CN107297127B - VOCs waste gas treatment method - Google Patents

VOCs waste gas treatment method Download PDF

Info

Publication number
CN107297127B
CN107297127B CN201710477947.5A CN201710477947A CN107297127B CN 107297127 B CN107297127 B CN 107297127B CN 201710477947 A CN201710477947 A CN 201710477947A CN 107297127 B CN107297127 B CN 107297127B
Authority
CN
China
Prior art keywords
treatment
vocs
gas
waste gas
plasma
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201710477947.5A
Other languages
Chinese (zh)
Other versions
CN107297127A (en
Inventor
王守国
卞忠华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JIANGSU CHUNSHENTANG PHARMACEUTICAL Co.,Ltd.
Original Assignee
Jiangsu Chunshentang Pharmaceutical Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Jiangsu Chunshentang Pharmaceutical Co ltd filed Critical Jiangsu Chunshentang Pharmaceutical Co ltd
Priority to CN202010520808.8A priority Critical patent/CN111659232B/en
Priority to CN201710477947.5A priority patent/CN107297127B/en
Publication of CN107297127A publication Critical patent/CN107297127A/en
Application granted granted Critical
Publication of CN107297127B publication Critical patent/CN107297127B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/18Absorbing units; Liquid distributors therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/007Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by irradiation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1406Multiple stage absorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1487Removing organic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/32Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by electrical effects other than those provided for in group B01D61/00
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/38Removing components of undefined structure
    • B01D53/44Organic components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/46Removing components of defined structure
    • B01D53/72Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34Chemical or biological purification of waste gases
    • B01D53/74General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2256/00Main component in the product gas stream after treatment
    • B01D2256/22Carbon dioxide
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/702Hydrocarbons
    • B01D2257/7027Aromatic hydrocarbons
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/70Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
    • B01D2257/708Volatile organic compounds V.O.C.'s
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/80Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
    • B01D2259/818Employing electrical discharges or the generation of a plasma

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Environmental & Geological Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Toxicology (AREA)
  • Treating Waste Gases (AREA)

Abstract

The invention discloses a VOCs waste gas treatment method, which comprises the steps of water curtain spraying treatment, atomization spraying treatment, gas-liquid separation treatment, plasma treatment and infrared absorption particle treatment which are sequentially carried out; the invention realizes that the removal rate of the VOCs waste gas can reach more than 90 percent at most, solves the problem that the existing waste gas treatment technology is difficult to meet the continuously improved emission standard requirement, and eliminates the emission pollution of the VOCs waste gas to the environment; the whole treatment process is simple and easy to operate, the treatment efficiency is high, the required equipment is few, the energy consumption of the equipment is low, the requirements of modern enterprises on energy conservation and emission reduction and production benefit improvement are well met, and the method has great significance for saving resources and reducing cost.

Description

VOCs waste gas treatment method
Technical Field
The invention belongs to the technical field of environmental protection, and particularly relates to a VOCs waste gas treatment method.
Background
In recent years, more serious air pollution events occur nationwide, which leads people to pay more and more attention to air quality, and meanwhile, various levels of governments and environmental protection departments develop a plurality of special policies aiming at the phenomenon, so that the waste gas treatment industry is developed vigorously. In the VOCs (volatile organic compounds) waste gas treatment industry, the activated carbon adsorption method with low technical content and high operation cost is adopted in the early stage and is developed slowly. After environmental protection standards are raised in various places, VOCs are required to be treated by enterprises which discharge VOCs but do not treat or do not reach the standard after treatment.
The existing VOCs waste gas treatment technology mainly comprises an adsorption method (spraying and activated carbon adsorption), a recovery method (condensation and spraying) and a direct removal method (low-temperature plasma, photocatalytic oxidation and concentrated combustion). Combustion methods, mainly including concentrated combustion, thermal combustion and catalytic combustion; the concentration combustion method is a method for directly combusting high-concentration VOCs by further concentrating most of components of organic waste gas and increasing the concentration of the VOCs; the thermal combustion is a method of mixing and then combusting fuels such as natural gas and the like with VOCs; catalytic combustion is a process for completely oxidizing VOCs at a relatively low temperature (250 ℃ to 450 ℃) by the action of a catalyst. An absorption (recovery) method, which mainly comprises solvent absorption, electrostatic adsorption and condensation recovery; the solvent absorption method utilizes the principle of similar intermiscibility, and VOCs are separated and reused after being absorbed by an organic solvent; condensing and recycling different components of VOCs with different boiling points, and cooling and recycling certain components; the electrostatic adsorption is mainly used for treating oily waste gas, and the electrostatic field is utilized to charge oil drops and then adsorb the oil dropsAnd (6) recovering. The adsorption method mainly adopts activated carbon adsorption, and the activated carbon mainly adsorbs particles or gas molecules through micropore adsorption and surface unbalanced van der waals force and chemical bond force, so that the aim of removing VOCs is fulfilled. Decomposition methods, mainly including photocatalysis, infrared absorption particle technology and low temperature plasma method; the photocatalysis is based on the principle that the photocatalyst has strong oxidizability under the irradiation of ultraviolet light, and VOCs gas molecules adsorbed on the surface are oxidized and decomposed; low temperature plasma method utilizes energetic particles and radicals in the plasma to decompose VOCs into CO2And water. The traditional method has the problems of low removal rate (such as spraying, low-temperature plasma and activated carbon adsorption) of the waste gas difficult to treat, high operation cost (such as activated carbon adsorption, concentrated combustion and photocatalytic oxidation) and the like. For example, activated carbon adsorption, on one hand, the activated carbon adsorption equipment of many manufacturers is in long-term shutdown due to high operation cost and is only used during environmental protection inspection; on the other hand, activated carbon need handle according to dangerous chemicals after using, practicality greatly reduced, as traditional low temperature plasma processing technology again, it adopts power frequency high voltage power supply or direct current high voltage power supply, form such as through corona discharge gets rid of VOCs, however particle can't break some chemical bonds of major bond energy in its plasma that produces for it is underground to some VOCs clearance, is beaten into the micromolecule to the macromolecule even, and benzene class organic matter is handled back VOCs concentration and is 1-2 times than before handling on the contrary.
Therefore, it is an urgent technical problem to be solved by those skilled in the art to provide an exhaust gas treatment technology for removing VOCs with high removal rate, high efficiency, low operation cost, simple process and wide applicability.
Disclosure of Invention
The invention aims to solve the technical problems of overcoming one or more defects in the prior art and providing a VOCs waste gas treatment method combining the steps of water curtain spraying treatment, atomization spraying treatment, gas-liquid separation treatment, plasma treatment and infrared absorption particle treatment so as to realize low-cost, high-efficiency and safe removal of VOCs, improve living environment and promote social sustainable development.
In order to solve the technical problems, the invention adopts a technical scheme as follows:
the VOCs waste gas treatment method comprises the steps of water curtain spraying treatment, atomization spraying treatment, gas-liquid separation treatment, plasma treatment and infrared absorption particle treatment which are sequentially carried out.
In some embodiments of the present invention, in the water curtain spraying treatment step, the VOCs waste gas is introduced from the bottom of the water curtain spraying tower, and flows out from the top after being sprayed by the water curtain, the water curtain spraying treatment method adopts annular spraying, and the annular spraying includes a plurality of spraying portions, and the plurality of spraying portions are spirally distributed in the water curtain spraying tower.
In some embodiments of the present invention, in the atomized spray treatment step, the spray liquid comprises an aqueous liquid, and the aqueous liquid is atomized by an atomizer to form a layer of water film, wherein the water film is used for capturing fine particles in the waste gas of the VOCs, and the fine particles comprise paint particles, toluene and xylene.
In some embodiments of the present invention, in the gas-liquid separation treatment step, the mist and/or liquid droplets in the VOCs off-gas are removed by a gas-liquid separator, which is operated at normal temperature and pressure.
In some embodiments of the present invention, in the plasma treatment step, the VOCs waste gas treated in the gas-liquid separation treatment step passes through the plasma generation electrode in a direction parallel to an electric field of the plasma generation electrode of the plasma generation device, so that an overall electrically neutral plasma including electrons, positive ions, neutral particles, and radicals is generated in the VOCs waste gas; and charging the surface of dust particles in the VOCs exhaust gas; the plasma reacts with oxygen molecules and water molecules in the VOCs waste gas to generate H, O, OH and O with strong oxidizing property3The active particles, VOCs in the VOCs waste gas generate gaseous carbon dioxide and water under the action of the active particles.
In some embodiments of the present invention, the plasma generating electrode includes a set of high voltage electrodes and a set of ground electrodes, the high voltage electrodes and the ground electrodes are both coated with an insulating medium, and the high voltage electrodes and the ground electrodes are both arranged in a linear shape; the high-voltage electrode is connected with a high-voltage power supply, and the high-voltage power supply is one or a combination of a positive polarity direct-current high-voltage power supply, a positive polarity pulse high-voltage power supply or a positive polarity direct-current superposed alternating-current high-voltage power supply.
In some embodiments of the invention, in the infrared absorbing particulate treatment step, the waste gas of VOCs treated in the plasma treatment step is heated by an infrared heating device, so that the VOCs in the waste gas absorb infrared energy and further react with plasma remaining in the gas stream and decompose to form carbon dioxide and water; the infrared heating device comprises an infrared emitter, a gas containing cavity and infrared absorption particles distributed on the inner wall of the gas containing cavity, wherein a plurality of stand columns are arranged in the gas containing cavity, airflow is enabled to flow in a snake shape through the stand columns, and the infrared emitter outputs infrared light with the wavelength of 760 and 850 nm.
In some embodiments of the present invention, the method for treating the waste gas containing VOCs employs the following treatment systems:
the treatment system comprises a water curtain spray tower, an atomization spray tower, a gas-liquid separator, a plasma generation device and an infrared heating device which are sequentially connected and communicated;
the water curtain spray tower comprises a plurality of spraying parts, and the plurality of spraying parts are spirally distributed in the water curtain spray tower; the atomization spray tower comprises an atomizer and spray liquid, and the spray liquid forms layered film-shaped fog drops through the atomizer;
the plasma generating device comprises a plasma generating electrode and a high-voltage power supply, wherein the plasma generating electrode comprises a group of high-voltage electrodes and a group of grounding electrodes, the high-voltage electrodes and the grounding electrodes are both coated with insulating media, and the high-voltage electrodes and the grounding electrodes are both arranged in a linear mode; the high-voltage electrode is connected with the high-voltage power supply, and the high-voltage power supply is one or a combination of a positive polarity direct-current high-voltage power supply, a positive polarity pulse high-voltage power supply or a positive polarity direct-current superposed alternating-current high-voltage power supply;
the infrared heating device comprises an infrared emitter, a gas containing cavity and infrared absorption particles distributed in the gas containing cavity, wherein a plurality of stand columns are arranged in the gas containing cavity, airflow is enabled to flow in a snake shape through the stand columns, and the infrared emitter outputs infrared light with the wavelength of 760 and 850 nm.
Further, the plasma generating device also comprises a pressure sensor and a temperature sensor, wherein the pressure sensor and the temperature sensor are used for monitoring the pressure and the temperature in the plasma generating device in real time.
In the invention, the total removal rate of VOCs in the waste gas treated by the VOCs waste gas treatment method is more than or equal to 75%, wherein: carrying out dry-mass cultivation on the seeds at a speed of less than or equal to 17 mg/m; carrying out Toluene cultivation at a speed of less than or equal to 60 mg/m; and (5) carrying out xylene up to 90 mg/m.
Due to the adoption of the technical scheme, compared with the prior art, the invention has the following advantages:
1. the invention organically combines the steps of water curtain spraying treatment, atomization spraying treatment, gas-liquid separation treatment, plasma treatment and infrared absorption particle treatment, so that the steps are mutually cooperated to realize standard emission of VOCs, and the invention has the advantages of simple treatment process, low operation cost, wide applicability and high VOCs removal rate.
2. The invention solves the problem of low removal rate of the waste gas difficult to decompose in the traditional low-temperature plasma technology, and the flow direction of the VOCs waste gas is set to be parallel to the electric field direction of the plasma generating electrode of the plasma generating device, so that the reduction of the plasma processing effect caused by overlarge or undersize flow rate of the waste gas is overcome, the contact time and the contact area of the waste gas and the plasma are increased, and the high-efficiency utilization of the plasma is realized.
3. The invention adopts a unique infrared absorption particle treatment step and a plasma treatment step, realizes high removal rate of VOCs waste gas, has simple device, low cost and low energy consumption, meets the practical requirement and is suitable for large-area popularization.
4. The VOCs waste gas treatment method of the invention has the advantages of low investment, low operation and maintenance cost, small equipment floor area and high treatment efficiency, and can realize high-efficiency deodorization and peculiar smell removal, the treated waste gas can completely meet the specific technical index requirements of various local environmental protection authorities, and simultaneously, the deflagration caused by safety accidents such as rapid increase of VOCs concentration in short time caused by exhaust faults or other reasons and the like is avoided by additionally arranging temperature control and pressure control, the deflagration is prevented from spreading to workshops to cause injury and death of workers, and the safety performance is greatly improved.
Drawings
In order to more clearly illustrate the embodiments of the present invention or the technical solutions in the prior art, the drawings used in the description of the embodiments or the prior art will be briefly described below, it is obvious that the drawings in the following description are only some embodiments of the present invention, and for those skilled in the art, other drawings can be obtained according to the drawings without creative efforts.
FIG. 1 is a schematic flow diagram of a VOCs treatment process of the present invention;
FIG. 2 is a schematic diagram of one embodiment of the VOCs treatment process of the present invention;
FIG. 3 is a schematic structural diagram of a plasma generator according to the present invention;
fig. 4 is a schematic structural diagram of an infrared heating device of the present invention.
Detailed Description
The technical solution and the advantages thereof will be described in detail with reference to the following embodiments and the accompanying drawings.
Example 1
The sampling analysis is carried out on the VOCs waste gas of a certain factory, and the specific properties are as follows:
wherein, in the exhaust gas: carrying out dry bottom row cultivation on the root, 106.3 mg/m; carrying out Toluene 287.5 mg/m; dilute ethanol 627.5 mg/m.
As shown in fig. 1-4, the present embodiment provides a method for treating VOCs waste gas, comprising the steps of:
1) water curtain spray treatment
Introducing VOCs waste gas from the bottom of a water curtain spray tower 1, spraying the waste gas through a water curtain and then flowing out from the upper part, wherein the water curtain spray treatment mode adopts annular spray, the annular spray comprises a plurality of spray parts 11, and the plurality of spray parts 11 are spirally distributed in the water curtain spray tower 1;
2) atomized spray treatment
The spraying liquid comprises water liquid, the water liquid is atomized through an atomizer 21 to form a layer of water film, the water film is used for capturing fine particles in VOCs waste gas, and the fine particles comprise paint particles, toluene and xylene;
3) gas-liquid separation treatment
Removing fog drops and/or liquid drops in the VOCs waste gas through a gas-liquid separator 3, wherein the gas-liquid separator 3 is operated at normal temperature and normal pressure;
4) plasma treatment
Passing the VOCs waste gas treated by the gas-liquid separation treatment step through a plasma generating electrode of a plasma generating device 4 along an electric field direction parallel to the plasma generating electrode, so that plasma which is electrically neutral and comprises electrons, positive ions, neutral particles and free radicals is generated in the VOCs waste gas; and charging the surface of dust particles in the VOCs exhaust gas; the plasma reacts with oxygen molecules and water molecules in the VOCs waste gas to generate H, O, OH and O with strong oxidizing property3The VOCs in the VOCs waste gas generate gaseous carbon dioxide and water under the action of the active particles; the plasma generating electrode comprises a group of high-voltage electrodes 42 and a group of grounding electrodes 43, the high-voltage electrodes 42 and the grounding electrodes 43 are both coated with insulating media 41, and the high-voltage electrodes 42 and the grounding electrodes 43 are both arranged in a linear mode; the high-voltage electrode 42 is connected with a high-voltage power supply 46, and the high-voltage power supply 46 is one or a combination of a positive polarity direct-current high-voltage power supply, a positive polarity pulse high-voltage power supply or a positive polarity direct-current superposed alternating-current high-voltage power supply;
in the embodiment, the direction of the electric field of the plasma is set to be consistent with the direction of the VOCs airflow, so that the contact time and the contact area of the VOCs airflow and the plasma beam are increased, the plasma beam is utilized to the maximum extent, and further, the energy conservation, the consumption reduction and the cost saving can be realized.
5) Infrared absorbing particulate treatment
Heating the VOCs waste gas treated by the plasma treatment step by an infrared heating device 5, so that VOCs in the waste gas absorb infrared energy and further react with plasma remained in the gas flow, and are decomposed to form carbon dioxide and water; the infrared heating device 5 comprises an infrared emitter, a gas accommodating cavity 53 and infrared absorption particles 52 distributed in the gas accommodating cavity 53, wherein a plurality of upright posts 51 are arranged in the gas accommodating cavity 53, airflow is enabled to flow in a snake shape through the upright posts 51, and the infrared emitter outputs infrared light with the wavelength of 800 nm;
the final exhaust gas is discharged via a stack 6.
Meanwhile, the treatment method of the VOCs waste gas of the embodiment adopts the following treatment system for treatment:
the treatment system comprises a water curtain spray tower 1, an atomization spray tower 2, a gas-liquid separator 3, a plasma generation device 4 and an infrared heating device 5 which are sequentially connected and communicated;
the water curtain spray tower 1 comprises a plurality of spraying parts 11, and the plurality of spraying parts 11 are spirally distributed in the water curtain spray tower 1; the atomization spray tower 2 comprises an atomizer 21 and spray liquid, and the spray liquid forms film-shaped fogdrops layer by layer through the atomizer 21;
the plasma generating device 4 comprises a plasma generating electrode and a high-voltage power supply, the plasma generating electrode comprises a group of high-voltage electrodes 42 and a group of grounding electrodes 43, the high-voltage electrodes 42 and the grounding electrodes 43 are both coated with insulating media 41, and the high-voltage electrodes 42 and the grounding electrodes 43 are both arranged in a linear shape; the high-voltage electrode 42 is connected with the high-voltage power supply 46, and the high-voltage power supply 46 is one or a combination of a positive-polarity direct-current high-voltage power supply, a positive-polarity pulse high-voltage power supply or a positive-polarity direct-current superposed alternating-current high-voltage power supply;
the infrared heating device 5 comprises an infrared emitter (not shown), a gas containing cavity 53 and infrared absorption particles 52 distributed in the gas containing cavity 53, wherein a plurality of upright posts 51 are arranged in the gas containing cavity 53, the upright posts 51 enable airflow to flow in a snake shape, and the output wavelength of the infrared emitter is 800nm infrared light.
Further, the plasma generating device 4 further comprises a pressure sensor 45 and a temperature sensor 44, wherein the pressure sensor 45 and the temperature sensor 44 are used for monitoring the pressure and the temperature in the plasma generating device 4 in real time.
The whole set of VOCs waste gas treatment process is to initially capture large-particle dust by spraying water curtain; then, fine particles (paint particles, toluene, xylene and the like) in the waste gas are captured by water in a dust remover through a layer of water film formed by atomizing spray liquid in the atomizing spray tower 2 through the atomizer 21, pass through a water curtain and enter a gas-water channel, so that part of organic VOCs gas and particles after atomization and absorption enter a sewage system through spraying, and the VOCs removal efficiency can reach about 15 percent through the step; the temperature sensor 44 and the pressure sensor 45 are arranged to avoid explosion and explosion caused by safety accidents such as rapid increase of the concentration of VOCs in a short time caused by exhaust faults or other reasons; the gas-liquid separation treatment is used as a pretreatment process of the plasma treatment, so that most of water vapor and the like caused by spraying can be removed, and the plasma treatment efficiency is prevented from being influenced; the plasma technology and the infrared absorption particle technology decompose the residual VOCs gas molecules into CO2And H2The highest decomposition rate of total VOCs gas can reach more than 90 percent, and the tail gas has no peculiar smell or stink of the common treatment method.
The total removal rate of VOCs in the exhaust gas treated by the VOCs exhaust gas treatment method of the embodiment is 92%, wherein: carrying out ethanol distillation at a ratio of 8.5 mg/m; carrying out toluene cultivation at 23.0 mg/m; hexarene 50.2 mg/m.
From the above description, the beneficial effects of the present invention are: the removal rate of the VOCs waste gas can reach more than 90 percent at most, the problem that the existing waste gas treatment technology is difficult to meet the continuously improved emission standard requirement is solved, and the emission pollution of the VOCs waste gas to the environment is thoroughly eliminated; the whole treatment process is simple and easy to operate, the treatment efficiency is high, the required equipment is few, the energy consumption of the equipment is low, the requirements of modern enterprises on energy conservation and emission reduction and production benefit improvement are well met, and the method has great significance for saving resources and reducing cost.
Comparative example 1
The general process flow of the low-temperature plasma treatment technology is as follows: water curtain spray → low temperature plasma treatment → water spray → discharge
And (3) processing results: the total removal of VOCs was 50%, wherein in the exhaust gas: carrying out dry bulb harvest with the benzene content of 53.1 mg/m; carrying out high yield and high yield cultivation on the seeds with the toluene content of 143.3 mg/m; the xylene content was 313.8 mg/m.
Comparative example No. two
This example is substantially the same as example 1 except that the plasma treatment in this example employs low temperature plasma treatment and does not include infrared absorbing particulate treatment.
The process flow is as follows: water curtain spray → atomization spray → gas-liquid separation → low temperature plasma treatment → discharge
And (3) processing results: the total removal rate of VOCs in the waste gas is 60%, wherein: carrying out dry bulb harvest with the benzene content of 42.5 mg/m; carrying out high-yield high; the xylene content is 251.0 mg/m.
The above embodiments are merely illustrative of the technical concept and features of the present invention, and the purpose thereof is to enable those skilled in the art to understand the content of the present invention and implement the invention, and not to limit the scope of the invention, and all equivalent changes or modifications made according to the spirit of the present invention should be covered by the scope of the present invention.

Claims (6)

1. The VOCs waste gas treatment method is characterized by comprising the steps of water curtain spraying treatment, atomization spraying treatment, gas-liquid separation treatment, plasma treatment and infrared absorption particle treatment which are sequentially carried out;
in the atomization spraying treatment step, spraying liquid comprises water liquid, the water liquid is atomized through an atomizer to form a layer of water film, the water film is used for capturing fine particles in VOCs waste gas, and the fine particles comprise paint particles, toluene and xylene;
in the plasma treatment step, the gas is separated into gas and liquidThe VOCs waste gas treated in the separation treatment step passes through a plasma generating electrode of a plasma generating device along the direction parallel to the electric field of the plasma generating electrode, so that the VOCs waste gas generates plasma which is electrically neutral and comprises electrons, positive ions, neutral particles and free radicals; and charging the surface of dust particles in the VOCs exhaust gas; the plasma reacts with oxygen molecules and water molecules in the VOCs waste gas to generate H, O, OH and O with strong oxidizing property3The VOCs in the VOCs waste gas generate gaseous carbon dioxide and water under the action of the active particles;
in the infrared absorption particle treatment step, the VOCs waste gas treated in the plasma treatment step is heated by an infrared heating device, so that VOCs in the waste gas absorb infrared energy and further react with plasma remained in the gas flow, and are decomposed to form carbon dioxide and water; the infrared heating device comprises an infrared emitter, a gas containing cavity and infrared absorption particles distributed in the gas containing cavity, wherein a plurality of stand columns are arranged in the gas containing cavity, airflow is enabled to flow in a snake shape through the stand columns, and the infrared emitter outputs infrared light with the wavelength of 760 and 850 nm;
the total removal rate of VOCs in the waste gas treated by the VOCs waste gas treatment method is more than or equal to 75 percent, wherein: carrying out dry-mass cultivation on the seeds at a speed of less than or equal to 17 mg/m; carrying out Toluene cultivation at a speed of less than or equal to 60 mg/m; and (5) carrying out xylene up to 90 mg/m.
2. The method according to claim 1, wherein in the step of water curtain spraying treatment, the waste gas containing VOCs is introduced from the bottom of a water curtain spray tower and flows out from the top after being sprayed by the water curtain, and the water curtain spraying treatment is performed by annular spraying, wherein the annular spraying comprises a plurality of spraying parts, and the plurality of spraying parts are spirally distributed in the water curtain spray tower.
3. The method according to claim 1, wherein in the gas-liquid separation treatment step, mist and/or liquid droplets in the VOCs off-gas are removed by a gas-liquid separator that operates at normal temperature and pressure.
4. The method according to claim 1, wherein the plasma generating electrodes comprise a set of high voltage electrodes and a set of ground electrodes, the high voltage electrodes and the ground electrodes are both coated with an insulating medium, and the high voltage electrodes and the ground electrodes are both arranged in a linear manner; the high-voltage electrode is connected with a high-voltage power supply, and the high-voltage power supply is one or a combination of a positive polarity direct-current high-voltage power supply, a positive polarity pulse high-voltage power supply or a positive polarity direct-current superposed alternating-current high-voltage power supply.
5. A method for treating waste gases containing VOCs according to any of claims 1 to 4, wherein the method for treating waste gases containing VOCs uses the following treatment system:
the treatment system comprises a water curtain spray tower, an atomization spray tower, a gas-liquid separator, a plasma generation device and an infrared heating device which are sequentially connected and communicated;
the water curtain spray tower comprises a plurality of spraying parts, and the plurality of spraying parts are spirally distributed in the water curtain spray tower; the atomization spray tower comprises an atomizer and spray liquid, and the spray liquid forms layered film-shaped fog drops through the atomizer;
the plasma generating device comprises a plasma generating electrode and a high-voltage power supply, wherein the plasma generating electrode comprises a group of high-voltage electrodes and a group of grounding electrodes, the high-voltage electrodes and the grounding electrodes are both coated with insulating media, and the high-voltage electrodes and the grounding electrodes are both arranged in a linear mode; the high-voltage electrode is connected with the high-voltage power supply, and the high-voltage power supply is one or a combination of a positive polarity direct-current high-voltage power supply, a positive polarity pulse high-voltage power supply or a positive polarity direct-current superposed alternating-current high-voltage power supply;
the infrared heating device comprises an infrared emitter, a gas containing cavity and infrared absorption particles distributed on the inner wall of the gas containing cavity, wherein a plurality of stand columns are arranged in the gas containing cavity, airflow is enabled to flow in a snake shape through the stand columns, and the infrared emitter outputs infrared light with the wavelength of 760 and 850 nm.
6. A method as claimed in claim 5, wherein the plasma generator further comprises a pressure sensor and a temperature sensor, and the pressure sensor and the temperature sensor are used for monitoring the pressure and the temperature in the plasma generator in real time.
CN201710477947.5A 2017-06-21 2017-06-21 VOCs waste gas treatment method Active CN107297127B (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN202010520808.8A CN111659232B (en) 2017-06-21 2017-06-21 VOCs exhaust-gas treatment system
CN201710477947.5A CN107297127B (en) 2017-06-21 2017-06-21 VOCs waste gas treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710477947.5A CN107297127B (en) 2017-06-21 2017-06-21 VOCs waste gas treatment method

Related Child Applications (1)

Application Number Title Priority Date Filing Date
CN202010520808.8A Division CN111659232B (en) 2017-06-21 2017-06-21 VOCs exhaust-gas treatment system

Publications (2)

Publication Number Publication Date
CN107297127A CN107297127A (en) 2017-10-27
CN107297127B true CN107297127B (en) 2020-06-19

Family

ID=60135036

Family Applications (2)

Application Number Title Priority Date Filing Date
CN201710477947.5A Active CN107297127B (en) 2017-06-21 2017-06-21 VOCs waste gas treatment method
CN202010520808.8A Active CN111659232B (en) 2017-06-21 2017-06-21 VOCs exhaust-gas treatment system

Family Applications After (1)

Application Number Title Priority Date Filing Date
CN202010520808.8A Active CN111659232B (en) 2017-06-21 2017-06-21 VOCs exhaust-gas treatment system

Country Status (1)

Country Link
CN (2) CN107297127B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109045968A (en) * 2018-05-28 2018-12-21 四川锐源能环科技有限公司 A kind of ultra-clean processing technique equipment of volatile organic waste gas
CN111265990A (en) * 2020-03-27 2020-06-12 湖南京茂环保科技有限公司 Volatile organic compound exhaust treatment system
CN113144846A (en) * 2021-04-07 2021-07-23 扬州绿泉环保工程技术有限公司 VOCs incineration waste gas treatment device and treatment method

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104958990A (en) * 2015-07-13 2015-10-07 杭州科瑞特环境技术有限公司 Photoelectric integrated processing device and photoelectric integrated processing technique for waste gases generated by spraying paint
CN105396440A (en) * 2015-12-25 2016-03-16 浙江工商大学 Apparatus and method for heat corona discharge catalytic oxidation treatment of VOCs in industrial exhaust gas

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6534754B2 (en) * 1997-08-14 2003-03-18 Westinghouse Savannah River Company, L.L.C. Microwave off-gas treatment apparatus and process
WO2003047729A1 (en) * 2001-12-04 2003-06-12 Ebara Corporation Method and apparatus for treating exhaust gas
CN202315662U (en) * 2011-10-31 2012-07-11 上海凯展环保科技有限公司 Feed waste gas treatment device
CN104470181A (en) * 2014-12-29 2015-03-25 江苏康易达医疗科技有限公司 Absolutely airtight plasma surface treatment device
CN106310892B (en) * 2016-10-18 2019-04-09 浙江工业大学 A spraying waste gas treatment system and its application

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104958990A (en) * 2015-07-13 2015-10-07 杭州科瑞特环境技术有限公司 Photoelectric integrated processing device and photoelectric integrated processing technique for waste gases generated by spraying paint
CN105396440A (en) * 2015-12-25 2016-03-16 浙江工商大学 Apparatus and method for heat corona discharge catalytic oxidation treatment of VOCs in industrial exhaust gas

Also Published As

Publication number Publication date
CN111659232A (en) 2020-09-15
CN111659232B (en) 2022-05-06
CN107297127A (en) 2017-10-27

Similar Documents

Publication Publication Date Title
CN202398267U (en) Novel spray-painting waste gas treating device
CN105396440B (en) The device and method of thermoelectricity corona catalytic oxidation treatment industrial waste gas VOCs
CN105311931B (en) Industrial VOCs exhaust gas decomposing, purifying processing method and equipment
CN103055695A (en) Waste gas purification method and device
CN208066104U (en) A kind of chemical industry waste water station foul smell is collected and processing system
CN107297127B (en) VOCs waste gas treatment method
CN104028066A (en) Method and device for treating VOCs (Volatile Organic Chemicals) waste gas
CN107469506A (en) The method and device of low temperature plasma pyrolysis oxidization reactor for treatment foul waste gas
CN110624372A (en) A method for treating VOCs using low-temperature plasma jet
CN104923060B (en) VOCs removing method based on free radical advanced oxidation
CN105498476A (en) VOCs (volatile organic compounds) tail gas treatment technology and system
CN104857852B (en) VOCs removing method based on photocatalytic free radical advanced oxidation
CN205109351U (en) Stench waste gas treatment system
CN205717254U (en) The high-efficiency environment friendly exhaust gas processing device that a kind of chemical plant is special
CN204768126U (en) Charcoal kiln flue gas treatment system
CN107051195B (en) Organic waste gas partition oxidation cyclone purification method and device
CN206823546U (en) A kind of plasma-catalytic purification gas processing unit
CN210674748U (en) Purify organic waste gas's device in coordination
CN210473551U (en) VOC exhaust treatment device
CN104689692B (en) Device and method for treating waste gas by air plasma
CN204193765U (en) Organic exhaust gas Plasma burning cleaning equipment
CN202289838U (en) Tail gas treatment device for sebacic acid
CN207203847U (en) A kind of organic exhaust gas subregion aoxidizes rotating flow separators
CN212283463U (en) Oil chemical refining tail gas purification device
CN205549946U (en) Modular spraying exhaust gas purification system

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right

Effective date of registration: 20200528

Address after: 214437 floor 1-3, unit 2, building A3 and A4, No. 2, Dongsheng West Road, Jiangyin City, Wuxi City, Jiangsu Province

Applicant after: JIANGSU CHUNSHENTANG PHARMACEUTICAL Co.,Ltd.

Address before: Dongsheng Road, Jiangyin city 214400 Jiangsu city of Wuxi province A4-2 No. 2 unit on the first floor

Applicant before: JIANGSU KANGYIDA MEDICAL TECHNOLOGY Co.,Ltd.

TA01 Transfer of patent application right
GR01 Patent grant
GR01 Patent grant