat exchanger 30 is provided with a second cold side pipeline 31 and a second hot side pipeline 32, and the third heat exchanger 40 is provided with a third cold side pipeline 41 and a third The hot side pipeline 42, the fourth heat exchanger 50 is provided with a fourth cold side pipeline 51 and a fourth hot side pipeline 52, wherein one end of the first cold side delivery pipeline 23 is connected to the first cold side pipeline. The other end of the side pipeline 21 is connected, the other end of the first cold side delivery pipeline 23 is connected with one end of the fourth cold side pipeline 51, and one end of the fourth cold side delivery pipeline 53 is connected with the first cold side delivery pipeline 51. The other ends of the four cold-side pipelines 51 are connected, and the other end of the fourth cold-side delivery pipeline 53 is connected with the inlet 11 of the direct-fired incinerator (TO) 10 . In addition, this direct-fired incinerator (TO) 10 is provided with a burner 101 and a furnace 102, the burner 101 communicates with the furnace 102, and the first heat exchanger 20, the second heat exchanger 30, The third heat exchanger 40 and the fourth heat exchanger 50 are respectively located 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 located at the burner 101, and the inlet 11 is connected with the other end of the fourth cold side pipeline 51 of the fourth heat exchanger 50 Then, moreover, the outlet 12 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 burner 101 from the inlet 11 for combustion, and then The combusted gas can pass through the furnace 102 and be discharged to the chimney 80 through the outlet 12 to save energy.

And the burner head 101 of the above-mentioned direct-fired incinerator (TO) 10 is able to transport the high-temperature gas through incineration to one side of the fourth heat side pipeline 52 of the fourth heat exchanger 50 for heat exchange, And from the other side of the fourth heat side pipeline 52 of the fourth heat exchanger 50, the high-temperature gas through incineration is sent to one side of the third heat side pipeline 42 of the third heat exchanger 40 to Perform heat exchange, and then transport the incinerated high-temperature gas to the second heat side pipeline 32 of the second heat exchanger 30 from the other side of the third heat side pipeline 42 of the third heat exchanger 40 One side of the second heat exchanger 30 is used for heat exchange, and then the other side of the second heat side pipeline 32 of the second heat exchanger 30 is used to transport the burned high-temperature gas to the first heat exchanger 20 of the first heat exchanger 20. One side of the hot-side pipeline 22 is used for heat exchange, and finally the other side of the first heat-side pipeline 22 of the first heat exchanger 20 is transported to the outlet 12 of the furnace 102 (as shown in Fig. 1 to No. 4), and then transported to the chimney 80 by the outlet 12 of the furnace 102, so as to discharge through the chimney 80.

In addition, the first adsorption runner 60 of the present invention 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 pipeline 61 and a first clean gas discharge pipe. Road 62, a first cooling gas intake pipeline 63, a first cooling gas delivery pipeline 64, a first hot gas delivery pipeline 65 and a first desorption concentrated gas pipeline 66 (as shown in the first figure to the first 4), and the second adsorption runner 70 is provided with an adsorption zone 701, a cooling zone 702 and a desorption zone 703, and the second adsorption runner 70 is connected with a second Clean gas discharge pipeline 71, a second cooling gas inlet pipeline 72, a second cooling gas delivery pipeline 73, a second hot gas delivery pipeline 74 and a second desorption concentrated gas pipeline 75 (as the second 1 to 4). Wherein the first adsorption runner 60 and the second adsorption runner 70 are respectively zeolite concentration runners or concentration runners made of other materials.

And the main steps of this control method (as shown in Fig. 5) are to comprise: Step S100 input gas to be adsorbed: exhaust gas is sent into this first adsorption runner 60 through the other end of this exhaust gas inlet pipeline 61 One side of the adsorption zone 601. After the above step S100 is completed, the next step S110 is performed.

In addition, the step S110 carried out in the next step is adsorption by the first adsorption wheel: after the adsorption is carried out through the adsorption area 601 of the first adsorption wheel 60, the adsorbed The gas is output to the adsorption zone 701 of the second adsorption runner 70 through the other end of the first clean gas discharge pipeline 62 . After the above step S110 is completed, the next step S120 is performed.

The other side of the adsorption zone 701 of the second adsorption runner 70 in the above-mentioned step S110 is connected to the second clean gas discharge pipeline 71, so as to communicate with the second clean gas discharge pipeline 71 through the other end of the second clean gas discharge pipeline 71. The chimney 80 is connected, and the second clean air discharge pipeline 71 is provided with a fan 711 (as shown in Figure 3 and Figure 4), so that the second clean air discharge pipeline 71 can be passed through the fan 711 The adsorbed gas is pushed and pulled into the chimney 80 for discharge.

In addition, in the next step S120, the first cooling gas is input: through the other end of the first cooling gas inlet pipeline 63, the cooling gas is delivered to the cooling zone 602 of the first adsorption runner 60 for cooling, and then through the The other end of the first cooling air delivery pipeline 64 will be The cooling air passing through the cooling zone 602 of the first adsorption runner 60 is sent to one end of the third cold side pipeline 41 of the third heat exchanger 40 . After the above step S120 is completed, the next step S130 is performed.

Wherein the cooling zone 602 of the first adsorption runner 60 in the above-mentioned step S120 is provided with two implementations, wherein the first implementation is the first cooling zone 602 connected to the first adsorption runner 60. A cooling air inlet pipeline 63 is for fresh air or external air to enter (as shown in FIG. 1 ), and the cooling zone 602 of the first adsorption rotor 60 is provided for cooling down through the fresh air or external air. Another second embodiment is that the exhaust gas inlet pipeline 61 is provided with an exhaust gas communication pipeline 611, and the other end of the exhaust gas communication pipeline 611 is connected with the first cooling air inlet pipeline 63 (as in the third As shown in the figure), the exhaust gas in the exhaust gas inlet pipeline 61 can be transported to the cooling zone 602 of the first adsorption runner 60 through the exhaust gas communication pipeline 611 for cooling use, and the exhaust gas communication pipeline 611 is provided with an exhaust gas communication control valve 6111 to control the air volume of the exhaust gas communication pipeline 611 .

In addition, the step S130 carried out in the next step is to deliver the first hot gas for desorption: through the first hot gas delivery pipeline 65 connected to the other end of the third cold side pipeline 41 of the third heat exchanger 40, the hot gas is delivered to the third heat exchanger 40. The desorption zone 603 of the first adsorption runner 60 is desorbed, and then the desorbed condensed gas is delivered to the first cold side pipe of the first heat exchanger 20 through the other end of the first desorbed condensed gas pipeline 66 end of road 21. After the above step S130 is completed, the next step S140 is performed.

Wherein the first desorption concentrated gas pipeline 66 in the above-mentioned step S130 is provided with a fan 661 (as shown in Fig. 3 and Fig. 4), so that the desorbed concentrated gas can be pushed and pulled into the first heat exchanger 20 in the first cold side pipeline 21.

In addition, the next step S140 is to transport the desorbed concentrated gas: the desorbed concentrated gas passes through the first cold side delivery pipeline 23 connected to the other end of the first cold side pipeline 21 of the first heat exchanger 20 to one end of the fourth cold side pipeline 51 of the fourth heat exchanger 50, and then through the fourth cold side connected to the other end of the fourth cold side pipeline 51 of the fourth heat exchanger 50 The pipeline 53 is delivered 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, the next step S150 is to deliver the incinerated gas: the incinerated gas produced by burning the burner 101 of the direct-fired incinerator (TO) 10 is transported to the fourth heat exchanger 50. One end of the four heat side pipelines 52, and the other end of the fourth heat side pipeline 52 of the fourth heat exchanger 50 is transported to one end of the third heat side pipeline 42 of the third heat exchanger 40, and From the other end of the third heat side pipeline 42 of the third heat exchanger 40 to one end of the second heat side pipeline 32 of the second heat exchanger 30, The other end of the two heat side pipelines 32 is transported to one end of the first heat side pipeline 22 of the first heat exchanger 20, and finally delivered by the other end of the first heat side pipeline 22 of the first heat exchanger 20 To the outlet 12 of the direct-fired incinerator (TO) 10. After the above step S150 is completed, the next step S160 is performed.

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

In addition, in the next step S170, the second cooling gas is input: through the The other end of the second cooling air inlet pipeline 72 is used to transport cooling air to the cooling zone 702 of the second adsorption runner 70 for cooling, and then through the other end of the second cooling air delivery pipeline 73 to pass through the first The cooling air from the cooling zone 702 of the two adsorption runners 70 is sent to one end of the second cold side pipeline 31 of the second heat exchanger 30 . After the above step S170 is completed, the next step S180 is performed.

Wherein the cooling zone 702 of the second adsorption runner 70 in the above-mentioned step S170 is provided with two implementations, wherein the first implementation is the second cooling zone 702 connected to the second adsorption runner 70. The second cooling air intake pipeline 72 is for fresh air or external air to enter (as shown in Figure 1), through which the cooling zone 702 of the second adsorption rotor 70 is provided 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 with the second cooling air intake Pipeline 72 is connected (as shown in Figure 3 and Figure 4), so that the gas in the first clean gas discharge pipeline 62 can be delivered to the second adsorption rotor through the first clean gas communication pipeline 621. The cooling zone 702 of the wheel 70 is used for cooling down, and the first clean air communication pipeline 621 is provided with a first clean air communication control valve 6211 to control the air volume of the first clean air communication pipeline 621.

In addition, the next step S180 carried out in the next step is to deliver the second hot gas for desorption: through the second hot gas delivery pipeline 74 connected to the other end of the second cold side pipeline 31 of the second heat exchanger 30, the hot gas is delivered to the second heat exchanger 30. The desorption zone 703 of the second adsorption wheel 70 performs desorption, and then outputs the concentrated gas through the other end of the second desorption pipeline 75 . After the above step S180 is completed, the next step S190 is performed.

Wherein the second desorption concentrated gas pipeline 7 in the above-mentioned step S180 The other end of 5 has two kinds of implementation modes, and the first kind of implementation mode is that the other end of the second desorption concentrated gas pipeline 75 is connected with the waste gas inlet pipeline 61 (as the 1st figure and the 3rd As shown in the figure), the concentrated gas can enter the adsorption area 601 of the first adsorption runner 60 through the waste gas inlet pipeline 61 for re-adsorption. Another second kind of embodiment is that the other end of the second desorption concentrated gas pipeline 75 is connected with the first cooling gas inlet pipeline 63 (as shown in Fig. 2 and Fig. 4), so that the The concentrated gas can enter the cooling zone 602 of the first adsorption runner 60 through the first cooling gas inlet pipeline 63 for cooling. Furthermore, the second desorbed and concentrated gas pipeline 75 is provided with a fan 751 to push and pull the desorbed and concentrated gas into the waste gas inlet pipeline 61 or the first cooling gas inlet pipeline 63 . The desorption gas generated by the desorption area 703 of the second adsorption wheel 70 can enter the adsorption area 601 of the first adsorption wheel 60 or the cooling area 602 of the first adsorption wheel 60 for recycling, In order to improve the treatment efficiency of organic waste gas.

In addition, step S190, which is carried out in the next step, is to adjust the hot side forced exhaust pipeline: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot side forced exhaust pipeline 90, and one end of the hot side forced exhaust pipeline 90 It is connected with the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot side forced exhaust pipeline 90 is connected with the fourth heat side pipeline 52 of the fourth heat exchanger 50 and the third heat exchanger. The connection between the third hot-side pipeline 42 of the exchanger 40 is connected, and the hot-side forced exhaust pipeline 90 is provided with at least one damper 901 to adjust the direct combustion through the hot-side forced exhaust pipeline 90. The air volume of the furnace 102 of the type incinerator (TO) 10.

Wherein in the above-mentioned step S190, one end of the hot side forced exhaust pipeline 90 is connected with the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot side forced exhaust pipeline 90 is connected with the fourth The fourth heat side pipeline 52 of the heat exchanger 50 and the third heat exchanger 40 The connection between the third hot-side pipelines 42 is connected, wherein the hot-side forced exhaust pipeline 90 is provided with at least one damper 901, and two dampers (not shown) can also be provided in conjunction with the pipeline. , to regulate the air volume of the hot-side forced exhaust pipeline 90 through the damper 901, so when the concentration of volatile organic compounds (VOCs) becomes high, the direct combustion can be adjusted through the hot-side forced exhaust pipeline 90 The air volume of the furnace 102 of the type incinerator (TO) 10, and the partly incinerated high-temperature gas is sent to the fourth heat side pipeline 52 of the fourth heat exchanger 50 and the third heat of the third heat exchanger 40 The connection between the side pipes 42 allows the hot-side forced exhaust pipe 90 to 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 being damaged by the furnace. If the temperature is too high, the phenomenon of overheating will occur, and even the situation of shutting down will occur.

Furthermore, the energy-saving dual-rotor high-concentration hot side bypass temperature control method of the present invention mainly has four implementation forms, and the step S100 input of the first implementation form (as shown in Figure 5) Gas to be adsorbed, step S110 first adsorption runner adsorption, S120 input of first cooling gas, step S130 delivery of first hot gas desorption, step S140 desorption concentrated gas delivery, step S150 gas delivery after incineration, step S160 second Adsorption by the adsorption wheel, input of the second cooling gas in step S170, desorption of the second hot gas delivery in step S180, and adjustment of the hot side forced exhaust pipeline in step S190 have been explained above, please refer to the above explanation.

In the second implementation mode (as shown in Figure 6), step S200 inputs the gas to be adsorbed, step S210 the first adsorption runner absorbs, S220 inputs the first cooling gas, and step S230 transports the first hot gas for desorption, Step S240 desorption concentrated gas delivery, step S250 gas delivery after incineration, step S260 second adsorption runner adsorption, step S270 input second cooling gas and step S280 delivery second hot gas desorption, and the third In the implementation mode (as shown in Figure 7), step S300 is to input the gas to be adsorbed, step S310 is to adsorb the first adsorption wheel, S320 is to input the first cooling gas, step S330 is to transport the first hot gas for desorption, and step S340 is to desorb Concentrated gas transportation, step S350 gas transportation after incineration, step S360 second adsorption runner adsorption, step S370 input of second cooling gas and step S380 delivery of second hot gas desorption, and the fourth implementation mode (as shown in Figure 8 In the step S400 shown), the gas to be adsorbed is input in step S400, the first adsorption wheel is adsorbed in step S410, the first cooling gas is input in S420, the first hot gas is transported for desorption in step S430, the desorbed concentrated gas is transported in step S440, and after incineration in step S450 Gas delivery, step S460 second adsorption runner adsorption, step S470 input of second cooling gas and step S480 step S480 delivery of second hot gas desorption, all adopt the steps in the first embodiment (as shown in Figure 5) S100 Input the gas to be adsorbed, Step S110 Adsorption by the first adsorption runner, S120 Input the first cooling gas, Step S130 Transport the first hot gas for desorption, Step S140 Transport the desorbed concentrated gas, Step S150 Transport the gas after incineration, Step S160 The same design of adsorption by the second adsorption wheel, input of the second cooling gas in step S170, and desorption of the second hot gas in step S180, the only difference lies in the adjustment of the hot side forced exhaust pipeline in step S190.

Therefore, the above-mentioned step S100 input gas to be adsorbed, step S110 the first adsorption runner adsorption, S120 input the first cooling gas, step S130 transport the first hot gas for desorption, step S140 desorption concentrated gas transport, step S150 after incineration The same content of gas delivery, step S160 second adsorption wheel adsorption, step S170 input of second cooling gas, step S180 delivery of second hot gas desorption will not be repeated, please refer to the above description. The following will be aimed at step S290 hot side forced discharge pipeline adjustment in the second implementation (as shown in Figure 6), step S3 in the third implementation (as shown in Figure 7) 90 Hot Side Forced Exhaust Pipeline Adjustment and step S490 Hot Side Forced Exhaust Pipeline Adjustment in the fourth implementation mode (as shown in FIG. 8 ) will be described.

The difference of the second implementation mode (as shown in Fig. 6) is the adjustment of the hot-side forced exhaust pipeline in step S290: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced exhaust pipe Road 90, one end of the hot-side forced exhaust pipeline 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side forced exhaust pipeline 90 is connected to the third heat exchanger 40 The third hot side pipeline 42 is connected with the second hot side pipeline 32 of the second heat exchanger 30, and the hot side exhaust pipeline 90 is provided with at least one damper 901 to pass through the The hot-side forced exhaust pipeline 90 is used to adjust the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 .

Wherein in the above-mentioned step S290, one end of the hot side forced discharge pipeline 90 is connected with the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot side forced discharge pipeline 90 is connected with the third The connection between the third hot side pipeline 42 of the heat exchanger 40 and the second hot side pipeline 32 of the second heat exchanger 30 is connected, wherein the hot side exhaust pipeline 90 is provided with at least one damper 901, it is also possible to cooperate with the pipeline to be provided with two dampers (not shown), so as to regulate the air volume of the hot-side strong exhaust pipeline 90 through the damper 901, so when volatile organic compounds (VOCs) When the concentration becomes high, the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side forced exhaust pipeline 90, and the partly burned high-temperature gas can be sent to the third heat exchanger 40 The connection between the third hot-side pipeline 42 and the second hot-side pipeline 32 of the second heat exchanger 30 allows the hot-side strong exhaust pipeline 90 to have the effect of adjusting the heat recovery amount or concentration, so that the organic When the exhaust gas is being processed, it can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, and even cause shutdown.

Another difference of the third implementation pattern (as shown in Fig. 7) is that step S39 0 Hot-side forced exhaust pipeline adjustment: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced-exhaust pipeline 90, and one end of the hot-side forced-exhaust pipeline 90 is connected to the direct-fired incinerator The hearth 102 of the furnace (TO) 10 is connected, and the other end of the hot-side exhaust pipeline 90 is connected with the second heat-side pipeline 32 of the second heat exchanger 30 and the first heat exchanger of the first heat exchanger 20. The joints between the side pipelines 22 are connected, and the hot-side forced exhaust pipeline 90 is provided with at least one damper 901 to adjust the temperature of the direct-fired incinerator (TO) 10 through the hot-side forced exhaust pipeline 90. The air volume of the furnace 102.

Wherein the above-mentioned step S390 in the one end of this hot-side forced exhaust pipeline 90 is connected with the hearth 102 of this direct-fired incinerator (TO) 10, and the other end of this hot-side forced exhaust pipeline 90 is connected with the second The second hot side pipeline 32 of the heat exchanger 30 is connected to the first hot side pipeline 22 of the first heat exchanger 20, wherein the hot side exhaust pipeline 90 is provided with at least one damper 901, it is also possible to cooperate with the pipeline to be provided with two dampers (not shown), so as to regulate the air volume of the hot-side strong exhaust pipeline 90 through the damper 901, so when volatile organic compounds (VOCs) When the concentration becomes high, the air volume of the furnace 102 of the direct-fired incinerator (TO) 10 can be adjusted through the hot-side forced exhaust pipeline 90, and the high-temperature gas partially incinerated can be sent to the second heat exchanger 30 The connection between the second hot-side pipeline 32 of the first heat exchanger 20 and the first heat-side pipeline 22 of the first heat exchanger 20 allows the hot-side strong exhaust pipeline 90 to have the effect of adjusting the heat recovery amount or concentration, so that the organic When the exhaust gas is being processed, it can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, and even cause shutdown.

Furthermore, the difference of the fourth implementation pattern (as shown in Fig. 8) is the adjustment of the hot-side forced discharge pipeline in step S490: the furnace 102 of the direct-fired incinerator (TO) 10 is provided with a hot-side forced Exhaust pipeline 90, one end of the hot side forced exhaust pipeline 90 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot side forced exhaust pipeline 90 is connected to the direct-fired incinerator The outlet 12 of the furnace (TO) 10 is connected, and the hot-side forced exhaust pipeline 90 is provided with at least one damper 901 to adjust the direct-fired incinerator (TO) 10 through the hot-side forced exhaust pipeline 90. The air volume of the furnace 102.

One end of the hot-side forced exhaust pipeline 90 in the above-mentioned step S490 is connected to the furnace 102 of the direct-fired incinerator (TO) 10, and the other end of the hot-side forced exhaust pipeline 90 is connected to the direct-fired incinerator (TO) 10. Type incinerator (TO) 10 outlet 12, wherein the hot-side forced discharge pipeline 90 is provided with at least one damper 901, and two dampers (not shown) can also be provided with the pipeline, so as to The air volume of the hot-side forced exhaust pipeline 90 is regulated through the damper 901, so when the concentration of volatile organic compounds (VOCs) becomes high, the direct-fired incineration can be adjusted through the hot-side forced exhaust pipeline 90 The air volume of the hearth 102 of the furnace (TO) 10, and the partly incinerated high-temperature gas is sent to the outlet 12 of the direct-fired incinerator (TO) 10, so that the hot-side forced exhaust pipeline 90 has the capacity to adjust the heat recovery Or the efficiency of the concentration, so that when the organic waste gas is processed, it can prevent the direct-fired incinerator (TO) 10 from overheating due to too high furnace temperature, and even cause shutdown.

From the above detailed description, those who are familiar with this art can understand that the present invention can indeed achieve the aforementioned purpose, and have actually met the provisions of the Patent Law, so they should file an application for a patent for invention.

But the above-mentioned ones are only preferred embodiments of the present invention, and should not limit the scope of the present invention; therefore, all simple equivalent changes and modifications made according to the patent scope of the present invention and the contents of the description of the invention , should still fall within the scope covered by the patent of the present invention.

10: Direct fired incinerator (TO)

101: Stove head

102: Furnace

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 pipeline

40: The third heat exchanger

41: The third cold side pipeline

42: The third hot side pipeline

50: The fourth heat exchanger

51: The fourth cold side pipeline

52: The fourth hot side pipeline

53: The fourth cold side delivery pipeline

60: The first adsorption runner

601: adsorption area

602: cooling zone

603: Desorption area

61: Exhaust gas intake pipe

62: The first net gas discharge pipeline

63: The first cooling air intake pipeline

64: The first cooling air delivery pipeline

65: The first hot gas delivery pipeline

66: The first desorption concentrated gas pipeline

70:Second Adsorption Runner

701: adsorption area

702: cooling zone

703: Desorption area

71: The second net gas discharge pipeline

72: The second cooling air intake pipe

73: The second cooling air delivery pipeline

74: The second hot gas delivery pipeline

75: The second desorption concentrated gas pipeline

80: chimney

90:Hot side forced discharge pipeline

901: adjust damper

Claims (28)

An energy-saving dual-rotor high-concentration hot side bypass temperature control system, including: A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner is connected to the furnace, the direct-fired incinerator (TO) is provided with an entrance and an outlet, the inlet being located at the burner head and the outlet being located at the hearth; A first heat exchanger, the first heat exchanger is set in the direct-fired incinerator (TO), 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 set in the direct-fired incinerator (TO), 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 installed in the direct-fired incinerator (TO), the third heat exchanger is provided with a third cold side pipeline and a third hot side pipeline; A fourth heat exchanger, the fourth heat exchanger is installed in the direct-fired incinerator (TO), the fourth heat exchanger is provided with a fourth cold side pipeline and a fourth hot side pipeline; A first cold-side delivery pipeline, one end of the first cold-side delivery pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side delivery pipeline is connected to the fourth cold-side delivery pipeline. One end connection of the side pipe; A fourth cold-side delivery pipeline, one end of the fourth cold-side delivery pipeline is connected to the other end of the fourth cold-side pipeline, and the other end of the fourth cold-side delivery pipeline is connected to the direct-fired The inlet connection of the incinerator (TO); A first adsorption runner, the first adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, the first adsorption runner is connected with a waste gas inlet pipeline, a first clean gas discharge pipeline, A first cooling gas intake pipeline, a first cooling gas delivery pipeline, a first hot gas delivery pipeline and a first A desorption concentrated gas pipeline, one end of the exhaust gas inlet pipeline is connected to one side of the adsorption area of the first adsorption runner, one end of the first clean gas discharge pipeline is connected to the first adsorption runner One end of the first cooling air inlet pipeline is connected to one side of the cooling zone of the first adsorption runner, and one end of the first cooling air delivery pipeline is connected to the second The other side of the cooling zone of an adsorption runner is connected, the other end of the first cooling gas delivery pipeline is connected with one end of the third cold side pipeline of the third heat exchanger, the first hot gas delivery pipeline One end of the first adsorption wheel is connected to the other side of the desorption zone, the other end of the first hot gas delivery 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 wheel, and the other end of the first desorption concentrated gas pipeline is connected to the first heat exchanger. One end connection of a cold side pipeline; A second adsorption runner, the second adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, the second adsorption runner is connected with a second clean gas discharge pipeline, a second cooling gas intake Pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and a second desorption concentrated gas pipeline, one end of the first clean gas discharge pipeline is connected to the second adsorption runner One end of the second clean gas discharge pipeline is connected to the other side of the adsorption zone of the second adsorption wheel, and one end of the second cooling air intake 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 to the other side of the cooling zone of the second adsorption runner, and the other end of the second cooling gas delivery pipeline is connected to the other side of the cooling zone of the second adsorption runner. 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 with the other side of the desorption area of the second adsorption wheel, and the second hot gas delivery pipeline The other end of the pipeline is connected to the other end of the second cold side pipeline of the second heat exchanger, and one end of the second desorption concentrated gas pipeline is connected to one side of the desorption zone of the second adsorption wheel connect; a chimney to which the other end of the second clean gas discharge pipe is connected; and A hot-side forced exhaust pipeline, one end of the hot-side forced exhaust pipeline is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced exhaust pipeline is connected to the fourth heat exchanger The fourth hot-side pipeline is connected to the third heat-side pipeline of the third heat exchanger, and the hot-side forced exhaust pipeline is provided with at least one damper. An energy-saving dual-rotor high-concentration hot side bypass temperature control system, including: A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner is connected to the furnace, the direct-fired incinerator (TO) is provided with an entrance and an outlet, the inlet being located at the burner head and the outlet being located at the hearth; A first heat exchanger, the first heat exchanger is set in the direct-fired incinerator (TO), 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 set in the direct-fired incinerator (TO), 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 installed in the direct-fired incinerator (TO), the third heat exchanger is provided with a third cold side pipeline and a third hot side pipeline; A fourth heat exchanger, the fourth heat exchanger is installed in the direct-fired incinerator (TO), the fourth heat exchanger is provided with a fourth cold side pipeline and a fourth hot side pipeline; A first cold-side delivery pipeline, one end of the first cold-side delivery pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side delivery pipeline is connected to the fourth cold-side delivery pipeline. One end connection of the side pipe; A fourth cold-side delivery pipeline, one end of the fourth cold-side delivery pipeline is connected to the other end of the fourth cold-side pipeline, and the other end of the fourth cold-side delivery pipeline is connected to the direct-fired Incinerator (TO) ingress connection; A first adsorption runner, the first adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, the first adsorption runner is connected with a waste gas inlet pipeline, a first clean gas discharge pipeline, A first cooling gas inlet pipeline, a first cooling gas delivery pipeline, a first hot gas delivery pipeline and a first desorption concentrated gas pipeline, one end of the waste gas inlet pipeline is connected to the first One side of the adsorption zone of an adsorption runner, one end of the first clean gas discharge pipeline is connected to the other side of the adsorption zone of the first adsorption runner, and one end of the first cooling air intake pipeline is 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 heat exchanger is connected to one end of the third cold side pipeline, and one end of the first hot gas delivery pipeline is connected to the other side of the desorption zone of the first adsorption wheel. The other end of the first hot gas delivery 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 first adsorption runner. One side of the attached area is connected, and the other end of the first desorption concentrated 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 is provided with an adsorption zone, a cooling zone and a desorption zone, the second adsorption runner is connected with a second clean gas discharge pipeline, a second cooling gas intake Pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and a second desorption concentrated gas pipeline, one end of the first clean gas discharge pipeline is connected to the second adsorption runner One end of the second clean gas discharge pipeline is connected to the other side of the adsorption zone of the second adsorption wheel, and one end of the second cooling air intake 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 to the other side of the cooling zone of the second adsorption runner, and the other end of the second cooling gas delivery pipeline is connected to the other side of the cooling zone of the second adsorption runner. The first of the second heat exchanger One end of the two cold side pipelines is connected, one end of the second hot gas delivery pipeline is connected to the other side of the desorption area of the second adsorption runner, and the other end of the second hot gas delivery pipeline is connected to the first The other end of the second cold side pipeline of the second heat exchanger is connected, and one end of the second desorption concentrated gas pipeline is connected with one side of the desorption area of the second adsorption wheel; a chimney to which the other end of the second clean gas discharge pipe is connected; and A hot-side forced exhaust pipeline, one end of the hot-side forced exhaust pipeline is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced exhaust pipeline is connected to the third heat exchanger The connection between the third hot-side pipeline and the second hot-side pipeline of the second heat exchanger is connected, and the hot-side forced exhaust pipeline is provided with at least one damper. An energy-saving dual-rotor high-concentration hot side bypass temperature control system, including: A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner is connected to the furnace, the direct-fired incinerator (TO) is provided with an entrance and an outlet, the inlet being located at the burner head and the outlet being located at the hearth; A first heat exchanger, the first heat exchanger is set in the direct-fired incinerator (TO), 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 set in the direct-fired incinerator (TO), 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 installed in the direct-fired incinerator (TO), the third heat exchanger is provided with a third cold side pipeline and a third hot side pipeline; A fourth heat exchanger, the fourth heat exchanger is installed in the direct-fired incinerator (TO), the fourth heat exchanger is provided with a fourth cold side pipeline and a fourth hot side pipeline; A first cold-side delivery pipeline, one end of the first cold-side delivery pipeline is connected to the first cold-side pipeline The other end of the first cold-side delivery pipeline is connected to one end of the fourth cold-side pipeline; A fourth cold-side delivery pipeline, one end of the fourth cold-side delivery pipeline is connected to the other end of the fourth cold-side pipeline, and the other end of the fourth cold-side delivery pipeline is connected to the direct-fired The inlet connection of the incinerator (TO); A first adsorption runner, the first adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, the first adsorption runner is connected with a waste gas inlet pipeline, a first clean gas discharge pipeline, A first cooling gas inlet pipeline, a first cooling gas delivery pipeline, a first hot gas delivery pipeline and a first desorption concentrated gas pipeline, one end of the waste gas inlet pipeline is connected to the first One side of the adsorption zone of an adsorption runner, one end of the first clean gas discharge pipeline is connected to the other side of the adsorption zone of the first adsorption runner, and one end of the first cooling air intake pipeline is 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 heat exchanger is connected to one end of the third cold side pipeline, and one end of the first hot gas delivery pipeline is connected to the other side of the desorption zone of the first adsorption wheel. The other end of the first hot gas delivery 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 first adsorption runner. One side of the attached area is connected, and the other end of the first desorption concentrated 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 is provided with an adsorption zone, a cooling zone and a desorption zone, the second adsorption runner is connected with a second clean gas discharge pipeline, a second cooling gas intake Pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and a second desorption concentrated gas pipeline, one end of the first clean gas discharge pipeline is connected to the second adsorption runner One of the adsorption areas One end of the second clean gas discharge pipeline is connected to the other side of the adsorption area of the second adsorption runner, and one end of the second cooling air intake pipeline is connected to the cooling zone of the second adsorption runner. One side of the second cooling air delivery pipeline is connected to the other side of the cooling zone of the second adsorption wheel, and the other end of the second cooling air delivery pipeline is connected to the second heat One end of the second cold side pipeline of the exchanger is connected, one end of the second hot gas delivery pipeline is connected with the other side of the desorption area of the second adsorption wheel, and the other end of the second hot gas delivery pipeline is It 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 wheel; a chimney to which the other end of the second clean gas discharge pipe is connected; and A hot-side forced exhaust pipeline, one end of the hot-side forced exhaust pipeline is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced exhaust pipeline is connected to the second heat exchanger The second hot-side pipeline is connected to the first heat-side pipeline of the first heat exchanger, and the hot-side forced exhaust pipeline is provided with at least one damper. An energy-saving double-rotor high-concentration hot side bypass temperature control system, including: A direct-fired incinerator (TO), the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner is connected to the furnace, the direct-fired incinerator (TO) is provided with an entrance and an outlet, the inlet being located at the burner head and the outlet being located at the hearth; A first heat exchanger, the first heat exchanger is set in the direct-fired incinerator (TO), 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 set in the direct-fired incinerator (TO), 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 set in the direct-fired incinerator (TO), the first The third heat exchanger is provided with a third cold side pipeline and a third hot side pipeline; A fourth heat exchanger, the fourth heat exchanger is installed in the direct-fired incinerator (TO), the fourth heat exchanger is provided with a fourth cold side pipeline and a fourth hot side pipeline; A first cold-side delivery pipeline, one end of the first cold-side delivery pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side delivery pipeline is connected to the fourth cold-side delivery pipeline. One end connection of the side pipe; A fourth cold-side delivery pipeline, one end of the fourth cold-side delivery pipeline is connected to the other end of the fourth cold-side pipeline, and the other end of the fourth cold-side delivery pipeline is connected to the direct-fired The inlet connection of the incinerator (TO); A first adsorption runner, the first adsorption runner is provided with an adsorption zone, a cooling zone and a desorption zone, the first adsorption runner is connected with a waste gas inlet pipeline, a first clean gas discharge pipeline, A first cooling gas inlet pipeline, a first cooling gas delivery pipeline, a first hot gas delivery pipeline and a first desorption concentrated gas pipeline, one end of the waste gas inlet pipeline is connected to the first One side of the adsorption zone of an adsorption runner, one end of the first clean gas discharge pipeline is connected to the other side of the adsorption zone of the first adsorption runner, and one end of the first cooling air intake pipeline is 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 heat exchanger is connected to one end of the third cold side pipeline, and one end of the first hot gas delivery pipeline is connected to the other side of the desorption zone of the first adsorption wheel. The other end of the first hot gas delivery 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 first adsorption runner. One side of the attached area is connected, and the other end of the first desorption concentrated 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 is provided with an adsorption zone, a cooling zone and a desorption zone, the second adsorption runner is connected with a second clean gas discharge pipeline, a second cooling gas intake Pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and a second desorption concentrated gas pipeline, one end of the first clean gas discharge pipeline is connected to the second adsorption runner One end of the second clean gas discharge pipeline is connected to the other side of the adsorption zone of the second adsorption wheel, and one end of the second cooling air intake 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 to the other side of the cooling zone of the second adsorption runner, and the other end of the second cooling gas delivery pipeline is connected to the other side of the cooling zone of the second adsorption runner. 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 with the other side of the desorption area of the second adsorption wheel, and the second hot gas delivery pipeline The other end of the pipeline is connected to the other end of the second cold side pipeline of the second heat exchanger, and one end of the second desorption concentrated gas pipeline is connected to one side of the desorption zone of the second adsorption wheel connect; a chimney to which the other end of the second clean gas discharge pipe is connected; and A hot-side forced exhaust pipeline, one end of the hot-side forced exhaust pipeline is connected to the furnace of the direct-fired incinerator (TO), and the other end of the hot-side forced exhaust pipeline is connected to the direct-fired incinerator (TO) outlet connection, the hot side forced exhaust pipeline is equipped with at least one damper. The energy-saving double-rotor high-concentration heat side bypass temperature control system as described in item 1, 2, 3 or 4 of the patent application scope, wherein the outlet of the direct-fired incinerator (TO) is further connected to the chimney. The energy-saving double-rotor high-concentration hot side bypass temperature control system as described in item 1, 2, 3 or 4 of the scope of the patent application, wherein the first cooling air intake pipeline is further used for fresh air or external air to enter. The energy-saving dual-rotor high-concentration hot side bypass temperature control system as described in item 1, 2, 3 or 4 of the patent scope of the application, wherein the second cooling air intake pipeline is further used for fresh air or external air to enter. The energy-saving dual-rotor high-concentration hot side bypass temperature control system described in item 1, 2, 3 or 4 of the scope of the patent application, wherein the exhaust gas inlet pipeline is further provided with an exhaust gas communication pipeline, and the exhaust gas is connected to The pipeline is connected to the first cooling air 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 double-rotor high-concentration hot side bypass temperature control system as described in item 1, 2, 3 or 4 of the scope of the patent application, wherein the first clean gas discharge pipeline is further provided with a first clean gas connecting pipe The first clean gas communication pipeline is connected to the second cooling air inlet pipeline, and the first clean gas communication pipeline is further provided with a first clean gas communication control valve to control the first clean gas The air volume of the connecting pipeline. The energy-saving dual-rotor high-concentration hot side bypass temperature control system as described in item 1, 2, 3 or 4 of the scope of the patent application, wherein the first desorption concentrated gas pipeline is further equipped with a fan. The energy-saving double-rotor high-concentration hot side bypass temperature control system as described in item 1, 2, 3 or 4 of the scope of the patent application, wherein the second desorption concentrated gas pipeline is further equipped with a fan. The energy-saving double-rotor high-concentration hot side bypass temperature control system as described in item 1, 2, 3 or 4 of the scope of the patent application, wherein the second clean air discharge pipeline is further equipped with a fan. The energy-saving dual-rotor high-concentration hot side bypass temperature control system as described in item 1, 2, 3 or 4 of the patent scope of the application, wherein the other end of the second desorption concentrated gas pipeline is further Connect with the exhaust gas intake pipe. The energy-saving dual-rotor high-concentration hot side bypass temperature control system as described in item 1, 2, 3 or 4 of the scope of the patent application, wherein the other end of the second desorption concentrated gas pipeline is further connected to the first The cooling air intake pipe is connected. An energy-saving double-runner high-concentration heat side bypass temperature control method, mainly used in organic waste gas treatment systems, and equipped with a direct-fired incinerator (TO), a first heat exchanger, and a second heat exchanger , a third heat exchanger, a fourth heat exchanger, a first cold side delivery pipeline, a fourth cold side delivery pipeline, a first adsorption runner, a second adsorption runner and a chimney, the The direct-fired incinerator (TO) is provided with a burner and a furnace, and the burner is connected to the furnace. The direct-fired incinerator (TO) is provided with an inlet and an outlet, and the inlet is set on the burner The outlet is located at the furnace, the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline, the second heat exchanger is provided with a second cold side pipeline and The second hot side pipeline, the third heat exchanger is provided with the third cold side pipeline and the third hot side pipeline, the fourth heat exchanger is provided with the fourth cold side pipeline and the fourth hot side pipeline 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 one end of the fourth cold-side pipeline, One end of the fourth cold-side delivery pipeline is connected to the other end of the fourth cold-side pipeline, and the other end of the fourth cold-side delivery pipeline is connected to the inlet of the direct-fired incinerator (TO), The first adsorption wheel system is provided with an adsorption area, a cooling area, and a desorption area. The first adsorption wheel system is connected with a waste gas inlet pipeline, a first clean gas discharge pipeline, and a first cooling gas inlet pipeline. Pipeline, a first cooling gas delivery pipeline, a first hot gas delivery pipeline and a first desorption concentrated gas pipeline, the second adsorption wheel system is provided with an adsorption area, a cooling area and a desorption area, the The second adsorption runner system is connected with a second clean air discharge pipeline, a second cooling air intake pipeline, and a second cooling air delivery pipeline, a second hot gas delivery pipeline and a second desorption concentrated gas pipeline, and the main steps of the control method include: Input the gas to be adsorbed: send the waste gas to one side of the adsorption area of the first adsorption runner through the other end of the waste gas inlet pipeline; Adsorption by the first adsorption wheel: after adsorption through the adsorption area of the first adsorption wheel, the adsorbed gas is passed through the first clean gas discharge pipeline from the other side of the adsorption area of the first adsorption wheel The other end is output to the adsorption area of the second adsorption wheel; Input the first cooling gas: through the other end of the first cooling gas intake pipeline to transport the cooling gas to the cooling zone of the first adsorption runner for cooling, and then through the other end of the first cooling gas delivery pipeline to Delivering the cooling air passing through the cooling zone of the first adsorption runner to one end of the third cold side pipeline of the third heat exchanger; Delivery of the first hot gas desorption: through the first hot gas delivery pipeline connected to the other end of the third cold side pipeline of the third heat exchanger, the hot gas is delivered to the desorption area of the first adsorption wheel for desorption Attach, and then transport the desorbed condensed gas to one end of the first cold side pipeline of the first heat exchanger through the other end of the first desorbed condensed gas pipeline; Delivery of desorbed concentrated gas: the desorbed concentrated gas is then sent to the first cold side pipeline connected to the other end of the first cold side pipeline of the first heat exchanger to the second end of the fourth heat exchanger. One end of the four cold-side pipelines, and then transported to the direct-fired incinerator (TO) through the fourth cold-side delivery pipeline connected to the other end of the fourth cold-side pipeline of the fourth heat exchanger Entrance; Delivery of incinerated gas: The incinerated gas produced by burning the burner head of the direct-fired incinerator (TO) is delivered to one end of the fourth heat side pipeline of the fourth heat exchanger, and the The other end of the fourth heat side pipeline of the fourth heat exchanger is sent to the third heat side of the third heat exchanger One end of the pipeline, and the other end of the third heat side pipeline of the third heat exchanger is sent to one end of the second heat side pipeline of the second heat exchanger, and then from the second heat exchanger The other end of the second hot-side pipeline is sent to one end of the first hot-side pipeline of the first heat exchanger, and finally the other end of the first hot-side pipeline of the first heat exchanger is sent to the direct-fired Type incinerator (TO) export; Adsorption by the second adsorption wheel: transport the adsorbed gas in the first clean gas discharge pipeline to the side of the adsorption area of the second adsorption wheel for adsorption, and then pass the second adsorbed gas through the second Clean gas discharge pipeline to transport to the chimney discharge; Input the second cooling gas: through the other end of the second cooling gas inlet pipeline to transport the cooling gas to the cooling zone of the second adsorption runner for cooling, and then through the other end of the second cooling gas delivery pipeline to Delivering the cooling air passing through the cooling zone of the second adsorption runner to one end of the second cold side pipeline of the second heat exchanger; Conveying the second hot gas for desorption: through the second hot gas delivery pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, the hot gas is transported to the desorption area of the second adsorption wheel for desorption attached, and then output through the other end of the second desorbed concentrated gas pipeline; and Hot-side forced exhaust pipeline adjustment: the furnace of the direct-fired incinerator (TO) is equipped with a hot-side forced-exhaust pipeline, and one end of the hot-side forced-exhaust pipeline is connected to the direct-fired incinerator (TO) Furnace connection, the other end of the hot-side forced exhaust pipeline is connected to the joint between the fourth heat-side pipeline of the fourth heat exchanger and the third heat-side pipeline of the third heat exchanger, the heat The side forced exhaust pipeline is provided with at least one damper to adjust the air volume of the furnace of the direct-fired incinerator (TO) through the hot side forced exhaust pipeline. An energy-saving dual-rotor high-concentration heat side bypass temperature control method, mainly used for organic Exhaust gas treatment system, and equipped with a direct-fired incinerator (TO), a first heat exchanger, a second heat exchanger, a third heat exchanger, a fourth heat exchanger, and a first cold-side delivery pipe Road, a fourth cold-side delivery pipeline, a first adsorption runner, a second adsorption runner and a chimney, the direct-fired incinerator (TO) is provided with a burner and a furnace, the burner and The hearth is connected, the direct-fired incinerator (TO) is provided with an inlet and an outlet, the inlet is located at the burner, the outlet is located at the furnace, and the first heat exchanger is provided with a second A 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 third heat exchanger is provided with a third cold-side pipeline Road and the third hot side pipeline, the fourth heat exchanger is provided with the fourth cold side pipeline and the fourth hot side pipeline, one end of the first cold side delivery pipeline is connected with the first cold side pipeline The other end of the first cold-side delivery pipeline is connected to one end of the fourth cold-side pipeline, and one end of the fourth cold-side delivery pipeline is connected to the other end of the fourth cold-side pipeline. One end is connected, and the other end of the fourth cold side delivery pipeline is connected to the inlet of the direct-fired incinerator (TO). The first adsorption wheel system is provided with an adsorption area, a cooling area and a desorption area. The second An adsorption runner system is connected with a waste gas intake pipeline, a first clean gas discharge pipeline, a first cooling gas intake pipeline, a first cooling gas delivery pipeline, a first hot gas delivery pipeline and a The first desorption concentrated gas pipeline, the second adsorption wheel system is provided with an adsorption area, a cooling area and a desorption area, the second adsorption wheel system is connected with a second clean gas discharge pipeline, a second cooling gas Intake pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and a second desorption concentrated gas pipeline, and the main steps of the control method include: Input the gas to be adsorbed: send the waste gas to one side of the adsorption area of the first adsorption runner through the other end of the waste gas inlet pipeline; Adsorption by the first adsorption wheel: after adsorption through the adsorption area of the first adsorption wheel, the The other side of the adsorption area of an adsorption wheel outputs the adsorbed gas to the adsorption area of the second adsorption wheel through the other end of the first clean gas discharge pipeline; Input the first cooling gas: through the other end of the first cooling gas intake pipeline to transport the cooling gas to the cooling zone of the first adsorption runner for cooling, and then through the other end of the first cooling gas delivery pipeline to Delivering the cooling air passing through the cooling zone of the first adsorption runner to one end of the third cold side pipeline of the third heat exchanger; Delivery of the first hot gas desorption: through the first hot gas delivery pipeline connected to the other end of the third cold side pipeline of the third heat exchanger, the hot gas is delivered to the desorption area of the first adsorption wheel for desorption Attach, and then transport the desorbed condensed gas to one end of the first cold side pipeline of the first heat exchanger through the other end of the first desorbed condensed gas pipeline; Delivery of desorbed concentrated gas: the desorbed concentrated gas is then sent to the first cold side pipeline connected to the other end of the first cold side pipeline of the first heat exchanger to the second end of the fourth heat exchanger. One end of the four cold-side pipelines, and then transported to the direct-fired incinerator (TO) through the fourth cold-side delivery pipeline connected to the other end of the fourth cold-side pipeline of the fourth heat exchanger Entrance; Delivery of incinerated gas: The incinerated gas produced by burning the burner head of the direct-fired incinerator (TO) is delivered to one end of the fourth heat side pipeline of the fourth heat exchanger, and the The other end of the fourth heat side pipeline of the fourth heat exchanger is sent to one end of the third heat side pipeline of the third heat exchanger, and the other end of the third heat side pipeline of the third heat exchanger One end is transported to one end of the second heat side pipeline of the second heat exchanger, and then the other end of the second heat side pipeline of the second heat exchanger is transported to the first heat side of the first heat exchanger One end of the pipeline is finally transported to the outlet of the direct-fired incinerator (TO) by the other end of the first heat side pipeline of the first heat exchanger; Adsorption by the second adsorption wheel: transport the adsorbed gas in the first clean gas discharge pipeline to the side of the adsorption area of the second adsorption wheel for adsorption, and then pass the second adsorbed gas through the second Clean gas discharge pipeline to transport to the chimney discharge; Input the second cooling gas: through the other end of the second cooling gas inlet pipeline to transport the cooling gas to the cooling zone of the second adsorption runner for cooling, and then through the other end of the second cooling gas delivery pipeline to Delivering the cooling air passing through the cooling zone of the second adsorption runner to one end of the second cold side pipeline of the second heat exchanger; Conveying the second hot gas for desorption: through the second hot gas delivery pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, the hot gas is transported to the desorption area of the second adsorption wheel for desorption attached, and then output through the other end of the second desorbed concentrated gas pipeline; and Hot-side forced exhaust pipeline adjustment: the furnace of the direct-fired incinerator (TO) is equipped with a hot-side forced-exhaust pipeline, and one end of the hot-side forced-exhaust pipeline is connected to the direct-fired incinerator (TO) Furnace connection, the other end of the hot-side forced exhaust pipeline is connected to the connection between the third heat-side pipeline of the third heat exchanger and the second heat-side pipeline of the second heat exchanger, the heat The side forced exhaust pipeline is provided with at least one damper to adjust the air volume of the furnace of the direct-fired incinerator (TO) through the hot side forced exhaust pipeline. An energy-saving double-runner high-concentration heat side bypass temperature control method, mainly used in organic waste gas treatment systems, and equipped with a direct-fired incinerator (TO), a first heat exchanger, and a second heat exchanger , a third heat exchanger, a fourth heat exchanger, a first cold side delivery pipeline, a fourth cold side delivery pipeline, a first adsorption runner, a second adsorption runner and a chimney, the The direct-fired incinerator (TO) is provided with a burner and a furnace, and the burner is connected to the furnace. The direct-fired incinerator (TO) is provided with an inlet and an outlet, and the inlet is set on the burner place, the export system Located at the furnace, the first heat exchanger is provided with a first cold-side pipeline and a first hot-side pipeline, and the second heat exchanger is provided with a second cold-side pipeline and a second hot-side pipe road, the third heat exchanger is provided with a third cold side pipeline and a third hot side pipeline, the fourth heat exchanger is provided with a fourth cold side pipeline and a fourth hot side pipeline, the first One end of the cold-side delivery pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side delivery pipeline is connected to one end of the fourth cold-side pipeline. One end of the delivery pipeline is connected to the other end of the fourth cold-side pipeline, and the other end of the fourth cold-side delivery pipeline is connected to the inlet of the direct-fired incinerator (TO). The wheel train is provided with an adsorption zone, a cooling zone and a desorption zone. The first adsorption runner train is connected with a waste gas intake pipeline, a first clean gas discharge pipeline, a first cooling gas intake pipeline, a first A cooling gas delivery pipeline, a first hot gas delivery pipeline and a first desorption concentrated gas pipeline, the second adsorption wheel system is provided with an adsorption area, a cooling area and a desorption area, the second adsorption wheel It is connected with a second clean gas discharge pipeline, a second cooling gas intake pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and a second desorption concentrated gas pipeline, and the The main steps of the control method include: Input the gas to be adsorbed: send the waste gas to one side of the adsorption area of the first adsorption runner through the other end of the waste gas inlet pipeline; Adsorption by the first adsorption wheel: after adsorption through the adsorption area of the first adsorption wheel, the adsorbed gas is passed through the first clean gas discharge pipeline from the other side of the adsorption area of the first adsorption wheel The other end is output to the adsorption area of the second adsorption wheel; Input the first cooling gas: through the other end of the first cooling gas intake pipeline to transport the cooling gas to the cooling zone of the first adsorption runner for cooling, and then through the other end of the first cooling gas delivery pipeline to The cooling air passing through the cooling zone of the first adsorption wheel is transported to the third heat exchanger One end of the third cold side pipeline of the exchanger; Delivery of the first hot gas desorption: through the first hot gas delivery pipeline connected to the other end of the third cold side pipeline of the third heat exchanger, the hot gas is delivered to the desorption area of the first adsorption wheel for desorption Attach, and then transport the desorbed condensed gas to one end of the first cold side pipeline of the first heat exchanger through the other end of the first desorbed condensed gas pipeline; Delivery of desorbed concentrated gas: the desorbed concentrated gas is then sent to the first cold side pipeline connected to the other end of the first cold side pipeline of the first heat exchanger to the second end of the fourth heat exchanger. One end of the four cold-side pipelines, and then transported to the direct-fired incinerator (TO) through the fourth cold-side delivery pipeline connected to the other end of the fourth cold-side pipeline of the fourth heat exchanger Entrance; Delivery of incinerated gas: The incinerated gas produced by burning the burner head of the direct-fired incinerator (TO) is delivered to one end of the fourth heat side pipeline of the fourth heat exchanger, and the The other end of the fourth heat side pipeline of the fourth heat exchanger is sent to one end of the third heat side pipeline of the third heat exchanger, and the other end of the third heat side pipeline of the third heat exchanger One end is transported to one end of the second heat side pipeline of the second heat exchanger, and then the other end of the second heat side pipeline of the second heat exchanger is transported to the first heat side of the first heat exchanger One end of the pipeline is finally transported to the outlet of the direct-fired incinerator (TO) by the other end of the first heat side pipeline of the first heat exchanger; Adsorption by the second adsorption wheel: transport the adsorbed gas in the first clean gas discharge pipeline to the side of the adsorption area of the second adsorption wheel for adsorption, and then pass the second adsorbed gas through the second Clean gas discharge pipeline to transport to the chimney discharge; Input the second cooling gas: through the other end of the second cooling gas inlet pipeline to transport the cooling gas to the cooling zone of the second adsorption runner for cooling, and then through the second cooling gas delivery pipeline The other end is used to deliver the cooling air passing through the cooling zone of the second adsorption wheel to the second cold side pipeline of the second heat exchanger; Conveying the second hot gas for desorption: through the second hot gas delivery pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, the hot gas is transported to the desorption area of the second adsorption wheel for desorption attached, and then output through the other end of the second desorbed concentrated gas pipeline; and Hot-side forced exhaust pipeline adjustment: the furnace of the direct-fired incinerator (TO) is equipped with a hot-side forced-exhaust pipeline, and one end of the hot-side forced-exhaust pipeline is connected to the direct-fired incinerator (TO) Furnace connection, the other end of the hot side forced exhaust pipeline is connected to the joint between the second heat side pipeline of the second heat exchanger and the first heat side pipeline of the first heat exchanger, the heat The side forced exhaust pipeline is provided with at least one damper to adjust the air volume of the furnace of the direct-fired incinerator (TO) through the hot side forced exhaust pipeline. An energy-saving double-runner high-concentration heat side bypass temperature control method, mainly used in organic waste gas treatment systems, and equipped with a direct-fired incinerator (TO), a first heat exchanger, and a second heat exchanger , a third heat exchanger, a fourth heat exchanger, a first cold side delivery pipeline, a fourth cold side delivery pipeline, a first adsorption runner, a second adsorption runner and a chimney, the The direct-fired incinerator (TO) is provided with a burner and a furnace, and the burner is connected to the furnace. The direct-fired incinerator (TO) is provided with an inlet and an outlet, and the inlet is set on the burner The outlet is located at the furnace, the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline, the second heat exchanger is provided with a second cold side pipeline and The second hot side pipeline, the third heat exchanger is provided with the third cold side pipeline and the third hot side pipeline, the fourth heat exchanger is provided with the fourth cold side pipeline and the fourth hot side pipeline One end of the first cold-side delivery pipeline is connected to the other end of the first cold-side pipeline, and the other end of the first cold-side delivery pipeline is connected to one end of the fourth cold-side pipeline One end of the fourth cold-side delivery pipeline is connected to the other end of the fourth cold-side delivery pipeline, and the other end of the fourth cold-side delivery pipeline is connected to the inlet of the direct-fired incinerator (TO) connected, the first adsorption wheel system is provided with an adsorption area, a cooling area and a desorption area, and the first adsorption wheel system is connected with a waste gas inlet pipeline, a first clean gas discharge pipeline, a first cooling gas Intake pipeline, a first cooling gas delivery pipeline, a first hot gas delivery pipeline and a first desorption concentrated gas pipeline, the second adsorption wheel system is provided with an adsorption zone, a cooling zone and a desorption zone , the second adsorption runner is connected with a second clean gas discharge pipeline, a second cooling gas intake pipeline, a second cooling gas delivery pipeline, a second hot gas delivery pipeline and a second desorption enriched gas pipeline, and the main steps of the control method include: Input the gas to be adsorbed: send the waste gas to one side of the adsorption area of the first adsorption runner through the other end of the waste gas inlet pipeline; Adsorption by the first adsorption wheel: after adsorption through the adsorption area of the first adsorption wheel, the adsorbed gas is passed through the first clean gas discharge pipeline from the other side of the adsorption area of the first adsorption wheel The other end is output to the adsorption area of the second adsorption wheel; Input the first cooling gas: through the other end of the first cooling gas intake pipeline to transport the cooling gas to the cooling zone of the first adsorption runner for cooling, and then through the other end of the first cooling gas delivery pipeline to Delivering the cooling air passing through the cooling zone of the first adsorption runner to one end of the third cold side pipeline of the third heat exchanger; Delivery of the first hot gas desorption: through the first hot gas delivery pipeline connected to the other end of the third cold side pipeline of the third heat exchanger, the hot gas is delivered to the desorption area of the first adsorption wheel for desorption Attach, and then transport the desorbed condensed gas to one end of the first cold side pipeline of the first heat exchanger through the other end of the first desorbed condensed gas pipeline; Delivery of desorbed concentrated gas: the desorbed concentrated gas is then sent to the first cold side pipeline connected to the other end of the first cold side pipeline of the first heat exchanger to the second end of the fourth heat exchanger. One end of the four cold-side pipelines, and then transported to the direct-fired incinerator (TO) through the fourth cold-side delivery pipeline connected to the other end of the fourth cold-side pipeline of the fourth heat exchanger Entrance; Delivery of incinerated gas: The incinerated gas produced by burning the burner head of the direct-fired incinerator (TO) is delivered to one end of the fourth heat side pipeline of the fourth heat exchanger, and the The other end of the fourth heat side pipeline of the fourth heat exchanger is sent to one end of the third heat side pipeline of the third heat exchanger, and the other end of the third heat side pipeline of the third heat exchanger One end is transported to one end of the second heat side pipeline of the second heat exchanger, and then the other end of the second heat side pipeline of the second heat exchanger is transported to the first heat side of the first heat exchanger One end of the pipeline is finally transported to the outlet of the direct-fired incinerator (TO) by the other end of the first heat side pipeline of the first heat exchanger; Adsorption by the second adsorption wheel: transport the adsorbed gas in the first clean gas discharge pipeline to the side of the adsorption area of the second adsorption wheel for adsorption, and then pass the second adsorbed gas through the second Clean gas discharge pipeline to transport to the chimney discharge; Input the second cooling gas: through the other end of the second cooling gas inlet pipeline to transport the cooling gas to the cooling zone of the second adsorption runner for cooling, and then through the other end of the second cooling gas delivery pipeline to Delivering the cooling air passing through the cooling zone of the second adsorption runner to one end of the second cold side pipeline of the second heat exchanger; Conveying the second hot gas for desorption: through the second hot gas delivery pipeline connected to the other end of the second cold side pipeline of the second heat exchanger, the hot gas is transported to the desorption area of the second adsorption wheel for desorption attached, and then output through the other end of the second desorbed concentrated gas pipeline; and Hot-side forced exhaust pipeline adjustment: the furnace of the direct-fired incinerator (TO) is equipped with a hot-side forced-exhaust pipeline, and one end of the hot-side forced-exhaust pipeline is connected to the direct-fired incinerator (TO) Furnace connection, the other end of the hot-side forced exhaust pipeline is connected to the outlet of the direct-fired incinerator (TO), and the hot-side forced exhaust pipeline is equipped with at least one damper to pass through the hot-side forced exhaust The pipeline is used to adjust the air volume of the furnace of the direct-fired incinerator (TO). The energy-saving dual-rotor high-concentration hot side bypass temperature control method as described in item 15, 16, 17 or 18 of the scope of application, wherein the outlet of the direct-fired incinerator (TO) is further connected to the chimney. The energy-saving dual-rotor high-concentration hot side bypass temperature control method as described in item 15, 16, 17 or 18 of the scope of the patent application, wherein the first cooling air intake pipeline is further used for fresh air or external air to enter. The energy-saving dual-rotor high-concentration hot side bypass temperature control method as described in item 15, 16, 17 or 18 of the scope of patent application, wherein the second cooling air intake pipeline is further used for fresh air or external air to enter. The energy-saving double-rotor high-concentration hot side bypass temperature control method as described in item 15, 16, 17 or 18 of the scope of the patent application, wherein the exhaust gas inlet pipeline is further provided with an exhaust gas communication pipeline, and the exhaust gas is connected to The pipeline is connected to the first cooling air 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 dual-rotor high-concentration hot side bypass temperature control method as described in item 15, 16, 17 or 18 of the scope of the patent application, wherein the first clean gas discharge pipeline is further provided with a first clean gas connecting pipe Road, the first clean air communication pipeline is connected with the second cooling air intake pipeline connected, the first clean air communication pipeline is further provided with a first clean air communication control valve to control the air volume of the first clean air communication pipeline. The energy-saving double-rotor high-concentration hot side bypass temperature control method as described in item 15, 16, 17 or 18 of the scope of patent application, wherein the first desorption concentrated gas pipeline is further equipped with a fan. The energy-saving dual-rotor high-concentration hot side bypass temperature control method as described in item 15, 16, 17 or 18 of the scope of patent application, wherein the second desorption concentrated gas pipeline is further equipped with a fan. The energy-saving dual-rotor high-concentration hot side bypass temperature control method as described in item 15, 16, 17 or 18 of the scope of patent application, wherein the second clean air discharge pipeline is further equipped with a fan. The energy-saving double-rotor high-concentration hot side bypass temperature control method as described in item 15, 16, 17 or 18 of the scope of patent application, wherein the second desorption concentrated gas pipe in the step of transporting the second hot gas for desorption The other end of the road is further connected with the exhaust gas intake pipeline. The energy-saving double-rotor high-concentration hot side bypass temperature control method as described in item 15, 16, 17 or 18 of the scope of patent application, wherein the second desorption concentrated gas pipe in the step of transporting the second hot gas for desorption The other end of the passage is further connected with the first cooling air intake pipeline.

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