CN102266699A - Method for treating flue gas of dyeing and finishing setting machine - Google Patents
Method for treating flue gas of dyeing and finishing setting machine Download PDFInfo
- Publication number
- CN102266699A CN102266699A CN2011102032056A CN201110203205A CN102266699A CN 102266699 A CN102266699 A CN 102266699A CN 2011102032056 A CN2011102032056 A CN 2011102032056A CN 201110203205 A CN201110203205 A CN 201110203205A CN 102266699 A CN102266699 A CN 102266699A
- Authority
- CN
- China
- Prior art keywords
- flue gas
- tower body
- washing unit
- heat exchanger
- unit
- 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.)
- Granted
Links
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 title claims abstract description 60
- 239000003546 flue gas Substances 0.000 title claims abstract description 59
- 238000004043 dyeing Methods 0.000 title claims abstract description 16
- 238000000034 method Methods 0.000 title claims abstract description 9
- 238000005406 washing Methods 0.000 claims abstract description 49
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 47
- 239000007788 liquid Substances 0.000 claims abstract description 17
- 238000005367 electrostatic precipitation Methods 0.000 claims description 38
- 239000007921 spray Substances 0.000 claims description 20
- 238000007789 sealing Methods 0.000 claims description 16
- 238000012856 packing Methods 0.000 claims description 14
- 238000013459 approach Methods 0.000 claims description 13
- 239000007789 gas Substances 0.000 claims description 13
- 238000003672 processing method Methods 0.000 claims description 12
- 238000012545 processing Methods 0.000 claims description 8
- 239000000428 dust Substances 0.000 claims description 6
- 238000010438 heat treatment Methods 0.000 claims description 6
- 239000004744 fabric Substances 0.000 claims description 5
- 239000002351 wastewater Substances 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 4
- 239000002699 waste material Substances 0.000 claims description 4
- 239000002245 particle Substances 0.000 abstract description 17
- 230000000694 effects Effects 0.000 abstract description 4
- 239000003517 fume Substances 0.000 abstract description 3
- 238000004140 cleaning Methods 0.000 abstract description 2
- 238000005507 spraying Methods 0.000 abstract 3
- 239000002918 waste heat Substances 0.000 abstract 1
- 239000000779 smoke Substances 0.000 description 8
- 238000009833 condensation Methods 0.000 description 4
- 230000005494 condensation Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000001914 filtration Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 239000004033 plastic Substances 0.000 description 4
- 230000007646 directional migration Effects 0.000 description 2
- 230000005686 electrostatic field Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 239000010865 sewage Substances 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 239000004753 textile Substances 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 238000009941 weaving Methods 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 239000000443 aerosol Substances 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000019504 cigarettes Nutrition 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 238000009940 knitting Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000035900 sweating Effects 0.000 description 1
Images
Landscapes
- Electrostatic Separation (AREA)
- Treating Waste Gases (AREA)
Abstract
The invention discloses a method for treating flue gas of a dyeing and finishing setting machine, wherein a heat exchanger, a washing unit, an oil-water separator and an electrostatic dedusting unit are disposed at the rear end of the setting machine. The method comprises the following steps: (1) performing counterflow heat exchanger of flue gas of the setting machine with air by the heat exchanger, recovering waste heat, which saves energy; (2) allowing the flue gas treated by the heat exchanger to enter from the bottom of the washing unit, spraying and washing the flue gas by spraying liquid in the washing unit, allowing the flue gas to counterflow-contact the spraying liquid so as to remove most of the oil fume particles with a particle size of above 1 micron; (3) performing dedusting treatment of the flue gas treated in the washing unit by the wet-type electrostatic dedusting unit, allowing most of the oil fume particles with a particle size of below 1 micron to be attached together by high-density electrons, allowing the charged particles to migrate directionally to a condensing tube wall and to be collected and captured by the tube wall, allowing the liquid film on the condensing tube inner wall to update continuously so as to realize the effect of self-cleaning of the condensing tube inner wall.
Description
The application is to be that February 25, application number in 2010 are 201010113417.0, denomination of invention is to the applying date: the dividing an application of a kind of processing method of flue gas of dyeing and finishing setter.
Technical field
The present invention relates to the processing method that a kind of industrial high temperature oil-containing contains wet flue gas, especially relate to a kind of processing method of flue gas of dyeing and finishing setter.
Background technology
Chemical fibre textile often needs to add multiple oiliness textile chemistry auxiliary agent in processes such as upstream system of knitting and dyeing, in the arrangement type-approval process of printing and dyeing mill, can produce a large amount of high temperature oil-containings and contain wet flue gas when forming machine heating, oven dry.
Usually, generally in 160-190 ℃ of scope, capacity is every forming machine 50-210 Nm to the temperature of forming machine flue gas
3/ min; Pollutant in the flue gas mainly contains the oil of weaving cotton cloth, spinning oil, Clean-organic solvent and the dyestuff and the dyeing assistant etc. of refining of upstream weaving.Particle concentration is at 70-230mg/m
3, wherein the concentration of toughness particle is at 25-120mg/m
3, particle diameter distributes mainly between 0.01-1
μBetween the m.
The forming machine flue gas shows as white or nattier blue smog, be mingled with stench and pungent smell, the atmospheric environment of plant area of severe contamination factory and periphery, billowing white cigarette not only has a strong impact on worker of enterprise and peripheral resident's normal life and healthy, especially under the low pressure weather condition, also can have influence on the traffic safety of enterprise's peripheral path.
Summary of the invention
Technical problem to be solved by this invention provides the processing method of the flue gas of dyeing and finishing setter of a kind of not only energy-conservation but also environmental protection.
The present invention solves the problems of the technologies described above the technical scheme that is adopted: a kind of processing method of flue gas of dyeing and finishing setter, the forming machine rear end is provided with heat exchanger, washing unit, oil water separator and electrostatic precipitation unit, described forming machine is communicated with the washing unit by heat exchanger, described washing unit is communicated with oil water separator, described washing unit is communicated with the electrostatic precipitation unit, and concrete steps comprise:
(1) flue gas that forming machine is discharged is input in the heat exchanger, the air inversion heat exchange of the flue gas and the heat exchanger of flowing through, air after the over-heat-exchanger heat exchange is input to the external heat device, and the typing that is input to forming machine by the air after the heating of external heat device again is indoor as drying medium;
(2) flue gas after the heat exchanger processing is input in the washing unit, spray liquid in the washing unit carries out spray washing to flue gas, flue gas and spray liquid counter current contacting, oil-polluted water after the washing is input to oil water separator, waste oil after the oil water separator processing is recycled, and the waste water after simultaneously oil water separator being handled is as spray liquid;
(3) will wash flue gas after the cell processing is input to the electrostatic precipitation unit and carries out dust removal process.
Described washing unit and described electrostatic precipitation unit branch are arranged.
Described washing unit and described electrostatic precipitation unit are wholely set.
Described washing unit comprises the washing tower body, the lower end of described washing tower body is provided with first gas approach and first blowdown outlet, the upper end of described washing tower body is provided with first exhaust outlet, be provided with shower and filter packing layer in the described washing tower body, described filter packing layer is positioned at the below of described shower, the top of described first gas approach is provided with baffle liner, and the end of described baffle liner is provided with the knuckle hypotenuse.
Described electrostatic precipitation unit comprises the electrostatic precipitation tower body, the upper end of described electrostatic precipitation tower body is provided with second exhaust outlet, the lower end of described electrostatic precipitation tower body is provided with second gas approach and second blowdown outlet, be set with sealing plate in the described electrostatic precipitation tower body, be provided with a plurality of condenser pipes in the described electrostatic precipitation tower body, described sealing plate is stretched out in the lower end of described condenser pipe, described electrostatic precipitation tower body is provided with water inlet, described water inlet is in the lower end part place of described condenser pipe, be inserted with electrode bar in the described condenser pipe, described electrode bar is fixedlyed connected with the electrode suppor that is installed in described condenser pipe top, and described electrode suppor is fixedlyed connected with described electrostatic precipitation tower body by insulated column.
Described electrostatic precipitation unit is arranged on the top of described washing unit, concrete structure is: comprise tower body, the lower end of described tower body is provided with gas approach and blowdown outlet, the upper end of described tower body is provided with exhaust outlet, be provided with shower and filter packing layer in the described tower body, described filter packing layer is positioned at the below of described shower, the top of described gas approach is provided with baffle liner, the end of described baffle liner is provided with the knuckle hypotenuse, be set with sealing plate in the described tower body, described sealing plate is arranged on the top of described shower, be provided with antispray layer between described sealing plate and the described shower, be provided with a plurality of condenser pipes in the described tower body, described sealing plate is stretched out in the lower end of described condenser pipe, described tower body is provided with water inlet, described water inlet is in the lower end part place of described condenser pipe, be inserted with electrode bar in the described condenser pipe, described electrode bar is fixedlyed connected with the electrode suppor that is installed in described condenser pipe top, and described electrode suppor is fixedlyed connected with described tower body by insulated column.
The upper end of described condenser pipe is set with jagged cloth water ring.Under the irregular situation in the upper end of condenser pipe, also can guarantee to form uniform moisture film after cooling water flows into the condenser pipe inwall.
The inwall of described condenser pipe is provided with at least one annular groove, makes the moisture film that flows in the condenser pipe through after the peptizaiton of annular groove, is evenly distributed in more on the condenser pipe inwall.
Described insulated column is provided with the anti-device that reveals, described anti-dew device comprises the antisweat covering that is set on the described insulated column, described antisweat covering is fixedly connected on the described electrostatic precipitation tower body, and described antisweat covering is provided with the warm-air pipe that is connected with heated air source.Around insulated column, be blown into hot blast, prevented that effectively steam and oil smoke etc. from causing the inefficacy of insulated column at the insulated column surface sweating, improved the service life and the result of use of insulated column.
Be provided with electrothermal tube in the described insulated column.Make the temperature of insulated column be higher than the flue gas dew point temperature, the anti-like this better effects if of revealing.
Compared with prior art, the invention has the advantages that the forming machine flue gas is after heat exchanger and air inversion heat exchange, the temperature of forming machine flue gas drops to 100～110 ℃ from original 160～190 ℃, air rises to 80～100 ℃ from normal temperature,, indoor as drying medium by the air after heating as the typing of steam or heat-conducting oil heating to 140～160 ℃ forming machine again through the external heat device; Used heat is reclaimed, saved the energy.
Flue gas can be removed wherein most of particle diameter 1 through the washing unit
μThe smoke particle that m is above, oil-polluted water is after water-oil separating, and the waste water after the separation can be used as spray liquid and recycles, and rationally utilizes waste water, has reduced the sewage quantity of decontaminated water treatment plant simultaneously.
Water capacity is discharged from the washing unit near saturated flue gas, upwards enters in the high-pressure electrostatic precipitation unit, and flue gas is cooled in pipe, heat is passed to cooling medium outside the pipe; Water vapour condensation in the flue gas becomes water smoke, under the high-voltage pulse electrostatic field, and major part 1 in the water smoke
μSmoke particle below the m is caught to condensation tube wall directional migration and by the tube wall collection by charged particle together by highdensity electron attachment.Liquid film on the condenser pipe inwall is brought in constant renewal in, and reaches the effect of cleaning the condenser pipe inwall voluntarily, and the mixed liquor of condensed water and oil smoke splashes into downwards in the saturated chilling spray scrubbing tower, becomes the part of spray liquid.Adopt above-mentioned tertiary treatment mode, reached the purpose that heat recovery, fume purifying and waste oil reclaim.
The high-temperature flue gas that contains humidity and particle dust enters into tower body from gas approach, run into the baffle liner on the tower body madial wall, flue gas is forced to be rotated, and makes the effect of the dust of larger particles because of inertia and deceleration, and quilt is thrown to the tower body inwall and is deposited to the bottom.
Shower on the filter packing layer sprays, form water curtain behind the water process filter packing layer, the dust of larger particles is melted in water, and high-temperature flue gas enters into the filter packing layer, carries out the gas-liquid exchange with water in the filter packing layer, in the gas-liquid exchange, can not only filter oil smoke and particle in the high-temperature flue gas, and high-temperature flue gas lowered the temperature, water is because of evaporating by heat, flue gas enters into spray district further cooling and purification
Be provided with the bolster bed of material on the top of shower, electrostatic field be short-circuited thereby big water droplet that produces when preventing to spray effectively or water column are flushed on the flue gas in the condenser pipe.The bolster bed of material also is one deck filter course, and the flue gas that the spray back produces filters once more, obtains than clean flue gas.
The electron attachment of the high-pressure electrostatic that the lower flue gas of relative temperature is produced by electrode bar is easily collected to condensation tube wall directional migration and by tube wall by charged particle and to be caught.The unpleasant material of stench during ozone that produces or the oxidation of plasma free radical energy remove smoke makes flue gas obtain advanced treating; Flue gas enters in the condenser pipe of high-pressure electrostatic, and tube wall makes the aerosol condensation owing to temperature is lower, drip to the bolster bed of material along tube wall, and the bottom that flow into tower body is again discharged by sewage outlet; Electrode suppor and insulated column are fixedly connected, and prevent the escape of static, and cleaned air passes discharges by exhaust outlet layer by layer.
Description of drawings
Fig. 1 is a FB(flow block) of the present invention;
Fig. 2 is the device connection diagram in the embodiment of the invention one;
Fig. 3 is the structure chart of electrostatic precipitation tower body in the embodiment of the invention one;
Fig. 4 is an A-A cutaway view among Fig. 3;
Fig. 5 is the structure chart of washing tower body in the embodiment of the invention one;
Fig. 6 is the formation schematic diagram of moisture film on the B place condenser pipe inwall among Fig. 3;
Fig. 7 is the expansion schematic diagram of cloth water ring in the embodiment of the invention one;
Fig. 8 is the device connection diagram in the embodiment of the invention two;
Fig. 9 is the housing structure figure among the embodiment two among the present invention.
The specific embodiment
Embodiment describes in further detail the present invention below in conjunction with accompanying drawing.
Embodiment one: as shown in Figure 1, a kind of processing method of flue gas of dyeing and finishing setter, the forming machine rear end is provided with heat exchanger 44, washing unit 46, oil water separator 45 and electrostatic precipitation unit 47, forming machine is communicated with washing unit 46 by heat exchanger 44, washing unit 46 is communicated with oil water separator 45, washing unit 46 is communicated with electrostatic precipitation unit 47, and concrete steps comprise:
(1) flue gas that forming machine is discharged is input in the heat exchanger 44, the air inversion heat exchange of the flue gas and the heat exchanger 44 of flowing through, air after over-heat-exchanger 44 heat exchange is input to the external heat device, and the typing that is input to forming machine by the air after the heating of external heat device again is indoor as drying medium;
(2) flue gas after heat exchanger 44 processing is input in the washing unit 46, spray liquid in the washing unit 46 carries out spray washing to flue gas, flue gas and spray liquid counter current contacting, oil-polluted water after the washing is input to oil water separator 45, waste oil after oil water separator 45 processing is recycled, and the waste water after oil water separator 45 is handled simultaneously is as spray liquid;
(3) will wash flue gas after unit 46 is handled is input to electrostatic precipitation unit 47 and carries out dust removal process.
In embodiment one, will wash unit 46 and electrostatic precipitation unit and be arranged in 47 minutes.
As Fig. 2, Fig. 3 and shown in Figure 4, electrostatic precipitation unit 47 comprises electrostatic precipitation tower body 8, the upper end of electrostatic precipitation tower body 8 is provided with second exhaust outlet 9, the lower end of electrostatic precipitation tower body 9 is provided with second gas approach 10 and second blowdown outlet 11, be set with sealing plate 12 in the electrostatic precipitation tower body 8, be provided with a plurality of condenser pipes 13 in the electrostatic precipitation tower body 8, sealing plate 12 is stretched out in the lower end of condenser pipe 13, electrostatic precipitation tower body 8 is provided with water inlet 14, water inlet 14 is in the lower end part place of condenser pipe 13, be inserted with electrode bar 15 in the condenser pipe 13, electrode bar 15 is fixedlyed connected with the electrode suppor 16 that is installed in condenser pipe 13 tops, and electrode suppor 16 is fixedlyed connected with electrostatic precipitation tower body 8 by insulated column 17.
As shown in Figure 5, washing unit 46 comprises washing tower body 1, the lower end of washing tower body 1 is provided with first gas approach 2 and first blowdown outlet 3, the upper end of washing tower body 1 is provided with first exhaust outlet, be provided with shower 4 and filter packing layer 5 in the washing tower body 1, filter packing layer 5 is positioned at the below of shower 4, and the top of first gas approach 2 is provided with baffle liner 6, and the end of baffle liner 6 is provided with knuckle hypotenuse 7.Filtering plastic layer 5 is arranged on the filtering plastic layer support 51.Shower is provided with a plurality of spray heads 41.
The upper end of condenser pipe 13 is set with jagged cloth water ring 19.
Embodiment two: as Fig. 8 and shown in Figure 9, other parts are identical with embodiment one, and its difference is that electrostatic precipitation unit 47 and washing unit 46 are wholely set composition wet static dedusting tower body 43.
The electrostatic precipitation unit is arranged on the top of washing unit, concrete structure is: comprise tower body 23, the lower end of tower body 23 is provided with gas approach 24 and blowdown outlet 25, the upper end of tower body 23 is provided with exhaust outlet 26, be provided with shower 27 and filter packing layer 28 in the tower body 23, filtering plastic layer 28 is arranged on the filtering plastic layer support 37, filter packing layer 28 is positioned at the below of shower 27, the top of gas approach 24 is provided with baffle liner 29, the end of baffle liner 29 is provided with knuckle hypotenuse 30, be set with sealing plate 31 in the tower body 23, sealing plate 31 is arranged on the top of shower 27, be provided with antispray layer 32 between sealing plate 31 and the shower 27, be provided with a plurality of condenser pipes 33 in the tower body 23, sealing plate 31 is stretched out in the lower end of condenser pipe 33, condenser pipe 33 inwall be provided with at least one annular groove 42, tower body 23 is provided with water inlet 34, water inlet 34 is in the lower end part place of condenser pipe 33, be inserted with electrode bar 34 in the condenser pipe 33, electrode bar 34 is fixedlyed connected with the electrode suppor 35 that is installed in condenser pipe 33 tops, electrode suppor 35 is fixedlyed connected with tower body 23 by insulated column 36, is provided with electrothermal tube (figure does not show) in the insulated column.
Claims (5)
1. the processing method of a flue gas of dyeing and finishing setter, it is characterized in that the forming machine rear end is provided with heat exchanger, washing unit, oil water separator and electrostatic precipitation unit, described forming machine is communicated with the washing unit by heat exchanger, described washing unit is communicated with oil water separator, described washing unit is communicated with the electrostatic precipitation unit, and concrete steps comprise:
(1) flue gas that forming machine is discharged is input in the heat exchanger, the air inversion heat exchange of the flue gas and the heat exchanger of flowing through, air after the over-heat-exchanger heat exchange is input to the external heat device, and the typing that is input to forming machine by the air after the heating of external heat device again is indoor as drying medium;
(2) flue gas after the heat exchanger processing is input in the washing unit, spray liquid in the washing unit carries out spray washing to flue gas, flue gas and spray liquid counter current contacting, oil-polluted water after the washing is input to oil water separator, waste oil after the oil water separator processing is recycled, and the waste water after simultaneously oil water separator being handled is as spray liquid;
(3) will wash flue gas after the cell processing is input to the electrostatic precipitation unit and carries out dust removal process;
Described washing unit and described electrostatic precipitation unit are wholely set;
Described electrostatic precipitation unit is arranged on the top of described washing unit, concrete structure is: comprise tower body, the lower end of described tower body is provided with gas approach and blowdown outlet, the upper end of described tower body is provided with exhaust outlet, be provided with shower and filter packing layer in the described tower body, described filter packing layer is positioned at the below of described shower, the top of described gas approach is provided with baffle liner, the end of described baffle liner is provided with the knuckle hypotenuse, be set with sealing plate in the described tower body, described sealing plate is arranged on the top of described shower, be provided with antispray layer between described sealing plate and the described shower, be provided with a plurality of condenser pipes in the described tower body, described sealing plate is stretched out in the lower end of described condenser pipe, described tower body is provided with water inlet, described water inlet is in the lower end part place of described condenser pipe, be inserted with electrode bar in the described condenser pipe, described electrode bar is fixedlyed connected with the electrode suppor that is installed in described condenser pipe top, and described electrode suppor is fixedlyed connected with described tower body by insulated column.
2. the processing method of a kind of flue gas of dyeing and finishing setter according to claim 1 is characterized in that the upper end of described condenser pipe is set with jagged cloth water ring.
3. the processing method of a kind of flue gas of dyeing and finishing setter according to claim 1 is characterized in that the inwall of described condenser pipe is provided with at least one annular groove.
4. the processing method of a kind of flue gas of dyeing and finishing setter according to claim 1, it is characterized in that described insulated column is provided with the anti-device that reveals, described anti-dew device comprises the antisweat covering that is set on the described insulated column, described antisweat covering is fixedly connected on the described electrostatic precipitation tower body, and described antisweat covering is provided with the warm-air pipe that is connected with heated air source.
5. the processing method of a kind of flue gas of dyeing and finishing setter according to claim 1 is characterized in that being provided with electrothermal tube in the described insulated column.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110203205.6A CN102266699B (en) | 2010-02-25 | 2010-02-25 | Method for treating flue gas of dyeing and finishing setting machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201110203205.6A CN102266699B (en) | 2010-02-25 | 2010-02-25 | Method for treating flue gas of dyeing and finishing setting machine |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010101134170A Division CN101766943B (en) | 2010-02-25 | 2010-02-25 | Method for treating flue gas of dyeing and finishing setter |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102266699A true CN102266699A (en) | 2011-12-07 |
| CN102266699B CN102266699B (en) | 2014-03-05 |
Family
ID=45049270
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201110203205.6A Expired - Fee Related CN102266699B (en) | 2010-02-25 | 2010-02-25 | Method for treating flue gas of dyeing and finishing setting machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102266699B (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103394254A (en) * | 2013-07-01 | 2013-11-20 | 李川凌 | Physical purification device for boarding machine oil smoke |
| CN103463907A (en) * | 2013-08-20 | 2013-12-25 | 灵璧鸿峰科技环保设备有限责任公司 | Waste gas purifier |
| CN105854579A (en) * | 2016-05-10 | 2016-08-17 | 湖州荣大环境科技有限公司 | Flue gas treatment technology and flue gas treatment equipment for textile printing and dyeing setter |
| CN105944555A (en) * | 2016-05-10 | 2016-09-21 | 湖州荣大环境科技有限公司 | Flue gas treatment device of printing and dyeing setting machine |
| CN107185339A (en) * | 2017-06-02 | 2017-09-22 | 江阴市红柳被单厂有限公司 | Sizing oil smoke high-efficient treatment device and processing method that a kind of antistatic is produced |
| CN113532142A (en) * | 2021-05-06 | 2021-10-22 | 广东晟远新能源科技有限公司 | Bleaching and dyeing industry cloth forming machine smoke temperature purification and latent heat and sensible heat recovery system thereof |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4305909A (en) * | 1979-10-17 | 1981-12-15 | Peabody Process Systems, Inc. | Integrated flue gas processing system |
| CN1142784A (en) * | 1994-01-03 | 1997-02-12 | 孟山都公司 | Apparatus and method for controlling pollution |
| CN201231119Y (en) * | 2008-07-21 | 2009-05-06 | 尤今 | Vertical electrostatic type fume purification device |
-
2010
- 2010-02-25 CN CN201110203205.6A patent/CN102266699B/en not_active Expired - Fee Related
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4305909A (en) * | 1979-10-17 | 1981-12-15 | Peabody Process Systems, Inc. | Integrated flue gas processing system |
| CN1142784A (en) * | 1994-01-03 | 1997-02-12 | 孟山都公司 | Apparatus and method for controlling pollution |
| CN201231119Y (en) * | 2008-07-21 | 2009-05-06 | 尤今 | Vertical electrostatic type fume purification device |
Non-Patent Citations (1)
| Title |
|---|
| 姜辉: "喷淋-冷凝式静电除尘净化定型机废气的研究", 《中国优秀硕士学位论文全文数据库 工程科技I辑》 * |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103394254A (en) * | 2013-07-01 | 2013-11-20 | 李川凌 | Physical purification device for boarding machine oil smoke |
| CN103463907A (en) * | 2013-08-20 | 2013-12-25 | 灵璧鸿峰科技环保设备有限责任公司 | Waste gas purifier |
| CN105854579A (en) * | 2016-05-10 | 2016-08-17 | 湖州荣大环境科技有限公司 | Flue gas treatment technology and flue gas treatment equipment for textile printing and dyeing setter |
| CN105944555A (en) * | 2016-05-10 | 2016-09-21 | 湖州荣大环境科技有限公司 | Flue gas treatment device of printing and dyeing setting machine |
| CN107185339A (en) * | 2017-06-02 | 2017-09-22 | 江阴市红柳被单厂有限公司 | Sizing oil smoke high-efficient treatment device and processing method that a kind of antistatic is produced |
| CN113532142A (en) * | 2021-05-06 | 2021-10-22 | 广东晟远新能源科技有限公司 | Bleaching and dyeing industry cloth forming machine smoke temperature purification and latent heat and sensible heat recovery system thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102266699B (en) | 2014-03-05 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101766943B (en) | Method for treating flue gas of dyeing and finishing setter | |
| KR101854113B1 (en) | High-viscosity contaminants processing method of tenter rear of dyeing industry using washing/dust collector, dehumidifying/heating and electric precipitator | |
| CN102266699B (en) | Method for treating flue gas of dyeing and finishing setting machine | |
| US4284609A (en) | Condensation cleaning of particulate laden gases | |
| KR102175549B1 (en) | Multi-stage exhaust gas treatment process system having means to reduce odor, white smoke in exhaust gas after tenter and means for recovery of highly viscous pollutants | |
| US4028072A (en) | Apparatus for scrubbing of hydrocarbons from gas | |
| CN109647114B (en) | Flue gas treatment system and process for high-polymer waterproof coiled material production line | |
| CN101280497B (en) | Environment-protecting technology and device for reclaiming and purifying waste heat of dying setting machine | |
| CN202401267U (en) | System for utilizing flue gas waste heat of setting machine and conducting wet type electrostatic process on flue gas of setting machine | |
| CN105854486A (en) | Waste heat recycling type waste gas treating device for setting machine | |
| WO2013060244A1 (en) | Active coke regeneration mixed vapor treatment method and apparatus | |
| KR102171442B1 (en) | High-viscosity contaminants processing method of tenter rear of dyeing industry using heat recovery of exhaust gas | |
| CN110215791A (en) | A kind of textile printing and dyeing industry waste gas treatment equipment | |
| CN203791337U (en) | Organic contaminated soil thermal desorption system without generating secondary pollution to environment | |
| CN106669353A (en) | Waste gas treatment process for printing-dyeing process | |
| CN108568186A (en) | A kind of high temperature fume purification device | |
| CN102872671A (en) | Asphalt waste gas purifying method and device | |
| CN107008098A (en) | Eliminate the device and removing method of fuel boiler flue gas hangover | |
| CN111632460A (en) | Water-saving forming machine exhaust treatment system | |
| CN201493167U (en) | Wet-type electrostatic dust collector for high-temperature flammable waste gas treatment | |
| CN107854946A (en) | A kind of aerosol particle substance treating method and its aerosol particle thing processing equipment | |
| CN104668090B (en) | Two-region wet electrostatic cooking fume remover | |
| CN214270654U (en) | Sludge drying device with spray dust removal function | |
| CN208493681U (en) | A kind of high temperature fume purification device | |
| CN109173664A (en) | Setting machine waste gas purification processing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140305 |