CN217247883U - Workshop waste gas environmental protection collecting system, concentrated system - Google Patents
Workshop waste gas environmental protection collecting system, concentrated system Download PDFInfo
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- CN217247883U CN217247883U CN202121166787.0U CN202121166787U CN217247883U CN 217247883 U CN217247883 U CN 217247883U CN 202121166787 U CN202121166787 U CN 202121166787U CN 217247883 U CN217247883 U CN 217247883U
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- 239000002912 waste gas Substances 0.000 title claims abstract description 283
- 230000007613 environmental effect Effects 0.000 title description 4
- 238000003795 desorption Methods 0.000 claims description 153
- 238000001179 sorption measurement Methods 0.000 claims description 127
- 239000007789 gas Substances 0.000 claims description 115
- 238000001816 cooling Methods 0.000 claims description 108
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 98
- 230000001172 regenerating effect Effects 0.000 claims description 24
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 18
- 238000012824 chemical production Methods 0.000 claims description 15
- 239000000463 material Substances 0.000 claims description 10
- 238000005192 partition Methods 0.000 claims description 9
- 238000007789 sealing Methods 0.000 claims description 9
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 6
- 150000001298 alcohols Chemical class 0.000 claims description 6
- 239000008096 xylene Substances 0.000 claims description 6
- 150000002170 ethers Chemical class 0.000 claims description 5
- 150000002576 ketones Chemical class 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 5
- 230000008929 regeneration Effects 0.000 claims description 5
- 238000011069 regeneration method Methods 0.000 claims description 5
- 239000003566 sealing material Substances 0.000 claims description 5
- 238000000746 purification Methods 0.000 abstract description 9
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000012855 volatile organic compound Substances 0.000 description 66
- 229910052799 carbon Inorganic materials 0.000 description 22
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- 229910021536 Zeolite Inorganic materials 0.000 description 5
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
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- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
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- 239000012141 concentrate Substances 0.000 description 3
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- LGRFSURHDFAFJT-UHFFFAOYSA-N Phthalic anhydride Natural products C1=CC=C2C(=O)OC(=O)C2=C1 LGRFSURHDFAFJT-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
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- 229920003180 amino resin Polymers 0.000 description 1
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- 238000007664 blowing Methods 0.000 description 1
- JHIWVOJDXOSYLW-UHFFFAOYSA-N butyl 2,2-difluorocyclopropane-1-carboxylate Chemical compound CCCCOC(=O)C1CC1(F)F JHIWVOJDXOSYLW-UHFFFAOYSA-N 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
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- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 1
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Classifications
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Abstract
The invention discloses an environment-friendly workshop waste gas collecting system and a concentrating system, and particularly relates to a concentrating system and an environment-friendly collecting system applying a high-concentration-ratio waste gas concentrating device. The invention can effectively improve the treatment efficiency of the waste gas environment-friendly collection system and reduce the operation cost, the purification rate of VOC waste gas is lower than the national waste gas emission standard, the concentration rate of the waste gas is high, the cost and the energy consumption are lower, the environment is protected, and the invention is especially suitable for factory workshops with high, medium and low concentration waste gas.
Description
Technical Field
The invention relates to the field of industrial waste gas treatment, in particular to an environment-friendly workshop waste gas collecting system and a concentrating system.
Background
VOCs are volatile hydrocarbons, and benzene, toluene, xylene, butyl esters, and 200# gasoline, etc. are generally used as diluents in the production of solvent-based coatings. When amino resin is produced, the raw materials usually adopt alcohols, benzenes, phthalic anhydride, pentaerythritol and the like which are easy to volatilize, and although the production process is in a closed system, volatile toxic gas can still be emitted to the working environment in the production process due to the influence of various uncontrollable factors, so that VOC pollution is caused.
In the prior art, RTO is combined with a concentration rotating wheel to treat organic waste gas, and research shows that investment and operation cost of RTO equipment are related to air volume and concentration of organic waste gas to be treated. The larger the air quantity is, the higher the investment and operation cost is, and the higher the concentration is, the lower the operation cost is. Although the coating treatment method in the prior art can meet the requirements of exhaust emission standards, the conventional exhaust gas environment-friendly collection system cannot cope with the situation that a high-concentration exhaust gas closed chamber and a low-concentration exhaust gas closed chamber are generated at the same time, and meanwhile, the treatment efficiency of exhaust gas treatment equipment used in the system is low, so that the treatment cost is increased and energy is wasted.
On the other hand, the heat conductivity of the adsorbent such as zeolite is greatly affected by the adsorption amount and the temperature, and the higher the temperature is, the higher the heat conductivity is, and the higher the adsorption amount is, the higher the heat conductivity is. Concentrated runner device among the prior art only sets up two sectors, and the left adsorption zone in middle desorption district receives the waste heat to influence, and the adsorbed VOC waste gas of adsorption material has the phenomenon of dissipating, though some foreign products have increased sealed measure in desorption district, but this VOC waste gas that prevents desorption district high temperature desorption and come out reveals other regions yet, can not prevent the adsorption efficiency decline of adsorption district, leads to the concentration multiple of reality to reach the numerical value of settlement.
Disclosure of Invention
The invention mainly provides a workshop waste gas environment-friendly collecting system, a concentrating system and an environment-friendly treatment method thereof, and particularly relates to a concentrating system using a high-concentration-ratio waste gas concentrating device, which can greatly improve the treatment efficiency of the waste gas environment-friendly collecting system, reduce the operation cost and further improve the waste gas purification rate of a concentrating rotating wheel device.
In order to achieve the purpose, the invention adopts the following technical scheme:
the utility model provides a workshop waste gas concentration system, includes high concentration ratio waste gas concentration device, high concentration ratio waste gas concentration device comprises frame support and the cake form runner of rotatably locating in the frame support, and the frame support is around for link up, sealed metal frame all around, and the runner is pieced together by the sector that constitutes with adsorbing material of a plurality of equant circles, keeps apart through subregion frame or sealing material between the sector, the runner sector divide into adsorption zone, high temperature desorption district, two cooling space according to the function, and two cooling space are located high temperature desorption district both sides and are adjoined with the adsorption zone, are equipped with the functional area frame that corresponds with adsorption zone, high temperature desorption district, two cooling space on the frame support.
Further, the sector of the adsorption area is 90-180 degrees, the sector of the high-temperature desorption area is 60-90 degrees, and the sectors of the two cooling areas are 45-60 degrees.
Furthermore, the sector of the adsorption area is 180 degrees, the sector of the high-temperature desorption area is 60 degrees, and the sectors of the two cooling areas are 60 degrees, so that on the premise of not influencing the high-temperature desorption effect, when the sector of the high-temperature desorption area is smaller and is equivalent to the sector of the cooling areas, the concentration rate of the waste gas reaches the highest at the same temperature and air quantity, and at the moment, the limitation effect of the cooling areas on the waste heat of the high-temperature desorption area on the two sides is the largest.
Further, high temperature desorption district, adsorption zone connecting tube department are equipped with the sealed cowling and install on the functional area frame, set up the sealed cowling and can further reduce the waste gas in high temperature desorption district and leak other functional areas to and the left side cooling zone dissipated waste gas leaks in high temperature desorption district or the adsorption zone.
An environment-friendly workshop waste gas collecting system using the workshop waste gas concentrating system comprises a closed outdoor space, an equipment closed chamber, a high-concentration-ratio waste gas concentrating device, a waste gas treatment device, an activated carbon adsorption device and a chimney, wherein the closed outdoor space in the workshop is not closed, a plurality of equipment closed chambers are arranged in the workshop, chemical production equipment forms air isolation with the workshop environment through the equipment closed chambers, the equipment closed chambers are provided with air exchange devices, the air inlet flow of the air exchange devices is slightly smaller than the exhaust flow of waste gas, the generated high-concentration waste gas equipment closed chamber is connected with the waste gas treatment device and the activated carbon adsorption device through pipelines, the generated low-concentration waste gas equipment closed chamber is connected with the high-concentration-ratio waste gas concentrating device through a pipeline, the purified air is conveyed to the chimney by the high-concentration-ratio waste gas concentrating device, and the concentrated high-concentration waste gas is conveyed to the waste gas treatment device or the activated carbon adsorption device through a pipeline, the waste gas treatment device and the activated carbon adsorption device are connected with a chimney through a pipeline, and purified air is discharged through the chimney.
The workshop of the system comprises a closed outdoor space and a plurality of equipment closed chambers, and because the equipment closed chambers collect waste gas in a closed manner, almost no waste gas leaks into the closed outdoor space, and the closed outdoor space is subjected to inorganization emission treatment; a plurality of equipment closed chambers are arranged in the workshop, chemical production equipment forms an isolation space with the outside through the equipment closed chambers, and the air inlet flow of an air interchanger of the equipment closed chambers is slightly smaller than the exhaust flow of waste gas, so that the equipment closed chambers are in a tiny negative pressure state, and the waste gas is ensured not to leak; this system is through dividing the equipment enclosure into two kinds of equipment enclosure, the equipment enclosure that produces high concentration waste gas, produces low concentration waste gas equipment enclosure, and high concentration waste gas is directly carried to exhaust treatment device or active carbon adsorption device, and it becomes high concentration waste gas to concentrate low concentration waste gas through high concentration ratio exhaust gas concentration device, carries to exhaust treatment device or active carbon adsorption device together with original high concentration waste gas, discharges by the chimney after the purification.
The VOC concentration of the closed chamber of the equipment for generating the high-concentration waste gas is 500-600 mg/m 3 The VOC concentration of the closed chamber of the equipment for generating the low-concentration waste gas is 50-60 mg/m 3 Wherein the chemical production equipment that produces VOC includes that three-roller grinds machine, the sand mill, high-speed dispersion machine, stirred tank, the packing district, the batching district, vacuum pump delivery pipe, reation kettle pressure release pipe, raw materials groove gas vent, the useless warehouse space of danger etc. produce high concentration exhaust equipment closed room and produce solvent formula product, produce low concentration exhaust equipment closed room and produce UV type product, produce high concentration exhaust equipment closed room and can contain the equipment that produces low concentration waste gas in a small amount, produce low concentration exhaust equipment closed room and sealThe chamber can contain a small amount of equipment for generating high-concentration waste gas, and the closed equipment chamber can also contain a closed operation bag room for generating low-concentration waste gas;
the waste gas treatment device is a commercial RTO heat storage combustion device or a commercial CO catalytic combustion device, the rotating wheel of the high-concentration-ratio waste gas concentration device is a commercial zeolite rotating wheel or a commercial honeycomb activated carbon rotating wheel, and the size and the pore diameter of the rotating wheel and the pore diameter of the adsorbing material can be adjusted and replaced according to the concentration and the air volume of the waste gas.
The VOC waste gas treated by the system comprises toluene, xylene, ethers, ketones and alcohols.
Furthermore, the front side of the adsorption area is connected with a closed chamber of equipment for generating low-concentration waste gas through a pipeline, and the back side of the adsorption area is connected with a chimney and a fresh air fan through pipelines; the front side of the high-temperature desorption area is connected with the waste gas treatment device and the activated carbon adsorption device through pipelines, and the back side of the high-temperature desorption area is connected with the regeneration heater through pipelines; the front sides of the two cooling areas are connected with a fresh air fan through a pipeline, and the back sides of the two cooling areas are connected with a regenerative heater through a pipeline.
According to the application, the cooling zones are arranged on two sides of the high-temperature desorption zone, and cold air is introduced in the direction opposite to that of the desorption hot air, so that on one hand, the right cooling zone is used for cooling the high-temperature desorption runner sector to recover the adsorption force; on the other hand, because the temperature of the high-temperature desorption region is higher, and the adsorption capacity of the cooling region on the left side of the high-temperature desorption region is larger, the heat conductivity coefficient of the cooling region on the left side of the high-temperature desorption region is relatively higher, especially when the runner rotates to a position where the partition frame is not overlapped with the high-temperature desorption region, that is, when the high-temperature region and the low-temperature region of the runner are in the same runner sector, the adsorbed VOC is easily diffused to other regions in advance due to the influence of the waste heat of the high-temperature desorption region on the left side cooling region, so that the waste gas concentration of the high-temperature desorption region is reduced and the waste gas concentration of the adsorption region is increased, and the waste gas concentration multiple cannot reach a preset value, therefore, cold air is reversely introduced into the cooling regions on both sides and the high-temperature desorption region, the waste heat range of the high-temperature desorption region is limited, cold and hot air convection is formed, most of the VOC waste gas scattered at the junction of the high-temperature desorption region and the left side cooling region enters the left side cooling region again for secondary desorption region along with the cold air, then become the desorption hot-blast through the heating of regenerative heater, a small amount of scattered VOC waste gas gets into the high temperature desorption district along with the desorption hot-blast and leads to exhaust treatment device or active carbon adsorption device, effectively prevents VOC and dissipates, has higher waste gas concentration multiple under same temperature and amount of wind, is particularly useful for being equipped with the runner of subregion frame, because the subregion frame adopts metal material mostly, the cost of manufacture is lower, but heat conduction more easily.
The exhaust gas concentration multiple among the prior art equals the air volume that waste gas passes through the adsorption zone and the specific value of high temperature desorption district desorption air volume, nevertheless because VOC dissipation problem leads to this exhaust gas concentration multiple and the ratio of concentration before the actual exhaust gas adsorbs and concentration after the desorption to have a difference, therefore the exhaust gas concentration multiple uses the ratio of concentration before the actual exhaust gas adsorbs and concentration after the desorption as the standard herein.
In this application, all pipeline turnings adopt 45 degrees angles, reduce waste gas air current resistance.
An environment-friendly treatment method based on the workshop waste gas environment-friendly collection system comprises the following steps:
(1) the exhaust gas discharged from the closed chamber of the equipment for generating high-concentration exhaust gas is discharged at 3000m 3 The total delivery air volume of the air/h is discharged to a waste gas treatment device or an active carbon adsorption device through a pipeline;
(2) 20000m for the exhaust gas discharged from the closed chamber of the equipment for generating low-concentration exhaust gas 3 The total conveying air quantity is conveyed to an adsorption area of a high concentration ratio waste gas concentration device through a pipeline, VOC components in the waste gas are rotated to a sector corresponding to the adsorption area by a rotating wheel to be adsorbed into purified gas, and the purified gas is conveyed to a chimney through the pipeline to be discharged into the atmosphere; after the sector adsorbing the VOC is transferred to a high-temperature desorption area, hot air of a regenerative heater is introduced into the high-temperature desorption area to heat and desorb the VOC on the sector of the rotating wheel corresponding to the high-temperature desorption area, and the concentrated and desorbed high-concentration VOC waste gas is conveyed to a waste gas treatment device or an active carbon adsorption device through a pipeline;
(3) fresh air fan can be used for blowing clean air into the air duct by 1400-4000 m 3 The delivery air volume of the/h is introduced into the cooling zones at the two sides, so that the rotating wheel enters the sector of the cooling zone at the right side for cooling after passing through the high-temperature desorption zone, the adsorption capacity is recovered, and meanwhile, the residual heat zone of the cooling zone at the left side is reducedAnd then heating the obtained product from the cooling zones at two sides to 150-200 ℃ through a regenerative heater, and leading the product to a high-temperature desorption zone.
(4) The waste gas treatment device or the activated carbon adsorption device burns or adsorbs the VOC waste gas to become purified gas and discharges the purified gas into the atmosphere through a chimney.
Further, the method also comprises the following steps: purified gas is conveyed to the fresh air fan again through a pipeline.
Furthermore, the rotating speed of a rotating wheel of the high-concentration-ratio waste gas concentration device is 6-8 r/h.
Furthermore, the concentration multiple of the waste gas can be adjusted by adjusting the conveying air quantity of the fresh air fan and the heating temperature of the regenerative heater, and the multiple range is 5-15 times; when the high concentration ratio waste gas concentration device has VOC waste gas dissipation, the higher the heating temperature of the regenerative heater is or the lower the conveying air volume of the fresh air fan is, the smaller the marginal benefit of the waste gas concentration ratio adjustment is, and on the premise that the VOC waste gas dissipation of the high concentration ratio waste gas concentration device is controllable, the more stable the waste gas concentration ratio adjustment is.
The invention has the beneficial effects that:
1. this application all sets up the cooling space in high temperature desorption district both sides, and reversely let in cold wind with the high temperature desorption district, restrict the waste heat scope in high temperature desorption district, form cold and hot wind convection, high temperature desorption district and left side cooling space juncture scattered VOC waste gas partly along with cold wind reentrant left side cooling space secondary desorption, another part gets into high temperature desorption district along with hot wind and accesss to exhaust treatment device or active carbon adsorption device, effectively prevent left side cooling space VOC waste gas dissipation, higher waste gas concentration multiple has under same temperature and the amount of wind, high waste gas concentration ratio and high concentration efficiency have, be particularly useful for the runner that is equipped with the subregion frame.
2. The high concentration ratio waste gas concentration device of this application can adjust the waste gas concentration multiple through the amount of wind and the regenerative heater heating temperature who adjusts the new trend fan, and the waste gas concentration multiple is adjusted easily and stably more, and adjustment cost and energy consumption are lower.
3. The device adopts the closed chamber to isolate the waste gas generated by the chemical production device, and the space outside the closed chamber is subjected to inorganization discharge treatment, so that the waste gas treatment cost is reduced; divide into the equipment enclosure and produce high concentration exhaust gas equipment enclosure, produce two kinds of low concentration exhaust gas equipment enclosures, high concentration waste gas is direct to be carried to exhaust treatment device or active carbon adsorption device, it becomes high concentration waste gas to concentrate low concentration waste gas through the high concentration ratio exhaust gas concentration device of this application, carry to exhaust treatment device or active carbon adsorption device together with original high concentration waste gas, discharge by the chimney after the purification, the system adopts can be according to exhaust concentration and the real-time adjustment exhaust concentration multiple of flux when actual production behind the high concentration ratio exhaust gas concentration device of this application, promote the treatment effeciency of waste gas environmental protection collection system greatly and reduce the running cost, be particularly useful for high, in, the factory workshop that low concentration waste gas is coexisted.
Drawings
FIG. 1 is a schematic structural diagram of a workshop waste gas environment-friendly collection system;
FIG. 2 is a schematic view of the external gas flow of the high concentration ratio exhaust gas concentration device;
FIG. 3 is a schematic view of the internal gas flow of the high concentration ratio exhaust gas concentration device;
FIG. 4 is a schematic view of the runner structure;
FIG. 5 is a schematic view showing the construction of a high concentration ratio exhaust gas concentrating apparatus;
FIG. 6 is a schematic structural view of a high concentration ratio exhaust gas concentration device with a sealing cap;
the system comprises a device for generating high-concentration waste gas, a device for generating low-concentration waste gas, a 3-ventilation device, a 4-fan, a 5-fresh air fan, a 6-high-concentration-ratio waste gas concentration device, a 7-regenerative heater, an 8-waste gas treatment device, a 9-activated carbon adsorption device, a 10-chimney, an 11-pipeline, a 12-high-temperature desorption region, a 13 a-right cooling region, a 13 b-left cooling region, a 14-adsorption region, a 15-closed outdoor space, a 16-outer frame support, a 17-functional region frame, an 18-rotating wheel, a 19-sector and a 20-sealing cover, wherein the device comprises a device for generating high-concentration waste gas, a device for generating low-concentration waste gas, and a device for generating low-concentration waste gas.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the present invention is further described in detail below with reference to the accompanying drawings and examples. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
Example 1
Referring to fig. 1 to 6, a workshop waste gas concentration system comprises a high-concentration-ratio waste gas concentration device 6, wherein the high-concentration-ratio waste gas concentration device 6 is composed of an outer frame support 16 and a round disc-shaped rotating wheel 18 rotatably arranged in the outer frame support 16, the outer frame support 16 is a metal frame which is through from front to back and sealed at the periphery, the rotating wheel 18 is formed by splicing a plurality of equally-rounded sectors 19 formed by adsorbing materials, the sectors 19 are isolated by partition frames or sealing materials, the sectors 19 of the rotating wheel 18 are divided into an adsorption area 14, a high-temperature desorption area 12 and two cooling areas 13a and 13b according to functions, the two cooling areas 13a and 13b are positioned at two sides of the high-temperature desorption area 12 and are adjacent to the adsorption area 14, and the outer frame support 16 is provided with a functional area frame 17 corresponding to the adsorption area 14, the high-temperature desorption area 12 and the two cooling areas 13a and 13 b.
Further, the sector of the adsorption area 14 is 180 degrees, the sector of the high-temperature desorption area 12 is 90 degrees, and the two cooling areas 13 a 13b has a sector of 45 deg..
Further, the high-temperature desorption region 12 and the adsorption region 14 are provided with the sealing cover 20 at the connecting pipeline 11 and are installed on the functional region frame 17, the sealing cover 20 is arranged to further reduce the leakage of the exhaust gas of the high-temperature desorption region 12 to other functional regions, and the exhaust gas dissipated from the left cooling region 13b leaks to the high-temperature desorption region 12 or the adsorption region 14.
An environment-friendly workshop waste gas collecting system using the workshop waste gas concentrating system comprises a closed outdoor space 15, equipment closed chambers, a high-concentration-ratio waste gas concentrating device 6, a waste gas treatment device 8, an activated carbon adsorption device 9 and a chimney 10, wherein the closed outdoor space 15 in a workshop is not closed, a plurality of equipment closed chambers are arranged in the workshop, chemical production equipment forms air isolation with the workshop environment through the equipment closed chambers, the equipment closed chambers are provided with air interchangers 3, the air intake flow of the air interchangers 3 is slightly smaller than the exhaust flow of waste gas, the equipment closed chambers 1 for generating high-concentration waste gas are connected with the waste gas treatment device 8 and the activated carbon adsorption device 9 through pipelines 11, the equipment closed chambers 2 for generating low-concentration waste gas are connected with the high-concentration-ratio waste gas concentrating device 6 through the pipelines 11, the high-concentration-ratio waste gas concentrating device 6 conveys purified air to the chimney 10 through the pipelines 11, the concentrated high-concentration waste gas is conveyed to a waste gas treatment device 8 or an activated carbon adsorption device 9 through a pipeline 11, the waste gas treatment device 8 and the activated carbon adsorption device 9 are connected with a chimney 10 through a pipeline 11, and the purified air is discharged through the chimney 10.
The workshop of the system comprises a closed outdoor space 15 and a plurality of equipment closed chambers, and because the equipment closed chambers collect waste gas in a closed manner, almost no waste gas leaks into the closed outdoor space 15, and the closed outdoor space 15 is subjected to inorganization discharge treatment; a plurality of equipment closed chambers are arranged in the workshop, chemical production equipment forms an isolation space with the outside through the equipment closed chambers, and the air inlet flow of the air interchanger 3 of the equipment closed chambers is slightly smaller than the exhaust flow of waste gas, so that the equipment closed chambers are in a tiny negative pressure state, and the waste gas is ensured not to leak; this system is through dividing into the equipment enclosure and producing high concentration waste gas equipment enclosure 1, produce low concentration waste gas equipment enclosure 2 two kinds, and high concentration waste gas is directly carried to exhaust treatment device 8 or active carbon adsorption device 9, and the low concentration waste gas becomes high concentration waste gas through high concentration ratio exhaust gas concentration device 6 concentration, carries to exhaust treatment device 8 or active carbon adsorption device 9 with original high concentration waste gas together, discharges by chimney 10 after the purification.
The concentration of VOC in the closed chamber 1 of the equipment for generating high-concentration waste gas is 500-600 mg/m 3 The VOC concentration of the closed chamber 2 of the equipment for generating the low-concentration waste gas is 50-60 mg/m 3 Wherein the chemical production equipment that produces VOC includes that the three-roller grinds the machine, the sand mill, high-speed dispersion machine, the stirred tank, the packing district, the batching district, the vacuum pump delivery pipe, reation kettle pressure release pipe, the former feed tank gas vent, the useless warehouse space of danger etc, produce high concentration exhaust equipment enclosed room 1 production solvent formula product, produce 2 production UV type products of low concentration exhaust equipment enclosed room, produce equipment that high concentration exhaust equipment enclosed room 1 can contain a small amount of production low concentration waste gas, produce equipment that low concentration exhaust equipment enclosed room 2 can contain a small amount of production high concentration waste gas, can also contain the airtight operation package room that produces low concentration waste gas in the equipment enclosed room；
The waste gas treatment device 8 is a commercial RTO heat storage combustion device or a commercial CO catalytic combustion device, the rotating wheel 18 of the high-concentration-ratio waste gas concentration device 6 is a commercial zeolite rotating wheel or a commercial honeycomb activated carbon rotating wheel, and the size and the pore diameter of the rotating wheel 18 and the pore diameter of an adsorbing material can be adjusted and replaced according to the waste gas concentration and the air volume of a fan.
The VOC waste gas treated by the system comprises toluene, xylene, ethers, ketones and alcohols.
Furthermore, the front side of the adsorption area 14 is connected with the closed chamber 2 of the equipment for generating low-concentration waste gas through a pipeline 11, and the back side is connected with a chimney 10 and a fresh air fan 5 through a pipeline 11; the front side of the high-temperature desorption zone 12 is connected with the waste gas treatment device 8 and the activated carbon adsorption device 9 through a pipeline 11, and the back side is connected with the regeneration heater 7 through a pipeline 11; the front surfaces of the two cooling areas 13a and 13b are connected with the fresh air fan 5 through a pipeline 11, and the back surfaces of the two cooling areas are connected with the regenerative heater 7 through a pipeline 11.
According to the application, the cooling zones 13a and 13b are arranged on the two sides of the high-temperature desorption zone 12, and cold air is introduced into the high-temperature desorption zone in the direction opposite to the direction of desorption hot air, so that on one hand, the right cooling zone 13a is used for cooling the sector 19 of the rotating wheel 18 subjected to high-temperature desorption to recover the adsorption force; on the other hand, because the temperature of the high-temperature desorption region 12 is high, and the adsorption capacity of the cooling region 13b on the left side of the high-temperature desorption region 12 is large, the thermal conductivity coefficient of the cooling region 13b on the left side of the high-temperature desorption region 12 is relatively high, especially when the runner 18 rotates to a position where the partition frame is not overlapped with the high-temperature desorption region 12, that is, when the high-temperature region and the low-temperature region of the runner 18 are in the same runner sector 19, the VOC adsorbed by the cooling region 13b on the left side is easily affected by the residual heat of the high-temperature desorption region to diffuse to other regions in advance, so that the exhaust gas concentration of the high-temperature desorption region 12 is reduced, the exhaust gas concentration of the adsorption region 14 is increased, and the exhaust gas concentration multiple cannot reach a predetermined value, therefore, cold air is reversely introduced into the cooling regions 13a and 13b on both sides and the high-temperature desorption region 12 to limit the residual heat range of the high-temperature desorption region, thereby forming cold-hot air convection, most of the VOC exhaust gas scattered at the junction of the high-temperature desorption region 12 and the cooling region 13b enters the left side cooling region 13b for secondary desorption, then become desorption hot-blast through the heating of regenerative heater 7, a small amount of scattered VOC waste gas gets into high temperature desorption district 12 along with desorption hot-blast and leads to exhaust treatment device 8 or active carbon adsorption device 9, effectively prevents VOC and dissipates, has higher waste gas concentration multiple under same temperature and amount of wind, is particularly useful for being equipped with runner 18 of subregion frame, because the subregion frame adopts metal material mostly, the cost of manufacture is lower, but heat conduction more easily.
In this application, all 11 turnings of pipeline adopt 45 degrees angles, reduce waste gas air current resistance.
An environment-friendly treatment method based on the workshop waste gas treatment system comprises the following steps:
(1) 3000m of exhaust gas discharged from the closed chamber 1 of the apparatus for generating high-concentration exhaust gas 3 The total delivery air volume per hour is discharged to a waste gas treatment device 8 or an active carbon adsorption device 9 through a pipeline 11;
(2) the exhaust gas discharged from the closed chamber 2 of the apparatus for generating low-concentration exhaust gas is cooled to 20000m 3 The total conveying air quantity of/h is sent to an adsorption area 14 of the high concentration ratio waste gas concentration device 6 through a pipeline 11, VOC components in the waste gas are transferred to a sector 19 corresponding to the adsorption area 14 by a rotating wheel 18 to be adsorbed into purified gas, and the purified gas is conveyed to a chimney 10 through the pipeline 11 to be discharged into the atmosphere; after the sector 19 adsorbing the VOC is transferred to the high temperature desorption region 12, the hot air of the regenerative heater 7 is introduced into the high temperature desorption region 12, the VOC on the sector 19 of the high temperature desorption region 12 corresponding to the runner 18 is heated and desorbed, and the concentrated and desorbed high concentration VOC exhaust gas is conveyed to the exhaust gas treatment device 8 or the activated carbon adsorption device 9 through the pipeline 11;
(3) the fresh air fan 5 blows clean air at 2000m 3 The delivery air volume of the/h is introduced into the cooling zones 13a and 13b at the two sides, so that the rotating wheel 18 enters the sector 19 of the cooling zone 13a at the right side after passing through the high-temperature desorption zone 12 for cooling, the adsorption capacity is recovered, meanwhile, the influence of the residual heat of the cooling zone 14 at the left side is reduced, and the rotating wheel is heated to 150-200 ℃ from the cooling zones 13a and 13b at the two sides through the regenerative heater 7 and then is led to the high-temperature desorption zone 12.
(4) The VOC exhaust gas is burned or adsorbed by the exhaust gas treatment device 8 or the activated carbon adsorption device 9 to be purified gas, and is discharged to the atmosphere through a chimney 10.
Further, the method also comprises the following steps: the cleaned gas is again fed to the fresh air fan 5 via a line 11.
Further, the rotation speed of the runner 18 of the high concentration ratio exhaust gas concentration device 6 is 6 r/h.
Furthermore, the concentration multiple of the waste gas can be adjusted by adjusting the conveying air quantity of the fresh air fan 5 and the heating temperature of the regenerative heater 7, and the multiple range is 5-15 times;
example 2
Referring to fig. 1 to 6, a workshop waste gas concentration system comprises a high-concentration-ratio waste gas concentration device 6, wherein the high-concentration-ratio waste gas concentration device 6 is composed of an outer frame support 16 and a round disc-shaped rotating wheel 18 rotatably arranged in the outer frame support 16, the outer frame support 16 is a metal frame which is through from front to back and sealed at the periphery, the rotating wheel 18 is formed by splicing a plurality of equally-rounded sectors 19 formed by adsorbing materials, the sectors 19 are isolated by partition frames or sealing materials, the sectors 19 of the rotating wheel 18 are divided into an adsorption area 14, a high-temperature desorption area 12 and two cooling areas 13a and 13b according to functions, the two cooling areas 13a and 13b are positioned at two sides of the high-temperature desorption area 12 and are adjacent to the adsorption area 14, and the outer frame support 16 is provided with a functional area frame 17 corresponding to the adsorption area 14, the high-temperature desorption area 12 and the two cooling areas 13a and 13 b.
Further, the sector of the adsorption zone 14 is 180 °, the sector of the high-temperature desorption zone 12 is 60 °, and the sectors of the two cooling zones 13a and 13b are 60 °.
Further, the high-temperature desorption region 12 and the adsorption region 14 are provided with the sealing cover 20 at the connecting pipeline 11 and are installed on the functional region frame 17, the sealing cover 20 is arranged to further reduce the leakage of the exhaust gas of the high-temperature desorption region 12 to other functional regions, and the exhaust gas dissipated from the left cooling region 13b leaks to the high-temperature desorption region 12 or the adsorption region 14.
An environment-friendly workshop waste gas collecting system using the workshop waste gas concentrating system comprises a closed outdoor space 15, equipment closed chambers, a high-concentration-ratio waste gas concentrating device 6, a waste gas treatment device 8, an activated carbon adsorption device 9 and a chimney 10, wherein the closed outdoor space 15 in a workshop is not closed, a plurality of equipment closed chambers are arranged in the workshop, chemical production equipment forms air isolation with the workshop environment through the equipment closed chambers, the equipment closed chambers are provided with air interchangers 3, the air intake flow of the air interchangers 3 is slightly smaller than the exhaust flow of waste gas, the equipment closed chambers 1 for generating high-concentration waste gas are connected with the waste gas treatment device 8 and the activated carbon adsorption device 9 through pipelines 11, the equipment closed chambers 2 for generating low-concentration waste gas are connected with the high-concentration-ratio waste gas concentrating device 6 through the pipelines 11, the high-concentration-ratio waste gas concentrating device 6 conveys purified air to the chimney 10 through the pipelines 11, the concentrated high-concentration waste gas is conveyed to a waste gas treatment device 8 or an activated carbon adsorption device 9 through a pipeline 11, the waste gas treatment device 8 and the activated carbon adsorption device 9 are connected with a chimney 10 through a pipeline 11, and the purified air is discharged through the chimney 10.
The workshop of the system comprises a closed outdoor space 15 and a plurality of equipment closed chambers, and because the equipment closed chambers collect waste gas in a closed manner, almost no waste gas leaks into the closed outdoor space 15, and the closed outdoor space 15 is subjected to inorganization discharge treatment; a plurality of equipment closed chambers are arranged in the workshop, chemical production equipment forms an isolation space with the outside through the equipment closed chambers, and the air inlet flow of the air interchanger 3 of the equipment closed chambers is slightly smaller than the exhaust flow of waste gas, so that the equipment closed chambers are in a tiny negative pressure state, and the waste gas is ensured not to leak; this system is through dividing into the equipment enclosure and producing high concentration waste gas equipment enclosure 1, produce low concentration waste gas equipment enclosure 2 two kinds, and high concentration waste gas is directly carried to exhaust treatment device 8 or active carbon adsorption device 9, and the low concentration waste gas becomes high concentration waste gas through high concentration ratio exhaust gas concentration device 6 concentration, carries to exhaust treatment device 8 or active carbon adsorption device 9 with original high concentration waste gas together, discharges by chimney 10 after the purification.
The concentration of VOC in the closed chamber 1 of the equipment for generating high-concentration waste gas is 500-600 mg/m 3 The VOC concentration of the closed chamber 2 of the equipment for generating the low-concentration waste gas is 50-60 mg/m 3 The chemical production equipment for generating VOC comprises a three-roller grinder, a sand mill, a high-speed dispersion machine, a stirring kettle, a packaging area, a batching area, a vacuum pump discharge pipe, a reaction kettle pressure relief pipe, a raw material groove exhaust port, a hazardous waste warehouse space and the like, wherein a solvent type product is produced in a high-concentration waste gas equipment closed chamber 1, a UV type product is produced in a low-concentration waste gas equipment closed chamber 2, and a high-concentration waste gas equipment closed chamber is producedThe chamber 1 may contain a small amount of equipment for generating a low concentration exhaust gas, the equipment for generating a low concentration exhaust gas, and the enclosure 2 may contain a small amount of equipment for generating a high concentration exhaust gas, and the equipment enclosure may further contain a closed operation booth for generating a low concentration exhaust gas.
The waste gas treatment device 8 is a commercial RTO heat storage combustion device or a commercial CO catalytic combustion device, the rotating wheel 18 of the high-concentration-ratio waste gas concentration device 6 is a commercial zeolite rotating wheel or a commercial honeycomb activated carbon rotating wheel, and the size and the aperture of the rotating wheel 18 and the aperture of an adsorbing material can be adjusted and replaced according to the waste gas concentration and the air volume of a fan.
The VOC waste gas treated by the system comprises toluene, xylene, ethers, ketones and alcohols.
Furthermore, the front side of the adsorption area 14 is connected with the closed chamber 2 of the equipment for generating low-concentration waste gas through a pipeline 11, and the back side is connected with a chimney 10 and a fresh air fan 5 through a pipeline 11; the front side of the high-temperature desorption zone 12 is connected with the waste gas treatment device 8 and the activated carbon adsorption device 9 through a pipeline 11, and the back side is connected with the regeneration heater 7 through a pipeline 11; the front surfaces of the two cooling areas 13a and 13b are connected with the fresh air fan 5 through a pipeline 11, and the back surfaces of the two cooling areas are connected with the regenerative heater 7 through a pipeline 11.
According to the application, the cooling zones 13a and 13b are arranged on the two sides of the high-temperature desorption zone 12, and cold air is introduced in the direction opposite to that of the desorption hot air, so that on one hand, the right cooling zone 13a is used for cooling the sector 19 of the rotating wheel 18 undergoing high-temperature desorption to recover the adsorption force; on the other hand, because the temperature of the high-temperature desorption region 12 is high, and the adsorption capacity of the cooling region 13b on the left side of the high-temperature desorption region 12 is large, the thermal conductivity coefficient of the cooling region 13b on the left side of the high-temperature desorption region 12 is relatively high, especially when the runner 18 rotates to a position where the partition frame is not overlapped with the high-temperature desorption region 12, that is, when the high-temperature region and the low-temperature region of the runner 18 are in the same runner sector 19, the VOC adsorbed by the cooling region 13b on the left side is easily affected by the residual heat of the high-temperature desorption region to diffuse to other regions in advance, so that the exhaust gas concentration of the high-temperature desorption region 12 is reduced, the exhaust gas concentration of the adsorption region 14 is increased, and the exhaust gas concentration multiple cannot reach a predetermined value, therefore, cold air is reversely introduced into the cooling regions 13a and 13b on both sides and the high-temperature desorption region 12 to limit the residual heat range of the high-temperature desorption region, thereby forming cold-hot air convection, most of the VOC exhaust gas scattered at the junction of the high-temperature desorption region 12 and the cooling region 13b enters the left side cooling region 13b for secondary desorption, then become desorption hot-blast through the heating of regenerative heater 7, a small amount of scattered VOC waste gas gets into high temperature desorption district 12 along with desorption hot-blast and leads to exhaust treatment device 8 or active carbon adsorption device 9, effectively prevents VOC and dissipates, has higher waste gas concentration multiple under same temperature and amount of wind, is particularly useful for being equipped with runner 18 of subregion frame, because the subregion frame adopts metal material mostly, the cost of manufacture is lower, but heat conduction more easily.
In this application, all 11 turnings of pipeline adopt 45 degrees angles, reduce waste gas air current resistance.
An environment-friendly treatment method based on the workshop waste gas treatment system comprises the following steps:
(1) 3000m of exhaust gas discharged from the closed chamber 1 of the apparatus for generating high-concentration exhaust gas 3 The total delivery air volume per hour is discharged to a waste gas treatment device 8 or an active carbon adsorption device 9 through a pipeline 11;
(2) the exhaust gas discharged from the closed chamber 2 of the apparatus for generating low-concentration exhaust gas is 20000m 3 The total conveying air quantity of/h is sent to an adsorption area 14 of the high concentration ratio waste gas concentration device 6 through a pipeline 11, VOC components in the waste gas are transferred to a sector 19 corresponding to the adsorption area 14 by a rotating wheel 18 to be adsorbed into purified gas, and the purified gas is conveyed to a chimney 10 through the pipeline 11 to be discharged into the atmosphere; after the sector 19 adsorbing the VOC is transferred to the high temperature desorption region 12, the hot air of the regenerative heater 7 is introduced into the high temperature desorption region 12, the VOC on the sector 19 of the high temperature desorption region 12 corresponding to the runner 18 is heated and desorbed, and the concentrated and desorbed high concentration VOC exhaust gas is conveyed to the exhaust gas treatment device 8 or the activated carbon adsorption device 9 through the pipeline 11;
(3) the fresh air fan 5 blows clean air at 2000m 3 The delivery air volume of the/h is introduced into the cooling zones 13a and 13b at the two sides, so that the rotating wheel 18 enters the sector 19 of the cooling zone 13a at the right side after passing through the high-temperature desorption zone 12 for cooling, the adsorption capacity is recovered, meanwhile, the influence of the residual heat of the cooling zone 14 at the left side is reduced, and the rotating wheel is heated to 150-200 ℃ from the cooling zones 13a and 13b at the two sides through the regenerative heater 7 and then is led to the high-temperature desorption zone 12.
(4) The VOC exhaust gas is burned or adsorbed by the exhaust gas treatment device 8 or the activated carbon adsorption device 9 and then discharged as a purified gas into the atmosphere through the chimney 10.
Further, the method also comprises the following steps: the cleaned gas is again fed to the fresh air fan 5 via a line 11.
Further, the rotation speed of the runner 18 of the high concentration ratio exhaust gas concentration device 6 was 7 r/h.
Furthermore, the concentration multiple of the waste gas can be adjusted by adjusting the conveying air quantity of the fresh air fan 5 and the heating temperature of the regenerative heater 7, and the multiple range is 5-15 times;
example 3
Referring to fig. 1 to 6, a workshop waste gas concentration system comprises a high-concentration-ratio waste gas concentration device 6, wherein the high-concentration-ratio waste gas concentration device 6 is composed of an outer frame support 16 and a round disc-shaped rotating wheel 18 rotatably arranged in the outer frame support 16, the outer frame support 16 is a metal frame which is through from front to back and sealed at the periphery, the rotating wheel 18 is formed by splicing a plurality of equally-rounded sectors 19 formed by adsorbing materials, the sectors 19 are isolated by partition frames or sealing materials, the sectors 19 of the rotating wheel 18 are divided into an adsorption area 14, a high-temperature desorption area 12 and two cooling areas 13a and 13b according to functions, the two cooling areas 13a and 13b are positioned at two sides of the high-temperature desorption area 12 and are adjacent to the adsorption area 14, and the outer frame support 16 is provided with a functional area frame 17 corresponding to the adsorption area 14, the high-temperature desorption area 12 and the two cooling areas 13a and 13 b.
Further, the sector of the adsorption zone 14 is 150 °, the sector of the high-temperature desorption zone 12 is 90 °, and the sectors of the two cooling zones 13a and 13b are 60 °.
Further, the high-temperature desorption region 12 and the adsorption region 14 are provided with the sealing cover 20 at the connecting pipeline 11 and are installed on the functional region frame 17, the sealing cover 20 is arranged to further reduce the leakage of the exhaust gas of the high-temperature desorption region 12 to other functional regions, and the exhaust gas dissipated from the left cooling region 13b leaks to the high-temperature desorption region 12 or the adsorption region 14.
An environment-friendly workshop waste gas collecting system using the workshop waste gas concentrating system comprises a closed outdoor space 15, equipment closed chambers, a high-concentration-ratio waste gas concentrating device 6, a waste gas treatment device 8, an activated carbon adsorption device 9 and a chimney 10, wherein the closed outdoor space 15 in a workshop is not closed, a plurality of equipment closed chambers are arranged in the workshop, chemical production equipment forms air isolation with the workshop environment through the equipment closed chambers, the equipment closed chambers are provided with air interchangers 3, the air intake flow of the air interchangers 3 is slightly smaller than the exhaust flow of waste gas, the equipment closed chambers 1 for generating high-concentration waste gas are connected with the waste gas treatment device 8 and the activated carbon adsorption device 9 through pipelines 11, the equipment closed chambers 2 for generating low-concentration waste gas are connected with the high-concentration-ratio waste gas concentrating device 6 through the pipelines 11, the high-concentration-ratio waste gas concentrating device 6 conveys purified air to the chimney 10 through the pipelines 11, and (3) conveying the concentrated high-concentration waste gas to a waste gas treatment device 8 or an activated carbon adsorption device 9 through a pipeline 11, connecting the waste gas treatment device 8 and the activated carbon adsorption device 9 with a chimney 10 through a pipeline 11, and discharging the purified air through the chimney 10.
The workshop of the system comprises a closed outdoor space 15 and a plurality of equipment closed chambers, and because the equipment closed chambers collect waste gas in a closed manner, almost no waste gas leaks into the closed outdoor space 15, and the closed outdoor space 15 is subjected to inorganization discharge treatment; a plurality of equipment closed chambers are arranged in the workshop, chemical production equipment forms an isolation space with the outside through the equipment closed chambers, and the air inlet flow of the air interchanger 3 of the equipment closed chambers is slightly smaller than the exhaust flow of waste gas, so that the equipment closed chambers are in a tiny negative pressure state, and the waste gas is ensured not to leak; this system is through dividing into the equipment enclosure and producing high concentration waste gas equipment enclosure 1, produce low concentration waste gas equipment enclosure 2 two kinds, and high concentration waste gas is directly carried to exhaust treatment device 8 or active carbon adsorption device 9, and the low concentration waste gas becomes high concentration waste gas through high concentration ratio exhaust gas concentration device 6 concentration, carries to exhaust treatment device 8 or active carbon adsorption device 9 with original high concentration waste gas together, discharges by chimney 10 after the purification.
The concentration of VOC in the closed chamber 1 of the equipment for generating high-concentration waste gas is 500-600 mg/m 3 The VOC concentration of the closed chamber 2 of the equipment for generating the low-concentration waste gas is 50-60 mg/m 3 Wherein the chemical production equipment for producing VOC comprises a three-roller grinder, a sand grinder, a high-speed dispersion machine, a stirring kettle, a packaging area, a batching area, a vacuum pump discharge pipe and a reverse-flow typeShould cauldron pressure release pipe, raw materials groove gas vent, the useless warehouse space of danger etc. produce high concentration waste gas equipment closed room 1 and produce solvent type product, produce low concentration waste gas equipment closed room 2 and produce UV type product, produce the equipment that high concentration waste gas equipment closed room 1 can contain a small amount of production low concentration waste gas, produce low concentration waste gas equipment closed room 2 and can contain a small amount of equipment that produces high concentration waste gas, can also contain the airtight operation package room that produces low concentration waste gas in the equipment closed room.
The waste gas treatment device 8 is a commercial RTO heat storage combustion device or a commercial CO catalytic combustion device, the rotating wheel 18 of the high-concentration-ratio waste gas concentration device 6 is a commercial zeolite rotating wheel or a commercial honeycomb activated carbon rotating wheel, and the size and the pore diameter of the rotating wheel 18 and the pore diameter of an adsorbing material can be adjusted and replaced according to the waste gas concentration and the air volume of a fan.
The VOC waste gas treated by the system comprises toluene, xylene, ethers, ketones and alcohols.
Furthermore, the front side of the adsorption area 14 is connected with the closed chamber 2 of the equipment for generating low-concentration waste gas through a pipeline 11, and the back side is connected with a chimney 10 and a fresh air fan 5 through a pipeline 11; the front side of the high-temperature desorption zone 12 is connected with the waste gas treatment device 8 and the activated carbon adsorption device 9 through a pipeline 11, and the back side is connected with the regeneration heater 7 through a pipeline 11; the front surfaces of the two cooling areas 13a and 13b are connected with the fresh air fan 5 through a pipeline 11, and the back surfaces of the two cooling areas are connected with the regenerative heater 7 through a pipeline 11.
According to the application, the cooling zones 13a and 13b are arranged on the two sides of the high-temperature desorption zone 12, and cold air is introduced into the high-temperature desorption zone in the direction opposite to the direction of desorption hot air, so that on one hand, the right cooling zone 13a is used for cooling the sector 19 of the rotating wheel 18 subjected to high-temperature desorption to recover the adsorption force; on the other hand, because the temperature of the high-temperature desorption region 12 is high, and the adsorption capacity of the cooling region 13b on the left side of the high-temperature desorption region 12 is large, the thermal conductivity coefficient of the cooling region 13b on the left side of the high-temperature desorption region 12 is relatively high, especially when the runner 18 rotates to a position where the partition frame is not overlapped with the high-temperature desorption region 12, that is, when the high-temperature region and the low-temperature region of the runner 18 are in the same runner sector 19, the VOC adsorbed by the cooling region 13b on the left side is easily affected by the residual heat of the high-temperature desorption region to diffuse to other regions in advance, so that the exhaust gas concentration of the high-temperature desorption region 12 is reduced, the exhaust gas concentration of the adsorption region 14 is increased, and the exhaust gas concentration multiple cannot reach a predetermined value, therefore, cold air is reversely introduced into the cooling regions 13a and 13b on both sides and the high-temperature desorption region 12 to limit the residual heat range of the high-temperature desorption region, thereby forming cold-hot air convection, most of the VOC exhaust gas scattered at the junction of the high-temperature desorption region 12 and the cooling region 13b enters the left side cooling region 13b for secondary desorption, then become desorption hot-blast through regenerative heater 7 heating, a small amount of scattered VOC waste gas gets into high temperature desorption district 12 along with desorption hot-blast and leads to exhaust treatment device 8 or active carbon adsorption device 9, effectively prevents VOC from scattering, has higher waste gas concentration multiple under same temperature and amount of wind, is particularly useful for the runner 18 that is equipped with the subregion frame, because the subregion frame adopts metal material mostly, the cost of manufacture is lower, but heat conduction more easily.
In this application, all 11 turnings of pipeline adopt 45 degrees angles, reduce waste gas air current resistance.
An environment-friendly treatment method based on the workshop waste gas environment-friendly collection system comprises the following steps:
(1) 3000m of exhaust gas discharged from the closed chamber 1 of the apparatus for generating high-concentration exhaust gas 3 The total delivery air volume per hour is discharged to a waste gas treatment device 8 or an active carbon adsorption device 9 through a pipeline 11;
(2) the exhaust gas discharged from the closed chamber 2 of the apparatus for generating low-concentration exhaust gas is 20000m 3 The total conveying air quantity of/h is sent to an adsorption area 14 of the high concentration ratio waste gas concentration device 6 through a pipeline 11, VOC components in the waste gas are transferred to a sector 19 corresponding to the adsorption area 14 by a rotating wheel 18 to be adsorbed into purified gas, and the purified gas is conveyed to a chimney 10 through the pipeline 11 to be discharged into the atmosphere; after the sector 19 adsorbing the VOC is transferred to the high temperature desorption region 12, the hot air of the regenerative heater 7 is introduced into the high temperature desorption region 12, the VOC on the sector 19 of the high temperature desorption region 12 corresponding to the runner 18 is heated and desorbed, and the concentrated and desorbed high concentration VOC exhaust gas is conveyed to the exhaust gas treatment device 8 or the activated carbon adsorption device 9 through the pipeline 11;
(3) the fresh air fan 5 blows clean air at 2000m 3 The delivery air volume of/h is introduced into the cooling zones 13a and 13b at the two sides, so that the rotating wheel 18 enters the right side for cooling after passing through the high-temperature desorption zone 12The sector 19 of the cooling zone 13a is cooled to recover the adsorption capacity, meanwhile, the influence of the residual heat of the left cooling zone 14 is reduced, and the left cooling zone 13a and the left cooling zone 13b are heated to 150-200 ℃ from the two cooling zones 13a and 13b through the regenerative heater 7 and then lead to the high-temperature desorption zone 12.
(4) The VOC exhaust gas is burned or adsorbed by the exhaust gas treatment device 8 or the activated carbon adsorption device 9 to be purified gas, and is discharged to the atmosphere through a chimney 10.
Further, the method also comprises the following steps: the cleaned gas is again fed to the fresh air fan 5 via a line 11.
Further, the rotation speed of the runner 18 of the high concentration ratio exhaust gas concentration device 6 is 8 r/h.
Furthermore, the exhaust gas concentration multiple can be adjusted by adjusting the conveying air quantity of the fresh air fan 5 and the heating temperature of the regenerative heater 7, wherein the multiple range is 5-15 times;
example 4
The clean air conveying amount of the fresh air fan 5 is 4000m 3 The rest of the procedure was as in example 2.
Example 5
The clean air conveying amount of the fresh air fan 5 is 1400m 3 The rest of the procedure was as in example 2.
Comparative example 1
Two cooling areas 13 of the high concentration ratio waste gas concentration device 6 are removed, the sector of the adsorption area 14 is 270 degrees, the sector of the high temperature desorption area 12 is 90 degrees, and the rest is the same as that of the embodiment 2.
Comparative example 2
The cooling area 13 at the left side of the high concentration ratio waste gas concentration device is removed, the sector of the adsorption area 14 is 180 degrees, the sector of the high temperature desorption area 12 is 90 degrees, the sector of the cooling area 13 at the right side is 90 degrees, and the rest is the same as the embodiment 2.
Comparative example 3
The rotation speed of the high concentration ratio exhaust gas concentrating device 6 was set to 2r/h, and the same as in example 3 was applied.
The exhaust gas concentration that sets up to detect to dissipate from high concentration ratio exhaust gas concentration device adopts VOC monitoring analysis appearance to detect high concentration ratio exhaust gas concentration device exhaust gas concentration before the absorption and adsorb back exhaust gas concentration, calculates the exhaust gas concentration multiple to and detect chimney exhaust gas's VOC concentration.
TABLE 1
It can be seen from the table that after the system is used for processing, the concentration multiple of the high-concentration-ratio waste gas concentration device is higher, the VOC concentration of the gas discharged from the chimney is extremely low, and the concentration effect and the purification effect are very excellent.
According to the application, the cooling zones 13a and 13b are arranged on the two sides of the high-temperature desorption zone 12, cold air is reversely introduced into the high-temperature desorption zone 12, the range of waste heat of the high-temperature desorption zone 12 is limited, cold and hot air convection is formed, one part of VOC waste gas which is scattered at the junction of the high-temperature desorption zone 12 and the left cooling zone 13b enters the left cooling zone 13b again along with the cold air for secondary desorption, the other part of VOC waste gas enters the high-temperature desorption zone 12 along with the hot air and is led to the waste gas treatment device 8 or the activated carbon adsorption device 9, the left cooling zone 13bVOC waste gas is effectively prevented from being scattered, the waste gas concentration ratio is higher under the same temperature and air quantity, the waste gas concentration ratio and the high concentration efficiency are high, and the rotary wheel is particularly suitable for the rotary wheel 18 with a partition frame;
the high concentration ratio waste gas concentration device 6 of this application can adjust the waste gas concentration multiple through the amount of wind and the 7 heating temperature of regenerative heater who adjusts new trend fan 5, and the waste gas concentration multiple adjusts easier and stable, and it is lower to adjust cost and energy consumption.
The device adopts the closed chamber of the device to isolate the waste gas generated by the chemical production device, and the space 15 outside the closed chamber is subjected to inorganization discharge treatment, so that the waste gas treatment cost is reduced; divide into the equipment enclosure and produce high concentration exhaust gas equipment enclosure 1, produce 2 two kinds of low concentration exhaust gas equipment enclosures, high concentration waste gas is direct to be carried to exhaust treatment device 8 or active carbon adsorption device 9, it becomes high concentration waste gas to concentrate low concentration waste gas through the high concentration ratio exhaust gas concentration device 6 of this application, carry to exhaust treatment device 8 or active carbon adsorption device 9 together with original high concentration waste gas, discharge by chimney 10 after the purification, the system adopts can be according to exhaust concentration and the real-time adjustment waste gas concentration multiple of flux when actual production behind the high concentration ratio exhaust gas concentration device 6 of this application, promote waste gas environmental protection collection system's treatment effeciency greatly and reduce the running cost, be particularly useful for high, medium, the factory workshop that low concentration waste gas coexisted.
In light of the foregoing description of the preferred embodiments of the present invention, it is clear that the skilled person can, by means of the foregoing description, determine the technical scope of the present invention without departing from the scope of the technical idea of the present invention, which is not limited to the contents of the description, but rather must be determined by the scope of the appended claims.
Claims (6)
1. The workshop waste gas concentration system is characterized by comprising a high-concentration-ratio waste gas concentration device (6), wherein the high-concentration-ratio waste gas concentration device (6) is composed of an outer frame support (16) and a circular-cake-shaped rotating wheel (18) rotatably arranged in the outer frame support (16), the outer frame support (16) is a metal frame which is through from front to back and sealed at the periphery, the rotating wheel (18) is formed by splicing a plurality of equally-rounded sectors (19) formed by adsorbing materials, the sectors (19) are isolated by partition frames or sealing materials, the sectors (19) of the rotating wheel (18) are divided into an adsorption area (14), a high-temperature desorption area (12) and two cooling areas (13a and 13b) according to functions, the two cooling areas (13a and 13b) are positioned at two sides of the high-temperature desorption area (12) and are adjacent to the adsorption area (14), and the outer frame support (16) is provided with the adsorption area (14), the high-temperature desorption area (12), Two cooling zones (13a, 13b) correspond to a functional zone frame (17).
2. The workshop waste gas concentration system of claim 1, wherein the sector of the adsorption area is 90-180 degrees, the sector of the high-temperature desorption area is 60-90 degrees, and the sectors of the two cooling areas are 45-60 degrees.
3. The workshop waste gas concentration system as claimed in claim 2, wherein the high-temperature desorption zone and the adsorption zone are provided with sealing covers at connecting pipelines and are mounted on the functional zone frame.
4. An environment-friendly workshop waste gas collecting system using the workshop waste gas concentrating system of claim 1, which comprises a closed outdoor space, an equipment closed chamber, a high-concentration-ratio waste gas concentrating device, a waste gas treatment device, an activated carbon adsorption device and a chimney, wherein the closed outdoor space in the workshop is not closed, a plurality of equipment closed chambers are arranged in the workshop, chemical production equipment is isolated from the workshop environment through the equipment closed chambers, the equipment closed chambers are provided with air interchangers, the air intake flow of the air interchangers is slightly smaller than the exhaust flow of waste gas, the equipment closed chamber for generating high-concentration waste gas is connected with the waste gas treatment device and the activated carbon adsorption device through pipelines, the equipment closed chamber for generating low-concentration waste gas is connected with the high-concentration-ratio waste gas concentrating device through a pipeline, the high-concentration-ratio waste gas concentrating device conveys purified air to the chimney through a pipeline, and conveys the concentrated high-concentration waste gas to the waste gas treatment device or the activated carbon adsorption device through a pipeline, the waste gas treatment device and the activated carbon adsorption device are connected with a chimney through a pipeline, and purified air is discharged through the chimney.
5. The environment-friendly workshop waste gas collecting system according to claim 4, wherein the front side of the adsorption area is connected with a low-concentration waste gas generating equipment closed chamber through a pipeline, and the back side of the adsorption area is connected with a chimney and a fresh air fan through pipelines; the front side of the high-temperature desorption area is connected with the waste gas treatment device and the activated carbon adsorption device through pipelines, and the back side of the high-temperature desorption area is connected with the regeneration heater through pipelines; the front sides of the two cooling areas are connected with a fresh air fan through a pipeline, and the back sides of the two cooling areas are connected with a regenerative heater through a pipeline.
6. The environment-friendly workshop exhaust gas collection system according to claim 4, wherein the VOC exhaust gas collected by the environment-friendly collection system comprises toluene, xylene, ethers, ketones, and alcohols.
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