CN1372996A - Lifting wheel or adsorption system method for increasing efficiency to remove high-boiling-point waste organic gas - Google Patents
Lifting wheel or adsorption system method for increasing efficiency to remove high-boiling-point waste organic gas Download PDFInfo
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- CN1372996A CN1372996A CN 01109267 CN01109267A CN1372996A CN 1372996 A CN1372996 A CN 1372996A CN 01109267 CN01109267 CN 01109267 CN 01109267 A CN01109267 A CN 01109267A CN 1372996 A CN1372996 A CN 1372996A
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Abstract
A process for increasing the efficiency of removing high-boiling-point waste organic gas from rotary drum or adsorption system includes prefiltering the concentrated gas desorbed from the rotary-drum desorption region for removing solvent, reflux, mixing it with the waste gas to be treated, delivering the gas mixture to the cooling region of rotary drum system, cooling the rotary drum and regenerated adsorbent, heating to 120-250 deg.c in heat exchanger to become carrier gas for regeneration, introducing the gas stream to rotary drum system and regenerating region, desorbing and regenerating the adsorbent, and directly burning the rest of concentrated waste gas to decompose it to become clean gas.
Description
The invention provides a kind of method of exhaust-gas treatment, be meant a kind of method that promotes runner or adsorption system removal high-boiling-point waste organic gas efficient especially.
Absorption method is a kind of method that is widely used on the industry as pump-down process, utilize the character of adsorbent porous, VOC, stink or poisonous gas in the industry exhaust can be produced the absorption of physics, and it is adsorbed in the hole of adsorbent, to reach the purpose of purification industry exhaust.Yet adsorbent must be via the program of regeneration after absorption is saturated, and filling is adsorbed matter (for example volatile organic molecule, higher boiling chemical substance in adsorbent ... Deng) remove, just reusable.Wherein runner type adsorption system is a regenerative operation system on a kind of continous way line of succeeding in developing in recent years.Mainly be with adsorbent coating or be coated on the wheel of the various round or column types of making the honeycomb base material, for example be coated with activated carbon, zeolite or silica gel ... on the honeycomb base material wheel Deng the ripple glaze that various fiber is made of adsorbent, fiber commonly used includes ceramic fibre, carbon fiber, glass fibre or adhesive-bonded fabric etc.Again wheel is divided absorption 1, desorption 2 and cools off 3 (as Fig. 1 or Fig. 21,2,3 shown in) between three operating spaces.Wheel A rotates with certain speed, the industry waste gas that contains volatility organic component or stink composition or toxic chemical is when absorption imports adsorption zone 1, adsorbent on the runner is with volatile organic matter or stink composition or toxicant absorption, and reaching the purpose of waste gas purification, the waste gas after the purification can directly be thrown in the atmosphere-desorption district 2.When runner changes the desorption district over to, the pre-heated air of one stock-traders' know-how stream enters the volatile organic matter desorption that the desorption district will be adsorbed in the wheel surface adsorbent and comes out to flow 4 opposite directions with waste gas after the B heating, make adsorbent reactivation and use (as shown in Figure 3) so that continue, the temperature of general desorption manipulation is decided on the material of adsorbent and base material between 100-220 ℃.The concentrated waste gas that desorption comes out then imports a burner through 5 and carries out combustion decomposition, or imports a condenser and carry out condensation and reclaim.Usually the multiple that concentrates is high more has an economic benefit more, but considers the restriction of explosive range, generally is desorption when carrying gas with the air, concentrated multiple be controlled at 4-30 doubly between.In addition, for increasing the benefit of handling, set up behind the desorption district cooling zone is arranged, flow into the direction identical with one cold air or industry waste gas with waste gas stream, the base material cooling of the condition of high temperature will be in, promoting the absorption benefit of follow-up adsorption zone, the band temperature waste gas that flows out then imports heater, is heated to behind the desorption temperature usefulness as desorption gas again.Because the adsorption system that is adopted is for to coat the honeycomb wheel surface with straight-through duct with adsorbent, pressure fall general granular ADSORPTION IN A FIXED BED commonly used system will be low many, therefore the high approximately 5-10 of the ADSORPTION IN A FIXED BED system that the linear velocity of its operation is more general doubly is particularly suitable for the usefulness of the exhaust-gas treatment of big air quantity.But owing to have regeneration and use continuously on the line, therefore advantages of simple operation is widely used in semiconductor industry and application industry etc. again.Though the runner adsorption system has volume little, the high advantage of handling air quantity, but owing to absorption, desorption are all operated in certain finite interval, and for continous way is carried out, the removal efficiency in desorption district not only influences the service life of follow-up adsorption operations efficient and runner and the concentration that influence purifies the back discharging waste gas.Especially the waste gas that contains the higher boiling chemical substance in processing for example contains N. methyl one pyrrole noise made in coughing or vomiting ketone (n-Methyl Pyrolidone), methyl-sulfoxide (Dimethyl Sulfoxide); Monoethanolamine (2-Amino-Ethanol); When the waste gas of ethylene glycol (Ethylene Glycol) etc. is formed, often can't effectively remove these materials when then carrying out desorption and regeneration in the desorption district, cause in its adsorbent hole that residues in wheel surface, long-term accumulation not only causes the decline of follow-up adsorption capacity, emission gases does not reach within the environmental regulation specified standard, and, the danger of catching fire is often arranged and must change runner or do other processing because high solvent accumulates in the runner.For example runner is pulled down with line outward more the mode of high temperature (300-1000 ℃) burn off these materials are removed, this involves the runner base material again can be not high temperature resistant, even some runner base material (for example ceramic fibre) can be high temperature resistant, though but the mode of high temperature burn off can effectively be decomposed or removes being stranded in the intrapore high boiling substance of adsorbent, but often easily cause the destruction of adsorbent pore space structure, and lose adsorption capacity, or thereby deterioration and cause the surfacial spalling of adsorbent self-rotation wheel to predetermined substance.In addition, at cargo handling process, there is secondary pollution problem to exist unavoidably.
Traditional rotor design, normally adsorbing below 45 ℃, adsorb and promptly directly enter the regeneration of desorption district after saturated, the operation of desorption is with one thermal air current (or waste gas stream) that increases temperature (120-200 ℃) desorption district that flows through, the organic solvent desorption that utilizes hot poor mode will be adsorbed in the adsorbent comes out, the temperature difference in common two districts is between 80-160 ℃, in addition in order to keep higher operational benefits, the time of staying in the desorption district is unsuitable oversize again, often cause runner base material temperature skewness, position in outlet does not reach predefined desorption temperature, and the temperature of entrance location is quite high, make in the adsorbent of entrance location and produced desorption, but meet when arriving near the exit position cold be adsorbed once again again or produce condense and attached work in the surface (runner honeycomb duct is near the position of outlet) of adsorbent (see figure 4).Especially when processing contained high boiling substance waste gas, this kind phenomenon was more obvious.
In order to improve the shortcoming of existing runner system, the objective of the invention is to, a kind of method that promotes runner or adsorption system removal high-boiling-point waste organic gas efficient is provided, it has desorption efficient height, long service life and can make full use of used heat, can save the energy consumption of operation, not have the puzzlement of fire burning again
A kind of method that promotes runner or adsorption system removal high-boiling-point waste organic gas efficient of the present invention, it is characterized in that, be the concentrated waste gas that runner desorption district institute desorption is come out, wherein some refluxes after removing solvent with prefilter, and be mixed into blast-cold gas with the pending waste gas that enters runner, runner after will regenerating in the blast-cold district that this blast-cold gas enters runner system and adsorbent cooling, enter a heat exchanger again through being heated to the 120-250 ℃ of gas that carries that becomes regeneration usefulness, this strand air-flow is through importing the renewing zone of runner system, wheel surface is adsorbed saturated adsorbent desorption and regeneration, and the concentrated waste gas of another part is then directly sent into the cremation facilities heating and is decomposed into Purge gas.
Wherein blast-cold gas can be the industry exhaust, or air, or nitrogen, or other active gases not.
Wherein the high concentration desorption gas of Hui Liuing is between the 10-70% for total desorption gas volume.
Wherein the desorption gas of Hui Liuing is to mix with the waste gas inlet air flow, and after demist, imports the runner blast-cold more respectively and take off the district.
Wherein the runner pattern is wheeled or drum type brake, and with ceramic fibre, or carbon fiber, or macromolecular fibre is base material, and the surface is coated with zeolite, or activated carbon, or laminated soil, or polymeric sorbent.
Wherein the area of adsorption zone for the runner axle center by the open angle angle of center two radius be 180 to 330 spend between included areal extent person; The areal extent in desorption district is angle angle 10-120 degree person; The areal extent in blast-cold district is the 10-72 degree for the angle angle.
Wherein waste gas is that speed with 0.3 meter per second-5 meter per second enters runner.
Wherein equipment for after-treatment can be that incineration place is buried or solvent recovering system.
Wherein defogging equipment can be demister or filter screen, or condenser, or scrubbing tower.
Wherein desorption gas be with through be heated to 150-300 ℃ blast-cold gas for it.
Be convenient understanding superiority of the present invention, bright the present invention is described in further detail below in conjunction with drawings and Examples, wherein:
Fig. 1 is the vertical runner organigram;
Fig. 2 is a column type runner structure schematic diagram;
Fig. 3 is exhaust treatment system figure;
Fig. 4 is runner internal solvent and temperature profile;
Fig. 5 is exhaust treatment system figure of the present invention.
Desorption airduct after the runner adsorption system is added a manifold, the part high concentration that desorption is come out After contained condensing waste liquid is removed in the waste gas, lead go back to again adsorption zone and blast-cold district. This not only can reduce The temperature difference between adsorption system and desorption system makes the temperature in desorption district can be evenly distributed fast quilt The VOC that is adsorbed in the wheel surface adsorbent can be gone out by desorption in the adsorbent hole Come, and break away from fast the honey comb like duct of runner, not the temperature contrast in the reason duct once again by Near condensation and accumulating on the exit position, runner duct is processed benefit and reduce. In addition, Shang Kebao Hold identical concentration rate, the unlikely fuel that affects consumes. Main operation as shown in Figure 5, industry The waste gas 1 of discharging mixes with the reflux gas 2 that desorption concentrates, after demister D removes droplet, Be divided into two circuits and enter runner E, wherein the 60-95% of air quantity enters adsorption zone by pipeline Pending waste gas 3, carry out adsorption treatment, it is useless that purified gas 6 is delivered to bypass through blower fan H Gas 13 with the burning after exhaust mix after, the Purge gas 12 of secondary interchanger is again via pipeline Be disposed in chimney J or the atmosphere. Wherein the concentrated waste gas of desorption backflow is with the 10-of desorption gas 70% is advisable, and the droplet desorption method that is suitable for can be adopted demister or condenser, or scrubbing tower. Row The purifying exhaust air of putting also can be adopted respectively independently smoke stack emission with the waste gas that burning purifies, and only mixes row Be placed with the advantage that reduces EGT. The 5-40% of air quantity then enters runner by pipeline 4 in addition The blast-cold district, below the adsorbent blast-cold to 45 ℃ after the regeneration, Exhaust Gas 7 is advanced by pipeline Enter heat exchanger F after being heated to 150-300 ℃, enter again the desorption district and will adsorb saturated Runner be heated between 70-150 ℃, will absorption the volatile materials self-absorbent in take off Go out, the gas 5 of discharge is connected with admission line with a manifold, enters the demist drip apparatus after the mixing D enters respectively absorption place buried district and the blast-cold district of runner after demist, in addition, desorption comes out The concentrated waste gas 9 of 30-90% then can be sent into another heat exchanger via blower fan C and pipeline G is heated to 300-570 ℃, imports incinerator through pipeline, directly incineration process. Combustion High-temp waste gas after the burning is then sent into respectively the shell-side of aforesaid heat exchangers G, F, in order to reclaim used heat. In addition, the high dense waste gas of desorption also can directly be sent into other equipment for after-treatment, such as condenser, or electricity Slurry decomposer etc.
A kind of lifting wheel of the present invention or adsorption system are removed the method for high-boiling-point waste organic gas efficient, Be the concentrated waste gas that runner desorption district institute desorption is come out, wherein some is being removed with prefilter Reflux behind the solvent, and be mixed into blast-cold gas with the pending waste gas that enters runner, this blast-cold gas Runner after will regenerating in the blast-cold district that enters runner system and adsorbent cooling enter a heat exchange again Device is through being heated to the 120-250 ℃ of gas that carries that becomes regeneration usefulness, and this strand air-flow turns to through importing Saturated adsorbent desorption and regeneration is adsorbed with wheel surface in the renewing zone of wheel system, and another part Concentrated waste gas then directly send into cremation facilities heating and be decomposed into Purge gas.
Advantage of the present invention is to improve the efficient of desorption, and then promotes the performance of reproducing adsorbent, Make to be suitable for long period of operation, can guarantee that not only the long period of operation emission gases can meet the regulation of environmental protection, And can prolong the life-span of adsorbent (or runner). In addition, because direct control on the line does not have two The doubt of inferior pollution; In addition, take full advantage of used heat, can save the energy consumption of operation, do not have again in a large number molten Agent is accumulated in the exit position, causes the puzzlement of runner catching fire. System of the present invention be particularly suitable for into The exhaust-gas treatment of row Wind Volume is because runner is adopted honey comb like drill way layout, even under high flow rate Operation does not still have the too high problem of Pressure Drop, and the linear velocity of gas-operated can be generally fixed The 5-10 of adsorbent bed doubly, to be advisable between 0.3 meter per second-5 meter per second, wherein with 0.3 meter per second-3.5 meter per second the best; The shared area of adsorption zone is centered by the runner axle center Angle angle 180 degree that two radius is opened are advisable renewing zone, desorption between 330 degree The angle angle in district is advisable with the 10-120 degree, and the blast-cold district is with angle angle 10-72 degree Be advisable, the adsorbent of wheel surface coating can be zeolite, or activated carbon, or resin, or laminated soil, Or silica gel etc. Another benefit of the present invention is the gas that carries in desorption district, and the industry that can be is discharged Waste gas, or air, or with not active nitrogen for it, identical benefit is arranged all. The present invention System can be as the concentration of various mists, or recycling usefulness, and its treatment effeciency all Traditional runner promotes more than 10%, especially forms in the processing emission gases to include higher boiling During compound matter, all can keep for a long time high removal efficient. Times number average of general concentration is established Meter is below solvent gas explosive range lower limit. Therefore when using as concentrating and treating system with industry The waste gas of discharging as blast-cold district and desorption district to carry gas the most economical, general treatment effeciency Can meet more than 95%. Especially when processing discharging waste gas composition includes the higher boiling chemical substance, still Can keep clearance more than 95%. During as solvent recovering system, because of all at high concentration model Enclose operation, then be advisable as the gas that carries in blast-cold district or desorption district with nitrogen, treatment effeciency also Can reach more than 95%.
Be convenient understanding superiority of the present invention, specify for example that below the present invention promotes the characteristic that runner type adsorption system is removed the volatile organic waste gas efficiency method, the related content of each testing equipment is shown in the embodiment.The industry exhaust gas discharged is with GC, and (THC, FID) grade is carried out qualitative and be quantitative for GC-MASS and full carbon-hydrogen analyzer.Removal efficient in the embodiment is calculated according to following formula (1), and cycles of concentration calculates according to following formula (2).Following all examples are only for being used for representative special case of the present invention.Yet scope of the present invention is not limited to these embodiment.
Below all concentration be basic calculation all with the THC analysis result
Embodiment one
The waste gas of certain industry hydrocarbon to contain (THC) analyzer continuous monitoring result, its concentration changes between 45ppm-500ppm.Include methyl-sulfoxide 0-15ppm through irregularly sampling with gas chromatograph analysis result composition, monoethanolamine 20-30ppm, the N-methyl-than noise made in coughing or vomiting ketone 0-10ppm, DMDS alcohol 0.5-10nnm, ethylene glycol 5-20ppm, isopropyl alcohol 20-150ppm, the waste gas air quantity is 90000 a cubes/meters per hour, delivery temperature is between 20-40 ℃, through being 4250mm with diameter as shown in Figure 6, thickness is that the zeolite runner adsorption system of 400mm is handled, wherein the shared area of adsorption zone is the areal extents of 270 degree with the rotating shaft by the open angle number of degrees of center two radius, the folded angle number in desorption district is 30 degree, and the folded angle number of degrees in blast-cold district are 30 degree, and processing procedure waste gas is through being 1000 cubes/meters per hour with after concentrated waste gas desorption backflow mixes with air quantity, after a demister removes drop, wherein one waste gas enters the runner adsorption zone with 84100 cubic metres/hour speed, through adsorption treatment after smoke stack emission to atmosphere, it is 99% that the initial stage exhaust is buried benefit through the place as a result that analyzes with THC.Another strand air quantity is the blast-cold district that 6900 cubic metres/hour waste gas then imports runner, exhaust after tested as a result temperature be 105 ℃, after importing a heat exchanger heats to 200 ℃, import the desorption district again, the adsorbent desorption and regeneration that absorption on the runner is saturated, waste gas behind the desorption by analysis as a result temperature be 100 ℃, cycles of concentration is 13.The concentrated waste gas of desorption is incited somebody to action wherein with manifold, and 1000 cubic metres/hour air quantity is back to the air inlet airduct, air quantity is that 6900 cubic metres/hour concentrated waste gas then directly imports another heat exchanger in addition, after being heated to 510 ℃, directly send into incinerator, the waste gas after the decomposition carries out importing smoke stack emission in atmosphere after used heat is reclaimed in heat exchange through heat exchanger and secondary heat exchanger respectively.Through continued operation 3 months, the removal efficient of adsorption zone was between the 98%-99% through the continuous monitoring analysis result.
Embodiment two
Certain industry waste gas is so that carbon-hydrogen analyzer (THC) continuous monitoring result, its concentration changes by analysis between 30-600ppm, and its composition includes isopropyl alcohol, acetone, trimethyl silanol, toluene and tetramethyl two silicon ammoniums, the waste gas air quantity is 25000 cubic metres/hour, delivery temperature is that 40 ℃ of warps are 2500mm with a diameter, thickness is that the zeolite runner of 300mm carries out concentration, wherein the shared area of adsorption zone is to be that two radius open angle 330 degree in center are adsorption zone with the rotating shaft, the angle in desorption district and blast-cold district then is respectively 15 degree, the concentrated gas air quantity that desorption refluxes is 1600 cubic metres/hour, through mixing with the waste gas inlet air flow, after the demist, wherein one waste gas enters the runner adsorption zone with 24000 cubic metres/hour, the exhaust warp is with the THC analysis result, and clearance is 96%.Another strand waste gas then enters the blast-cold district with 2500 cubic metres/hour speed, the blast-cold gas of the discharging analysis result of flowing through is 80 ℃, this strand gas stream imports the desorption district more again after a heat exchanger heats to 160 ℃, carry out the desorption and regeneration of wheel surface adsorbent, desorption gas is cycles of concentration 10 as a result by analysis, and temperature is 150 ℃.Other will concentrate waste gas heating back and import the incinerator processing as the system of embodiment one.This cover system is removed efficient and is changed between 95-98% through the continuous monitoring analysis result through continued operation 5 months.
Embodiment three
Certain industry waste gas with full carbon-hydrogen analyzer (THC) continuous monitoring as a result concentration between 3000-15000ppm, change, include Methylethyl rim, toluene and dimethyl and send out amine through forming with the gas chromatograph analysis result.The waste gas air quantity is 7000 cubic metres/hour, delivery temperature is 80 ℃, waste gas is after being cooled to 35 ℃, through being 1500mm with the diameter, thickness is that the adsorption system of the activated carbon runner of 40mm reclaims, and warp is to carry out exhaust-gas treatment as embodiment one identical method, equipment for after-treatment then changes solvent recovery into, the angle that other changes adsorption zone is 300 degree, and the angle in desorption, blast-cold district is respectively 30 degree, as the treatment system of embodiment one.Wherein 6700 cubic metres/hour waste gas stream imports adsorption zone fully, and desorption backflow air quantity is 200 cubic metres/hour.Another strand gas enters the blast-cold district with 500 cubic metres/hour speed, and with the adsorbent cooling after the regeneration, exhaust result by analysis is 90 ℃, after a heat exchanger heats to 190 ℃, enters the desorption district and carries out desorption and regeneration.The exhaust in desorption district by analysis as a result temperature be 115 ℃, cycles of concentration is 12.Thickened waste gas is to handle with embodiment one identical processing mode.This cover system through the removal efficient of 3 months adsorption zones of continued operation between 95-97%.Comparative example one
Form with the identical waste gas of embodiment one and onesize zeolite runner carries out the waste gas concentration, only change the absorption that is designed to of runner, three zones of desorption and blast-cold, wherein adsorb shared area and be folder angle 300 degree scopes with the runner axle center, blast-cold and desorption then respectively are 30 degree, wherein one waste gas enters adsorption zone with 83100 cubic metres of/hour speed, the initial stage purifying exhaust gas by analysis the result to remove efficient be 98%, another strand waste gas directly imports the blast-cold district with 6900 cubic metres of/hour speed, the blast-cold exhaust is the result by analysis, temperature is 105 ℃, after a heat exchanger heats to 200 ℃, import the desorption district again, carry out the regeneration of wheel surface adsorbent, desorption gas by analysis as a result temperature be 50 ℃, cycles of concentration is 12 times.After 3 months, it is 87% that decrease in efficiency is removed in the purification of adsorption zone to this cover system through continued operation, finds that through shutdown inspection the outlet side accumulation in runner desorption district has yellow liquid material, is methyl-sulfoxide and monoethanolamine through the GC-MASS qualification result.
By the result of embodiment one, two, three and comparative example one the inventive method as can be known, not only can promote the runner adsorption system maintenance of VOC long-term disposal is removed efficient more than 95%, and can increase the operation lifetime of runner.
Claims (10)
1. one kind promotes the method that runner or adsorption system are removed high-boiling-point waste organic gas efficient, it is characterized in that, be the concentrated waste gas that runner desorption district institute desorption is come out, wherein some refluxes after removing solvent with prefilter, and be mixed into blast-cold gas with the pending waste gas that enters runner, runner after will regenerating in the blast-cold district that this blast-cold gas enters runner system and adsorbent cooling, enter a heat exchanger again through being heated to the 120-250 ℃ of gas that carries that becomes regeneration usefulness, this strand air-flow is through importing the renewing zone of runner system, wheel surface is adsorbed saturated adsorbent desorption and regeneration, and the concentrated waste gas of another part is then directly sent into the cremation facilities heating and is decomposed into Purge gas.
2. lifting runner according to claim 1 or adsorption system are removed the method for high-boiling-point waste organic gas efficient, it is characterized in that wherein blast-cold gas can be the industry exhaust, or air, or nitrogen, or other active gases not.
3. lifting runner according to claim 1 or adsorption system are removed the method for high-boiling-point waste organic gas efficient, it is characterized in that, wherein the high concentration desorption gas of Hui Liuing is between the 10-70% for total desorption gas volume.
4. lifting runner according to claim 3 or adsorption system are removed the method for high-boiling-point waste organic gas efficient, it is characterized in that wherein the desorption gas of Hui Liuing is to mix with the waste gas inlet air flow, and after demist, import the runner blast-cold more respectively and take off the district.
5. lifting runner according to claim 1 or adsorption system are removed the method for high-boiling-point waste organic gas efficient, it is characterized in that, wherein the runner pattern is wheeled or drum type brake, with ceramic fibre, or carbon fiber, or macromolecular fibre is a base material, the surface is coated with zeolite, or activated carbon, or laminated soil, or the polymeric sorbent person.
6. lifting runner according to claim 1 or adsorption system are removed the method for high-boiling-point waste organic gas efficient, it is characterized in that, wherein the area of adsorption zone for the runner axle center by the open angle angle of center two radius be 180 to 330 spend between included areal extent person; The areal extent in desorption district is angle angle 10-120 degree person; The areal extent in blast-cold district is the 10-72 degree for the angle angle.
7. lifting runner according to claim 1 or adsorption system are removed the method for high-boiling-point waste organic gas efficient, it is characterized in that, wherein waste gas is that speed with 0.3 meter per second-5 meter per second enters runner.
8. lifting runner according to claim 1 or adsorption system are removed the method for high-boiling-point waste organic gas efficient, it is characterized in that, wherein equipment for after-treatment can be that incineration place is buried or solvent recovering system.
9. lifting runner according to claim 4 or adsorption system are removed the method for high-boiling-point waste organic gas efficient, it is characterized in that wherein defogging equipment can be demister or filter screen, or condenser, or scrubbing tower.
10. lifting runner according to claim 1 or adsorption system are removed the method for high-boiling-point waste organic gas efficient, it is characterized in that, wherein desorption gas be with through be heated to 150-300 ℃ blast-cold gas for it.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01109267 CN1226071C (en) | 2001-02-28 | 2001-02-28 | Lifting wheel or adsorption system method for increasing efficiency to remove high-boiling-point waste organic gas |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01109267 CN1226071C (en) | 2001-02-28 | 2001-02-28 | Lifting wheel or adsorption system method for increasing efficiency to remove high-boiling-point waste organic gas |
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| CN1226071C CN1226071C (en) | 2005-11-09 |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105582688A (en) * | 2014-10-29 | 2016-05-18 | 石家庄天龙环保科技有限公司 | High-effective purifying and thermal-energy-utilizing method for gas containing VOCs |
| CN105597490A (en) * | 2014-11-20 | 2016-05-25 | 杰智环境科技股份有限公司 | Organic exhaust gas adsorption/desorption, concentration and purifying system and method thereof |
| CN107485977A (en) * | 2016-06-13 | 2017-12-19 | 河北子瑜环保科技有限公司 | A kind of VOCs waste gas treatment process and processing unit |
| CN112023620A (en) * | 2019-05-17 | 2020-12-04 | 华懋科技股份有限公司 | High-temperature desorption method of volatile organic waste gas treatment system |
| CN114307539A (en) * | 2021-11-01 | 2022-04-12 | 株式会社西部技研 | Gas treatment device |
| CN114984721A (en) * | 2022-05-24 | 2022-09-02 | 光大环境科技（中国）有限公司 | System and method for recovering carbon dioxide in flue gas |
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2001
- 2001-02-28 CN CN 01109267 patent/CN1226071C/en not_active Expired - Lifetime
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105582688A (en) * | 2014-10-29 | 2016-05-18 | 石家庄天龙环保科技有限公司 | High-effective purifying and thermal-energy-utilizing method for gas containing VOCs |
| CN105597490A (en) * | 2014-11-20 | 2016-05-25 | 杰智环境科技股份有限公司 | Organic exhaust gas adsorption/desorption, concentration and purifying system and method thereof |
| CN105597490B (en) * | 2014-11-20 | 2020-12-01 | 杰智环境科技股份有限公司 | Organic waste gas adsorption, desorption, concentration and purification system and method thereof |
| CN107485977A (en) * | 2016-06-13 | 2017-12-19 | 河北子瑜环保科技有限公司 | A kind of VOCs waste gas treatment process and processing unit |
| CN112023620A (en) * | 2019-05-17 | 2020-12-04 | 华懋科技股份有限公司 | High-temperature desorption method of volatile organic waste gas treatment system |
| CN114307539A (en) * | 2021-11-01 | 2022-04-12 | 株式会社西部技研 | Gas treatment device |
| CN114984721A (en) * | 2022-05-24 | 2022-09-02 | 光大环境科技（中国）有限公司 | System and method for recovering carbon dioxide in flue gas |
| CN114984721B (en) * | 2022-05-24 | 2024-01-26 | 光大环境科技（中国）有限公司 | System and method for recycling carbon dioxide in flue gas |
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| CN1226071C (en) | 2005-11-09 |
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