CN115405937A

CN115405937A - Rotary wheel system with hot medium oil and method thereof

Info

Publication number: CN115405937A
Application number: CN202110900419.2A
Authority: CN
Inventors: 郑石治; 扶亚民
Original assignee: Shanghai Huamao Environmental Protection Energy Saving Equipment Co ltd; Desiccant Technology Corp
Current assignee: Shanghai Huamao Environmental Protection Energy Saving Equipment Co ltd; Desiccant Technology Corp
Priority date: 2021-05-28
Filing date: 2021-08-06
Publication date: 2022-11-29
Also published as: TW202246702A; TWI811690B

Abstract

The invention provides a runner system with hot medium oil and a method thereof, which mainly increase the design of a hot medium oil system, wherein the hot medium oil system is provided with a hot medium oil tank, an air inlet heat exchanger and a hearth heat exchanger, the air inlet heat exchanger is arranged on a waste gas inlet pipeline, the hearth heat exchanger is arranged in a hearth of a direct-fired incinerator (TO), so that source waste gas can be heated and treated through a hot side pipeline of the air inlet heat exchanger, and the burnt gas can be treated through the hot side pipeline of the hearth heat exchanger and can be circulated back and forth through the hot medium oil system, thereby improving the treatment efficiency of organic waste gas.

Description

Rotary wheel system with hot medium oil and method thereof

Technical Field

The present invention relates to a rotary wheel system with heating medium oil and a method thereof, and more particularly, to an organic waste gas treatment system or the like which can improve the organic waste gas treatment efficiency and is suitable for the semiconductor industry, the photoelectric industry, or the chemical industry.

Background

At present, volatile organic gases (VOC) are generated in the manufacturing process of semiconductor industry or photoelectric industry, so that processing equipment for processing the VOC is installed in each factory to prevent the VOC from being directly discharged into the air to cause air pollution. At present, most of the concentrated gas desorbed by the treatment equipment is delivered to the incinerator for combustion, and the combusted gas is delivered to a chimney for emission.

Therefore, the present inventors have made the above-mentioned drawbacks and have desired to provide a runner system with a heat transfer oil and a method thereof, which can be easily assembled by a user, and which are intended to provide convenience to the user through careful research and design.

BRIEF SUMMARY OF THE PRESENT DISCLOSURE

The invention mainly aims TO provide a runner system with hot medium oil and a method thereof, which mainly increase the design of a hot medium oil system, wherein the hot medium oil system is provided with a hot medium oil groove, an air inlet heat exchanger and a hearth heat exchanger, the air inlet heat exchanger is arranged on an exhaust gas inlet pipeline, the hearth heat exchanger is arranged in a hearth of a direct-fired incinerator (TO), so that source exhaust gas can be heated and treated through a hot side pipeline of the air inlet heat exchanger, and the burnt gas can be treated through the hot side pipeline of the hearth heat exchanger and circulates back and forth through the hot medium oil system, so that the organic exhaust gas treatment efficiency is improved, and the overall practicability is further increased.

Another objective of the present invention is to provide a runner system with heat medium oil and a method thereof, wherein the heat medium oil system is provided with a heat medium oil tank, an air intake heat exchanger and a hearth heat exchanger, the heat medium oil tank of the heat medium oil system is composed of a heat medium as a heat source, and the heat medium is a liquid oil product, and the heat medium can be circularly heated and used through the air intake heat medium oil output pipeline, the air intake heat medium oil input pipeline, the hearth heat medium oil output pipeline and the hearth heat medium oil input pipeline, so that the relative humidity of the source exhaust gas can be reduced through a circulation manner, thereby enhancing the adsorption efficiency of the adsorption zone entering the adsorption runner, and further increasing the whole adsorbability.

The present invention provides a rotary wheel system with a heating medium oil and a method thereof, wherein the desorption zone of the adsorption rotary wheel is performed by hot gas, and the hot gas has two sources, the first type is that a third heat exchanger is arranged in the direct-fired incinerator (TO), the third heat exchanger is arranged between the hearth heat exchanger and the first heat exchanger or between the second heat exchanger and the hearth heat exchanger, and one end of the hot gas delivery pipeline is connected with the other side of the desorption zone of the adsorption rotary wheel, the other end of the hot gas delivery pipeline is connected with the other end of a third cold side pipeline of the third heat exchanger, the other second type is that a heater is arranged, wherein the heater is any one of an air-TO-air heat exchanger, a liquid-TO-air heat exchanger, an electric heater and a gas heater, and the other end of the hot gas delivery pipeline is connected with the heater, and one end of the hot gas delivery pipeline is connected with the other side of the desorption zone of the adsorption rotary wheel, so that the adsorbed desorption zone can have a high-temperature desorption effect, thereby increasing the whole operability.

For a better understanding of the nature, features and aspects of the present invention, reference should be made to the following detailed description of the invention, taken in conjunction with the accompanying drawings, which are provided for purposes of illustration and description only and are not intended to be limiting.

Drawings

Fig. 1 is a schematic system structure diagram of the main embodiment of the present invention.

Fig. 2 is a schematic structural diagram of a system with a fan according to a main embodiment of the present invention.

Fig. 3 is a schematic view showing the system structure of the third heat exchange means at different positions in the main embodiment of the present invention.

Fig. 4 is a schematic diagram of a system structure of a third heat exchanger in different positions and fans in the main embodiment of the present invention.

Fig. 5 is a schematic system structure according to another embodiment of the present invention.

Fig. 6 is a schematic structural diagram of a system with a fan according to another embodiment of the present invention.

FIG. 7 is a flowchart of the steps of the main embodiment of the present invention.

FIG. 8 is a flowchart illustrating steps of a second embodiment of the present invention.

FIG. 9 is a flowchart illustrating steps of a third embodiment of the present invention.

Description of the reference numerals

10: direct-fired incinerator (TO)

101: furnace end

102: hearth box

11: inlet

12: an outlet

20: first heat exchanger

21: first cold side pipeline

22: first hot side pipeline

30: second heat exchanger

31: second cold side pipeline

32: second hot side pipeline

40: third heat exchanger

41: third cold side pipeline

42: third hot side pipeline

50: heating device

61: first cold side conveying pipeline

62: second cold side transfer line

70: adsorption rotating wheel

701: adsorption zone

702: cooling zone

703: desorption zone

71: waste gas inlet pipeline

711. Waste gas communicating pipeline

7111: waste gas communicating control valve

712: fan blower

72: clean gas discharge pipeline

721: fan blower

73: cooling gas inlet pipeline

74: cooling gas conveying pipeline

75: hot gas conveying pipeline

76: concentrated gas desorption pipeline

761: fan blower

80: chimney

90: heating medium oil system

91: heat medium oil groove

911: air inlet heat medium oil output pipeline

912: air inlet heat medium oil input pipeline

913: hearth heat medium oil output pipeline

914: hearth heating medium oil input pipeline

92: air intake heat exchanger

921: cold side pipeline

922: hot side pipeline

93: hearth heat exchanger

931: cold side pipeline

932: hot side pipeline

S100: source exhaust gas transport

S110: passing source exhaust gas through an intake heat exchanger

S120: the adsorption rotating wheel performs adsorption

S130: cooling gas is introduced into the cooling zone

S140: the desorption zone carries out desorption

S150: desorption of concentrated gas delivery

S160: conveying the incinerated gas

S170: the incinerated gas passes through a hearth heat exchanger

S180: gas outlet output after incineration

S200: source exhaust gas delivery

S210: passing source exhaust gas through an intake heat exchanger

S220: the adsorption rotating wheel performs adsorption

S230: cooling gas is introduced into the cooling zone

S240: the desorption zone carries out desorption

S250: desorption of concentrated gas delivery

S260: conveying the incinerated gas

S270: the incinerated gas passes through the hearth heat exchanger

S280: gas outlet output after incineration

S300: source exhaust gas transport

S310: passing source exhaust gas through an intake heat exchanger

S320: the adsorption rotating wheel performs adsorption

S330: cooling gas is introduced into the cooling zone

S340: the desorption zone carries out desorption

S350: delivery of desorbed concentrated gas

S360: conveying the incinerated gas

S370: the incinerated gas passes through the hearth heat exchanger

S380: gas outlet output after incineration

Detailed Description

Referring to fig. 1 to 9, there are shown schematic views illustrating a rotary wheel system with heating medium oil and a method thereof according to an embodiment of the present invention, which are applied to a voc emission treatment system or the like in the semiconductor industry, the photovoltaic industry or the chemical industry to improve the efficiency of the voc emission treatment.

The runner system with hot media oil of the present invention mainly includes a combination design of a direct-fired incinerator (TO) 10, a first heat exchanger 20, a second heat exchanger 30, a third heat exchanger 40, a first cold side delivery pipe 61, a second cold side delivery pipe 62, an adsorption runner 70, a chimney 80 and a hot media oil system 90 (as shown in fig. 1 TO fig. 2), wherein the first heat exchanger 20 is provided with a first cold side pipe 21 and a first hot side pipe 22, the second heat exchanger 30 is provided with a second cold side pipe 31 and a second hot side pipe 32, and the third heat exchanger 40 is provided with a third cold side pipe 41 and a third hot side pipe 42. In addition, the direct-fired incinerator (TO) 10 is provided with a furnace end 101 and a furnace chamber 102, the furnace end 101 is communicated with the furnace chamber 102, the first heat exchanger 20, the second heat exchanger 30 and the third heat exchanger 40 are respectively arranged in the furnace chamber 102 of the direct-fired incinerator (TO) 10, the direct-fired incinerator (TO) 10 is provided with an inlet 11 and an outlet 12, the inlet 11 is arranged at the furnace end 101, and the outlet 12 of the direct-fired incinerator (TO) 10 is connected TO the chimney 80, so that organic waste gas can enter the furnace end 101 from the inlet 11 for combustion, and combusted gas can pass through the furnace chamber 102 and be discharged TO the chimney 80 from the outlet 11 for discharge, thereby having the energy-saving effect.

The adsorption rotor 70 of the present invention is further provided with an adsorption zone 701, a cooling zone 702 and a desorption zone 703, and the adsorption rotor 70 is connected to a waste gas inlet line 71, a clean gas discharge line 72, a cooling gas inlet line 73, a cooling gas delivery line 74, a hot gas delivery line 75 and a desorption concentrated gas line 76 (as shown in fig. 1 to 2). Wherein the adsorption wheel 70 is a zeolite concentration wheel or a concentration wheel made of other materials. One end of the waste gas inlet pipe 71 is connected to one side of the adsorption region 701 of the adsorption rotor 70, so that the waste gas inlet pipe 71 can deliver the source waste gas to one side of the adsorption region 701 of the adsorption rotor 70, one end of the clean gas discharge pipe 72 is connected to the other side of the adsorption region 701 of the adsorption rotor 70, the other end of the clean gas discharge pipe 72 is connected to the chimney 80, and the clean gas discharge pipe 72 is provided with a fan 721 (shown in fig. 2), so that the adsorbed gas in the clean gas discharge pipe 72 can be pushed and pulled into the chimney 80 by the fan 721 to be discharged.

In addition, one side of the cooling region 702 of the sorption rotor 70 is connected to the cooling gas inlet pipe 73 for allowing the gas to enter the cooling region 702 of the sorption rotor 70 for cooling, the other side of the cooling region 702 of the sorption rotor 70 is connected to one end of the cooling gas conveying pipe 74, and the other end of the cooling gas conveying pipe 74 is connected to one end of the third cold-side pipe 41 of the third heat exchanger 40 (as shown in fig. 1 to 2), so as to convey the gas entering the cooling region 702 of the sorption rotor 70 into the third heat exchanger 40 for heat exchange. Furthermore, one end of the hot gas conveying pipeline 75 is connected to the other side of the desorption region 703 of the adsorption rotor 70, and the other end of the hot gas conveying pipeline 75 is connected to the other end of the third cold-side pipeline 41 of the third heat exchanger 40, so that the high-temperature hot gas heat-exchanged by the third heat exchanger 40 can be conveyed to the desorption region 703 of the adsorption rotor 70 through the hot gas conveying pipeline 75 for desorption.

The cooling zone 702 of the sorption rotor 70 has two embodiments, wherein the first embodiment is that the cooling air inlet pipe 73 connected to one side of the cooling zone 702 of the sorption rotor 70 is used for introducing fresh air or external air (as shown in fig. 1), and the cooling zone 702 of the sorption rotor 70 is cooled by the fresh air or the external air. In the second embodiment, the exhaust gas inlet pipe 71 is provided with an exhaust gas communication pipe 711, and the other end of the exhaust gas communication pipe 711 is connected to the cooling gas inlet pipe 73 (as shown in fig. 2) so as to convey the source exhaust gas in the exhaust gas inlet pipe 71 to the cooling zone 702 of the sorption rotary wheel 70 for cooling through the exhaust gas communication pipe 711, and the exhaust gas communication pipe 711 is provided with an exhaust gas communication control valve 7111 (as shown in fig. 2) so as to control the air volume of the exhaust gas communication pipe 711.

In addition, one end of the desorption concentrated gas pipe 76 is connected TO one side of the desorption region 703 of the adsorption rotor 70, and the other end of the desorption concentrated gas pipe 76 is connected TO one end of the first cold-side pipe 21 of the first heat exchanger 20, wherein the other end of the first cold-side pipe 21 of the first heat exchanger 20 is connected TO one end of the first cold-side transfer pipe 61, the other end of the first cold-side transfer pipe 61 is connected TO one end of the second cold-side pipe 31 of the second heat exchanger 30, the other end of the second cold-side pipe 31 of the second heat exchanger 30 is connected TO one end of the second cold-side transfer pipe 62, and the other end of the second cold-side transfer pipe 62 is connected TO the inlet 11 of the direct-fired incinerator (TO) 10 (as shown in fig. 1 TO 2), so that the desorbed concentrated gas desorbed at a high temperature can be transported TO one end of the first cold-side pipe 21 of the first heat exchanger 20 through the desorbed concentrated gas pipe 76, TO one end of the first cold-side transport pipe 61 through the other end of the first cold-side pipe 21 of the first heat exchanger 20, TO one end of the second cold-side pipe 31 of the second heat exchanger 30 through the other end of the first cold-side transport pipe 61, TO one end of the second cold-side transport pipe 62 through the other end of the second cold-side pipe 31 of the second heat exchanger 30, and TO the inlet 11 of the direct combustion type incinerator (TO) 10 through the other end of the second cold-side transport pipe 62, so that the burner 101 of the direct combustion type incinerator (TO) 10 can be pyrolyzed TO reduce volatile organic compounds. The desorption concentrate gas line 76 is further provided with a blower 761 (as shown in fig. 2) for pushing and pulling the desorption concentrate gas into one end of the first cold-side line 21 of the first heat exchanger 20.

In addition, the present invention mainly adds a design of a heat medium oil system 90, the heat medium oil system 90 is provided with a heat medium oil tank 91, an air intake heat exchanger 92 and a hearth heat exchanger 93, and the heat medium oil tank 91 is provided with an air intake heat medium oil output pipeline 911, an air intake heat medium oil input pipeline 912, a hearth heat medium oil output pipeline 913 and a hearth heat medium oil input pipeline 914 (as shown in fig. 1 to 2), the air intake heat exchanger 92 is provided on the exhaust gas air intake pipeline 71, the air intake heat exchanger 92 is provided with a cold side pipeline 921 and a hot side pipeline 922, one end of the cold side pipeline 921 is connected with the air intake heat medium oil output pipeline 911 of the heat medium oil tank 91, and the other end of the cold side pipeline 921 is connected with the air intake heat medium oil input pipeline 912 of the heat medium oil tank 91, the source exhaust gas of the exhaust gas air intake pipeline 71 firstly enters one end of the hot side pipeline 922 of the air intake heat exchanger 92, then is output from the other end of the hot side pipeline 922 of the air intake heat exchanger 92, and is conveyed to the adsorption area 701 of the adsorption rotor 70 through the exhaust gas pipeline 71. The exhaust gas inlet pipe 71 is further provided with a fan 712 (shown in fig. 2) to push and pull the source exhaust gas into one end of the hot side pipe 922 of the inlet heat exchanger 92.

In addition, the furnace heat exchanger 93 is disposed in the furnace 102 of the direct-fired incinerator (TO) 10, the furnace heat exchanger 93 is provided with a cold side pipeline 931 and a hot side pipeline 932 (as shown in fig. 1 TO 2), one end of the cold side pipeline 931 is connected TO the furnace heat medium oil output pipeline 913 of the heat medium oil tank 91, the other end of the cold side pipeline 931 is connected TO the furnace heat medium oil input pipeline 914 of the heat medium oil tank 91, one end of the hot side pipeline 932 of the furnace heat exchanger 93 is connected TO the other end of the second hot side pipeline 32 of the second heat exchanger 30 (as shown in fig. 1 TO 2), and the other end of the hot side pipeline 932 of the furnace heat exchanger 93 is connected TO one end of the third pipeline hot side 42 of the third heat exchanger 40.

The heat medium oil groove 91 of the heat medium oil system 90 uses the heat medium as the heat source, and the heat medium is a liquid oil product, and the heat medium can be circularly heated and used through the air inlet heat medium oil output pipeline 911, the air inlet heat medium oil input pipeline 912, the furnace heat medium oil output pipeline 913 and the furnace heat medium oil input pipeline 914, so that the relative humidity of the source exhaust gas can be reduced through a circulation manner, and the adsorption efficiency of the source exhaust gas entering the adsorption area 701 of the adsorption rotating wheel 70 can be improved.

The burner 101 of the direct combustion type incinerator (TO) 10 can firstly deliver the burned gas TO one side of the second hot side pipeline 32 of the second heat exchanger 30 for heat exchange, then deliver the burned gas TO the other side of the second hot side pipeline 32 of the second heat exchanger 30 TO the hot side pipeline 932 of the furnace heat exchanger 93 (as shown in fig. 1 TO 2), and deliver the burned gas TO one side of the third hot side pipeline 42 of the third heat exchanger 40 for heat exchange after passing through the hot side pipeline 932 of the furnace heat exchanger 93, then deliver the burned gas TO one side of the first hot side pipeline 22 of the first heat exchanger 20 for heat exchange, finally deliver the burned gas TO the outlet 12 of the direct combustion type incinerator (TO) 10 from the other side of the first hot side pipeline 22 of the first heat exchanger 20, and then deliver the burned gas TO the chimney 80 from the outlet 12 of the direct combustion type incinerator (TO) 10 (as shown in fig. 1 TO 2) for discharge through the chimney 80.

In addition, the furnace heat exchanger 93 of the present invention can adjust the position in the furnace chamber 102 of the direct combustion incinerator (TO) 10 according TO the requirement of the third heat exchanger 40 for the burned gas with higher temperature, the furnace head 101 of the direct combustion incinerator (TO) 10 can firstly transport the burned gas TO one side of the second hot-side pipeline 32 of the second heat exchanger 30 for heat exchange, then transport the burned gas TO the third hot-side pipeline 42 of the third heat exchanger 40 again from the other side of the second hot-side pipeline 32 of the second heat exchanger 30 (as shown in fig. 3 TO 4), and transport the burned gas TO one side of the hot-side pipeline 932 of the furnace heat exchanger 93 for heat exchange after passing through the third hot-side pipeline 42 of the third heat exchanger 40, then transport the burned gas TO one side of the first hot-side pipeline 22 of the first heat exchanger 20 for heat exchange from the other side of the furnace heat exchanger 93, and finally transport the burned gas TO one side of the first hot-side pipeline 22 of the first heat exchanger 20 TO the outlet 12 of the direct combustion incinerator 10 through the chimney 80 (as shown in fig. 3 TO 4) for discharging the incinerator 10 through the chimney 80.

In addition, another embodiment of the runner system with hot medium of the present invention (as shown in fig. 5 TO 6) is provided, wherein the direct-fired incinerator (TO) 10, the first heat exchanger 20, the second heat exchanger 30, the first cold-side delivery pipe 61, the second cold-side delivery pipe 62, the adsorption runner 70, the chimney 80 and the hot medium system 90 are designed in the same manner as described above, and therefore, the contents of the direct-fired incinerator (TO) 10, the first heat exchanger 20, the second heat exchanger 30, the first cold-side delivery pipe 61, the second cold-side delivery pipe 62, the adsorption runner 70, the chimney 80 and the hot medium system 90 are not repeated, and please refer TO the above description.

The difference is that in another embodiment, the third heat exchanger 40 connected TO the other end of the hot gas conveying pipeline 75 and disposed in the furnace chamber 102 of the direct combustion incinerator (TO) 10 is removed, and the other end of the hot gas conveying pipeline 75 is connected TO a heater 50 (as shown in fig. 5 TO 6) disposed outside the furnace chamber 102 of the direct combustion incinerator (TO) 10, wherein the heater 50 is any one of an air-TO-air heat exchanger, a liquid-TO-air heat exchanger, an electric heater, and a gas heater, the other end of the cooling gas conveying pipeline 74 connected TO the other side of the cooling zone 702 of the adsorption rotor 70 is connected TO the heater 50 (as shown in fig. 5 TO 6), so that the gas entering the cooling zone 702 of the adsorption rotor 70 is conveyed into the heater 50 for heating, and one end of the hot gas conveying pipeline 75 is connected TO the other side of the desorption zone 703 of the adsorption rotor 70, and the other end of the hot gas conveying pipeline 75 is connected TO the heater 50, so that the hot gas heated by the heater 50 is conveyed TO the desorption zone 703 of the adsorption rotor 70 for desorption.

The method for turning the hot oil mainly includes a direct-fired incinerator (TO) 10, a first heat exchanger 20, a second heat exchanger 30, a third heat exchanger 40, a first cold side transfer pipe 61, a second cold side transfer pipe 62, an adsorption wheel 70, a chimney 80 and a hot oil system 90 (as shown in fig. 1 TO 2), wherein the first heat exchanger 20 is provided with a first cold side pipe 21 and a first hot side pipe 22, the second heat exchanger 30 is provided with a second cold side pipe 31 and a second hot side pipe 32, the third heat exchanger 40 is provided with a third cold side pipe 41 and a third hot side pipe 42, one end of the first cold side transfer pipe 61 is connected with the other end of the first cold side pipe 21, the other end of the first cold side transfer pipe 61 is connected with one end of the second cold side pipe 31, one end of the second cold side transfer pipe 62 is connected with the other end of the second cold side pipe 31, and the other end of the second cold side transfer pipe 62 is connected with the inlet 11 of the direct-fired incinerator (TO) 10. The direct combustion type incinerator (TO) 10 is further provided with a burner 101 and a hearth 102, the burner 101 is communicated with the hearth 102, the first heat exchanger 20, the second heat exchanger 30 and the third heat exchanger 40 are respectively disposed in the hearth 102 of the direct combustion type incinerator (TO) (as shown in fig. 1 TO 2), the direct combustion type incinerator (TO) 10 is provided with an inlet 11 and an outlet 12, the inlet 11 is disposed at the burner 101, the outlet 12 of the direct combustion type incinerator (TO) 10 is connected TO the chimney 80, the hot medium oil system 90 is further provided with a hot medium oil tank 91, an air inlet heat exchanger 92 and a hearth heat exchanger 93, the hot medium oil tank 91 is provided with an air inlet hot medium oil outlet pipeline 911, an air inlet hot medium oil inlet pipeline 912, a hearth hot medium oil outlet pipeline 913 and a hearth oil inlet pipeline 914 (as shown in fig. 1 TO 2), thereby, the organic waste gas can enter the hearth 101 from the inlet 11 for combustion, and the gas after combustion can pass through the burner 102 and be discharged from the hearth outlet 12 TO the chimney 80 for energy saving.

The adsorption rotor 70 of the present invention is further provided with an adsorption zone 701, a cooling zone 702 and a desorption zone 703, and the adsorption rotor 70 is connected to an exhaust gas inlet line 71, a clean gas discharge line 72, a cooling gas inlet line 73, a cooling gas delivery line 74, a hot gas delivery line 75 and a desorption concentrated gas line 76 (as shown in fig. 1 to fig. 2). Wherein the adsorption wheel 70 is a zeolite concentration wheel or a concentration wheel made of other materials.

The heat medium oil groove of the heat medium oil system 90 uses the heat medium as the heat source, and the heat medium is a liquid oil product, and the heat medium can be used by circulating heating through the air intake heat medium oil output pipeline 911, the air intake heat medium oil input pipeline 912, the furnace heat medium oil output pipeline 913, and the furnace heat medium oil input pipeline 914, so that the relative humidity of the source waste gas can be reduced in a circulating manner, and the adsorption efficiency of the adsorption zone 701 entering the adsorption rotating wheel 70 can be improved. The intake heat exchanger 92 is disposed on the exhaust gas intake pipe 71, the intake heat exchanger 92 has a cold side pipe 921 and a hot side pipe 922 (as shown in fig. 1 to fig. 2), one end of the cold side pipe 921 is connected to the intake heat medium oil output pipe 911 of the heat medium oil tank 91, and the other end of the cold side pipe 921 is connected to the intake heat medium oil input pipe 912 of the heat medium oil tank 91. Furthermore, the furnace heat exchanger 93 is disposed in the furnace 102 of the direct combustion incinerator (TO) 10, the furnace heat exchanger 93 is provided with a cold side pipeline 931 and a hot side pipeline 932 (as shown in fig. 1 TO fig. 2), one end of the cold side pipeline 931 is connected TO the furnace heat medium oil output pipeline 913 of the heat medium oil tank 91, and the other end of the cold side pipeline 931 is connected TO the furnace heat medium oil input pipeline 914 of the heat medium oil tank 91.

The method steps of the main embodiment (as shown in fig. 7) include: step S100, transporting the source exhaust gas: source exhaust gas is delivered through the exhaust gas inlet conduit 71 to one end of the hot side conduit 922 of the inlet heat exchanger 92. After the step S100 is completed, the next step S110 is performed.

In addition, the next step is that the source exhaust gas passes through an intake heat exchanger in step S110: the source exhaust gas passes through the hot side pipe 922 of the intake heat exchanger 92, is output from the other end of the hot side pipe 922 of the intake heat exchanger 92, and is delivered to one side of the adsorption region 701 of the adsorption rotor 70 through the exhaust gas intake pipe 71. After the step S110 is completed, the next step S120 is performed.

In the above steps S100 and S110, the source exhaust gas of the exhaust gas inlet pipeline firstly enters one end of the hot side pipeline 922 of the inlet heat exchanger 92, and then is output from the other end of the hot side pipeline 922 of the inlet heat exchanger 92, and is delivered to one side of the adsorption area of the adsorption rotating wheel through the exhaust gas inlet pipeline. The exhaust gas inlet pipe 71 is further provided with a fan 712 (shown in fig. 2) to push and pull the source exhaust gas into one end of the hot side pipe 922 of the inlet heat exchanger 92.

In addition, the next step is that the adsorption runner in step S120 performs adsorption: after being adsorbed by the adsorption region 701 of the adsorption rotor 70, the adsorbed gas is discharged from the other side of the adsorption region 701 of the adsorption rotor 70 through the other end of the clean gas discharge line 72. After the step S120 is completed, the next step S130 is performed.

In the step S120, one end of the net gas discharging pipeline 72 is connected to the other side of the adsorption region 701 of the adsorption rotating wheel 70, the other end of the net gas discharging pipeline 72 is connected to the chimney 80 (as shown in fig. 1 to 2), and the net gas discharging pipeline 72 is provided with a fan 721 (as shown in fig. 2), so that the fan 721 can push and pull the adsorbed gas in the net gas discharging pipeline 72 into the chimney 80 for discharging.

Further, the next step, step S130, is to input cooling zone cooling gas: the cooling gas is supplied to the cooling zone 702 of the sorption rotor 70 through the other end of the cooling gas inlet conduit 73 for cooling, and the cooling gas passing through the cooling zone 702 of the sorption rotor 70 is supplied to one end of the third cold-side conduit 41 of the third heat exchanger 40 through the other end of the cooling gas supply conduit 74. After the step S130 is completed, the next step S140 is performed.

In the above step S130, one side of the cooling region 702 of the sorption rotor 70 is connected to the cooling air inlet pipe 73, so that the air enters the cooling region 702 of the sorption rotor 70 for cooling, the other side of the cooling region 702 of the sorption rotor 70 is connected to one end of the cooling air conveying pipe 74 (as shown in fig. 1 to 2), and the other end of the cooling air conveying pipe 74 is connected to one end of the third cold-side pipe 41 of the third heat exchanger 40, so that the air entering the cooling region 702 of the sorption rotor 70 is conveyed into the third heat exchanger 40 for heat exchange.

The cooling zone 702 of the sorption rotor 70 has two embodiments, wherein in the first embodiment, the cooling air inlet pipe 73 connected to one side of the cooling zone 702 of the sorption rotor 70 is used for introducing fresh air or external air (as shown in fig. 1), and the cooling zone 702 of the sorption rotor 70 is cooled by the fresh air or the external air. In the second embodiment, the exhaust gas inlet pipe 71 is provided with an exhaust gas communication pipe 711 (as shown in fig. 2), and the other end of the exhaust gas communication pipe 711 is connected to the cooling gas inlet pipe 73 so as to convey the source exhaust gas in the exhaust gas inlet pipe 71 to the cooling zone 702 of the sorption rotary wheel 70 for cooling through the exhaust gas communication pipe 711, and the exhaust gas communication pipe 711 is provided with an exhaust gas communication control valve 7111 (as shown in fig. 2) so as to control the air volume of the exhaust gas communication pipe 711.

In addition, the next step is to perform desorption in the desorption zone of step S140: hot gas is delivered to the desorption region 703 of the adsorption rotor 70 for desorption through the hot gas delivery line 75 connected to the other end of the third cold-side line 41 of the third heat exchanger 40, and desorption concentrated gas is delivered to one end of the first cold-side line 21 of the first heat exchanger 20 through the other end of the desorption concentrated gas line 76. After the step S140 is completed, the next step S150 is performed.

In the step S140, one end of the hot gas conveying pipeline 75 is connected to the other side of the desorption region 703 of the adsorption rotor 70, and the other end of the hot gas conveying pipeline 75 is connected to the other end of the third cold-side pipeline 41 of the third heat exchanger 40 (as shown in fig. 1 to 2), so that the high-temperature hot gas heat-exchanged by the third heat exchanger 40 can be conveyed to the desorption region 703 of the adsorption rotor 70 through the hot gas conveying pipeline 75 for desorption.

Further, the next step, step S150, is to desorb the concentrated gas delivery: the desorbed concentrated gas is further transferred TO one end of the second cold side pipe 31 of the second heat exchanger 30 through the first cold side transfer pipe 61 TO which the other end of the first cold side pipe 21 of the first heat exchanger 20 is connected, and is further transferred TO the inlet 11 of the direct combustion type incinerator (TO) 10 through the second cold side transfer pipe 62 TO which the other end of the second cold side pipe 31 of the second heat exchanger 30 is connected. After the step S150 is completed, the next step S160 is performed.

In the above step S150, the other end of the first cold-side pipe 21 of the first heat exchanger 20 is connected TO one end of the first cold-side conveying pipe 61, the other end of the first cold-side conveying pipe 61 is connected TO one end of the second cold-side pipe 31 of the second heat exchanger 30, the other end of the second cold-side pipe 31 of the second heat exchanger 30 is connected TO one end of the second cold-side conveying pipe 62, and the other end of the second cold-side conveying pipe 62 is connected TO the inlet 11 of the direct-fired incinerator (TO) 10 (as shown in fig. 1 TO 2), so that the desorption concentrated gas desorbed by high temperature can be conveyed into one end of the first cold-side pipe 21 of the first heat exchanger 20 through the desorption concentrated gas pipe 76, and conveyed into one end of the first cold-side conveying pipe 61 by the other end of the first cold-side pipe 21 of the first heat exchanger 20, and conveyed into one end of the second cold-side conveying pipe 31 of the second heat exchanger 30 by the other end of the first cold-side conveying pipe 61, and the second cold-side conveying pipe 62 (TO) can be conveyed into the second cold-side conveying pipe 31 of the second heat exchanger 30 through the direct-fired incinerator 10, so that the organic compound can be reduced, and the desorption concentrated gas can be conveyed into the second cold-side conveying pipe 62 by the desorption concentrated gas. The desorption concentrate gas line 76 is further provided with a blower 761 (as shown in fig. 2) for pushing and pulling the desorption concentrate gas into one end of the first cold-side line 21 of the first heat exchanger 20.

Further, the burned gas of step S160 to be carried out next is: burned gas generated by combustion at the burner 101 of the direct combustion incinerator (TO) 10 is transferred TO one end of the second hot side pipe 32 of the second heat exchanger 30, and is transferred from the other end of the second hot side pipe 32 of the second heat exchanger 30 TO one end of the hot side pipe 932 of the furnace heat exchanger 93. After the step S160 is completed, the next step S170 is performed.

In addition, the burned gas of the next step S170 passes through a furnace heat exchanger: the burned gas passes through the hot-side duct 932 of the furnace heat exchanger 93, and is output from the other end of the hot-side duct 932 of the furnace heat exchanger 93 to one end of the third hot-side duct 42 of the third heat exchanger 40. After the step S170 is completed, the next step S180 is performed.

In addition, the next step is that the burnt gas output of the step S180 is output: the burned gas is then transferred from the other end of the third hot-side pipe 42 of the third heat exchanger 40 TO one end of the first hot-side pipe 22 of the first heat exchanger 20, and finally transferred from the other end of the first hot-side pipe 22 of the first heat exchanger 20 TO the outlet 12 of the direct combustion type incinerator (TO) 10.

Wherein the burner 101 of the direct combustion type incinerator (TO) 10 can firstly deliver the burned gas TO one side of the second hot side pipe 32 of the second heat exchanger 30 for heat exchange (as shown in fig. 1 TO 2), secondly deliver the burned gas TO the hot side pipe 932 of the furnace heat exchanger 93 from the other side of the second hot side pipe 32 of the second heat exchanger 30, and after the burned gas passes through the hot side pipe 932 of the furnace heat exchanger 93, secondly deliver the burned gas TO one side of the third hot side pipe 42 of the third heat exchanger 40 for heat exchange, thirdly deliver the burned gas TO one side of the first hot side pipe 22 of the first heat exchanger 20 for heat exchange from the other side of the third hot side pipe 42 of the third heat exchanger 40, thirdly deliver the burned gas TO the outlet 12 of the direct combustion type incinerator (TO) 10 from the outlet 12 of the direct combustion type incinerator (TO) 10 for heat exchange, finally deliver the burned gas TO the chimney 80 (as shown in fig. 1 TO 2) for discharge through the chimney 80.

In addition, in the turning method with heat medium oil according to the present invention, as shown in fig. 7, in the main embodiment, the source exhaust gas is conveyed in step S100, the source exhaust gas is adsorbed by the adsorption turning wheel in step S110, the cooling gas is input in the cooling zone in step S130, the desorption zone is desorbed in step S140, the concentrated gas is desorbed in step S150, the burned gas in step S160 is conveyed, the burned gas in step S170 is conveyed through the furnace heat exchanger, and the burned gas in step S180 is output through the gas outlet, which has been already proposed and described above, please refer to the above description.

The position of the furnace heat exchanger 93 of the present invention in the furnace 102 of the direct combustion incinerator (TO) 10 can be adjusted according TO the burned gas with higher temperature required by the third heat exchanger 40, and the source exhaust gas of step S200 is transported, the source exhaust gas of step S210 is adsorbed by the adsorption runner of step S220, the cooling gas of step S230 is input TO the cooling zone, the desorption of step S240 and the desorption of step S250 are transported by the same design as that of the source exhaust gas of step S100, the source exhaust gas of step S110 is adsorbed by the adsorption runner of step S120, the cooling gas of step S130 is input TO the cooling zone, the desorption of step S140 and the desorption of step S150 in the main embodiment (shown in fig. 7) in the second embodiment (shown in fig. 8) having the third heat exchanger 40, and only the difference is that the burned gas of step S160 is transported, the burned gas of step S170 is transported by the heat exchanger and the burned gas outlet of step S180.

The difference of the second embodiment with the third heat exchanger 40 is that the burned gas is delivered in step S260: burned gas generated by combustion at the burner 101 of the direct combustion type incinerator (TO) 10 is transferred TO one end of the second hot side pipe 32 of the second heat exchanger 30, and is transferred TO one end of the third hot side pipe 42 of the third heat exchanger 40 from the other end of the second hot side pipe 32 of the second heat exchanger 30. After the step S260 is completed, the next step S270 is performed.

In addition, the burned gas of the next step S270 passes through a furnace heat exchanger: the burned gas is transported from the other end of the third hot side pipeline 42 of the third heat exchanger 40 to one end of the hot side pipeline 932 of the furnace heat exchanger 93, and the burned gas passes through the hot side pipeline 932 of the furnace heat exchanger 93 and is then output from the other end of the hot side pipeline 932 of the furnace heat exchanger 93. After the step S270 is completed, the next step S280 is performed.

Further, the next step is to output the burned gas at the outlet in step S280: the burned gas is further transported from the other end of the hot-side pipe 932 of the furnace heat exchanger 93 TO one end of the first hot-side pipe 22 of the first heat exchanger 20, and finally transported from the other end of the first hot-side pipe 22 of the first heat exchanger 20 TO the outlet 12 of the direct combustion incinerator (TO) 10.

Wherein the burner 101 of the direct combustion type incinerator (TO) 10 can firstly transfer the burned gas TO one side of the second hot side pipe 32 of the second heat exchanger 30 for heat exchange, secondly transfer the burned gas TO the third hot side pipe 42 of the third heat exchanger 40 from the other side of the second hot side pipe 32 of the second heat exchanger 30 (as shown in fig. 3 TO 4) and transfer the burned gas TO one side of the hot side pipe 932 of the furnace heat exchanger 93 for heat exchange after passing through the third hot side pipe 42 of the third heat exchanger 40, thirdly transfer the burned gas TO one side of the first hot side pipe 22 of the first heat exchanger 20 for heat exchange from the other side of the hot side pipe 932 of the furnace heat exchanger 93, thirdly transfer the burned gas TO one side of the first hot side pipe 22 of the first heat exchanger 20 for heat exchange, thirdly transfer the burned gas TO the outlet 12 of the direct combustion type incinerator (TO) 10 from the outlet 12 of the direct combustion type incinerator (TO) 10 (as shown in fig. 3 TO 4) for discharge through the chimney 80.

In addition, in the turning method with heat medium oil according to the present invention (as shown in fig. 7), in the main embodiment, the source exhaust gas is conveyed in step S100, the source exhaust gas is adsorbed by the gas inlet heat exchanger in step S110, the adsorption turning wheel in step S120 is adsorbed, the cooling gas is input in the cooling zone in step S130, the desorption zone in step S140 is desorbed, the concentrated gas is desorbed in step S150 and conveyed, the burned gas in step S160 is conveyed, the burned gas in step S170 is output through the furnace heat exchanger and the burned gas outlet in step S180, and the above description is referred to.

The source exhaust gas transportation in step S300, the source exhaust gas adsorption in step S310, the concentrated desorption gas transportation in step S350, and the gas incineration in step S360 in the third embodiment (shown in fig. 9) are all the same as the source exhaust gas transportation in step S100, the source exhaust gas adsorption in step S110, the concentrated desorption gas transportation in step S150, and the gas incineration in step S160 in the main embodiment (shown in fig. 7), except that the cooling zone cooling gas is input in step S130, the desorption zone is desorbed in step S140, and the gas incineration in step S170 is output through the furnace heat exchanger and the gas incineration in step S180.

Therefore, the same contents as those of the source exhaust gas transportation in step S300, the source exhaust gas adsorption by the intake heat exchanger in step S310, the adsorption by the adsorption rotor in step S320, the desorption/concentration gas transportation in step S350, and the gas transportation after incineration in step S360 are not repeated, and the above description is referred to. The following description will be made with respect to the cooling zone cooling gas input at step S330, the desorption zone desorption at step S340, and the gas burned at step S370 through the furnace heat exchanger and the gas outlet output burned at step S380 in the third embodiment (shown in fig. 9).

The difference of the third embodiment is that step S330 inputs cooling air of the cooling area: the cooling gas is supplied to the cooling zone 702 of the sorption rotor 70 through the other end of the cooling gas inlet conduit 73 for cooling, and the cooling gas passing through the cooling zone 702 of the sorption rotor 70 is outputted through the other end of the cooling gas supply conduit 74. After the step S330 is completed, the next step S340 is performed.

In addition, the desorption zone in the next step S340 is to perform desorption: one end of the hot gas conveying pipeline 75 is connected to the desorption region 703 of the adsorption rotor 70, and is desorbed by the desorption region 703 of the adsorption rotor 70, and then the desorption concentrated gas is conveyed to one end of the first cold-side pipeline 21 of the first heat exchanger 20 through the desorption concentrated gas pipeline 76.

In the above steps S330 and S340, the hot gas conveying pipeline 75 takes away the third heat exchanger 40 whose another end is connected TO the inside of the furnace 102 of the direct-fired incinerator (TO) 10, and connects another end of the hot gas conveying pipeline 75 TO a heater 50 (as shown in fig. 5 TO 6) which is additionally disposed outside the furnace 102 of the direct-fired incinerator (TO) 10, wherein the heater 50 is any one of an air-TO-air heat exchanger, a liquid-TO-air heat exchanger, an electric heater, and a gas heater, the other end of the cooling gas conveying pipeline 74 connected TO another side of the cooling zone 702 of the adsorption rotor 70 is connected TO the heater 50, so that the gas entering the cooling zone 702 of the adsorption rotor 70 is conveyed into the heater 50 TO be heated (as shown in fig. 5 TO 6), one end of the hot gas conveying pipeline 75 is connected TO another side of the desorption zone 703 of the adsorption rotor 70, and another end of the hot gas conveying pipeline 75 is connected TO the heater 50, so that the high-temperature hot gas heated by the heater 50 can be conveyed TO the desorption zone 703 of the adsorption rotor 70 TO be desorbed for use.

The burned gas in step S370 passes through a furnace heat exchanger: the burned gas passes through the hot-side duct 932 of the furnace heat exchanger 93, and is output from the other end of the hot-side duct 932 of the furnace heat exchanger 93 to one end of the first hot-side duct 22 of the first heat exchanger 20. After the step S370 is completed, the next step S380 is performed.

Further, the next step is to output the burned gas at the gas outlet in step S380: the incinerated gas is finally delivered from the other end of the first hot-side pipe 22 of the first heat exchanger 20 TO the outlet 12 of the direct-fired incinerator (TO) 10.

In the above steps S370 and S380, the burner 101 of the direct combustion type incinerator (TO) 10 can firstly deliver the burned gas TO one side of the second hot-side pipeline 32 of the second heat exchanger 30 for heat exchange, then deliver the burned gas TO the furnace heat exchanger 93 from the other side of the second hot-side pipeline 32 of the second heat exchanger 30, and deliver the burned gas TO one side of the first hot-side pipeline 22 of the first heat exchanger 20 for heat exchange after passing through the furnace heat exchanger 93 (as shown in fig. 5 TO 6), and finally deliver the burned gas TO the outlet 12 of the direct combustion type incinerator (TO) 10 from the other side of the first hot-side pipeline 22 of the first heat exchanger 20, and deliver the burned gas TO the chimney 80 from the outlet 12 of the direct combustion type incinerator (TO) 10 for discharge through the chimney 80.

From the above detailed description, it will be apparent to those skilled in the art that the foregoing objects and advantages of the present invention are achieved and are in accordance with the requirements of the patent laws.

The above description is only a preferred embodiment of the present invention, and the scope of the present invention should not be limited thereby; therefore, any changes or equivalent substitutions which can be easily made by those skilled in the art are within the protection scope of the claims of the present invention.

Claims

1. A runner system with heating medium oil is characterized by comprising:

the direct-fired incinerator (TO) is provided with a furnace end and a hearth, the furnace end is communicated with the hearth, the direct-fired incinerator (TO) is provided with an inlet and an outlet, and the inlet is arranged at the furnace end;

a first heat exchanger, which is arranged in the hearth of the direct-fired incinerator (TO) and is provided with a first cold-side pipeline and a first hot-side pipeline;

a second heat exchanger, which is arranged in the hearth of the direct-fired incinerator (TO) and is provided with a second cold-side pipeline and a second hot-side pipeline;

a third heat exchanger, which is arranged in the hearth of the direct-fired incinerator (TO) and is provided with a third cold-side pipeline and a third hot-side pipeline;

the first cold side conveying pipeline is connected with one end of the first cold side pipeline, and the other end of the first cold side conveying pipeline is connected with one end of the second cold side pipeline;

a second cold side transfer pipe, one end of which is connected with the other end of the second cold side pipe, and the other end of which is connected with the inlet of the direct-fired incinerator (TO);

the adsorption rotating wheel is provided with an adsorption area, a cooling area and a desorption area, the adsorption rotating wheel is connected with a waste gas inlet pipeline, a clean gas discharge pipeline, a cooling gas inlet pipeline, a cooling gas conveying pipeline, a hot gas conveying pipeline and a desorption concentrated gas pipeline, one end of the waste gas inlet pipeline is connected to one side of the adsorption area of the adsorption rotating wheel, one end of the clean gas discharge pipeline is connected with the other side of the adsorption area of the adsorption rotating wheel, one end of the cooling gas inlet pipeline is connected with one side of the cooling area of the adsorption rotating wheel, one end of the cooling gas conveying pipeline is connected with the other side of the cooling area of the adsorption rotating wheel, the other end of the cooling gas conveying pipeline is connected with one end of a third cold side pipeline of the third heat exchanger, one end of the hot gas conveying pipeline is connected with the other side of the desorption area of the adsorption rotating wheel, the other end of the desorption concentrated gas pipeline is connected with one side of the desorption area of the adsorption rotating wheel, and the other end of the desorption concentrated gas pipeline is connected with a first cold side of the first heat exchanger;

the other end of the purified gas discharge pipeline is connected with the chimney; and

the hot medium oil system is provided with a hot medium oil groove, an air inlet heat exchanger and a hearth heat exchanger, the hot medium oil groove is provided with an air inlet hot medium oil output pipeline, an air inlet hot medium oil input pipeline, a hearth hot medium oil output pipeline and a hearth hot medium oil input pipeline, the air inlet heat exchanger is arranged on the waste gas inlet pipeline, the air inlet heat exchanger is provided with a cold side pipeline and a hot side pipeline, one end of the cold side pipeline is connected with the air inlet hot medium oil output pipeline of the hot medium oil groove, the other end of the cold side pipeline is connected with the air inlet hot medium oil input pipeline of the hot medium oil groove, source waste gas of the waste gas inlet pipeline firstly enters one end of the hot side pipeline of the air inlet heat exchanger and then is output by the other end of the hot side pipeline of the air inlet heat exchanger and is conveyed TO one side of an adsorption area of the hearth through the waste gas inlet pipeline, the heat exchanger is arranged in the hearth of the direct combustion type incinerator (TO), the heat exchanger is provided with a cold side pipeline and a hot side pipeline, one end of the cold side pipeline is connected with one end of the hot side pipeline of the hot medium oil groove, the hot side pipeline of the hot medium oil groove is connected with the second hot side pipeline of the hot medium oil groove, and the second hot medium oil groove, and the hot side pipeline of the hot medium oil heat exchanger are connected with one end of the hot medium oil groove.

2. A runner system with heating medium oil is characterized by comprising:

the hot medium oil system is provided with a hot medium oil groove, an air inlet heat exchanger and a hearth heat exchanger, the hot medium oil groove is provided with an air inlet hot medium oil output pipeline, an air inlet hot medium oil input pipeline, a hearth hot medium oil output pipeline and a hearth hot medium oil input pipeline, the air inlet heat exchanger is arranged on the waste gas inlet pipeline, the air inlet heat exchanger is provided with a cold side pipeline and a hot side pipeline, one end of the cold side pipeline is connected with the air inlet hot medium oil output pipeline of the hot medium oil groove, the other end of the cold side pipeline is connected with the air inlet hot medium oil input pipeline of the hot medium oil groove, source waste gas of the waste gas inlet pipeline firstly enters one end of the hot side pipeline of the air inlet heat exchanger and then is output by the other end of the hot side pipeline of the air inlet heat exchanger and is conveyed TO one side of an adsorption area of the hearth through the waste gas inlet pipeline, the heat exchanger is arranged in the hearth of the direct combustion furnace (TO), the heat exchanger is provided with a cold side pipeline and a hot side pipeline, one end of the cold side pipeline is connected with one end of the hot side pipeline of the hot medium oil groove, the hot side pipeline is connected with the first hot medium oil groove, and the hot side pipeline of the first hot medium oil groove.

3. A runner system with heating medium oil is characterized by comprising:

the adsorption rotating wheel is provided with an adsorption area, a cooling area and a desorption area, the adsorption rotating wheel is connected with a waste gas inlet pipeline, a clean gas discharge pipeline, a cooling gas inlet pipeline, a cooling gas conveying pipeline, a hot gas conveying pipeline and a desorption concentrated gas pipeline, one end of the waste gas inlet pipeline is connected to one side of the adsorption area of the adsorption rotating wheel, one end of the clean gas discharge pipeline is connected with the other side of the adsorption area of the adsorption rotating wheel, one end of the cooling gas inlet pipeline is connected with one side of the cooling area of the adsorption rotating wheel, one end of the cooling gas conveying pipeline is connected with the other side of the cooling area of the adsorption rotating wheel, one end of the hot gas conveying pipeline is connected with the other side of the desorption area of the adsorption rotating wheel, one end of the desorption concentrated gas pipeline is connected with one side of the desorption area of the adsorption rotating wheel, and the other end of the desorption concentrated gas pipeline is connected with one end of a first cold side pipeline of the first heat exchanger;

the hot medium oil system is provided with a hot medium oil groove, an air inlet heat exchanger and a hearth heat exchanger, the hot medium oil groove is provided with an air inlet hot medium oil output pipeline, an air inlet hot medium oil input pipeline, a hearth hot medium oil output pipeline and a hearth hot medium oil input pipeline, the air inlet heat exchanger is arranged on the waste gas inlet pipeline, the air inlet heat exchanger is provided with a cold side pipeline and a hot side pipeline, one end of the cold side pipeline is connected with the air inlet hot medium oil output pipeline of the hot medium oil groove, the other end of the cold side pipeline is connected with the air inlet hot medium oil input pipeline of the hot medium oil groove, source waste gas of the waste gas inlet pipeline firstly enters one end of the hot side pipeline of the air inlet heat exchanger and then is output by the other end of the hot side pipeline of the air inlet heat exchanger and is conveyed TO one side of an adsorption area of the hearth through the waste gas inlet pipeline, the heat exchanger is arranged in the hearth of the direct combustion type furnace (TO), the heat exchanger is provided with a cold side pipeline and a hot side pipeline, one end of the cold side pipeline is connected with one end of the hot side pipeline of the hot side heat exchanger of the hearth, and the second hot side pipeline of the hot medium oil groove, and the hot side pipeline are connected with one end of the first hot medium oil groove.

4. The runner system with heating medium oil according TO any one of claims 1 TO 3, characterized in that the outlet of the direct-fired incinerator (TO) is further connected TO the chimney.

5. The runner system with heating medium oil of any one of claims 1 to 3, wherein the cooling air inlet pipeline is further used for supplying fresh air or external air.

6. The runner system with heating medium oil of any one of claims 1 to 3, wherein the exhaust gas inlet pipe is further provided with an exhaust gas communication pipe connected to the cooling gas inlet pipe, and the exhaust gas communication pipe is further provided with an exhaust gas communication control valve for controlling the air volume of the exhaust gas communication pipe.

7. The runner system with heating medium oil as claimed in any one of claims 1 to 3, wherein the desorption/concentration gas pipeline is further provided with a blower.

8. The rotary wheel system with heating medium oil as claimed in any one of claims 1 to 3, wherein the net gas discharge line is further provided with a blower.

9. The rotary wheel system with heating medium oil as claimed in any one of claims 1 to 3, wherein the exhaust gas inlet pipeline is further provided with a blower.

10. The runner system with heating medium oil of claim 3, wherein the other end of the cold gas delivery pipeline is further connected to a heater, and the other end of the hot gas delivery pipeline is further connected to the heater, wherein the heater is further any one of an air-to-air heat exchanger, a liquid-to-air heat exchanger, an electric heater, and a gas heater.

11. The runner system with hot medium oil as claimed in any one of claims 1 to 3, wherein the hot medium oil tank of the hot medium oil system further uses hot medium as a heat source, the hot medium is a liquid oil, and the hot medium can be circulated and heated through the inlet hot medium oil output pipeline, the inlet hot medium oil input pipeline, the furnace hot medium oil output pipeline and the furnace hot medium oil input pipeline.

12. A method for turning wheel with heat medium oil is characterized in that a direct-fired incinerator (TO) is mainly provided, a first heat exchanger, a second heat exchanger, a third heat exchanger, a first cold side delivery pipeline, a second cold side delivery pipeline, an adsorption turning wheel, a chimney and a heat medium oil system are arranged, the direct-fired incinerator (TO) is provided with a furnace end and a furnace chamber, the furnace end is communicated with the furnace chamber, the direct-fired incinerator (TO) is provided with an inlet and an outlet, the inlet is arranged at the furnace end, the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, the third heat exchanger is provided with a third cold side pipeline and a third hot side pipeline, one end of the first cold side delivery pipeline is connected with the other end of the first cold side pipeline, the other end of the first cold side conveying pipeline is connected with one end of the second cold side pipeline, one end of the second cold side conveying pipeline is connected with the other end of the second cold side pipeline, the other end of the second cold side conveying pipeline is connected with an inlet of the direct combustion type incinerator (TO), the adsorption rotating wheel is provided with an adsorption area, a cooling area and a desorption area, the adsorption rotating wheel is connected with a waste gas inlet pipeline, a clean gas discharge pipeline, a cooling gas inlet pipeline, a cooling gas conveying pipeline, a hot gas conveying pipeline and a desorption concentrated gas pipeline, the hot medium oil system is provided with a hot medium oil tank, an inlet heat exchanger and a hearth heat exchanger, the hot medium oil tank is provided with an inlet hot medium oil output pipeline, an inlet hot medium oil input pipeline, a hearth hot medium oil output pipeline and a hearth hot medium oil input pipeline, the inlet heat exchanger is arranged on the waste gas inlet pipeline, this heat exchanger admits air is equipped with a cold side pipeline and a hot side pipeline, the one end of this cold side pipeline is connected with the heat medium oil output pipeline that admits air of this heat medium oil groove, the other end of this cold side pipeline is connected with the heat medium oil input pipeline that admits air of this heat medium oil groove, this furnace heat exchanger locates in the furnace of this direct combustion formula burning furnace (TO), this furnace heat exchanger is equipped with a cold side pipeline and a hot side pipeline, the one end of this cold side pipeline is connected with the furnace heat medium oil output pipeline of this heat medium oil groove, the other end of this cold side pipeline is connected with the furnace heat medium oil input pipeline of this heat medium oil groove, and the main step of this method includes:

conveying the source waste gas: the source waste gas is conveyed to one end of a hot side pipeline of the gas inlet heat exchanger through the waste gas inlet pipeline;

passing the source exhaust gas through an intake air heat exchanger: the source waste gas passes through the hot side pipeline of the air inlet heat exchanger, is output from the other end of the hot side pipeline of the air inlet heat exchanger, and is conveyed to one side of the adsorption area of the adsorption rotating wheel through the waste gas inlet pipeline;

the adsorption runner carries out adsorption: after the gas is adsorbed by the adsorption area of the adsorption rotating wheel, the gas after adsorption is output by the other side of the adsorption area of the adsorption rotating wheel through the other end of the purified gas discharge pipeline;

cooling gas input into the cooling area: conveying cooling gas to a cooling area of the adsorption rotating wheel for cooling through the other end of the cooling gas inlet pipeline, and conveying the cooling gas passing through the cooling area of the adsorption rotating wheel to one end of a third cold-side pipeline of the third heat exchanger through the other end of the cooling gas conveying pipeline;

and (3) carrying out desorption in a desorption area: the hot gas is conveyed to the desorption area of the adsorption rotating wheel for desorption through a hot gas conveying pipeline connected with the other end of the third cold side pipeline of the third heat exchanger, and then the desorption concentrated gas is conveyed to one end of the first cold side pipeline of the first heat exchanger through the other end of the desorption concentrated gas pipeline;

and (3) desorption and concentrated gas conveying: the desorbed concentrated gas is conveyed TO one end of a second cold side pipeline of the second heat exchanger through a first cold side conveying pipeline connected with the other end of the first cold side pipeline of the first heat exchanger, and is conveyed TO an inlet of the direct-fired incinerator (TO) through a second cold side conveying pipeline connected with the other end of the second cold side pipeline of the second heat exchanger;

conveying the incinerated gas: conveying incinerated gas generated by combustion of a burner of the direct-fired incinerator (TO) TO one end of a second hot-side pipeline of the second heat exchanger, and conveying the incinerated gas TO one end of a hot-side pipeline of the hearth heat exchanger from the other end of the second hot-side pipeline of the second heat exchanger;

the burned gas passes through a hearth heat exchanger: the incinerated gas passes through the hot side pipeline of the hearth heat exchanger and is output to one end of a third hot side pipeline of the third heat exchanger from the other end of the hot side pipeline of the hearth heat exchanger; and

gas outlet output after incineration: the incinerated gas is then conveyed from the other end of the third hot side pipeline of the third heat exchanger TO one end of the first hot side pipeline of the first heat exchanger, and finally conveyed from the other end of the first hot side pipeline of the first heat exchanger TO the outlet of the direct-fired incinerator (TO).

13. A method for turning wheel with heat medium oil is characterized in that a direct-fired incinerator (TO) is mainly provided, a first heat exchanger, a second heat exchanger, a third heat exchanger, a first cold side delivery pipeline, a second cold side delivery pipeline, an adsorption turning wheel, a chimney and a heat medium oil system are arranged, the direct-fired incinerator (TO) is provided with a furnace end and a furnace chamber, the furnace end is communicated with the furnace chamber, the direct-fired incinerator (TO) is provided with an inlet and an outlet, the inlet is arranged at the furnace end, the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, the third heat exchanger is provided with a third cold side pipeline and a third hot side pipeline, one end of the first cold side delivery pipeline is connected with the other end of the first cold side pipeline, the other end of the first cold side conveying pipeline is connected with one end of the second cold side pipeline, one end of the second cold side conveying pipeline is connected with the other end of the second cold side pipeline, the other end of the second cold side conveying pipeline is connected with an inlet of the direct combustion type incinerator (TO), the adsorption rotating wheel is provided with an adsorption area, a cooling area and a desorption area, the adsorption rotating wheel is connected with a waste gas inlet pipeline, a clean gas discharge pipeline, a cooling gas inlet pipeline, a cooling gas conveying pipeline, a hot gas conveying pipeline and a desorption concentrated gas pipeline, the hot medium oil system is provided with a hot medium oil tank, an inlet heat exchanger and a hearth heat exchanger, the hot medium oil tank is provided with an inlet hot medium oil output pipeline, an inlet hot medium oil input pipeline, a hearth hot medium oil output pipeline and a hearth hot medium oil input pipeline, the inlet heat exchanger is arranged on the waste gas inlet pipeline, the air intake heat exchanger is provided with a cold side pipeline and a hot side pipeline, one end of the cold side pipeline is connected with an air intake heat medium oil output pipeline of the heat medium oil tank, the other end of the cold side pipeline is connected with an air intake heat medium oil input pipeline of the heat medium oil tank, the hearth heat exchanger is arranged in a hearth of the direct-fired incinerator (TO), the hearth heat exchanger is provided with a cold side pipeline and a hot side pipeline, one end of the cold side pipeline is connected with a hearth heat medium oil output pipeline of the heat medium oil tank, the other end of the cold side pipeline is connected with a hearth heat medium oil input pipeline of the heat medium oil tank, and the method mainly comprises the following steps:

conveying source waste gas: the source waste gas is conveyed to one end of a hot side pipeline of the gas inlet heat exchanger through the waste gas inlet pipeline;

cooling gas input into the cooling zone: conveying cooling gas to a cooling area of the adsorption rotating wheel for cooling through the other end of the cooling gas inlet pipeline, and conveying the cooling gas passing through the cooling area of the adsorption rotating wheel to one end of a third cold-side pipeline of the third heat exchanger through the other end of the cooling gas conveying pipeline;

conveying the incinerated gas: conveying incinerated gas generated by combustion of a burner of the direct-fired incinerator (TO) TO one end of a second hot-side pipeline of the second heat exchanger, and conveying the incinerated gas TO one end of a third hot-side pipeline of the third heat exchanger from the other end of the second hot-side pipeline of the second heat exchanger;

the burned gas passes through a hearth heat exchanger: the incinerated gas is conveyed to one end of the hot side pipeline of the hearth heat exchanger from the other end of the third hot side pipeline of the third heat exchanger, and the incinerated gas passes through the hot side pipeline of the hearth heat exchanger and is output from the other end of the hot side pipeline of the hearth heat exchanger; and

gas outlet output after incineration: the incinerated gas is conveyed from the other end of the hot side pipeline of the hearth heat exchanger TO one end of the first hot side pipeline of the first heat exchanger, and finally conveyed from the other end of the first hot side pipeline of the first heat exchanger TO the outlet of the direct-fired incinerator (TO).

14. A runner method with hot media oil is characterized in that a direct-fired incinerator (TO) is mainly provided, a first heat exchanger, a second heat exchanger, a first cold side delivery pipeline, a second cold side delivery pipeline, an adsorption runner, a chimney and a hot media oil system, the direct-fired incinerator (TO) is provided with a furnace end and a furnace chamber, the furnace end is communicated with the furnace chamber, the direct-fired incinerator (TO) is provided with an inlet and an outlet, the inlet is arranged at the furnace end, the first heat exchanger is provided with a first cold side pipeline and a first hot side pipeline, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, one end of the first cold side delivery pipeline is connected with the other end of the first cold side pipeline, the other end of the first cold side delivery pipeline is connected with one end of the second cold side pipeline, one end of the second cold side delivery pipeline is connected with the other end of the second cold side pipeline, the other end of the second cold side delivery pipeline is connected with an inlet of the direct-fired incinerator (TO), the adsorption rotating wheel is provided with an adsorption area, a cooling area and a desorption area, the adsorption rotating wheel is connected with a waste gas inlet pipeline, a clean gas discharge pipeline, a cooling gas inlet pipeline, a cooling gas delivery pipeline, a hot gas delivery pipeline and a desorption concentrated gas pipeline, the hot medium oil system is provided with a hot medium oil tank, an air inlet heat exchanger and a hearth heat exchanger, the hot medium oil tank is provided with an air inlet hot medium oil output pipeline, an air inlet hot medium oil input pipeline, a hearth hot medium oil output pipeline and a hearth hot medium oil input pipeline, the air inlet heat exchanger is arranged on the waste gas inlet pipeline, and the air inlet heat exchanger is provided with a cold side pipeline and a hot side pipeline, one end of the cold side pipeline is connected with an air inlet heat medium oil output pipeline of the heat medium oil tank, the other end of the cold side pipeline is connected with an air inlet heat medium oil input pipeline of the heat medium oil tank, the hearth heat exchanger is arranged in a hearth of the direct-fired incinerator (TO), the hearth heat exchanger is provided with a cold side pipeline and a hot side pipeline, one end of the cold side pipeline is connected with the hearth heat medium oil output pipeline of the heat medium oil tank, the other end of the cold side pipeline is connected with the hearth heat medium oil input pipeline of the heat medium oil tank, and the method mainly comprises the following steps:

cooling gas input into the cooling area: conveying cooling gas to a cooling area of the adsorption rotating wheel for cooling through the other end of the cooling gas inlet pipeline, and outputting the cooling gas passing through the cooling area of the adsorption rotating wheel through the other end of the cooling gas conveying pipeline;

and (3) carrying out desorption in a desorption area: one end of the hot gas conveying pipeline is connected with the desorption area of the adsorption rotating wheel, desorption is carried out by the desorption area of the adsorption rotating wheel, and then desorption concentrated gas is conveyed to one end of the first cold side pipeline of the first heat exchanger through the desorption concentrated gas pipeline;

conveying the incinerated gas: conveying the burned gas generated by burning at the furnace end of the direct-fired incinerator (TO) TO one end of a second hot-side pipeline of the second heat exchanger, and conveying the gas TO one end of a hot-side pipeline of the hearth heat exchanger from the other end of the second hot-side pipeline of the second heat exchanger;

the burned gas passes through a hearth heat exchanger: the incinerated gas passes through a hot side pipeline of the hearth heat exchanger and is output to one end of a first hot side pipeline of the first heat exchanger from the other end of the hot side pipeline of the hearth heat exchanger; and

gas outlet output after incineration: the incinerated gas is finally transported from the other end of the first hot side pipe of the first heat exchanger TO the outlet of the direct fired incinerator (TO).

15. The rotary method with heating medium oil according TO any one of claims 12-14, characterized in that the outlet of the direct-fired incinerator (TO) is further connected TO the chimney.

16. The method for rotating a wheel with heating medium oil as claimed in any one of claims 12-14, wherein the cooling air inlet pipeline is further used for supplying fresh air or external air.

17. The method for rotating wheel with heating medium oil according to any one of claims 12-14, wherein the exhaust gas inlet pipeline is further provided with an exhaust gas communication pipeline, the exhaust gas communication pipeline is connected with the cooling gas inlet 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.

18. The rotary wheel method with heating medium oil as claimed in any one of claims 12-14, wherein the desorption/concentration gas pipeline is further provided with a blower.

19. The process for rotating a wheel with heating medium oil as claimed in any one of claims 12 to 14, wherein the net gas discharge line is further provided with a blower.

20. The method for rotating a wheel with heating medium oil according to any one of claims 12-14, wherein the exhaust gas inlet pipeline is further provided with a blower.

21. The rotary method with heating medium oil of claim 14, wherein the other end of the cold gas delivery line is further connected to a heater, and the other end of the hot gas delivery line is further connected to the heater, wherein the heater is further any one of an air-to-air heat exchanger, a liquid-to-air heat exchanger, an electric heater, and a gas heater.

22. The method for rotating wheel with heating medium oil as claimed in any one of claims 12-14, wherein the heating medium oil tank of the heating medium oil system further uses a heating medium as a heat source, the heating medium is a liquid oil, and the heating medium can be circulated and heated through the inlet heating medium oil output pipeline, the inlet heating medium oil input pipeline, the furnace heating medium oil output pipeline and the furnace heating medium oil input pipeline.