CN203447959U - Device for removing volatile organic compounds in industrial waste gas - Google Patents
Device for removing volatile organic compounds in industrial waste gas Download PDFInfo
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- CN203447959U CN203447959U CN201320553307.5U CN201320553307U CN203447959U CN 203447959 U CN203447959 U CN 203447959U CN 201320553307 U CN201320553307 U CN 201320553307U CN 203447959 U CN203447959 U CN 203447959U
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Abstract
The utility model belongs to the technical field of removal of volatile organic compounds in industrial waste gas, and particularly relates to a device for removing volatile organic compounds in industrial waste gas, solving the problem of an existing device for removing volatile organic compounds in industrial waste gas. The device comprises a rotary packed bed absorber, an absorption pregnant liquor storage tank, an absorption barren liquor storage tank, a regeneration device, a pregnant liquor circulating pump and a barren liquor circulating pump, wherein a gas inlet pipe of the rotary packed bed absorber is connected with a waste gas source, a liquor discharging pipe is connected with the absorption pregnant liquor storage tank, the absorption pregnant liquor storage tank is connected with the absorption barren liquor storage tank and the regeneration device respectively through the pregnant liquor circulating pump, and the absorption barren liquor storage tank is connected with a liquor inlet pipe of the rotary packed bed absorber through the barren liquor circulating pump. The device has the advantages of low requirement on the industrial waste gas, wide application range, high removal rate, compact structure, small size, less investment, and the like, is capable of recovering the volatile organic compounds, and prevents from being blocked.
Description
Technical field
The utility model belongs to the technical field that removes VOC in industrial waste gas, is specifically related to a kind of device that removes VOC in industrial waste gas.
Background technology
VOC (VOCs) is the important sources of atmosphere pollution.VOCs has been considered to be the atmosphere pollution that Equations of The Second Kind has a large capacity and a wide range after dust at present.What the VOCs of industrial discharge brought is not only problem of environmental pollution, has also produced certain economic loss simultaneously.VOCs is mainly derived from the waste gas of petroleum chemical industry discharge, the organic solvent of the industry loss such as papermaking, coating, mining, metal plating and weaving, and the tail gas of vehicle emissions, and other may discharge the pollution sources of organic exhaust gas.Most of VOCs are poisonous, stench and " three cause " effect, part VOCs also can damage the ozone layer, can with atmosphere in nitrogen oxide, hydrocarbon and oxidant generation photochemical reaction, generate photochemical fog, environment, vegeto-animal growth and human health have been caused to great harm.
The technology of administering VOCs can be divided into two large classes: a class is disruptive method, as direct oxidation burning, catalytic combustion, corona, plasma and ultraviolet light decomposition and bioanalysis degraded etc.; Another kind of is nondestructive method, as absorption, active carbon adsorption, condensation method and membrane separation process etc.Wherein two kinds of technology of combustion technology and charcoal absorption in industry, apply comparatively general, but all there is in actual applications certain restriction.Combustion technology temperature in operating process is higher, control comparatively difficulty, in catalytic combustion technique, the component in industrial waste gas is had to certain requirement, while having sulfur-bearing and chloride organic matter in industrial waste gas, burning can cause secondary pollution, and in combustion process, easily make catalyst poisoning, process failure.Active carbon adsorption technology is widely used in the improvement of the organic exhaust gas of large-wind-volume low-concentration, technique comparative maturity, but having relatively high expectations to industrial waste gas, as the humidity of industrial waste gas, concentration etc., conventionally need to be aided with the pretreatment process of industrial waste gas, technological process is huge, and energy consumption is high.
Absorption is morning, technical maturity, the chemical separation process that has wide range of applications of a kind of development, when eliminating gaseous contaminant, pollutant recycled, and be the improvement technology of conventional atmosphere pollution.In absorption process, to adopt diesel oil be the mineral oil of representative, high boiling organic solvent and composite absorber three classes to absorbent more, in recent years the research of absorbent also had to very large progress.Absorption plant to be adopted and take the conventional tower equipment that packed tower is representative, tower bulky, and plant investment is larger, and liquid circulation amount is large, and vapour lock is high, and start-stop car is inconvenient, and equipment operating cost is high; In addition,, to some coating and glue production of articles industry, in waste gas, conventionally contain micelle material and impurity, these materials can be attached on filler or column plate, after operation a period of time, can cause the obstruction of tower, reduce the mass-transfer performance of equipment, bring serious economic loss.Therefore, development of new absorption plant and process thereof are significant.
Rotary packed bed (Rotating Packed Bed, be called for short RPB) utilize driven by motor filler High Rotation Speed to produce Elevated Gravity, under this Elevated Gravity, gas-liquid mass transfer efficiency obtains the raising of 1 ~ 3 order of magnitude, liquid circulation amount reduces, equipment volume is dwindled greatly, the production efficiency of unit equipment volume improves, gas phase drag significantly reduces, start-stop car is convenient, whole technique can be stablized within very short time, the filler of High Rotation Speed has the effect of self-cleaning, can avoid conventional tower equipment because the filler blockage problem that micelle material causes.But research shows, existing rotary packed bedly have great raising to mass transfer in liquid phase speed, and not obvious to the improvement of mass transferring in gas phase speed, the existing rotary packed bed very large room for promotion that also has aspect mass-transfer performance.
Summary of the invention
The utility model, for the deficiency existing in above-mentioned technology, has proposed a kind of device that removes VOC in industrial waste gas.
The utility model adopts following technical scheme to realize:
Remove the device of VOC in industrial waste gas, comprise rotary packed bed absorber, absorption rich solution storage tank, absorb lean solution storage tank, regenerating unit, rich solution circulating pump and lean solution circulating pump.
Described rotary packed bed absorber comprises revolving bed main body, equipment supporter and transmission device, revolving bed main body comprises upper and lower two parts: collection chamber and main chamber, in main chamber, be provided with can high speed counter-rotating filler rotor, main chamber top connects air inlet pipe, main chamber's bottom connected drainage pipe, filler rotor center arranges liquid distribution trough, and liquid distribution trough connects feed tube, collection chamber top connects blast pipe, and the perforate of filler rotor top is communicated with collection chamber.
The air inlet pipe of rotary packed bed absorber connects source exhaust gas, discharging tube connects absorption rich solution storage tank, absorb rich solution storage tank and connect respectively and absorb lean solution storage tank and regenerating unit through rich solution circulating pump, absorb lean solution storage tank and through lean solution circulating pump, connect the feed tube of rotary packed bed absorber.
The filler rotor of described rotary packed bed absorber comprises top rotary table and the lower rotary table of independent rotation respectively, top rotary table bottom and lower rotary table top are separately installed with some concentric annular packing supports, packing support inside is equipped with filler and is formed packing ring, packing ring on upper and lower rotating disk is nested against one another, between adjacent packing ring, leave gap, top rotary table top is connected with solid shafting, and lower rotary table bottom is connected with hollow shaft, hollow shaft top connects liquid distribution trough, and hollow shaft bottom connects feed tube.
The top rotary table bottom of described rotary packed bed absorber and lower rotary table top are respectively arranged with the groove of some concentric annular, and packing ring is fixed in groove, and it is interior and leave gap with the bottom land of another rotating disk that the free end of packing ring stretches into the groove of another rotating disk.
Described main chamber and collection chamber are isolated by dividing plate, and the perforate of dividing plate center also arranges tubular construction along hole week, tubular construction bottom be connected in the hole week of filler rotor top perforate, solid shafting passes tubular construction and is connected with top rotary table.
The position that the filler rotor top perforate of described rotary packed bed absorber is communicated with collection chamber arranges hermetically-sealed construction, described hermetically-sealed construction comprises top cover labyrinth setting up and down and lower sealing cover, top cover labyrinth is placed on tubular construction, lower sealing cover is connected with top rotary table, lower sealing cover center is uniform arranges some scallop holes, upper and lower seal cover is provided with labyrinth ring, and the labyrinth ring of upper and lower seal cover is embedded in together mutually, and the outmost turns of labyrinth ring arranges oil sealing felt collar.
The packing support of described rotary packed bed absorber is tubular stainless steel coil, circumferentially densely covered perforate, packing support outer rim is provided with some form drag parts, described form drag part is that Metal Flake projection, profile are rectangle or triangle, at right angle setting is in the outer rim of packing support, and filler adopts porous ripple filler.
Remove the process of VOC in industrial waste gas, based on described in the utility model, remove the device of VOC in industrial waste gas and complete, step comprises: open rotary packed bed, by regulating motor to make multiple filling layers counter-rotating, on, lower rotary table rotating speed is 200 ~ 1600r/min, the industrial waste gas that contains VOC and absorption liquid are entered rotary packed bed by air inlet pipe and feed tube respectively, gas-liquid contact mode is adverse current, absorption liquid and be 0.5 ~ 10L/m3 containing the industrial waste gas liquid-gas ratio of VOC, gas-liquid on the filler of rotation, contacted industrial waste gas in the removing of VOC, then by blast pipe and discharging tube, discharged respectively.Absorption rich solution after absorbing is regenerated, and the absorption liquid after regeneration is cycled to used in absorption operation.
Absorption liquid is adopted as water, diesel oil, machine oil or aqueous surfactant solution etc. according to the difference of VOC.Absorption rich solution after absorbing is regenerated, and regeneration is selected according to different systems, comprises rectifying, hot-air stripping and water vapour stripping etc., and the absorption liquid after regeneration is cycled to used in absorption operation.
Research shows, tradition is rotary packed bed has great raising to mass transfer in liquid phase speed, and mass transferring in gas phase speed is not had greatly improved, and tradition is rotary packed bed also has very large room for promotion aspect mass-transfer performance.Technique described in the utility model is using Novel rotary packed bed as absorption plant, and absorption liquid becomes micron-sized drop, brin and liquid film through cutting, the dispersion of multiple layer high speed counter-rotating filler, has increased greatly the contact area of gas phase and liquid phase; And the industrial waste gas that contains VOC is through the disturbance of form drag part, can further promote the turbulent flow of gas phase, more kinetic energy is passed to fluid, tubulence energy increases, accelerate boundary renewal rate, the flow trace of gas-liquid is more tortuous, and the time of staying extends accordingly, mass transfer rate between gas-liquid is greatly improved, strengthening assimilation effect.
The filler of high speed counter-rotating of the present utility model also has the effect of self-cleaning, for the gas that contains colloidal particles, can avoid the blockage problem of conventional tower equipment.Filler is that porous ripple filler carries out surface modification according to different absorbing system, makes filler have the advantageous property of hydrophilic or oleophylic, improves moistened surface effect.
The utlity model has to industrial waste gas require low, applied range, high, the recyclable VOC of removal efficiency, apparatus structure compact, avoid stopping up, the advantage such as volume is little, small investment.
Accompanying drawing explanation
Fig. 1 is the flow chart that removes VOC technique in industrial waste gas,
Fig. 2 is rotary packed bed absorption equipment main body schematic diagram,
Fig. 3 is a kind of structural representation of form drag part,
Fig. 4 is the another kind of structural representation of form drag part,
Fig. 5 is the assembling schematic diagram of packing ring on upper lower rotary table,
The rotary packed bed absorber internal structure of Fig. 6 schematic diagram,
In figure: 1-is rotary packed bed, 2-absorbs rich solution storage tank, 3-rich solution circulating pump, and 4-absorbs lean solution storage tank, 5-lean solution circulating pump, 6-regenerating unit, 7,8-control valve,
1.1-air inlet pipe, 1.2-blast pipe, 1.3-revolving bed main body, 1.4-discharging tube, 1.5-swivel joint, 1.6-belt, 1.7-equipment supporter, 1.8-T type groove, 1.9-motor, 1.10-belt pulley, 1.11-main chamber, 1.12-packing ring, 1.13-absorber liquid distribution trough, 1.14-hollow shaft, 1.15-bearing, 1.16-axle sleeve I, 1.17-lower rotary table, 1.18-top rotary table, 1.19-top cover labyrinth, 1.20-collection chamber, 1.21-axle sleeve II, 1.22-solid shafting, 1.23-oil sealing, 1.24-lower sealing cover, 1.25-dividing plate.
The specific embodiment
By reference to the accompanying drawings the specific embodiment of the present utility model is described further.
Remove the device of VOC in industrial waste gas, comprise rotary packed bed 1, absorb rich solution storage tank 2, rich solution circulating pump 3, absorb lean solution storage tank 4, lean solution circulating pump 5 and regenerating unit 6.
Described rotary packed bed absorber comprises revolving bed main body 1.3, equipment supporter 1.7 and transmission device, revolving bed main body 1.3 comprises upper and lower two parts: collection chamber 1.20 and main chamber 1.11, in main chamber 1.11, be provided with can High Rotation Speed filler rotor, main chamber 1.11 tops connect air inlet pipe 1.1, main chamber's 1.11 bottom connected drainage pipes 1.4, filler rotor center arranges liquid distribution trough 1.13, liquid distribution trough 1.13 connects feed tube, collection chamber 1.20 tops connect blast pipe 1.2, and the perforate of filler rotor top is communicated with collection chamber 1.20.
The air inlet pipe of rotary packed bed absorber 1 connects source exhaust gas, discharging tube connects absorption rich solution storage tank 2, absorb rich solution storage tank 2 and connect respectively and absorb lean solution storage tank 4 and regenerating unit 6 through rich solution circulating pump 3, absorb lean solution storage tank 4 and through lean solution circulating pump 5, connect the feed tube of rotary packed bed absorber 1.
The filler rotor of described rotary packed bed absorber 1 comprises top rotary table 1.18 and the lower rotary table 1.17 of independent rotation respectively, top rotary table 1.18 bottoms and lower rotary table 1.17 tops are separately installed with some concentric annular packing supports, packing support inside is equipped with filler and is formed packing ring 1.12, on, packing ring on lower rotary table is nested against one another, between adjacent packing ring, leave gap, top rotary table 1.18 tops are connected with solid shafting 1.22, lower rotary table 1.17 bottoms are connected with hollow shaft 1.14, hollow shaft 1.14 tops connect liquid distribution trough 1.13, hollow shaft 1.14 bottoms connect feed tube.
Top rotary table 1.18 bottoms of described rotary packed bed absorber 1 and lower rotary table 1.17 tops are respectively arranged with the groove of some concentric annular, packing ring 1.12 is fixed in groove, and the free end of packing ring stretches in the groove of another rotating disk and leaves gap with the bottom land of another rotating disk.
Filler in described packing support adopts porous ripple filler, and porous ripple filler carries out surface modification according to different absorbing system, makes filler have the advantageous property of hydrophilic or oleophylic, improves moistened surface effect.
Described main chamber 1.11 and collection chamber 1.20 are isolated by dividing plate 1.25, dividing plate 1.25 center perforates also arrange tubular construction along hole week, tubular construction bottom be connected in the hole week of filler rotor top perforate, solid shafting 1.22 passes tubular construction and is connected with top rotary table 1.18.
The position that the filler rotor top perforate of described rotary packed bed absorber 1 is communicated with collection chamber arranges hermetically-sealed construction, described hermetically-sealed construction comprises top cover labyrinth setting up and down 1.19 and lower sealing cover 1.24, top cover labyrinth 1.19 is placed on tubular construction, lower sealing cover 1.24 is connected with top rotary table 1.18, lower sealing cover 1.24 centers are uniform arranges some scallop holes, upper and lower seal cover is provided with labyrinth ring, the labyrinth ring of upper and lower seal cover is embedded in together mutually, and the outmost turns of labyrinth ring arranges oil sealing felt collar.
The packing support of described rotary packed bed absorber 1 is tubular stainless steel coil, circumferentially densely covered perforate, the outer rim of packing support is provided with some form drag parts, and described form drag part is Metal Flake projection, profile is rectangle or triangle, and at right angle setting is in the outer rim of packing support.
Remove the process of VOC in industrial waste gas, step is: open rotary packed bed 1, regulate motor 1.9 to preset rotating direction and rotating speed, rotating speed is (200 ~ 1600) r/min, and the industrial waste gas containing VOC of certain tolerance is entered rotary packed bed 1 multilayer counter-rotating filler by air inlet pipe 1.1; Absorption liquid through lean solution circulating pump 5, is adjusted liquid measure and through rotary packed bed feed tube, is entered rotary packed bed packing layer by certain liquid-gas ratio in absorbing lean solution storage tank 4; In this process, in the formed Elevated Gravity of multiple layer high speed counter-rotating packing layer, complete the contact process of absorbent and VOC, the gas after absorption is discharged by rotary packed bed blast pipe 1.2, realizes qualified discharge; Absorbing rich solution enters and absorbs rich solution storage tank 2 through rotary packed bed discharging tube 1.4, under the effect of rich solution circulating pump 3, enter and absorb lean solution storage tank 4, absorbent recycles, when absorption efficiency drops to certain degree, absorb rich solution and enter regenerating unit 6 through the effect of rich solution circulating pump 3, absorb rich solution and after regenerative operation, enter absorbent storage tank 4, recycle.The concentration of the VOC in industrial waste gas is measured in rotary packed bed import and export.
According to the basic principle of absorption operation, low temperature and hyperbaric environment are conducive to absorption operation, so the temperature of industrial waste gas is controlled at 30 ~ 60 ℃, absorbent temperature is controlled at 10 ~ 35 ℃; Gas-liquid contact mode is cross-flow or adverse current; Absorbent can be the aqueous solution of water, diesel oil, machine oil, diisooctyl adipate or surfactant, and this determines according to the physical property of VOC and production actual conditions.Regeneration technology, according to the difference of concrete system, can adopt rectifying, water vapor desorption or hot air regeneration, and regenerating unit can adopt rectifying column, packed tower or rotary packed bed accordingly.
Embodiment 1:
Adjusting rotary packed bed 1 counter-rotating rotating speed is 400 r/min, is that the simulation industrial waste gas of 1000 ppm enters through rotary packed bed air inlet pipe 1.1 rotary packed bed 1 by toluene concentration, and gas flow is 110 m3/h; The surfactant A that is 1.2% by mass fraction, remainder is that the absorbent of water enters rotary packed bed 1 through rotary packed bed feed tube, regulating liquid-gas ratio is 6 L/m3, gas-liquid two-phase is contact absorption fast on the filler of High Rotation Speed, purified gas is discharged through rotary packed bed blast pipe 1.2, the absorption rich solution that has absorbed toluene enters and absorbs rich solution storage tank 2 through rotary packed bed discharging tube 1.4, through rich solution circulating pump 3, squeezes into absorbent storage tank 4, and absorbent recycles.Detect the toluene concentration at blast pipe place, when absorption efficiency drops to certain value, absorb rich solution and squeeze into regenerating unit 6 through rich solution circulating pump, adopt rotary packed bedly in this example, regeneration temperature is 95 ℃, and the absorbent after regeneration recycles.In whole process, absorption efficiency remains on more than 90%.
Embodiment 2:
Adjusting rotary packed bed 1 counter-rotating rotating speed is 1000 r/min, is that the industrial waste gas of 5000 ppm enters through rotary packed bed air inlet pipe 1.1 rotary packed bed 1 by hexane concentration, and gas flow is 190 m3/h; No. 0 diesel oil is absorbent, absorbent enters rotary packed bed 1 through rotary packed bed feed tube, regulating liquid-gas ratio is 9 L/m3, gas-liquid two-phase is contact absorption fast on the filler of High Rotation Speed, purified gas is discharged through rotary packed bed blast pipe 1.2, the absorption rich solution that has absorbed hexane enters and absorbs rich solution storage tank 2 through rotary packed bed discharging tube 1.4, through rich solution circulating pump 3, squeezes into and absorbs lean solution storage tank 4, and absorbent recycles.Detect the hexane concentration at blast pipe place, when absorption efficiency drops to certain value, absorb rich solution and squeeze into regenerating unit 6 through rich solution circulating pump, adopt packed tower in this example, the absorbent after regeneration recycles.In whole process, absorption efficiency remains on more than 92%.
Embodiment 3:
Adjusting rotary packed bed 1 counter-rotating rotating speed is 800 r/min, is that the industrial waste gas of 2500 ppm enters through rotary packed bed air inlet pipe 1.1 rotary packed bed 1 by toluene concentration, and gas flow is 150 m3/h; Diisooctyl adipate is absorbent, absorbent enters rotary packed bed 1 through rotary packed bed feed tube, regulating liquid-gas ratio is 2 L/m3, gas-liquid two-phase is contact absorption fast on the filler of High Rotation Speed, purified gas is discharged through rotary packed bed blast pipe 1.2, the absorption rich solution that has absorbed toluene enters and absorbs rich solution storage tank 2 through rotary packed bed discharging tube 1.4, through rich solution circulating pump 3, squeezes into and absorbs lean solution storage tank 4, and absorbent recycles.Detect the toluene concentration at blast pipe place, when absorption efficiency drops to certain value, absorb rich solution and squeeze into regenerating unit 6 through rich solution circulating pump, adopt packed tower in this example, the absorbent after regeneration recycles.In whole process, absorption efficiency remains on more than 98%.
Claims (6)
1. a device that removes VOC in industrial waste gas, it is characterized in that comprising rotary packed bed absorber (1), absorb rich solution storage tank (2), absorb lean solution storage tank (4), regenerating unit (6), rich solution circulating pump (3) and lean solution circulating pump (5)
Described rotary packed bed absorber comprises revolving bed main body (1.3), equipment supporter (1.7) and transmission device, revolving bed main body (1.3) comprises upper and lower two parts: collection chamber (1.20) and main chamber (1.11), in main chamber (1.11), be provided with can high speed counter-rotating filler rotor, main chamber (1.11) top connects air inlet pipe (1.1), main chamber (1.11) bottom connected drainage pipe (1.4), filler rotor center arranges liquid distribution trough (1.13), liquid distribution trough (1.13) connects feed tube, collection chamber (1.20) top connects blast pipe (1.2), the perforate of filler rotor top is communicated with collection chamber (1.20),
The air inlet pipe of rotary packed bed absorber (1) connects source exhaust gas, discharging tube connects absorption rich solution storage tank (2), absorb rich solution storage tank (2) and connect respectively and absorb lean solution storage tank (4) and regenerating unit (6) through rich solution circulating pump (3), absorb lean solution storage tank (4) and through lean solution circulating pump (5), connect the feed tube of rotary packed bed absorber (1).
2. the device that removes VOC in industrial waste gas according to claim 1, the filler rotor that it is characterized in that described rotary packed bed absorber (1) comprises independent top rotary table (1.18) and the lower rotary table (1.17) rotating respectively, top rotary table (1.18) bottom and lower rotary table (1.17) top are separately installed with some concentric annular packing supports, packing support inside is equipped with filler and is formed packing ring (1.12), on, packing ring on lower rotary table is nested against one another, between adjacent packing ring, leave gap, top rotary table (1.18) top is connected with solid shafting (1.22), lower rotary table (1.17) bottom is connected with hollow shaft (1.14), hollow shaft (1.14) top connects liquid distribution trough (1.13), hollow shaft (1.14) bottom connects feed tube.
3. the device that removes VOC in industrial waste gas according to claim 2, it is characterized in that top rotary table (1.18) bottom of described rotary packed bed absorber (1) and the groove that lower rotary table (1.17) top is respectively arranged with some concentric annular, packing ring (1.12) is fixed in groove, and the free end of packing ring stretches in the groove of another rotating disk and leaves gap with the bottom land of another rotating disk.
4. according to the device that removes VOC in industrial waste gas described in claim 2 or 3, it is characterized in that described main chamber (1.11) and collection chamber (1.20) are by dividing plate (1.25) isolation, dividing plate (1.25) center perforate also arranges tubular construction, is convenient to solid shafting (1.22) and is connected with top rotary table (1.18) through this hole.
5. the device that removes VOC in industrial waste gas according to claim 4, it is characterized in that the position that the filler rotor top perforate of rotary packed bed absorber (1) is communicated with collection chamber arranges hermetically-sealed construction, described hermetically-sealed construction comprises top cover labyrinth setting up and down (1.19) and lower sealing cover (1.24), top cover labyrinth (1.19) is placed on tubular construction, lower sealing cover (1.24) is connected with top rotary table (1.18), lower sealing cover (1.24) center is uniform arranges some scallop holes, on, lower sealing cover is provided with labyrinth ring, on, the labyrinth ring of lower sealing cover is embedded in together mutually, the outmost turns of labyrinth ring arranges oil sealing felt collar.
6. the device that removes VOC in industrial waste gas according to claim 5, the packing support that it is characterized in that described rotary packed bed absorber (1) is tubular stainless steel coil, circumferentially densely covered perforate, packing support outer rim is provided with some form drag parts, described form drag part is that Metal Flake projection, profile are rectangle or triangle, and at right angle setting is in the outer rim of packing support.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320553307.5U CN203447959U (en) | 2013-09-07 | 2013-09-07 | Device for removing volatile organic compounds in industrial waste gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201320553307.5U CN203447959U (en) | 2013-09-07 | 2013-09-07 | Device for removing volatile organic compounds in industrial waste gas |
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| CN203447959U true CN203447959U (en) | 2014-02-26 |
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| CN201320553307.5U Withdrawn - After Issue CN203447959U (en) | 2013-09-07 | 2013-09-07 | Device for removing volatile organic compounds in industrial waste gas |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103463938A (en) * | 2013-09-07 | 2013-12-25 | 中北大学 | Device and process method for removing volatile organic compound contained in industrial waste gas |
| US9216377B1 (en) | 2015-02-24 | 2015-12-22 | Chevron U.S.A. Inc. | Method and system for removing impurities from gas streams using rotating packed beds |
| CN107569973A (en) * | 2016-07-05 | 2018-01-12 | 北京化工大学苏州（相城）研究院 | The absorption processing method and system of VOC organic exhaust gas |
| CN109126456A (en) * | 2018-09-25 | 2019-01-04 | 南京圆点环境清洁技术有限公司 | A kind of photooxidation catalytic waste gas processing unit |
-
2013
- 2013-09-07 CN CN201320553307.5U patent/CN203447959U/en not_active Withdrawn - After Issue
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103463938A (en) * | 2013-09-07 | 2013-12-25 | 中北大学 | Device and process method for removing volatile organic compound contained in industrial waste gas |
| CN103463938B (en) * | 2013-09-07 | 2015-07-15 | 中北大学 | Device and process method for removing volatile organic compound contained in industrial waste gas |
| US9216377B1 (en) | 2015-02-24 | 2015-12-22 | Chevron U.S.A. Inc. | Method and system for removing impurities from gas streams using rotating packed beds |
| CN107569973A (en) * | 2016-07-05 | 2018-01-12 | 北京化工大学苏州（相城）研究院 | The absorption processing method and system of VOC organic exhaust gas |
| CN109126456A (en) * | 2018-09-25 | 2019-01-04 | 南京圆点环境清洁技术有限公司 | A kind of photooxidation catalytic waste gas processing unit |
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