CN110237638A - A kind of textile printing and dyeing industry emission control technology - Google Patents
A kind of textile printing and dyeing industry emission control technology Download PDFInfo
- Publication number
- CN110237638A CN110237638A CN201910601128.6A CN201910601128A CN110237638A CN 110237638 A CN110237638 A CN 110237638A CN 201910601128 A CN201910601128 A CN 201910601128A CN 110237638 A CN110237638 A CN 110237638A
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- exhaust gas
- emission control
- textile printing
- control technology
- dyeing industry
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/26—Drying gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation 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
- B01D53/32—Separation 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
- B01D53/323—Separation 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 by electrostatic effects or by high-voltage electric fields
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C3/00—Separating dispersed particles from gases or vapour, e.g. air, by electrostatic effect
- B03C3/017—Combinations of electrostatic separation with other processes, not otherwise provided for
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses a kind of textile printing and dyeing industry emission control technologies, include the following steps, exhaust gas carries out secondary filter;Filtered exhaust gas is cooled down twice;Exhaust gas after cooling carries out processing sedimentation to oil smoke therein, residual particles and wax by mixed cyclonic form;Electrostatic Absorption is carried out to oil smoke and residual particles again by high voltage power supply;By handle except water droplet processing and demisting to exhaust gas except liquid case;Bi-medium to block deodorizing process is carried out to exhaust gas;Exhaust gas after deodorization handle except white vapour;Cleaning gas discharge.The present invention is by secondary filter, reducing temperature twice, the removal of impurities of mixed stream, Electrostatic Absorption, water removal demisting, deodorization and removes white vapour multiple working procedure to printing and dyeing exhaust gas progress purified treatment, a variety of dopants such as large particulate matter, finely ground particle substance, wax and oil smoke in exhaust gas can be removed one by one, purify wide coverage, clean-up effect is excellent, it can accomplish resource recycling simultaneously, reduce entreprise cost.
Description
Technical field
The present invention relates to waste gas pollution control and treatment technical field more particularly to a kind of textile printing and dyeing industry emission control technologies.
Background technique
Printing and dyeing are also referred to as dyeing and finishing, and printing and dyeing are a kind of processing method and pre-treatment, dyeing, stamp, final finishing and wash water
Etc. processes general name, printing and dyeing each processing link in can generate a large amount of exhaust gas mostly, without processing direct emission can make
At serious environmental pollution, exhaust gas is generally passed through into electric field by existing exhaust-gas treatment mode, under electric field action, exhaust gas point
Son is in excitation state, and when the energy that emission molecule obtains is greater than the combination energy of its molecular bond energy, the molecular link of emission molecule is disconnected
It splits, a large amount of OH, the O etc. for directly resolving into simple substance atom or being obtained innocuous gas molecule by single atomic building, while being generated
Living radical and the extremely strong O of oxidisability3, can be chemically reacted with pernicious gas molecule, generate harmless products, but it is handled
Subject matter is limited, can not carry out all standing, pollutant can not be handled completely in exhaust gas, and pollutant process is incomplete, and being not achieved has
The requirement of machine waste gas emission standard.
Meanwhile it also will cause the waste of resource and the energy in waste gas treatment process, such as in preceding processing link, fabric needs
Gas steaming and drying are carried out by high temperature, the temperature in local environment is different and different according to fabric, ranges up to up to 200 DEG C of left sides
The right side, existing printing and dyeing emission-control equipment can not fast and effectively reduce exhaust gas temperature and recycle the energy, operation and maintenance cost
It is higher, increase business burden.
Summary of the invention
The purpose of the present invention is to provide a kind of textile printing and dyeing industry emission control technologies, pass through secondary filter, secondary drop
Temperature, the removal of impurities of mixed stream, Electrostatic Absorption, water removal demisting, deodorization and except white vapour multiple working procedure to printing and dyeing exhaust gas carry out purified treatment, can
To be removed one by one to a variety of dopants such as large particulate matter, finely ground particle substance, wax and oil smoke in exhaust gas, purification covering
Range is wide, and clean-up effect is excellent.
In order to achieve the above objectives, the technical solution adopted by the present invention is that: a kind of textile printing and dyeing industry emission control technology, packet
Include following steps,
S1) exhaust gas carries out secondary filter;
S2) filtered exhaust gas is cooled down twice;
S3 the exhaust gas after) cooling down carries out processing to oil smoke therein, residual particles and wax by mixed cyclonic form and sinks
Drop;
S4 Electrostatic Absorption) is carried out to oil smoke and residual particles again by high voltage power supply;
S5) by handle except water droplet processing and demisting to exhaust gas except liquid case;
S6 bi-medium to block deodorizing process) is carried out to exhaust gas;
S7) exhaust gas after deodorization handle except white vapour;
S8) cleaning gas discharges.
As further optimization, S1) in secondary filter include primary filter and secondary filter, primary filter is in exhaust gas
Large particle, hair ball and batting large particulate matter be filtered;Secondary filter is to the tiny batting in exhaust gas after primary filter
Finely ground particle substance is filtered.
As further optimization, S2) in reducing temperature twice include primary temperature reducing and secondary cooling, primary temperature reducing is useless to high temperature
Gas is cooled down by the heat exchange of high temperature air water;Secondary cooling carries out again the exhaust gas after primary temperature reducing by the heat exchange of low temperature air water
Cooling.
As further optimization, the high-temperature water generated to primary temperature reducing is recycled;The cleaning that secondary cooling is generated
Hot water carries out Treated sewage reusing.
As further optimization, S7) in except the processing of white vapour includes level-one high temperature except white vapour and second steam remove white vapour.
As further optimization, level-one high temperature is heated except white vapour using the high-temperature water that primary temperature reducing generates;Second level
Steam is heated except white vapour using enterprise's overbottom pressure steam.
As further optimization, level-one high temperature removes the water at low temperature conveying generated after white vapour for primary temperature reducing.
As further optimization, S3) in exhaust gas and mixed flowing liquid carry out gas-liquid emulsion reaction, pass through what rotation generated
Centrifugal force carries out gas-liquid separation, adsorbs pernicious gas by shower spray of solvent, by removing water drop except water layer, demisting, removing solvent.
As further optimization, exhaust gas is tangentially mixed with mixed flowing liquid.
As further optimization, intake air temperature and exhaust ports discharge at air inlet are monitored by monitoring device
The smell of gas.
Compared with prior art, the invention has the benefit that
1. by secondary filter, reducing temperature twice, the removal of impurities of mixed stream, Electrostatic Absorption, water removal demisting, deodorization and removing white vapour multiple tracks
Process carries out purified treatment to printing and dyeing exhaust gas, can be more to large particulate matter, finely ground particle substance, wax and oil smoke in exhaust gas etc.
Kind dopant is removed one by one, purifies wide coverage, and clean-up effect is excellent, accomplishes that colorless and odorless discharges;
2. recycling water resource and thermal resource by measures such as Treated sewage reusing, recyclings, energy-saving and emission-reduction reduce enterprise
Resources costs.
Detailed description of the invention
Fig. 1 is process route chart of the invention.
Specific embodiment
The following is specific embodiments of the present invention, and technical scheme of the present invention will be further described, but the present invention is simultaneously
It is not limited to these embodiments.
A kind of textile printing and dyeing industry emission control technology, includes the following steps,
S1 the intake air temperature at air inlet) is monitored by monitoring device, secondary filter is carried out to exhaust gas, secondary filter includes
Primary filter and secondary filter, primary filter is filtered large particle, hair ball and the batting large particulate matter in exhaust gas, secondary
Grade filtering is filtered the tiny batting finely ground particle substance in exhaust gas after primary filter;
S2) filtered exhaust gas is cooled down twice, and reducing temperature twice includes primary temperature reducing and secondary cooling, primary temperature reducing pair
High-temp waste gas by high temperature air water heat exchange cools down, secondary cooling to the exhaust gas after primary temperature reducing by low temperature air water exchange heat into
Row cools down again, and the high-temperature water generated to primary temperature reducing recycles;Water returns in the clear hot-water progress generated to secondary cooling
With;
S3 the exhaust gas after) cooling down carries out processing to oil smoke therein, residual particles and wax by mixed cyclonic form and sinks
Drop, exhaust gas tangentially mix laggard promoting the circulation of qi liquid emulsion reaction with mixed flowing liquid, carry out gas-liquid by the centrifugal force that rotation generates
Separation adsorbs pernicious gas by shower spray of solvent, by removing water drop except water layer, demisting, removing solvent, after filtering and cooling
Exhaust gas enters mixed stream tower, and exhaust gas enters high speed mixed stream track-type facilities under the action of blower tractive force, and exhaust gas is in centrifugal force
Under the action of carry out gas-liquid emulsion reaction, under the high speed rotation state of mixed flow liquid, exhaust gas and rotating liquid are sufficiently mixed suction
Receipts, which mix, increases flue dust specific gravity, reaches gas-liquid separation using the designed centrifugal force of mixed swirl-flow devices, and the gas after separation enters
Equal wind adsorption layer is moved since air-flow tangentially enters equipment in lateral circumferential, and avoiding mixed stream class equipment longitudinal movement causes
The phenomenon of the failure of equal stratification of wind blocking, then in turn through spiral nozzle and solid-cone vortex nozzle, the correspondence solvent of ejection is uniform
It is distributed on equal stratification of wind, due to the rational design of equal stratification of wind, exhaust gas has sufficient gas-liquid to mix to react with reaction solution on its surface
Time removes water droplet water mist except water layer using bilayer to greatest extent, this mixed stream tower to oil smoke, particulate matter, wax pre- place
It is ideal to manage effect;
S4 Electrostatic Absorption) is carried out to oil smoke and residual particles again by high voltage power supply, using vertical pipe type Electrostatic Absorption
Tower, it is internal to be designed for circular pipe type, Proper Match high-frequency and high-voltage power supply, it can be achieved that oil smoke and particulate matter efficient absorption, bottom
Steam cleaner is configured, top configures water washing device, and the two is cleaned automatically simultaneously, and cleaning effect is stablized, can be long-term
Keep stable adsorption efficiency.
S5) by aluminum profile except liquid case handle except water droplet processing and demisting to exhaust gas;
S6 bi-medium to block deodorizing process) is carried out to exhaust gas;
S7) exhaust gas after deodorization handle except white vapour, including level-one high temperature removes white vapour except white vapour and second steam, one
Grade high temperature is heated using the high-temperature water that primary temperature reducing generates except white vapour, second steam except white vapour use enterprise's overbottom pressure steam into
Row heating, level-one high temperature remove the water at low temperature conveying generated after white vapour for primary temperature reducing, realize the comprehensive utilization of the energy, energy conservation and
Environmental protection combines, before the high-temperature water of high temperature air water heat exchange be sent to end and carry out level-one high temperature except white vapour, to purified low
Warm exhaust gas carries out preheating except white vapour, carries out second steam in the overbottom pressure steam by enterprise and removes white vapour, thoroughly the row's of elimination spoken parts in an opera
Row mouthful " visual pollution " problem of color steam, realizes " colorless and odorless " minimum discharge;
S8) cleaning gas discharges, and the smell of exhaust ports discharge gas is monitored by monitoring device, according to practical exceeded model
It encloses and carries out pre-alarm and shutdown, to guarantee treatment effect.
Specific embodiment described herein is only an example for the spirit of the invention.The neck of technology belonging to the present invention
The technical staff in domain can make various modifications or additions to the described embodiments or replace by a similar method
In generation, however, it does not deviate from the spirit of the invention or beyond the scope of the appended claims.
Claims (10)
1. a kind of textile printing and dyeing industry emission control technology, which is characterized in that include the following steps,
S1) exhaust gas carries out secondary filter;
S2) filtered exhaust gas is cooled down twice;
S3 the exhaust gas after) cooling down carries out processing sedimentation to oil smoke therein, residual particles and wax by mixed cyclonic form;
S4 Electrostatic Absorption) is carried out to oil smoke and residual particles again by high voltage power supply;
S5) by handle except water droplet processing and demisting to exhaust gas except liquid case;
S6 bi-medium to block deodorizing process) is carried out to exhaust gas;
S7) exhaust gas after deodorization handle except white vapour;
S8) cleaning gas discharges.
2. textile printing and dyeing industry emission control technology according to claim 1, which is characterized in that S1) in secondary filter packet
Primary filter and secondary filter are included, primary filter is filtered large particle, hair ball and the batting large particulate matter in exhaust gas;
Secondary filter is filtered the tiny batting finely ground particle substance in exhaust gas after primary filter.
3. textile printing and dyeing industry emission control technology according to claim 1, which is characterized in that S2) in reducing temperature twice packet
Primary temperature reducing and secondary cooling are included, primary temperature reducing cools down to high-temp waste gas by the heat exchange of high temperature air water;Secondary cooling is to first
Exhaust gas after grade cooling is cooled down again by the heat exchange of low temperature air water.
4. textile printing and dyeing industry emission control technology according to claim 3, which is characterized in that generated to primary temperature reducing
High-temperature water is recycled;The clear hot-water generated to secondary cooling carries out Treated sewage reusing.
5. textile printing and dyeing industry emission control technology according to claim 4, which is characterized in that S7) in except white vapour handle
Including level-one high temperature except white vapour and second steam remove white vapour.
6. textile printing and dyeing industry emission control technology according to claim 5, which is characterized in that level-one high temperature makes except white vapour
It is heated with the high-temperature water that primary temperature reducing generates;Second steam is heated except white vapour using enterprise's overbottom pressure steam.
7. textile printing and dyeing industry emission control technology according to claim 6, which is characterized in that after level-one high temperature removes white vapour
The water at low temperature conveying of generation is used for primary temperature reducing.
8. textile printing and dyeing industry emission control technology according to claim 1, which is characterized in that S3) in exhaust gas and mixed
Flowing liquid carries out gas-liquid emulsion reaction, carries out gas-liquid separation by the centrifugal force that rotation generates, adsorbs by shower spray of solvent harmful
Gas, by removing water drop except water layer, demisting, removing solvent.
9. textile printing and dyeing industry emission control technology according to claim 1, which is characterized in that exhaust gas tangentially with mixed
Flowing liquid mixing.
10. textile printing and dyeing industry emission control technology according to claim 1, which is characterized in that supervised by monitoring device
Survey the smell of the intake air temperature and exhaust ports discharge gas at air inlet.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110215791A (en) * | 2019-07-04 | 2019-09-10 | 苏州思诚者信息科技有限公司 | A kind of textile printing and dyeing industry waste gas treatment equipment |
CN112221288A (en) * | 2020-09-23 | 2021-01-15 | 莱美科技股份有限公司 | Waste gas low temperature removes white peculiar smell system that removes |
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CN104096434A (en) * | 2013-04-03 | 2014-10-15 | 厦门大学 | Novel technology and novel device for dedusting and desulphurization of flue gas |
CN109225633A (en) * | 2018-11-22 | 2019-01-18 | 苏州敬天爱人环境科技有限公司 | A kind of atmosphere pollution Processing tecchnics |
CN109225634A (en) * | 2018-11-22 | 2019-01-18 | 苏州敬天爱人环境科技有限公司 | A kind of dying setting machine waste gas treatment equipment |
CN109745843A (en) * | 2019-03-01 | 2019-05-14 | 沈中增 | A kind of textile printing and dyeing waste gas processing method |
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Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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CN2356735Y (en) * | 1998-06-30 | 2000-01-05 | 北京市清新高科技开发公司 | Pneumatic emulsifying filter |
CN104096434A (en) * | 2013-04-03 | 2014-10-15 | 厦门大学 | Novel technology and novel device for dedusting and desulphurization of flue gas |
CN109225633A (en) * | 2018-11-22 | 2019-01-18 | 苏州敬天爱人环境科技有限公司 | A kind of atmosphere pollution Processing tecchnics |
CN109225634A (en) * | 2018-11-22 | 2019-01-18 | 苏州敬天爱人环境科技有限公司 | A kind of dying setting machine waste gas treatment equipment |
CN109745843A (en) * | 2019-03-01 | 2019-05-14 | 沈中增 | A kind of textile printing and dyeing waste gas processing method |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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CN110215791A (en) * | 2019-07-04 | 2019-09-10 | 苏州思诚者信息科技有限公司 | A kind of textile printing and dyeing industry waste gas treatment equipment |
CN112221288A (en) * | 2020-09-23 | 2021-01-15 | 莱美科技股份有限公司 | Waste gas low temperature removes white peculiar smell system that removes |
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Application publication date: 20190917 |