TWM581502U - Direct combustion, flow-division, and high-efficiency organic waste gas processing system - Google Patents

Abstract

The present invention is a direct-fired split high-efficiency organic waste gas treatment system, which mainly performs heat recovery of exhaust gas of a direct-fired incinerator via at least three heat exchangers, and discharges the direct-fired incinerator The gas is further heat-exchanged through a heat exchanger and an exhaust gas (adsorption treatment gas) of the clean gas discharge line at the outlet of the adsorption zone, and is cooled and then sent to the dust removal device for dust or cerium oxide (SiO _{2 ).} Separating the oxides, and finally delivering the gas outputted by the dust removal device to the exhaust gas intake line, and providing a clean gas bypass line in the clean gas discharge line to allow the clean gas discharge line to It has the effect of bypassing the flow, and allows the burned gas to enter the adsorption zone of the adsorption wheel for recycling, without passing through the chimney for discharge, so that the emission of the chimney can be reduced, and the treatment efficiency of the organic waste gas is improved. Can improve.

Description

Direct combustion split high efficiency organic waste gas treatment system

The present invention relates to a direct-fired high-efficiency organic waste gas treatment system, in particular to a recycling zone for the combustion of gas into the adsorption zone of the adsorption wheel, and without exhausting the chimney to cause organic waste gas The processing efficiency can be improved, and it is applicable to organic waste gas treatment systems or the like in the semiconductor industry, the photovoltaic industry or the chemical related industries.

According to the current production process in the semiconductor industry or the optoelectronic industry, volatile organic gases (VOC) are produced. Therefore, processing equipment for treating volatile organic gases (VOC) is installed in each plant to avoid volatile organic gases. (VOC) is directly discharged into the air and causes air pollution. At present, most of the concentrated gas desorbed by the processing equipment is sent to the incinerator for combustion, and the burned gas is sent to the chimney for discharge.

However, in recent years, both the central government and local governments have attached great importance to air pollution, and therefore have set air quality standards for suspended particulates (PM ₁₀ ) and fine aerosols (PM _2.5 ) on chimney emission standards. Based on the results of the domestic health impact study, the health impact was prioritized. The 24-hour value of "fine aerosol (PM _2.5 )" was set at 35 μg/m ³ and the annual average was set at 15 μg/m ³ . And the EPA has initially set a target of 15μg/m ³ of annual national average fine aerosol concentration in the Republic of China in 109 (2020), and will review its fine aerosol (PM _2.5 ) air quality standards on a phase-by-period basis in accordance with international regulatory trends. The air quality guideline value (25-hour value is set to 25 μg/m ³ and annual average is set to 10 μg/m ³ ) is the goal of achieving air quality improvement.

Therefore, in view of the above-mentioned shortcomings, the present creator can propose a direct-fired and split-flow high-efficiency organic waste gas treatment system with improved organic waste gas treatment efficiency, so that the user can easily operate the assembly, and is devoted to research and design to provide User convenience is the creative motive for the creator's desire to develop.

The main purpose of the present invention is to provide a direct-fired split high-efficiency organic waste gas treatment system, which mainly performs heat recovery of exhaust gas of a direct-fired incinerator via at least three heat exchangers, and directs the direct combustion The exhaust gas of the incinerator is further exchanged by a heat exchanger and an exhaust gas (adsorption treatment gas) of the clean gas discharge pipe at the outlet of the adsorption zone, and is cooled and then sent to the dust removal device for dust or two. Separation of oxides such as cerium oxide (SiO ₂ ), and finally, the gas outputted by the dust removing device is sent to the exhaust gas intake pipe, and a clean gas bypass pipe is provided in the clean gas discharge pipe to allow the net The gas discharge line can have the effect of bypassing the split flow, and the burned gas can be recycled into the adsorption zone of the adsorption wheel without being discharged through the chimney, so that the emission of the chimney can be reduced and The treatment efficiency of the organic waste gas can be increased, thereby increasing the overall utility.

Another object of the present invention is to provide a direct-fired split high-efficiency organic waste gas treatment system through which one end of the clean gas bypass line is connected to the clean gas discharge line, and the other end of the clean gas bypass line And connecting to the chimney discharge pipe, so that the clean gas discharge pipe can pass the heat exchange after entering the fifth cold side pipe of the fifth heat exchanger while transporting the purified gas; The clean gas bypass line connected to the clean gas discharge pipe is used for bypass splitting, so that part of the purified gas can flow directly to the chimney discharge pipe and then discharged through the chimney By this, through the clean gas bypass line, the clean gas discharge line can form a shunting effect, thereby increasing the overall usability.

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

10‧‧‧Direct-fired incinerator

11‧‧‧air inlet

12‧‧‧ air outlet

20‧‧‧Adsorption runner

201‧‧‧Adsorption zone

202‧‧‧Cooling area

203‧‧‧Decoupling area

21‧‧‧Exhaust air intake pipe

22‧‧‧Clean gas discharge pipeline

221‧‧‧ windmill

23‧‧‧Cooling air intake line

231‧‧‧ gas bypass line

24‧‧‧Cooling gas delivery line

241‧‧‧Cooling gas control valve

25‧‧‧hot gas delivery pipeline

251‧‧‧hot gas control valve

26‧‧‧Desorbed concentrated gas pipeline

27‧‧‧Connected pipeline

271‧‧‧Connected control valve

28‧‧‧ clean air bypass line

281‧‧‧ clean air bypass control valve

30‧‧‧First heat exchanger

301‧‧‧First cold side pipeline

302‧‧‧First hot side piping

31‧‧‧First hot gas recovery pipeline

32‧‧‧First incineration hot gas recovery pipeline

33‧‧‧First desorbed concentrated gas delivery line

40‧‧‧second heat exchanger

401‧‧‧Second cold side pipeline

402‧‧‧Second hot side piping

50‧‧‧ third heat exchanger

501‧‧‧ third cold side pipeline

502‧‧‧ third hot side pipeline

51‧‧‧ Third desorption concentrated gas delivery line

52‧‧‧ Third hot gas recovery pipeline

60‧‧‧fourth heat exchanger

601‧‧‧fourth cold side pipeline

602‧‧‧ fourth hot side pipeline

61‧‧‧fourth desorption concentrated gas delivery line

62‧‧‧fourth hot gas recovery pipeline

70‧‧‧ fifth heat exchanger

701‧‧‧ fifth cold side pipeline

702‧‧‧ fifth hot side pipeline

71‧‧‧ fifth hot gas recovery pipeline

80‧‧‧Dust removal equipment

81‧‧‧Dust intake manifold

82‧‧‧Dust extraction and exhaust pipe

821‧‧‧ windmill

90‧‧‧ chimney

91‧‧‧ chimney discharge line

The first figure is a schematic diagram of the main structure of the first embodiment of the creation.

Figure 2 is a schematic diagram of the architecture of the first proportional damper of the first embodiment of the present invention.

FIG. 3 is a schematic structural view of a second proportional damper of the first embodiment of the present invention.

Figure 4 is a schematic diagram of the main structure of the second embodiment of the present creation.

Figure 5 is a schematic diagram of the architecture of the first proportional damper of the second embodiment of the present invention.

Figure 6 is a schematic diagram showing the structure of a second proportional damper of the second embodiment of the present invention.

Please refer to FIG. 1 to FIG. 6 , which are schematic diagrams of the present embodiment. The best implementation of the direct combustion split high-efficiency organic waste gas treatment system of the present invention is applied to a volatile organic waste gas treatment system or the like in the semiconductor industry, the photovoltaic industry or the chemical related industry, mainly to allow the burned gas to enter the The adsorption zone of the adsorption runner is recycled, and the chimney is not used for discharge, so that the treatment efficiency of the organic waste gas can be improved.

The direct combustion split high-efficiency organic waste gas treatment system of the first embodiment of the present invention is mainly provided with a constant combustion incinerator 10, an adsorption reciprocating wheel 20, a first heat exchanger 30, and a second heat exchanger. 40, a third heat exchanger 50, a fifth heat exchanger 7 0, a dust removal device 80, a chimney 90 and a clean gas bypass line 28 (as shown in Figures 1 to 3), wherein the first heat exchanger 30 is provided with a first cold side line 301 And a first hot side line 302, the second heat exchanger 40 is provided with a second cold side line 401 and a second hot side line 402, and the third heat exchanger 50 is provided with a third cold side tube The fifth heat exchanger 70 is provided with a fifth cold side line 701 and a fifth hot side line 702, and the dust removing device 80 is a bag type dust collector and electricity. Bag type composite dust collector, inertial dust collector, electrostatic precipitator, centrifugal dust collector, filter cartridge type pulse dust collector, pulse bag type dust collector, pulse filter dust collector, pulse jet bag type dust collector, wet type dust collector, Wet electrostatic precipitator, wet electrostatic precipitator, water film dust collector, venturi tube dust collector, cyclone separator, flue dust collector, multi-layer dust collector, negative pressure backflush filter bag dust collector, low pressure long bag pulse dust removal , horizontal electrostatic precipitator, unpowered dust collector, charged water mist precipitator, multi-tube cyclone, explosion-proof dust collector, and The direct-fired incinerator (TO) 10 is provided with an air inlet 11 and an air outlet 12, and the direct-fired incinerator (TO) 10 is provided with a burner and a furnace, so that the organic exhaust gas can be The gas port 11 enters the burner for combustion, and the burned gas can pass through the furnace and be discharged from the gas outlet 12.

The adsorption runner 20 is a zeolite concentration runner or a concentrated runner of other materials, and the adsorption runner 20 is provided with an adsorption zone 201, a cooling zone 202 and a desorption zone 203, and the adsorption runner 20 is An exhaust gas intake line 21, a clean gas discharge line 22, a cooling gas intake line 23, a cooling gas delivery line 24, a hot gas delivery line 25, and a desorption concentrated gas line 26 are provided ( As shown in FIGS. 1 to 3, the other end of the exhaust gas intake line 21 is connected to one side of the adsorption zone 201 of the adsorption runner 20, so that the adsorption zone 201 of the adsorption runner 20 is The exhaust gas in the exhaust gas intake line 21 can be adsorbed, and the One end of the clean gas discharge pipe 22 is connected to the other side of the adsorption zone 201 of the adsorption runner 20, and the exhaust gas is purified by the adsorption zone 201 of the adsorption runner 20 and then from the clean gas discharge pipe 22 delivery.

In addition, one end of the cooling gas inlet pipe 23 is connected to one side of the cooling zone 202 of the adsorption wheel 20, and the cooling gas inlet pipe 23 has two embodiments, wherein the first embodiment The cooling air intake line 23 is for the outside air to enter (as shown in Figures 1 and 2), and the outside air is fresh air for the external air to be used for the transfer. The cooling zone 202 of the wheel 20 is provided for cooling use, and the second embodiment is characterized in that the cooling gas inlet pipe 23 is provided with a gas bypass line 231 (as shown in FIG. 3), the gas bypass pipe One end of the path 231 is connected to the cooling air intake line 23, and the other end of the gas bypass line 231 is connected to the exhaust gas intake line 21, and the gas bypass line 231 is used to pass the portion. The exhaust gas is delivered to the cooling zone 203 of the adsorption wheel 20 for use in cooling.

Another end of the cooling gas delivery line 24 is connected to the other side of the cooling zone 203 of the adsorption reel 20, and the other end of the cooling gas delivery line 24 is second to the second heat exchanger 40. One end of the cold side line 401 is connected to enable the cooling gas in the cooling gas delivery line 24 to be transferred into the second heat exchanger 40 for heat exchange (as shown in FIGS. 1 to 3). The other end of the second cold side line 401 of the second heat exchanger 40 is connected to the other end of the hot gas delivery line 25, and one end of the hot gas delivery line 25 is detached from the adsorption wheel 20. The other side of the zone 203 is connected, and one side of the desorption zone 203 of the adsorption reel 20 is connected to one end of the desorption concentrated gas line 26 so that the hot gas to be lifted via the second heat exchanger 50 It can be transported to the desorption zone 203 of the adsorption reel 20 through the hot gas delivery line 25 for desorption use, and will be desorbed by high temperature. The concentrated gas can be transported through the desorbed concentrated gas line 26.

In addition, a proportional damper is disposed between the cooling gas delivery line 24 and the hot gas delivery line 25 in the first embodiment, and the proportional damper is provided with two implementation designs, wherein the first implementation design A communication line 27 is disposed between the cooling gas delivery line 24 and the hot gas delivery line 25, and the communication line 27 is provided with a communication control valve 271, and the hot gas delivery line 25 is provided. There is a hot gas control valve 251 (as shown in FIG. 2), and the proportional damper is formed through the communication control valve 271 and the hot gas control valve 25, and the second implementation is designed to transport the cooling gas delivery line 24 and the hot gas. A communication line 27 is disposed between the pipelines 25, and the communication pipeline 27 is provided with a communication control valve 271, and the cooling gas delivery pipeline 24 is provided with a cooling gas control valve 241 (as shown in FIG. 3). And forming a proportional damper through the communication control valve 271 and the cooling gas control valve 241, thereby passing through or through the proportional damper of the design of the communication control valve 271 and the hot gas control valve 251 Control valve 271 and the cooling gas Valve system 241 of damper designed proportion, able to control the size of the adjustment of the wind, so that the temperature in the hot gas conduit 25 can be provided to maintain a certain temperature of the adsorption-desorption zone 20 of the runner 203.

Furthermore, the third heat exchanger 50 is connected to a third desorption concentrated gas delivery line 51 and a third hot gas recovery line 52, and one end of the third cold side line 51 of the third heat exchanger 50 Connected to the other end of the desorption concentrated gas line 26 (as shown in FIGS. 1 to 3), one end of the third desorbed concentrated gas delivery line 51 is connected to the third heat exchanger 50 The other end of the third cold side line 501 is connected, and the other end of the third desorbed concentrated gas delivery line 51 is connected to one end of the first cold side line 301 of the first heat exchanger 30. One end of the third hot gas recovery line 52 is connected to one end of the third hot side line 502 of the third heat exchanger 50, and the other end of the third hot gas recovery line 52 is connected to the second heat. The other end of the second hot side line 402 of the exchanger 40 is connected. Thereby, the desorbed concentrated gas desorbed by the desorption zone 203 of the adsorption reel 20 can be transmitted to the third cold side pipeline of the third heat exchanger 50 through the desorption concentrated gas pipeline 26. The heat exchange is performed by 502, and is further transmitted to the first cold side line 301 of the first heat exchanger 30 through the third desorbed concentrated gas delivery line 51 for heat exchange.

The first heat exchanger 30 is connected to a first hot gas recovery line 31, a first incineration hot gas recovery line 32 and a first desorbed concentrated gas delivery line 33, wherein the first incineration hot gas recovery line One end of the first incineration hot gas recovery line 32 is connected to the outlet 12 of the direct combustion incinerator 10 (As shown in FIGS. 1 to 3), one end of the first hot gas recovery line 31 is connected to the other end of the first hot side line 302 of the first heat exchanger 30, and the first hot gas is recovered. The other end of the pipeline 31 is connected to one end of the second hot side pipeline 402 of the second heat exchanger 40, and one end of the first desorbed concentrated gas delivery pipeline 33 is connected to the first heat exchanger 30. The other end of the first cold-side inflow line 301 is connected, and the other end of the first desorbed concentrated gas delivery line 33 is connected to the intake port 11 of the direct-fired incinerator 10. Thereby, the desorbed concentrated gas delivered through the first cold side line 301 of the first heat exchanger 30 can be sent to the direct combustion incinerator 10 through the first desorbed concentrated gas delivery line 33. The air inlet 11 and the gas burned by the direct-fired incinerator 10 can be transported from the air outlet 12 through the first incineration hot gas recovery line 32 to the first heat exchanger 30. Heat recovery in a hot side line 302 and via the first The hot gas recovery line 31 is sent to the second hot side line 402 of the second heat exchanger 40 for heat recovery, and is further sent to the third heat exchanger 50 via the third hot gas recovery line 52. Heat recovery is performed in the third hot side line 502.

The fifth heat exchanger 70 is connected to a fifth hot gas recovery line 71, and one end of the fifth cold side line 701 of the fifth heat exchanger 70 is connected to the other end of the clean gas discharge line 22. One end of the fifth hot gas recovery line 71 is connected to one end of the fifth hot side line 702 of the fifth heat exchanger 70, and the other end of the fifth hot gas recovery line 71 is connected to the third heat exchanger. The other end of the third hot side line 502 of 50 is connected (as shown in Figs. 1 to 3). The dust removing device 80 is connected to a dust removing air inlet line 81 and a dust removing air outlet line 82. One end of the dust removing air inlet line 81 is connected to the dust removing device 80, and the other end of the dust removing air inlet line 80 Connected to the other end of the fifth hot side line 702 of the fifth heat exchanger 70, one end of the dust removing and outgoing line 82 is connected to the dust removing device 80, and the other end of the dust removing and outgoing line 82 is The exhaust gas intake line 21 is connected. In addition, the dust removing and exhausting pipe 82 is provided with a windmill 821 for pushing the gas in the dust removing and exhausting pipe 82 into the exhaust gas intake pipe 21. Thereby, the gas burned by the direct-fired incinerator 10 can be transported from the third hot-side line 502 of the third heat exchanger 50 to the fifth heat through the fifth hot gas recovery line 71. The fifth hot side line 702 of the exchanger 70 is heat recovered, and then sent to the dust removing device 80 through the dust removing inlet line 81 to perform separation of oxides such as dust or cerium oxide (SiO ₂ ). The gas outputted by the dust removing device 80 is further sent to the exhaust gas intake pipe 21, so that the burned gas can be recycled into the adsorption zone 201 of the adsorption rotor 20 without being discharged through the chimney 90, so that The emissions of the chimney 90 can be reduced, and the processing efficiency of the organic exhaust gas can be improved.

Finally, the fifth heat exchanger is connected to the chimney 90. The chimney 90 is provided with a chimney discharge line 91. One end of the chimney discharge line 91 is connected to the chimney 90 (as shown in Figures 1 to 3). The other end of the chimney discharge line 91 is connected to the other end of the fifth cold side line 701 of the fifth heat exchanger 70. The purified gas discharged through the clean gas discharge line 22 can enter the fifth cold side line 701 of the fifth heat exchanger 70 for heat exchange, and then sent to the chimney 90 via the chimney discharge line 91. Carry out emissions. Further, the clean air discharge line 22 is provided with a windmill 221 for pushing the gas in the clean gas discharge line 22 into the fifth cold side line 701 of the fifth heat exchanger 70.

The net gas discharge line 22 is provided with a clean gas bypass line 28 (such as FIG. 1 to FIG. 3), and one end of the clean gas bypass line 28 is connected to the clean gas discharge line. 22 is connected, and the other end of the clean gas bypass line 28 is connected to the chimney discharge line 91, so that the clean gas discharge line 22 is in addition to entering the fifth heat exchanger when transporting the discharged purified gas. The fifth cold side line 701 of 70 performs heat exchange, and can also be bypassed by the clean gas bypass line 28 connected to the clean gas discharge line 22, so that part of the purified gas can be directly Flow to the chimney discharge line 91 is again discharged via the chimney 90. In addition, the clean gas bypass line 28 is provided with a clean gas bypass control valve 281 (such as FIG. 2 and FIG. 3) for adjusting the clean gas discharge line 22 through the clean gas bypass control valve 281. The amount of air supplied to the purified gas to form an adjustment control effect.

The direct combustion split high-efficiency organic waste gas treatment system of the second embodiment of the present invention is mainly provided with a constant combustion incinerator 10, an adsorption reciprocating wheel 20, a first heat exchanger 30, and a second heat exchanger. 40, a third heat exchanger 50, a fourth heat exchanger 60, a fifth heat exchanger 70, a dust removal device 80, a chimney 90 and a clean gas bypass line 2 8 (as shown in FIG. 4 to FIG. 6), wherein the first heat exchanger 30 is provided with a first cold side line 301 and a first hot side line 302, and the second heat exchanger 40 is provided There is a second cold side line 401 and a second hot side line 402. The third heat exchanger 50 is provided with a third cold side tube 501 and a third hot side line 502. The fourth heat exchanger 60 The fourth cold side line 601 and the fourth hot side line 602 are provided, and the fifth heat exchanger 70 is provided with a fifth cold side line 701 and a fifth hot side line 702, and the dust removing device 80 It is a bag type dust collector, electric bag type composite dust collector, inertial dust collector, electrostatic precipitator, centrifugal dust collector, filter cartridge type pulse dust collector, pulse bag type dust collector, pulse filter dust collector, pulse blowing bag type. Dust collector, wet dust collector, wet electrostatic precipitator, wet electrostatic precipitator, water film dust collector, venturi dust collector, cyclone separator, flue dust collector, multi-layer dust collector, negative pressure backflush filter bag Dust collector, low pressure long bag pulse dust collector, horizontal electrostatic precipitator, unpowered dust collector, charged water mist dust collector, multi-tube cyclone dust collector, explosion-proof dust collector In any of the above, the direct-fired incinerator (TO) 10 is provided with an air inlet 11 and an air outlet 12, and the direct-fired incinerator (TO) 10 is provided with a burner and a furnace, so that The organic exhaust gas can enter the burner from the gas inlet 11 for combustion, and the burned gas can pass through the furnace and be discharged from the gas outlet 12.

The adsorption runner 20 is a zeolite concentration runner or a concentrated runner of other materials, and the adsorption runner 20 is provided with an adsorption zone 201, a cooling zone 202 and a desorption zone 203, and the adsorption runner 20 is An exhaust gas intake line 21, a clean gas discharge line 22, a cooling gas intake line 23, a cooling gas delivery line 24, a hot gas delivery line 25, and a desorption concentrated gas line 26 are provided ( As shown in FIG. 4 to FIG. 6 , the other end of the exhaust gas intake line 21 is connected to one side of the adsorption zone 201 of the adsorption rotor 20 to make the adsorption zone 201 of the adsorption rotor 20 . The exhaust gas in the exhaust gas intake line 21 can be adsorbed, and the One end of the clean gas discharge pipe 22 is connected to the other side of the adsorption zone 201 of the adsorption runner 20, and the exhaust gas is purified by the adsorption zone 201 of the adsorption runner 20 and then from the clean gas discharge pipe 22 delivery.

In addition, one end of the cooling gas inlet pipe 23 is connected to one side of the cooling zone 202 of the adsorption wheel 20, and the cooling gas inlet pipe 23 has two embodiments, wherein the first embodiment The cooling air intake line 23 is for the outside air to enter (as shown in Figures 4 and 5), and the outside air is fresh air to be used to transport the external air to the adsorption transfer. The cooling zone 202 of the wheel 20 is provided for cooling use, and the second embodiment is characterized in that the cooling gas inlet pipe 23 is provided with a gas bypass line 231 (as shown in Fig. 6), the gas bypass pipe One end of the path 231 is connected to the cooling air intake line 23, and the other end of the gas bypass line 231 is connected to the exhaust gas intake line 21, and the gas bypass line 21 is used to pass the portion. The exhaust gas is delivered to the cooling zone 202 of the adsorption wheel 20 for use in cooling.

Another end of the cooling gas delivery line 24 is connected to the other side of the cooling zone 202 of the adsorption reel 20, and the other end of the cooling gas delivery line 24 is second with the second heat exchanger 40. One end of the cold side line 401 is connected to transfer the cooling gas in the cooling gas delivery line 24 to the second heat exchanger 40 for heat exchange (as shown in FIGS. 4 to 6). The other end of the second cold side line 401 of the second heat exchanger 40 is connected to the other end of the hot gas delivery line 25, and one end of the hot gas delivery line 25 is detached from the adsorption wheel 20. The other side of the zone 203 is connected, and one side of the desorption zone 203 of the adsorption reel 20 is connected to one end of the desorption concentrated gas line 26 so that the hot gas to be lifted through the second heat exchanger 40 It can be transported to the desorption zone 203 of the adsorption reel 20 through the hot gas delivery line 25 for desorption use, and will be desorbed by high temperature. The concentrated gas can be transported through the desorbed concentrated gas line 26.

In addition, a proportional damper is disposed between the cooling gas delivery line 24 and the hot gas delivery line 25 in the second embodiment, and the proportional damper is provided with two implementation designs, wherein the first implementation design A communication line 27 is disposed between the cooling gas delivery line 24 and the hot gas delivery line 25, and the communication line 27 is provided with a communication control valve 271, and the hot gas delivery line 25 is provided. There is a hot gas control valve 251 (as shown in FIG. 5), and the proportional damper is formed through the communication control valve 271 and the hot gas control valve 251, and the second embodiment is designed to transport the cooling gas delivery line 24 and the hot gas. A communication line 27 is disposed between the pipelines 25, and the communication pipeline 27 is provided with a communication control valve 271, and the cooling gas delivery pipeline 24 is provided with a cooling gas control valve 241 (as shown in Fig. 6). And a proportional damper is formed through the communication control valve 271 and the cooling gas control valve 241, thereby controlling the proportional damper through the design of the communication control valve 271 and the hot gas control valve 251 or through the communication control Valve 271 and the cooling air control Valve 241 proportions the damper design, able to control the size of the adjustment of the wind, so that the temperature in the hot gas conduit 25 can be provided to maintain a certain temperature of the adsorption-desorption zone 20 of the runner 203.

Furthermore, the fourth heat exchanger 60 is connected to a fourth desorption concentrated gas delivery line 61 and a fourth hot gas recovery line 62. One end of the fourth cold side line 601 is connected to the desorbed concentrated gas tube. The other end of the road 26 is connected, and one end of the fourth desorbed concentrated gas delivery line 61 is connected to the other end of the fourth cold side line 601 (as shown in FIGS. 4 to 6), the fourth The other end of the desorbed concentrated gas delivery line 61 is connected to one end of the third cold side line 501 of the third heat exchanger 50, and one end of the fourth hot gas recovery line 62 is Connected to one end of the fourth hot side line 602 of the fourth heat exchanger 60, the other end of the fourth hot gas recovery line 62 is connected to the third hot side line 502 of the third heat exchanger 50 Connected at one end. Thereby, the desorbed concentrated gas desorbed by the desorption zone 203 of the adsorption reel 20 can be transmitted to the fourth cold side pipeline of the fourth heat exchanger 60 through the desorption concentrated gas pipeline 26. The heat exchange is performed by 601, and is further transmitted to the third cold side line 501 of the third heat exchanger 50 through the fourth desorbed concentrated gas delivery line 61 for heat exchange.

The third heat exchanger 50 is connected to a third desorbed concentrated gas delivery line 51 and a third hot gas recovery line 52. One end of the third desorbed concentrated gas delivery line 51 is coupled to the third heat. The other end of the third cold side line 501 of the exchanger 50 is connected (as shown in FIGS. 4 to 6), and the other end of the third desorbed concentrated gas delivery line 51 is connected to the first heat exchanger. One end of the first cold side line 301 is connected to 30, and one end of the third hot gas recovery line 52 is connected to one end of the third hot side line 502 of the third heat exchanger 50. The third hot gas recovery tube The other end of the path 52 is connected to the other end of the second hot side line 402 of the second heat exchanger 40. Thereby, the desorbed concentrated gas is further transmitted through the third desorbed concentrated gas delivery line 51 to be transferred to the first cold side line 301 of the first heat exchanger 30 for heat exchange.

The first heat exchanger 30 is connected to a first hot gas recovery line 31, a first incineration hot gas recovery line 32 and a first desorbed concentrated gas delivery line 33, wherein the first incineration hot gas recovery line One end of the first incineration hot gas recovery line 32 is connected to the outlet end 11 of the direct combustion incinerator 10 (As shown in FIGS. 4 to 6), one end of the first hot gas recovery line 31 is connected to the first hot side line 30 of the first heat exchanger 30. The other end of the second hot gas recovery line 31 is connected to one end of the second hot side line 402 of the second heat exchanger 40, and the first desorbed concentrated gas delivery line 33 is One end is connected to the other end of the first cold side line 301 of the first heat exchanger 30, and the other end of the first desorbed concentrated gas delivery line 33 is connected to the inlet of the direct combustion incinerator 10. 12 connections. Thereby, the desorbed concentrated gas delivered through the first cold side line 301 of the first heat exchanger 30 can be sent to the direct combustion incinerator 10 through the first desorbed concentrated gas delivery line 33. The air inlet 11 and the gas burned by the direct-fired incinerator 10 can be transported from the air outlet 12 through the first incineration hot gas recovery line 32 to the first heat exchanger 30. Heat recovery is performed in a hot side line 302, and is sent to the second hot side line 402 of the second heat exchanger 40 via the first hot gas recovery line 31 for heat recovery, and further through the third The hot gas recovery line 52 is sent to the third hot side line 502 of the third heat exchanger 50 for heat recovery, and then sent to the fourth heat exchanger 60 via the fourth hot gas recovery line 62. Heat recovery is performed in the four hot side line 602.

The fifth heat exchanger 70 is connected to a fifth hot gas recovery line 71, and one end of the fifth cold side line 701 of the fifth heat exchanger 70 is connected to the other end of the clean gas discharge line 22. One end of the fifth hot gas recovery pipeline 71 is connected to one end of the fifth hot side pipeline 702 of the fifth heat exchanger 70 (as shown in FIGS. 4 to 6), the fifth hot gas recovery pipeline The other end of the 71 is connected to the other end of the fourth hot side line 602 of the fourth heat exchanger 60. The dust removing device 80 is connected to a dust removing air inlet line 81 and a dust removing air outlet line 82. One end of the dust removing air inlet line 81 is connected to the dust removing device 80, and the other end of the dust removing air inlet line 81 is connected. Connected to the other end of the fifth hot side line 702 of the fifth heat exchanger 70, one end of the dust removing and outgoing line 82 is connected to the dust removing device 80, and the other end of the dust removing and outgoing line 82 is connected to the exhaust gas. The intake line 21 is connected. In addition, the dust removing and exhausting pipe 82 is provided with a windmill 821 for pushing the gas in the dust removing and exhausting pipe 82 into the exhaust gas intake pipe 21. Thereby, the gas burned by the direct-fired incinerator 10 can be transported from the fourth hot-side line 602 of the fourth heat exchanger 60 to the fifth heat through the fifth hot gas recovery line 71. The fifth hot side line 702 of the exchanger 70 is heat recovered, and then sent to the dust removing device 80 through the dust removing inlet line 81 to perform separation of oxides such as dust or cerium oxide (SiO ₂ ). The gas outputted by the dust removing device 80 is further sent to the exhaust gas intake pipe 21, so that the burned gas can be recycled into the adsorption zone 201 of the adsorption rotor 20 without being discharged through the chimney 90, so that The emissions of the chimney 90 can be reduced, and the processing efficiency of the organic exhaust gas can be improved.

Finally, the fifth heat exchanger 70 is connected to the chimney 90. The chimney 90 is provided with a chimney discharge line 91. One end of the chimney discharge line 91 is connected to the chimney 90, and the chimney discharge line 91 is further One end is connected to the other end of the fifth cold side line 701 of the fifth heat exchanger 70 (as shown in Figs. 4 to 6). The purified gas discharged through the clean gas discharge line 22 can enter the fifth cold side line 701 of the fifth heat exchanger 70 for heat exchange, and then sent to the chimney 90 via the chimney discharge line 91. Carry out emissions. Further, the clean air discharge line 22 is provided with a windmill 221 for pushing the gas in the clean gas discharge line 22 into the fifth cold side line 701 of the fifth heat exchanger 70.

The net gas discharge line 22 is provided with a clean gas bypass line 28 (as shown in FIGS. 4 to 6), and one end of the clean gas bypass line 28 is connected to the clean gas discharge line. 22 is connected, and the other end of the clean gas bypass line 28 is connected to the chimney discharge line 91, so that the clean gas discharge line 22 is in addition to entering the fifth heat supply when the discharged purified gas is discharged. The fifth cold side line 701 of the converter 70 performs heat exchange, and can also bypass the clean gas bypass line 28 connected to the clean gas discharge line 22 to partially purge the purified gas. It can flow directly to the chimney discharge line 91 and then discharge through the chimney 90. In addition, the clean gas bypass line 28 is provided with a clean gas bypass control valve 281 (as shown in FIGS. 5 and 6) for adjusting the clean air discharge line 22 through the clean gas bypass control valve 281. The amount of air supplied to the purified gas to form an adjustment control effect.

By the above detailed description, it will be apparent to those skilled in the art that the present invention can achieve the foregoing objectives, and has been in compliance with the provisions of the Patent Law, and has filed a patent application.

However, the above is only the preferred embodiment of the present invention, and the scope of the creation of the present invention cannot be limited by this; therefore, the simple equivalent changes and modifications made by the scope of the patent application and the content of the creation specification are All should remain within the scope of this creation patent.

Claims (10)

The utility model relates to a direct-fired and split high-efficiency organic waste gas treatment system, which comprises: a constant-fired incinerator, the direct-fired incinerator is provided with an air inlet and an air outlet; and an adsorption runner is provided with adsorption. a zone, a cooling zone and a desorption zone, wherein the adsorption rotor is connected with an exhaust gas intake pipe, a clean gas exhaust pipe, a cooling gas intake pipe, a cooling gas delivery pipe, a hot gas conveying pipeline, and a desorption concentrated gas pipeline, the other end of the exhaust gas intake pipeline is connected to one side of the adsorption zone of the adsorption runner, and one end of the purge gas discharge pipeline is connected to the adsorption zone of the adsorption runner One side of the cooling gas inlet line is connected to one side of the cooling zone of the adsorption wheel, and one end of the cooling gas delivery line is connected to the other side of the cooling zone of the adsorption wheel. One end of the hot gas delivery line is connected to the other side of the desorption zone of the adsorption reel, and one end of the desorption concentrated gas line is connected to one side of the desorption zone of the adsorption reel; a heat exchanger, the first heat exchanger is provided with a first cold side pipeline and a hot side pipeline, the first heat exchanger is connected with a first hot gas recovery pipeline, a first incineration hot gas recovery pipeline and a first desorbed concentrated gas delivery pipeline, the first incineration hot gas recovery pipeline One end is connected to one end of the first hot side pipeline, and the other end of the first incineration hot gas recovery pipeline is connected to an outlet of the direct combustion incinerator, and one end of the first hot gas recovery pipeline is connected thereto The other end of the first hot side pipeline is connected to the other end of the second hot side pipeline, and one end of the first desorbed concentrated gas delivery pipeline is connected to the first The other end of the first desorption concentrated gas delivery line is connected to the inlet of the direct combustion incinerator; a second heat exchanger, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, and one end of the second cold side pipeline is connected to the other end of the cooling gas delivery pipeline Connecting, the other end of the second cold side pipeline is connected to the other end of the hot gas delivery pipeline; a third heat exchanger, the third heat exchanger is provided with a third cold side pipeline and a third heat a third pipeline is connected to a third desorbed concentrated gas delivery line and a third hot gas recovery line, and one end of the third cold side line is connected to the desorbed concentrated gas line The other end is connected, one end of the third desorbed concentrated gas delivery line is connected to the other end of the third cold side line, and the other end of the third desorbed concentrated gas delivery line is connected to the first cold side One end of the pipeline is connected, one end of the third hot gas recovery pipeline is connected to one end of the third hot side pipeline, and the other end of the third hot gas recovery pipeline is connected to the other end of the second hot side pipeline Connected to; a fifth heat exchanger, the fifth heat exchanger is provided with a fifth cold side pipeline and a fifth hot side pipeline, The fifth heat exchanger is connected to a fifth hot gas recovery pipeline, and one end of the fifth cold side pipeline is connected to the other end of the clean gas discharge pipeline, and one end of the fifth hot gas recovery pipeline is connected to the first One end of the five hot side pipeline is connected, and the other end of the fifth hot gas recovery pipeline is connected with the other end of the third hot side pipeline; a dust removing device is connected with a dust removing air inlet pipe and a a dust removal air outlet pipe, one end of the dust removal air intake pipe is connected to the dust removal device, and the other end of the dust removal air intake pipe is connected to the other end of the fifth hot side pipe, and one end of the dust removal air outlet pipe Connected to the dust removal device, the other end of the dust removal and exhaust pipe is connected to the exhaust gas intake pipe; a chimney is provided with a chimney discharge pipe, and one end of the chimney discharge pipe is connected with the chimney The other end of the chimney discharge line is connected to the other end of the fifth cold side line of the fifth heat exchanger; a clean gas bypass line, one end of the clean gas bypass line is connected to the clean gas discharge line, and the other end of the clean gas bypass line is connected to the chimney discharge line. The utility model relates to a direct-fired and split high-efficiency organic waste gas treatment system, which comprises: a constant-fired incinerator, the direct-fired incinerator is provided with an air inlet and an air outlet; and an adsorption runner is provided with adsorption. a zone, a cooling zone and a desorption zone, wherein the adsorption rotor is connected with an exhaust gas intake pipe, a clean gas exhaust pipe, a cooling gas intake pipe, a cooling gas delivery pipe, a hot gas delivery pipeline, and a desorption concentrated gas pipeline, the other end of the exhaust gas intake pipeline is connected to one side of the adsorption zone of the adsorption runner, and one end of the purge gas discharge pipeline is connected to the adsorption zone of the adsorption runner One side of the cooling gas inlet line is connected to one side of the cooling zone of the adsorption wheel, and one end of the cooling gas delivery line is connected to the other side of the cooling zone of the adsorption wheel. One end of the hot gas delivery line is connected to the other side of the desorption zone of the adsorption reel, and one end of the desorption concentrated gas line is connected to one side of the desorption zone of the adsorption reel; a heat exchanger, the first heat exchanger is provided with a first cold side pipeline and a hot side pipeline, the first heat exchanger is connected with a first hot gas recovery pipeline, a first incineration hot gas recovery pipeline and a first desorbed concentrated gas delivery pipeline, the first incineration hot gas recovery pipeline One end is connected to one end of the first hot side pipeline, and the other end of the first incineration hot gas recovery pipeline is connected to an outlet of the direct combustion incinerator, and one end of the first hot gas recovery pipeline is connected thereto The other end of the first hot side pipeline is connected to the other end of the second hot side pipeline, and one end of the first desorbed concentrated gas delivery pipeline is connected to the first The other end of the first desorption concentrated gas delivery line is connected to the inlet of the direct combustion incinerator; a second heat exchanger, the second heat exchanger is provided with a second cold side pipeline and a second hot side pipeline, and one end of the second cold side pipeline is connected to the other end of the cooling gas delivery pipeline Connecting, the other end of the second cold side pipeline is connected to the other end of the hot gas delivery pipeline; a third heat exchanger, the third heat exchanger is provided with a third cold side pipeline and a third heat a third pipeline is connected to a third desorbed concentrated gas delivery line and a third hot gas recovery line, and one end of the third desorbed concentrated gas delivery line is connected to the third cold side The other end of the pipeline is connected, and the other end of the third desorbed concentrated gas delivery pipeline is connected to one end of the first cold side pipeline, and one end of the third hot gas recovery pipeline is connected to the third hot side pipe One end of the road is connected, the other end of the third hot gas recovery line is connected to the other end of the second hot side line; a fourth heat exchanger is provided with a fourth cold side tube And a fourth hot side pipeline, the fourth heat exchanger is connected with a fourth desorption concentrated gas delivery pipeline and a fourth heat a recovery line, one end of the fourth cold side line is connected to the other end of the desorption concentrated gas line, and one end of the fourth desorption concentrated gas delivery line is connected to the fourth cold side line Connected at one end, the other end of the fourth desorbed concentrated gas delivery line is connected to one end of the third cold side line, and one end of the fourth hot gas recovery line is connected to one end of the fourth hot side line The other end of the fourth hot gas recovery line is connected to the other end of the third hot side line; a fifth heat exchanger having a fifth cold side line and a fifth a hot side pipeline, the fifth heat exchanger is connected to a fifth hot gas recovery pipeline, and one end of the fifth cold side pipeline is connected to the other end of the clean gas discharge pipeline, and the fifth hot gas recovery pipeline One end of the fifth hot gas recovery line is connected to one end of the fifth hot side line, and the other end of the fifth hot gas recovery line is connected to the other end of the fourth hot side line; a dust removal device, the dust removal device is connected with a dust removal air inlet pipe and a dust removal air outlet pipe, one end of the dust removal air intake pipe is connected with the dust removal device, and the other end of the dust removal air intake pipe is connected to the dust removal device The other end of the five hot side pipeline is connected, and one end of the dust removal air outlet line is connected to the dust removing device, and the other end of the dust removing air outlet line is connected with the exhaust gas intake pipe; a chimney, the chimney is provided with a a chimney discharge line, one end of the chimney discharge line is connected to the chimney, and the other end of the chimney discharge line is connected to the other end of the fifth cold side line of the fifth heat exchanger; a bypass line, one end of the clean gas bypass line is connected to the clean gas discharge line, and the other end of the clean gas bypass line is connected to the chimney discharge line. The direct-fired high-efficiency organic waste gas treatment system of claim 1 or 2, wherein the cooling gas delivery line and the hot gas delivery line are further provided with a communication line, the communication line A communication control valve is disposed, and the hot gas delivery pipeline is provided with a hot gas control valve, and the proportional damper is formed through the communication control valve and the hot gas control valve. The direct-fired high-efficiency organic waste gas treatment system of claim 1 or 2, wherein the cooling gas delivery line and the hot gas delivery line are further provided with a communication line, the communication line system A communication control valve is provided, and the cooling gas delivery pipeline is provided with a cooling gas control valve, and the proportional damper is formed through the communication control valve and the cooling gas control valve. The direct-fired high-efficiency organic waste gas treatment system according to claim 1 or 2, wherein the dust removal device is further a bag type dust remover, an electric bag type composite dust remover, an inertial dust collector, an electrostatic precipitator, and a centrifugal Dust collector, filter cartridge pulse dust collector, pulse bag type Dust collector, pulse filter dust collector, pulse jet bag filter, wet dust collector, wet electrostatic precipitator, wet electrostatic precipitator, water film dust collector, venturi dust collector, cyclone separator, flue Dust collector, multi-layer dust collector, negative pressure backflush filter bag dust collector, low pressure long bag pulse dust collector, horizontal electrostatic precipitator, unpowered dust collector, charged water mist dust collector, multi-tube cyclone dust collector, explosion-proof dust collector Any of them. The direct-fired split high-efficiency organic waste gas treatment system of claim 1 or 2, wherein the cooling gas intake line further transports external air to a cooling zone of the adsorption wheel, and the external gas system is fresh air. The direct-fired split high-efficiency organic waste gas treatment system according to claim 1 or 2, wherein the cooling gas intake line is further provided with a gas bypass line, and one end of the gas bypass line is The cooling gas inlet pipe is connected, and the other end of the gas bypass pipe is connected to the exhaust gas intake pipe. The direct-fired split high-efficiency organic waste gas treatment system according to claim 1 or 2, wherein the clean gas discharge pipeline is further provided with a windmill. The direct-fired split high-efficiency organic waste gas treatment system according to claim 1 or 2, wherein the dust-removing and outgoing gas pipeline is further provided with a windmill. The direct combustion split high efficiency organic waste gas treatment system according to claim 1 or 2, wherein the clean gas bypass line is further provided with a clean gas bypass control valve.