CN107671107A - One kind paint slag desiccation thermal oxide system - Google Patents

One kind paint slag desiccation thermal oxide system Download PDF

Info

Publication number
CN107671107A
CN107671107A CN201711013913.7A CN201711013913A CN107671107A CN 107671107 A CN107671107 A CN 107671107A CN 201711013913 A CN201711013913 A CN 201711013913A CN 107671107 A CN107671107 A CN 107671107A
Authority
CN
China
Prior art keywords
slag
paint
cylinder
desiccation
paint slag
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
Application number
CN201711013913.7A
Other languages
Chinese (zh)
Other versions
CN107671107B (en
Inventor
何群伟
李良城
王彩珍
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.)
Suzhou Krantz Environment Technology Co Ltd
Original Assignee
Suzhou Krantz Environment Technology 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 Suzhou Krantz Environment Technology Co Ltd filed Critical Suzhou Krantz Environment Technology Co Ltd
Priority to CN201711013913.7A priority Critical patent/CN107671107B/en
Publication of CN107671107A publication Critical patent/CN107671107A/en
Application granted granted Critical
Publication of CN107671107B publication Critical patent/CN107671107B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B11/00Machines or apparatus for drying solid materials or objects with movement which is non-progressive
    • F26B11/12Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices
    • F26B11/16Machines or apparatus for drying solid materials or objects with movement which is non-progressive in stationary drums or other mainly-closed receptacles with moving stirring devices the stirring device moving in a vertical or steeply-inclined plane
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F26DRYING
    • F26BDRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
    • F26B25/00Details of general application not covered by group F26B21/00 or F26B23/00
    • F26B25/04Agitating, stirring, or scraping devices
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Abstract

The present invention discloses a kind of paint slag desiccation thermal oxide system, and it includes painting slag bath, paint pulp pump, paint slag filter press, paint residue crusher structure, desiccation oxygenation machanism, waste gas dedusting mechanism and paint slag finished product recovering mechanism;The discharging opening for painting slag bath paints the charging aperture of slag filter press, slag notch connection paint residue crusher structure by painting pulp pump connection;Paint the slag notch connection desiccation oxygenation machanism of residue crusher structure;Desiccation oxygenation machanism includes drying oxidation cylinder, and the cylinder of dry oxidation cylinder is provided with bypasses interface for the heat of external thermal source, and agitator is provided with cylinder;Dry oxidation cylinder the paint slag in cylinder is dried and aoxidized, the exhaust gas transmission obtained after oxidation will be dried to waste gas dedusting mechanism, paint slag is transmitted to paint slag finished product recovering mechanism;Waste gas dedusting mechanism to waste gas be filtrated to get remaining paint slag and transmitted to paint slag finished product recovering mechanism, and the waste gas after filtering is discharged by gas outlet.Desiccation thermal oxidation can be carried out to paint slag, improve resolution process efficiency, reduce the generation of noxious material, reduce carbon emission amount using the present invention.

Description

One kind paint slag desiccation thermal oxide system
Technical field
The present invention relates to paint Slag treatment technical field, particularly a kind of paint slag desiccation thermal oxide system.
Background technology
Automotive paints and its waste residue are mainly made up of 4 kinds of resin, pigment, solvent and additive bases.Resin is oil The film forming matter of paint, it is divided into natural resin and Albertol, natural resin is mainly made up of the secretion of insect or trees, mainly Composition is rosin and shellac;Albertol's main component is acrylic resin, alkyd resin, melamine, NC Nitroncellulose, poly- Urethane resin, epoxy resin etc..Pigment is divided into inorganic pigment and organic pigment according to composition, and inorganic pigment is typically gloomy face Color, main component are metal oxides such as titanium dioxide, iron oxide red etc.;Organic pigment is typically bright color, mainly into It is benzimidazolone, heterocyclic ketone such as permanent yellow, permanent violet etc. to divide.Solvent is generally aliphatic hydrocarbon, fragrance of the boiling point below 250 DEG C Hydrocarbon(Benzene class), alcohol ethers and esters.
Prior art typically carries out desiccation using the means directly burned to paint slag, but the characteristic for painting slag is very viscous, and There is a special gluing phase stage in the drying process(Moisture content is 40%-60%), in this extremely narrow changeover portion, paint slag pole Easily caking, surface is hard, is difficult to crush, and the inside is still sposh shape, therefore desiccation degree is not high, and in paint slag burning process In, the noxious materials such as bioxin can be also produced, do not meet the requirement of national low-carbon environment-friendly.
RTO (Regenerative Thermal Oxidizer, abbreviation RTO), heat accumulating type oxidation furnace.
The content of the invention
It is an object of the invention to provide one kind to paint slag desiccation thermal oxide system and method, can carry out the hot oxygen of desiccation to paint slag Change is handled, and improves resolution process efficiency, reduces the generation of noxious material, reduces carbon emission amount.
The technical scheme that the present invention takes is specially:One kind paint slag desiccation thermal oxide system, including paint slag bath, paint pulp pump, Paint slag filter press, paint residue crusher structure, desiccation oxygenation machanism, waste gas dedusting mechanism and paint slag finished product recovering mechanism;
Paint slag filter press includes charging aperture, delivery port and slag notch, paints the discharging opening of slag bath by painting pulp pump connection paint slag press filtration The charging aperture of machine;Paint the slag notch connection paint residue crusher structure of slag filter press;
Paint residue crusher structure crushes to paint slag, its slag notch connection desiccation oxygenation machanism;
Desiccation oxygenation machanism includes drying oxidation cylinder, and drying oxidation cylinder includes cylinder, and cylinder is provided with charging aperture, discharging opening, use In the gas outlet of discharge waste gas, and the heat bypass interface for external thermal source, cylinder is interior to be provided with agitator;Oxidation cylinder is dried to cylinder Interior paint slag is dried and aoxidized, and will dry the waste gas obtained after oxidation by outlet port transmission to waste gas dedusting mechanism, will Dry the paint slag obtained after oxidation and slag finished product recovering mechanism is extremely painted by the port transmission that discharges;
Waste gas dedusting mechanism includes air inlet, gas outlet and slag notch;Waste gas dedusting mechanism to the waste gas being passed through filter Slag is painted to remnants, remnants paint slags are arranged by slagging tap port transmission to slag finished product recovering mechanism, the waste gas after filtering is painted by gas outlet Go out.
In use, drying oxidation cylinder can be dried and aoxidize to the paint slag after crushing, oxidation reaction can disappear the present invention The materials such as organic matter and carbon in paint removal slag.The contacting efficiency of paint slag and hot blast can be increased by drying the agitator in oxidation cylinder, from And improve and dry oxidation efficiency.
Further, present invention additionally comprises heat accumulating type oxidation furnace, the gas outlet of waste gas dedusting mechanism is connected by blower fan to be stored The air inlet of hot type oxidation furnace, the heat bypass interface of the gas outlet connection desiccation oxygenation machanism of heat accumulating type oxidation furnace.Can be by system The waste gas containing heat after middle processing is passed through in super drying machine, and realization recycles.
Preferably, the desiccation oxygenation machanism also includes charging basket and helical feed passage, and agitator, spiral are provided with charging basket Helical feed roller is provided with transfer passage;Charging basket is connected by helical feed passage dries oxidation cylinder.With will be from disintegrating mechanism The paint slag of acquisition, which is delivered to, to be dried in oxidation cylinder.Charging basket can be carried out to the endlessly paint slag obtained from paint residue crusher structure Stirring, paint slag in charging basket is promoted to enter in helical feed passage, while spiral shell in stirring in charging basket and helical feed passage The rotation of rotation conveying roller can also continue to play pulverization to paint slag, reduce paint slag particle footpath, improve contact effect of the paint slag with hot blast Rate.
Preferably, in desiccation oxygenation machanism, the cylinder for drying oxidation cylinder is rotatable cylinder, and the agitator in cylinder includes Both ends are respectively facing the rotating shaft of charging aperture and discharging opening, and the stirring vane that spiral is set around the shaft.At work, agitator Rotated simultaneously with cylinder, crushing further can be stirred to paint slag, while make it that contact of the hot blast with painting slag is more abundant, oxidation Reaction efficiency is higher.The agitator of spiral roller type can transport the paint slag in cylinder to discharging opening when rotating.
Disintegrating mechanism and desiccation thermal oxide mechanism in the present invention can use super drying machine, and super drying machine is existing production Product, crushing, stirring mechanism is provided with it, and rotatable cylinder itself also has the function of broken stirring.
Preferably, the delivery port connection paint slag bath of slag filter press is painted.Water can be achieved in paint slag bath between paint slag filter press Recycle.Mixing of the water with painting slag may be such that paint slag transmits more easily by paint pulp pump in pipeline.
Preferably, paint slag filter press uses plate and frame type filter-press.Plate and frame type filter-press is existing product, and it can enter to paint slag Row press filtration, to filter out moisture in paint slag etc..
Preferably, waste gas dedusting mechanism uses cyclone dust collectors, and it is existing product, can carry out dust removal process to waste gas.
It can be the existing device for being used to paint slag recovery that the present invention, which paints slag finished product recovering mechanism, by desiccation oxygenation machanism and give up The paint slag flowed out in gas dedusting mechanism can be entered in paint slag recovering mechanism by same transfer passage carries out packing and binding transport etc. Follow-up work, transfer passage can equally use helical feed form.
Beneficial effect
Compared with prior art, the present invention has advantages below and progress:
1)The setting of disintegrating mechanism can overcome the adhesion problem of paint slag, and the paint ground-slag in gluing phase stage is broken into little particle, improve Follow-up drying oxidation efficiency;
2)Paint slag can be dried and oxidation reaction for the setting of desiccation oxygenation machanism, except the moisture in coating removal slag, organic matter and Carbon, during do not produce the toxic gases such as bioxin, can reduce paint Slag treatment final carbon emission amount;
3)It is dry to common revolution to may be such that overall heat-transfer coefficient improves to compound for the cylinder and agitator rotated in desiccation oxygenation machanism 2 ~ 3 times of dry machine(Ua=200~600W/m2K);
4)Energy consumption is saved, economic value added is high:Material after crushed, adds its area contacted with hot blast so that hot blast obtains Utilized to sufficient, and exhaustion hot wind recycles, and can greatly reduce energy consumption;The paint residue product dried after oxidation is particle diameter For 1-5mm particle, and calorific value is high, if by working process, can be used as fuel;
5)The composition mechanism of present system it is simple, it is necessary to detection parts it is few, be easy to maintaining.
Brief description of the drawings
Fig. 1 show present system structural representation;
1- paints slag bath, 2- paint pulp pumps, 3- paint slag press filtrations pond, 4- paint residue crusher structures, 5- desiccation oxygenation machanisms, 51- charging baskets, 511- Charging basket agitator, 52- spiral conveying mechanisms, 53- heat bypass interfaces, 54- dry oxidation cylinder cylinder, 55- stirring vanes, and 56- turns Axle, 6- waste gas dedustings mechanism, 7- blower fans, 8- paint slag recovering mechanisms.
Embodiment
Further described below in conjunction with the drawings and specific embodiments.
With reference to figure 1, paint slag desiccation thermal oxide system of the invention, including paint slag bath 1, paint pulp pump, paint slag filter press 3, paint Residue crusher structure 4, desiccation oxygenation machanism 5, waste gas dedusting mechanism 6 and paint slag finished product recovering mechanism 8;
Paint slag filter press 3 includes charging aperture, delivery port and slag notch, paints the discharging opening of slag bath 1 by painting the connection paint slag pressure of pulp pump 2 The charging aperture of filter 3;Paint the slag notch connection paint residue crusher structure 4 of slag filter press 3;
Paint residue crusher structure 4 crushes to paint slag, its slag notch connection desiccation oxygenation machanism 5;
Desiccation oxygenation machanism 5 includes drying oxidation cylinder, and drying oxidation cylinder includes cylinder 54, and cylinder 54 is provided with charging aperture, discharging Mouth, the gas outlet for discharging waste gas, and the heat bypass interface 53 for external thermal source, cylinder 54 is interior to be provided with agitator;Dry Oxidation cylinder is dried and aoxidized to the paint slag in cylinder, and the waste gas obtained after dry aoxidize is removed by outlet port transmission to waste gas Dirt mechanism 6, the paint slag obtained after dry aoxidize is passed through into the port transmission that discharges and extremely paints slag finished product recovering mechanism 8;
Waste gas dedusting mechanism 6 includes air inlet, gas outlet and slag notch;Waste gas dedusting mechanism 6 filters to the waste gas being passed through Remaining paint slag is obtained, for remnants paint slags by port transmission of slagging tap to slag finished product recovering mechanism 8 is painted, the waste gas after filtering passes through gas outlet Discharge.
In use, drying oxidation cylinder can be dried and aoxidize to the paint slag after crushing, oxidation reaction can disappear the present invention The materials such as organic matter and carbon in paint removal slag.The contacting efficiency of paint slag and hot blast can be increased by drying the agitator in oxidation cylinder, from And improve and dry oxidation efficiency.
Embodiment
With reference to figure 1, the present embodiment includes paint slag bath 1, paint pulp pump, paint slag filter press 3, paint residue crusher structure 4, desiccation oxidation Mechanism 5, waste gas dedusting mechanism 6 and paint slag finished product recovering mechanism 8;Also include heat accumulating type oxidation furnace RTO, waste gas dedusting mechanism goes out Gas port connects the air inlet of heat accumulating type oxidation furnace by blower fan 7, the gas outlet connection desiccation oxygenation machanism of heat accumulating type oxidation furnace Heat bypass interface 53.The waste gas containing heat after being handled in system can be passed through in super drying machine, realization recycles.
Paint the delivery port connection paint slag bath of slag filter press.Water can be achieved in paint slag bath to the circulation profit between paint slag filter press With.Mixing of the water with painting slag may be such that paint slag transmits more easily by paint pulp pump in pipeline.
Desiccation oxygenation machanism also includes charging basket 51 and helical feed passage 52, and 51 are provided with agitator 511, spiral transferring in charging basket Send in passage 52 and be provided with helical feed roller;Charging basket 51 is connected by helical feed passage 52 dries oxidation cylinder.With will be from pulverizer The paint slag obtained in structure, which is delivered to, to be dried in oxidation cylinder.Charging basket 51 can be to the endlessly paint that obtains from paint residue crusher structure Slag is stirred, and promotes the paint slag in charging basket 51 to enter in helical feed passage 52, while the stirring in charging basket and spiral transferring Send the rotation of passage inside spin conveying roller to can also continue to play pulverization to paint slag, reduce paint slag particle footpath, improve paint slag and heat The contacting efficiency of wind.
In desiccation oxygenation machanism, the cylinder 54 for drying oxidation cylinder is rotatable cylinder, and the agitator in cylinder includes both ends It is respectively facing the rotating shaft 56 of charging aperture and discharging opening, and the stirring vane 55 that 56 spirals are set around the shaft.At work, stir Device rotates simultaneously with cylinder 54, further can be stirred crushing to paint slag, while make it that contact of the hot blast with painting slag is more abundant, Efficiency is higher.The agitator of spiral roller type can transport the paint slag in cylinder to discharging opening when rotating.
Disintegrating mechanism and desiccation thermal oxide mechanism can use super drying machine, and super drying machine is existing product, set in it Crushing, stirring mechanism is put, rotatable cylinder itself also has the function of broken stirring, can be by gluing shape thing and block etc. Material is crushed, disperseed, and increases hot blast contacting efficiency with this, and cylinder is so as to ensureing to obtain greater homogeneity in a short time(Grain Footpath is 1-5mm)Drying finished product.After paint slag material enters charging basket, preliminary stirring is carried out by the agitator in charging basket and crushed, then Conveyed by helical feed passage, material can be crushed again during conveying, and then is put into and is dried oxidation cylinder Cylinder in carry out intense agitation crush.Moved drying the circulation rotating that material starts from cylinder body bottom to top in oxidation cylinder Make, material is dropped from top due to Action of Gravity Field during rotation, and the stirring vane rotated at a high speed is ground into tiny Particle, this do action are carried out continuously always, until material is discharged outside stove.
The paint slag filter press 3 of the present embodiment uses plate and frame type filter-press.Plate and frame type filter-press is existing product, and it can be to paint Slag carries out press filtration, to filter out moisture in paint slag etc..Waste gas dedusting mechanism 7 uses cyclone dust collectors, and it is existing product, can be right Waste gas carries out dust removal process.
Present invention paint slag finished product recovering mechanism 8 can be the existing device for being used to paint slag recovery, by desiccation oxygenation machanism and The paint slag flowed out in waste gas dedusting mechanism can be entered in paint slag recovering mechanism by same transfer passage carries out packing and binding transport Deng follow-up work, transfer passage can equally use helical feed form.
The paint slag desiccation oxidative system of the present embodiment, workflow are:
1. the paint slag in paint slag bath is sent into plate and frame type filter-press with water by painting pulp pump;
2. entering disintegrating mechanism by funnel type discharge gate by forming paint clinker after press filtration, paint the water after being filtered in clinker and enter Enter to paint slag bath recycling;
3. disintegrating mechanism smashes the charging basket into desiccation oxygenation machanism by clinker is painted;
Dried 4. the broken paint slag in charging basket is transported to by helical feed passage in oxidation cylinder, dry the heat bypass interface of oxidation cylinder 850 DEG C or so of the hot-air discharged through RTO is passed through, heating carbonization is carried out to paint slag;
The following process such as packing and binding transport are carried out 5. drying the paint slag finished product after oxidation and entering paint slag recovering mechanism;
6. drying the waste gas in oxidation cylinder enters cyclone dust collectors, deduster filters the remaining tiny paint slag in waste gas, waste gas Enter RTO by blower fan to handle to discharge 850 DEG C or so of hot-air.
Compared with prior art, the present invention has advantages below and progress:
1)The setting of disintegrating mechanism can overcome the adhesion problem of paint slag, and the paint ground-slag in gluing phase stage is broken into little particle, improve Follow-up drying oxidation efficiency;
2)Paint slag can be dried and oxidation reaction for the setting of desiccation oxygenation machanism, except the moisture in coating removal slag, organic matter and Carbon, during do not produce the toxic gases such as bioxin, can reduce paint Slag treatment final carbon emission amount;
3)It is dry to common revolution to may be such that overall heat-transfer coefficient improves to compound for the cylinder and agitator rotated in desiccation oxygenation machanism 2 ~ 3 times of dry machine(Ua=200~600W/m2K);
4)Energy consumption is saved, economic value added is high:Material after crushed, adds its area contacted with hot blast so that hot blast obtains Utilized to sufficient, and exhaustion hot wind recycles, and can greatly reduce energy consumption;The paint residue product dried after oxidation is particle diameter For 1-5mm particle, and calorific value is high, if by working process, can be used as fuel;
5)The composition mechanism of present system it is simple, it is necessary to detection parts it is few, be easy to maintaining.
Described above is only the preferred embodiment of the present invention, it is noted that for the ordinary skill people of the art For member, without departing from the technical principles of the invention, some improvement and deformation can also be made, these are improved and deformation Also it should be regarded as protection scope of the present invention.

Claims (7)

1. one kind paint slag desiccation thermal oxide system, it is characterized in that, including paint slag bath, paint pulp pump, paint slag filter press, paint residue crusher Structure, desiccation oxygenation machanism, waste gas dedusting mechanism and paint slag finished product recovering mechanism;
Paint slag filter press includes charging aperture, delivery port and slag notch, paints the discharging opening of slag bath by painting pulp pump connection paint slag press filtration The charging aperture of machine;Paint the slag notch connection paint residue crusher structure of slag filter press;
Paint residue crusher structure crushes to paint slag, its slag notch connection desiccation oxygenation machanism;
Desiccation oxygenation machanism includes drying oxidation cylinder, and drying oxidation cylinder includes cylinder, and cylinder is provided with charging aperture, discharging opening, use In the gas outlet of discharge waste gas, and the heat bypass interface for external thermal source, cylinder is interior to be provided with agitator;Oxidation cylinder is dried to cylinder Interior paint slag is dried and aoxidized, and will dry the waste gas obtained after oxidation by outlet port transmission to waste gas dedusting mechanism, will Dry the paint slag obtained after oxidation and slag finished product recovering mechanism is extremely painted by the port transmission that discharges;
Waste gas dedusting mechanism includes air inlet, gas outlet and slag notch;Waste gas dedusting mechanism to the waste gas being passed through filter Slag is painted to remnants, remnants paint slags are arranged by slagging tap port transmission to slag finished product recovering mechanism, the waste gas after filtering is painted by gas outlet Go out.
2. paint slag desiccation thermal oxide system according to claim 1, it is characterized in that, in addition to heat accumulating type oxidation furnace, waste gas The gas outlet of dedusting mechanism connects the air inlet of heat accumulating type oxidation furnace, the gas outlet connection desiccation of heat accumulating type oxidation furnace by blower fan The heat bypass interface of oxygenation machanism.
3. paint slag desiccation thermal oxide system according to claim 1, it is characterized in that, the desiccation oxygenation machanism also includes material Bucket and helical feed passage, charging basket is interior to be provided with agitator, and helical feed roller is provided with helical feed passage;Charging basket passes through spiral transferring Passage connection is sent to dry oxidation cylinder.
4. paint slag desiccation thermal oxide system according to claim 1, it is characterized in that, in desiccation oxygenation machanism, dry oxidation The cylinder of cylinder be rotatable cylinder, and the agitator in cylinder is respectively facing the rotating shaft of charging aperture and discharging opening including both ends, and The stirring vane that spiral is set around the shaft.
5. paint slag desiccation thermal oxide system according to claim 1, it is characterized in that, the delivery port connection paint of paint slag filter press Slag bath.
6. paint slag desiccation thermal oxide system according to claim 1, it is characterized in that, paint slag filter press uses plate and frame press filtration Machine.
7. paint slag desiccation thermal oxide system according to claim 1, it is characterized in that, waste gas dedusting mechanism uses cyclone dust removal Device.
CN201711013913.7A 2017-10-26 2017-10-26 Paint slag drying thermal oxidation system Active CN107671107B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711013913.7A CN107671107B (en) 2017-10-26 2017-10-26 Paint slag drying thermal oxidation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711013913.7A CN107671107B (en) 2017-10-26 2017-10-26 Paint slag drying thermal oxidation system

Publications (2)

Publication Number Publication Date
CN107671107A true CN107671107A (en) 2018-02-09
CN107671107B CN107671107B (en) 2023-05-02

Family

ID=61142867

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711013913.7A Active CN107671107B (en) 2017-10-26 2017-10-26 Paint slag drying thermal oxidation system

Country Status (1)

Country Link
CN (1) CN107671107B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108889760A (en) * 2018-05-09 2018-11-27 陈善堂 A kind of regeneration device and application method of Oil Paint Slag
CN112676313A (en) * 2020-12-23 2021-04-20 东莞市慧江平成机械有限公司 Paint slag recycling equipment and recycling method thereof
WO2021138933A1 (en) * 2020-01-06 2021-07-15 杰瑞环保科技有限公司 Comprehensive treatment device for waste paint slag
CN115164511A (en) * 2022-07-05 2022-10-11 广东工业大学 Paint slag drying method, system and control method thereof

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09220553A (en) * 1996-02-16 1997-08-26 Toyota Motor Corp Method for treating paint refuse and apparatus therefor
US20030062431A1 (en) * 2001-10-02 2003-04-03 Kuniya Sonehara Process for reusing waste paint and processor therefor
CN101544406A (en) * 2009-05-05 2009-09-30 宁波科博特钴镍有限公司 Method for producing red iron oxide pigment
CN101664752A (en) * 2009-09-24 2010-03-10 浙江林学院 Method of recovering inorganic pigment from decorative paper factory waste residue
CN102580389A (en) * 2012-02-23 2012-07-18 北京水泥厂有限责任公司 Method for processing paint slag muck by separating slag muck from water
CN203830391U (en) * 2014-05-17 2014-09-17 郑州宇通环保科技有限公司 Paint slag processing device
CN104140837A (en) * 2013-05-10 2014-11-12 中冶焦耐(大连)工程技术有限公司 Thermal conduction molded coal moisturizing method with coke oven tail gas as carrying gas, and apparatus thereof
CN205133940U (en) * 2015-11-24 2016-04-06 长春市旭远机械制造有限公司 Crowded wetting system of lacquer sediment
CN105776277A (en) * 2014-12-24 2016-07-20 重庆蓝洁广顺净水材料有限公司 An environmental-friendly clean reaction device for producing solid polyaluminium chloride
CN105776279A (en) * 2014-12-24 2016-07-20 重庆蓝洁广顺净水材料有限公司 Environmental-friendly clean production line for solid polyaluminium chloride
CN205505661U (en) * 2016-03-03 2016-08-24 张崇祥 Auger formula wringing machine for coating
CN206269150U (en) * 2016-12-15 2017-06-20 苏州克兰茨环境科技有限公司 A kind of emission-control equipment based on RTO
CN207533664U (en) * 2017-10-26 2018-06-26 苏州克兰茨环境科技有限公司 A kind of paint slag desiccation thermal oxide system

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09220553A (en) * 1996-02-16 1997-08-26 Toyota Motor Corp Method for treating paint refuse and apparatus therefor
US20030062431A1 (en) * 2001-10-02 2003-04-03 Kuniya Sonehara Process for reusing waste paint and processor therefor
CN101544406A (en) * 2009-05-05 2009-09-30 宁波科博特钴镍有限公司 Method for producing red iron oxide pigment
CN101664752A (en) * 2009-09-24 2010-03-10 浙江林学院 Method of recovering inorganic pigment from decorative paper factory waste residue
CN102580389A (en) * 2012-02-23 2012-07-18 北京水泥厂有限责任公司 Method for processing paint slag muck by separating slag muck from water
CN104140837A (en) * 2013-05-10 2014-11-12 中冶焦耐(大连)工程技术有限公司 Thermal conduction molded coal moisturizing method with coke oven tail gas as carrying gas, and apparatus thereof
CN203830391U (en) * 2014-05-17 2014-09-17 郑州宇通环保科技有限公司 Paint slag processing device
CN105776277A (en) * 2014-12-24 2016-07-20 重庆蓝洁广顺净水材料有限公司 An environmental-friendly clean reaction device for producing solid polyaluminium chloride
CN105776279A (en) * 2014-12-24 2016-07-20 重庆蓝洁广顺净水材料有限公司 Environmental-friendly clean production line for solid polyaluminium chloride
CN205133940U (en) * 2015-11-24 2016-04-06 长春市旭远机械制造有限公司 Crowded wetting system of lacquer sediment
CN205505661U (en) * 2016-03-03 2016-08-24 张崇祥 Auger formula wringing machine for coating
CN206269150U (en) * 2016-12-15 2017-06-20 苏州克兰茨环境科技有限公司 A kind of emission-control equipment based on RTO
CN207533664U (en) * 2017-10-26 2018-06-26 苏州克兰茨环境科技有限公司 A kind of paint slag desiccation thermal oxide system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108889760A (en) * 2018-05-09 2018-11-27 陈善堂 A kind of regeneration device and application method of Oil Paint Slag
WO2021138933A1 (en) * 2020-01-06 2021-07-15 杰瑞环保科技有限公司 Comprehensive treatment device for waste paint slag
CN112676313A (en) * 2020-12-23 2021-04-20 东莞市慧江平成机械有限公司 Paint slag recycling equipment and recycling method thereof
CN112676313B (en) * 2020-12-23 2022-05-17 东莞市慧江平成机械有限公司 Paint slag recycling equipment and recycling method thereof
CN115164511A (en) * 2022-07-05 2022-10-11 广东工业大学 Paint slag drying method, system and control method thereof
CN115164511B (en) * 2022-07-05 2023-12-22 广东工业大学 Paint slag drying method, paint slag drying system and control method of paint slag drying system

Also Published As

Publication number Publication date
CN107671107B (en) 2023-05-02

Similar Documents

Publication Publication Date Title
CN107671107A (en) One kind paint slag desiccation thermal oxide system
CN110624647A (en) Method for preparing Chinese medicinal material extract at initial processing stage of Chinese medicinal material producing area
CN206399103U (en) A kind of coal slime drying system
CN210486365U (en) System for drying iron phosphate by using waste heat of roasting furnace
CN207533664U (en) A kind of paint slag desiccation thermal oxide system
TW201200241A (en) Method for comminution of mill feed
CN208829530U (en) A kind of three energy-efficient rotary drying equipments
CN205300185U (en) Thermal balance formula drying -machine
CN215711825U (en) Nano zinc oxide apparatus for producing based on resource utilization
CN102351398B (en) Combined linkage type rotor wing forced fluidized sludge drying machine
CN104693845A (en) High-toluene-light transmittance pigment carbon black subjected to oxidation treatment and production technique thereof
CN209077416U (en) Paint slag recycling system device
CN206959616U (en) A kind of novel frit kiln water quenching processing unit
CN206018654U (en) A kind of thoroughly Disposal System of Mud Burning that burns
CN110183122B (en) System and method for preparing cementing material based on industrial waste heat cooperative disposal of solid waste
CN210394281U (en) Coal industry processing apparatus that gives up admittedly
CN209680262U (en) Crushing and dry dual-purpose integrated machine and its automated production equipment
CN207430886U (en) A kind of soil repair system
CN206955899U (en) A kind of frit water quenching processing unit using fused block furnace residual heat drying frit
CN206604572U (en) A kind of direct draught abraum salt drying and crushing device and system
CN109266845A (en) A kind of production of zinc calcine and smoke processing system and method
CN214039309U (en) Filter cake drying system of high wet phosphate
CN113860356A (en) Resource utilization-based nano zinc oxide production device and method
CN209397135U (en) Sludge prepares production line as the haydite of fuel
CN1587060A (en) Method for producing zinc suboxide

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
GR01 Patent grant
GR01 Patent grant