CN202220201U - On-line water circulating and purifying device used in surface treatment process of fluorine-free, ammonia-free and four-in-one aluminum profile - Google Patents

On-line water circulating and purifying device used in surface treatment process of fluorine-free, ammonia-free and four-in-one aluminum profile Download PDF

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CN202220201U
CN202220201U CN2011203199517U CN201120319951U CN202220201U CN 202220201 U CN202220201 U CN 202220201U CN 2011203199517 U CN2011203199517 U CN 2011203199517U CN 201120319951 U CN201120319951 U CN 201120319951U CN 202220201 U CN202220201 U CN 202220201U
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free
clearing machine
surface treatment
ammonia
tank
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曹健
林洁丽
潘荣章
周开颜
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Abstract

The utility model discloses an on-line water circulating and purifying device used in the surface treatment process of a fluorine-free, ammonia-free and four-in-one aluminum profile, which comprises an alkali bath solution purifying machine, an oxidation bath solution purifying machine, a coloring bath solution purifying machine and a hole sealing bath solution purifying machine, wherein the flow of the alkali bath solution purifying machine and the flow the coloring bath solution purifying machine comprise a microfiltration membrane separation phase, a water drainage phase, a back flushing and deslagging phase and a back washing and regeneration phase; the flow of the oxidation bath solution purifying machine and the flow of the hole sealing bath solution purifying machine comprise a microfiltration membrane separation phase, a water drainage phase and a back washing and regeneration phase; and all the phases are controlled by a circuit and a programme. In the on-line water circulating and purifying device, the microfiltration membrane separation technology is first used in the surface treatment of the fluorine-free, ammonia-free and four-in-one aluminum profile, the scheme of purifying and circulating rinsing baths in all the phases in surface treatment process of the aluminum profile is proposed, and the recycling and the comprehensive utilization of drags are realized without using a flocculating agent, therefore, the water resources are reserved, the cost of the surface treatment of the aluminum profile is reduced, and the zero waste-water emission in the surface treatment of the fluorine-free, ammonia-free and four-in-one aluminum profile is realized.

Description

A kind of do not have the online water cycle refining plant that uses in the ammonia four unification aluminium shape surface treatment process in free-floride
Technical field
The utility model belongs to the environmental technology field in floride-free the no ammonia four unification aluminium shape surface treatment process, and more specifically relating to does not a kind ofly have ammonia four in free-floride and unify the online water cycle refining plant that uses in the aluminium shape surface treatment process.
Background technology
Surface treatment be utilize physics, chemistry, perhaps additive method, the one deck that forms in the metallic surface has certain thickness, is different from body material and the tectum of certain reinforcement, protection or specific function is arranged.Process of surface treatment comprises matrix pre-treatment, coating prepn, three parts of coating aftertreatment.The master operation that typical aluminium shape surface is handled comprises chemical rightenning, oil removing, alkali erosion, pickling, neutralization, oxidation, sealing of hole, painted, passivation etc.In each operation, all use various soda acids to make surperficial treatment solution; Because the viscosity of various treatment solutions and physicochemical property are different; Aluminium shape surface can be handled the thick liquid membrane of taking different amounts the tank liquor out of from these viscosity; Need a large amount of clear water to clean and remove these liquid films, handle aluminium per ton and consume 25~30 cubic metres of water approximately, the water after cleaning becomes the main waste water that aluminium shape surface is handled.The aluminium shape surface treatment process is traditional is divided into alkali etching technique and acid etching technology, no matter which kind of mode, each road technology that aluminium shape surface is handled includes handles and clean, and produces a large amount of Cleaning Wastewater and dense waste liquid.Present aluminium section bar manufacturing enterprise more than 90% adopts fluorine-containing technology that aluminium shape surface is handled, and produces waste water containing fluorine, because the chemical agent that each operation is added in chemical liquid groove is different, and the composition more complicated of pollutent.The major pollution thing comprises fluorion, ammonia nitrogen, COD, sexavalent chrome, organism, sulfate radical, phosphate radical etc. in the aluminium factory effluent; Know according to preceding surface analysis: even discharge by the secondary discharge standard of requirement at present; Still can cause certain pollution to water body, failing qualified discharge then endangers bigger.China has become the big producing country of world aluminum section bar through the great development of two more than ten years, and aluminium section bar output was sure to occupy the No. 1 in the world in continuous 5 years.Present national aluminium shape surface is handled annual 9200000 tons, and Guangdong Province's yearly capacity is above more than 200 ten thousand tons.Aluminium per ton consumes 15~40 kilograms of aluminium through surface treatment, produces 150~400 kilograms of waste slag of aluminum simultaneously.Calculate with this, national annual waste residue amount 138~3,680,000 tons be equivalent to several large-scale aluminium ores, and the bauxite resource of China is poor, is again simultaneously that aluminium consumes big country.Therefore should only not be conceived to how to handle making its emission standard that reaches regulation in China's Study on wastewater that processing is discharged to aluminium shape surface, more should pay attention to cycling utilization of wastewater research and waste reside comprehensive utilization.The waste residue combination treatment of at present many aluminium section bar manufacturing enterprises is stacked and is unfavorable for very much waste reside comprehensive utilization.
Tradition acid etching and alkali etching technique, water quality is good inadequately after treatment for the waste water of each operation discharging, causes the water of ability reuse less, and most of directly outwards discharging not only causes water pollution but also waste great amount of water resources.The viewpoint that floride-free no ammonia four unifications in 2010 are handled is suggested, and its advantage is: the first pair of waste water carries out filter operation (through the scum silica frost filter bag is set) thereby the cyclically utilizing water displacement of trying one's best is few; Second adopts and to add the flocculation agent mode waste residue is dewatered, but adds the performance that flocculation agent itself can destroy tank liquor, and making it not only can not reuse be to make that waste residue can not the efficient resource utilization on the contrary, and to the extra difficulty of waste residue dehydration generation.This new aluminium shape surface treatment process still has discharge of wastewater, also wastes resource.
In sum, China is as aluminium section bar big producing country, and its waste water circulation and waste reside comprehensive utilization all have very significant meaning for healthy Sustainable development of aluminium section bar production and environment protection.Can the usefulness that be recycled up to standard after the waste water that each operation produced of therefore hoping the aluminium shape surface treatment process in a hurry purifies, and waste residue fully utilized, also there is not technology can accomplish this step at present.Handle the online water cycle refining plant of floride-free no ammonia four unification technologies at following novel proposition aluminium shape surface of this background and realize wastewater zero discharge; Each operation that aluminium shape surface is handled realizes that online water cycle purifies; And dewater and become useful waste residue purifying trapped substance; Really accomplish waste water circulation and waste reside comprehensive utilization purpose that aluminium shape surface is handled, kill two birds with one stone.
The utility model content
Still there are discharge of wastewater and the unserviceable problem of waste residue in order to solve the floride-free no ammonia four unification technologies of aluminium shape surface processing; The purpose of the utility model is to provide a kind of aluminium shape surface to handle the online water cycle refining plant that uses in the floride-free no ammonia four unification technologies; A kind ofly can realize wastewater zero discharge; Each operation that aluminium shape surface is handled realizes that online water cycle purifies; And dewater and become useful waste residue purifying trapped substance, accomplish that really the waste water circulation that aluminium shape surface is handled and the aluminium shape surface of waste reside comprehensive utilization handle online water cycle purification system.For realizing above-mentioned purpose; The technical scheme that the utility model adopted is: a kind of do not have the online water cycle refining plant that uses in the ammonia four unification aluminium shape surface treatment process in free-floride; Floride-free no ammonia four unification aluminium shape surface treatment process comprise alkaline degreasing groove 1, alkali accumulator tank 2, take out slag chute 3, clear liquid backflash 4, washing are treated hopper 5, oxidation trough 6, sour backflash 7, acid recovery moisturizing groove 8, painted groove 9, take out slag chute 10, clear liquid backflash 11, pH value control flume 12, sealing of hole groove 13, sealing of hole accumulator tank 14 and sealing of hole recovery moisturizing groove 15; It is characterized in that; Said online water cycle refining plant comprise respectively with air E1, sour backflash 7, painted groove 9 and take out the colouring slot liquid clearing machine 19 that slag chute 10 is connected, the oxidation tank liquor clearing machine 18 that is connected with air E1, sour backflash 7 and oxidation trough 6 respectively, respectively with air E1, sour backflash 7, clear liquid backflash 4 and take out slag chute 3 alkali tank liquor clearing machine 17 that is connected and the liquor of hole-sealing tank clearing machine 20 that is connected with air E1, sour backflash 7, sealing of hole groove 13 and sealing of hole accumulator tank 14 respectively, said alkali tank liquor clearing machine 17, oxidation tank liquor clearing machine 18, colouring slot liquid clearing machine 19 all are connected dashpot 16 and air E1 with liquor of hole-sealing tank clearing machine 20.Said alkali tank liquor clearing machine 17 comprises microfiltration membrane tank body E11, switch-valve (V101, V102, V103, V104, V105, V106, V107, V108, V109, V110), pump (P3, P11, P12), belt filtering unit E12, cylinder C1 and cylinder C2.
More excellent, said oxidation tank liquor clearing machine 18 comprises microfiltration membrane tank body E21, switch-valve (V201, V202, V203, V204, V205, V206, V207), pump P3 and pump P21.
More excellent, said colouring slot liquid clearing machine 19 comprises microfiltration membrane tank body E31, switch-valve (V301, V302, V303, V304, V305, V306, V307, V308, V309), pump (P3, P31, P32), belt filtering unit E32, cylinder C3 and cylinder C4.
More excellent, said liquor of hole-sealing tank clearing machine 20 comprises microfiltration membrane tank body E41, switch-valve (V401, V402, V403, V404, V405, V406, V407), pump P3 and pump P41.
After adopting technique scheme; Its beneficial effect is: each road technical process synchronous operation that the utility model can cooperate aluminium shape surface to handle; Under the situation that does not add flocculation agent, the in-line purification of realization treatment solution also can recycle the clear water after the purification and will hold back the purpose that the material residue dewaters and reaches recovery aluminium slag.This device forms closed cycle with the washing bath of each road technology that aluminium shape surface is handled; Realize wastewater zero discharge; Conserve water resource but also environment do not caused any pollution greatly not only; Refining plant is except can water cycle purifying and can also dewater holding back material, and the waste residue after the dehydration can be recovered effective utilization.
Description of drawings
Fig. 1 does not a kind ofly have the online water cycle refining plant principle of work synoptic diagram that uses in the ammonia four unification aluminium shape surface treatment process in free-floride;
Fig. 2 is the structural representation of alkali tank liquor clearing machine;
Fig. 3 is the structural representation of oxidation tank liquor clearing machine;
Fig. 4 is the structural representation of colouring slot liquid clearing machine;
Fig. 5 is the structural representation of liquor of hole-sealing tank clearing machine.
Embodiment
Below in conjunction with accompanying drawing the utility model patent is done further detailed explanation.
Extremely shown in Figure 5 like Fig. 1; A kind of do not have the online water cycle refining plant that uses in the ammonia four unification aluminium shape surface treatment process in free-floride; Floride-free no ammonia four unification aluminium shape surface treatment process comprise alkaline degreasing groove 1, alkali accumulator tank 2, take out slag chute 3, clear liquid backflash 4, washing are treated hopper 5, oxidation trough 6, sour backflash 7, acid recovery moisturizing groove 8, painted groove 9, take out slag chute 10, clear liquid backflash 11, pH value control flume 12, sealing of hole groove 13, sealing of hole accumulator tank 14 and sealing of hole recovery moisturizing groove 15; Said online water cycle refining plant comprise respectively with air E1, sour backflash 7, painted groove 9 and take out the colouring slot liquid clearing machine 19 that slag chute 10 is connected, the oxidation tank liquor clearing machine 18 that is connected with air E1, sour backflash 7 and oxidation trough 6 respectively, respectively with air E1, sour backflash 7, clear liquid backflash 4 and take out slag chute 3 alkali tank liquor clearing machine 17 that is connected and the liquor of hole-sealing tank clearing machine 20 that is connected with air E1, sour backflash 7, sealing of hole groove 13 and sealing of hole accumulator tank 14 respectively; Said alkali tank liquor clearing machine 17, oxidation tank liquor clearing machine 18, look tank liquor clearing machine 19 all are connected dashpot 16 and air E1 with liquor of hole-sealing tank clearing machine 20; Said alkali tank liquor clearing machine 17 comprises microfiltration membrane tank body E11, switch-valve (V101, V102, V103, V104, V105, V106, V107, V108, V109, V110), pump (P3, P11, P12), belt filtering unit E12, cylinder C1 and cylinder C2; Said oxidation tank liquor clearing machine 18 comprises microfiltration membrane tank body E21, switch-valve (V201, V202, V203, V204, V205, V206, V207), pump P3 and pump P21; Said colouring slot liquid clearing machine 19 comprises microfiltration membrane tank body E31, switch-valve (V301, V302, V303, V304, V305, V306, V307, V308, V309), pump (P3, P31, P32), belt filtering unit E32, cylinder C3 and cylinder C4, and said liquor of hole-sealing tank clearing machine 20 comprises microfiltration membrane tank body E41, switch-valve (V401, V402, V403, V404, V405, V406, V407), pump P3 and pump P41.
Principle and beneficial effect: the structural design drawing that this patent needs protection has five: Fig. 1 is system process figure; Fig. 2-5 is respectively the structural representation of alkali tank liquor clearing machine, oxidation tank liquor clearing machine, colouring slot liquid clearing machine, liquor of hole-sealing tank clearing machine.
Label 1-15 among Fig. 1 is each operation of floride-free no ammonia four unification aluminium shape surface treatment process.The 16th, receive each clearing machine is just blowing the unfiltered residual waste solution under acting in the water-break stage dashpot.17-20 is the clearing machine of this patent.The dotted arrow of the 1-15 top among Fig. 1 is represented the processed technical process direction of device that the aluminium shape surface processing is processed; Solid arrow between the 1-15 is represented the flow direction of tank liquor.Alkali tank liquor clearing machine, oxidation tank liquor clearing machine and the colouring slot liquid clearing machine of this patent are when mounted; Waste water to each operation of surface treatment carries out decontamination cycle; Be that the fluid inlet of each clearing machine connects the waste water after corresponding operation is cleaned, each clearing machine to purification of waste water after water be recycled to circulation of last one procedure formation of each operation.The liquor of hole-sealing tank clearing machine reclaims sealing of hole and is recycled to the sealing of hole operation after tank liquor purifies and cleans.All be to use the liquid of acid recovery groove 7 during the work of each clearing machine in the water-break stage, the unfiltered water of the residue that tank body flows out during water-break is all guided to dashpot 16.So the tank liquor of dashpot 16 is waste liquids, will carry out the filtration, purification circulation by alkali tank liquor clearing machine 17.
Fig. 2 is the structural design drawing of alkali tank liquor clearing machine.It reclaims tank liquor with treated alkali and purifies, specifically: enter microfiltration membrane tank body E11 from taking out the waste liquid that slag chute 3 flows out, purify after water and flow to clear liquid backflash 4.Purifying waste water of clear liquid backflash 4 is recycled to each technology of surface treatment, when anti-wash phase, partly is used for cleaning the strainer of band filter.Workflow is divided into stage:
The firstth, the waste liquid filtering separation stage.This stage starting switch valve V101, V102, V107, V109 and pump P11 take out the waste liquid that slag chute 3 flows out and enter microfiltration membrane tank body E11, and through the filtering separation of microfiltration membrane, stream of cleaned water is to clear liquid backflash 4.
The secondth, the water-break stage.This stage is closed switch-valve V101, V102 and pump P11; Start air E1, switch-valve V105; Utilize the mode of just blowing on the one hand with the intravital a small amount of residue of jar not filtered liq be discharged to dashpot 16 through V103; Clear liquor in the microfiltration membrane pipe is circulated back to clear liquid backflash 4 through V109 on the other hand, makes the interior residual moisture of tank body reduce as far as possible like this, so just can accomplish the water-break work of system.
The 3rd is system's blowback deslagging stage.After the completion of water-break stage, clearing machine changes the into blowback deslagging stage at once.Start belt filtering unit E12 this moment; Under air E1 and cylinder C1, C2 effect; The material of holding back that is attached on the microfiltration membrane pipe is peeled off, and the waste residue of being stripped from is discharged on the E12 through the microfiltration membrane pipe tank body E11 bottom of opening, and overburden is discharged through scraper through the E12 dehydration.Deslagging finishes promptly to close microfiltration membrane pipe tank body E11 bottom, and E12 continues operation for some time, and the slag on its strainer is thoroughly discharged.Before E12 stops, the anti-washing unit of open system.
The 4th is the anti-cleaning and regeneration stage of system.Finish the anti-washing unit of back in the blowback deslagging stage through circuit and sequence control system open system.Unlatching scavenging pump P3 flows to microfiltration membrane pipe tank body E11 cleaning microfiltration membrane pipe with the liquid of acid recovery groove 7.Open scavenging pump P12 the clear liquor in the clear liquid backflash 4 is cleaned the operating strainer of belt filtering unit through strainer cleaning valve V110.
Fig. 3 is the structural design drawing of oxidation tank liquor clearing machine.It directly purifies the oxidation tank liquor, and specifically: the waste liquid that flows out from oxidation trough 6 enters the microfiltration membrane tank body, purifies after water and flows to acid recovery groove 7.Purifying waste water of acid recovery groove 7 is recycled to each technology of surface treatment.Do not need dehydration slagging when purifying for the waste liquid of oxidation trough 6, workflow was divided into for three stages;
The firstth, the waste liquid filtering separation stage.This stage starting switch valve V201, V207 and pump P21, the waste liquid that oxidation trough 6 flows out enters microfiltration membrane tank body E21, and through the filtering separation of microfiltration membrane, stream of cleaned water is to acid recovery groove 7.
The secondth, the water-break stage.This stage is closed switch-valve V201 and pump P21; Start air E1, switch-valve V204, V205; Utilize the mode of just blowing with the intravital a small amount of residue of jar not filtered liq be discharged to dashpot 16 through V202; Make the interior residual moisture of tank body reduce as far as possible like this, so just can accomplish the water-break work of system.
The 3rd is the anti-cleaning and regeneration stage of system.Finish the anti-washing unit of back in the water-break stage through circuit and sequence control system open system.Unlatching switch-valve V206 and scavenging pump P3 flow to microfiltration membrane pipe tank body E21 cleaning microfiltration membrane pipe with the liquid of acid recovery groove 7.
Fig. 4 is the structural design drawing of colouring slot liquid clearing machine.It purifies treated colouring slot liquid, and specifically: enter microfiltration membrane tank body E31 from taking out the waste liquid that slag chute 10 flows out, purify the most of stream of cleaned water in back to painted groove 9, few part is purified waste water and is back to dashpot.Purifying waste water of painted groove 9 is recycled to each technology of surface treatment, when anti-wash phase, partly is used for cleaning the strainer of band filter.Workflow is divided into stage:
The firstth, the waste liquid filtering separation stage.This stage starting switch valve V301, V306, V307 and pump P31 take out the waste liquid that slag chute 10 flows out and enter microfiltration membrane tank body E31, and through the filtering separation of microfiltration membrane, purifying waste water circulation flows to painted groove 9.
The secondth, the water-break stage.This stage is closed switch-valve V301 and pump P31; Start air E1, switch-valve V305; Utilize the mode of just blowing on the one hand with the intravital a small amount of residue of jar not filtered liq be discharged to dashpot 16 through V302; Clear liquor in the microfiltration membrane pipe is circulated back to through V303 and takes out slag chute 10 on the other hand, makes the interior residual moisture of tank body reduce as far as possible like this, so just can accomplish the water-break work of system.
The 3rd is system's blowback deslagging stage.After the completion of water-break stage, clearing machine changes the into blowback deslagging stage at once.Start belt filtering unit E12 this moment; Under air E1 and cylinder C3, C4 effect; The material of holding back that is attached on the microfiltration membrane pipe is peeled off, and the waste residue of being stripped from is discharged on the E32 through opening microfiltration membrane pipe tank body E31 bottom, and overburden is discharged through scraper through the E32 dehydration.Deslagging finishes promptly to close microfiltration membrane pipe tank body E31 bottom, and E32 continues operation for some time, and the slag on its strainer is thoroughly discharged.Before E32 stops, the anti-washing unit of open system.
The 4th is the anti-cleaning and regeneration stage of system.Finish the anti-washing unit of back in the blowback deslagging stage through circuit and sequence control system open system.Unlatching scavenging pump P3 flows to tank body E31 cleaning microfiltration membrane pipe with the liquid of acid recovery groove 7.Open scavenging pump P32 the clear liquor in the clear liquid backflash 4 is cleaned the operating strainer of belt filtering unit E32 through strainer cleaning valve V309.
Fig. 5 is the structural design drawing of liquor of hole-sealing tank clearing machine.It directly purifies liquor of hole-sealing tank, and specifically: the waste liquid that flows out from sealing of hole accumulator tank 14 enters the microfiltration membrane tank body E41, purifies after water and flows to sealing of hole groove 13.Purifying waste water of sealing of hole groove 13 is recycled to each technology of surface treatment.Do not need dehydration slagging when purifying for the waste liquid of sealing of hole accumulator tank 14, workflow was divided into for three stages:
The firstth, the waste liquid filtering separation stage.This stage starting switch valve V401, V407 and pump P41, the waste liquid that sealing of hole accumulator tank 14 flows out enters microfiltration membrane tank body E41, and through the filtering separation of microfiltration membrane, the circulation of purifying waste water flows to sealing of hole groove 13.
The secondth, the water-break stage.This stage is closed switch-valve V401 and pump P41; Start air E1, switch-valve V404, V405; Utilize the mode of just blowing with the intravital a small amount of residue of jar not filtered liq be discharged to dashpot 16 through V402; Make the interior residual moisture of tank body reduce as far as possible like this, so just can accomplish the water-break work of system.
The 3rd is the anti-cleaning and regeneration stage of system.Finish the anti-washing unit of back in the water-break stage through circuit and sequence control system open system.Unlatching switch-valve V406 and scavenging pump P3 flow to tank body E41 cleaning microfiltration membrane pipe with the liquid of acid recovery groove 7.
Each road technical process synchronous operation that the utility model can cooperate floride-free no ammonia four unification aluminium shape surfaces to handle; Under the situation that does not add flocculation agent, the in-line purification of realization treatment solution also can recycle the clear water after the purification and will hold back the purpose that the material residue dewaters and reaches recovery aluminium slag.This device forms closed cycle with the washing bath of each road technology that aluminium shape surface is handled; Realize wastewater zero discharge; Conserve water resource but also environment do not caused any pollution greatly not only; Refining plant is except can water cycle purifying and can also dewater holding back material, and the waste residue after the dehydration can be recovered effective utilization.
Above-described only is the preferred implementation of the utility model; Should be pointed out that for the person of ordinary skill of the art, under the prerequisite that does not break away from the utility model creation design; Can also make some distortion and improvement, these all belong to the protection domain of the utility model.

Claims (5)

1. one kind is not had the online water cycle refining plant that uses in the ammonia four unification aluminium shape surface treatment process in free-floride; Floride-free no ammonia four unification aluminium shape surface treatment process comprise alkaline degreasing groove (1), alkali accumulator tank (2), take out slag chute (3), clear liquid backflash (4), washing are treated hopper (5), oxidation trough (6), sour backflash (7), acid recovery moisturizing groove (8), painted groove (9), take out slag chute (10), clear liquid backflash (11), pH value control flume (12), sealing of hole groove (13), sealing of hole accumulator tank (14) and sealing of hole recovery moisturizing groove (15); It is characterized in that; Said online water cycle refining plant comprise respectively with air (E1), sour backflash (7), painted groove (9) and take out the colouring slot liquid clearing machine (19) that slag chute (10) is connected, the oxidation tank liquor clearing machine (18) that is connected with air (E1), sour backflash (7) and oxidation trough (6) respectively, respectively with air (E1), sour backflash (7), clear liquid backflash (4) and take out slag chute (3) alkali tank liquor clearing machine (17) that is connected and the liquor of hole-sealing tank clearing machine (20) that is connected with air (E1), sour backflash (7), sealing of hole groove (13) and sealing of hole accumulator tank (14) respectively, said alkali tank liquor clearing machine (17), oxidation tank liquor clearing machine (18), colouring slot liquid clearing machine (19) and liquor of hole-sealing tank clearing machine (20) all are connected dashpot (16) and air (E1).
2. according to claim 1 a kind ofly do not have the online water cycle refining plant that uses in the ammonia four unification aluminium shape surface treatment process in free-floride; It is characterized in that said alkali tank liquor clearing machine (17) comprises microfiltration membrane tank body (E11), switch-valve (V101, V102, V103, V104, V105, V106, V107, V108, V109, V110), pump (P3, P11, P12), belt filtering unit (E12), cylinder (C1) and cylinder (C2).
3. according to claim 1 a kind ofly do not have the online water cycle refining plant that uses in the ammonia four unification aluminium shape surface treatment process in free-floride; It is characterized in that said oxidation tank liquor clearing machine (18) comprises microfiltration membrane tank body (E21), switch-valve (V201, V202, V203, V204, V205, V206, V207), pump (P3) and pump (P21).
4. according to claim 1 a kind ofly do not have the online water cycle refining plant that uses in the ammonia four unification aluminium shape surface treatment process in free-floride; It is characterized in that said colouring slot liquid clearing machine (19) comprises microfiltration membrane tank body (E31), switch-valve (V301, V302, V303, V304, V305, V306, V307, V308, V309), pump (P3, P31, P32), belt filtering unit (E32), cylinder (C3) and cylinder (C4).
5. according to claim 1 a kind ofly do not have the online water cycle refining plant that uses in the ammonia four unification aluminium shape surface treatment process in free-floride; It is characterized in that said liquor of hole-sealing tank clearing machine (20) comprises microfiltration membrane tank body (E41), switch-valve (V401, V402, V403, V404, V405, V406, V407), pump (P3) and pump (P41).
CN2011203199517U 2011-08-24 2011-08-24 On-line water circulating and purifying device used in surface treatment process of fluorine-free, ammonia-free and four-in-one aluminum profile Expired - Fee Related CN202220201U (en)

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CN106065473A (en) * 2016-07-06 2016-11-02 陈衍旻 Realize iron and steel parts oxidation processing technique and the system of sewage zero-discharge
CN106367791A (en) * 2016-11-11 2017-02-01 佛山市三水雄鹰铝表面技术创新中心有限公司 Alkaline three-in-one grinding process capable of integrating pretreatment of aluminum with on-line recycle of aluminum hydroxide
CN106367792A (en) * 2016-11-11 2017-02-01 佛山市三水雄鹰铝表面技术创新中心有限公司 Aluminum pretreatment alkaline three-in-one online recycling system for demolding alkaline liquor for extruding mold aluminum material heads and aluminum hydroxide
CN103572294B (en) * 2012-07-27 2017-04-12 王润强 Treating method, technology and system for waste aluminum alloy chemical milling solution
CN106757268A (en) * 2016-11-11 2017-05-31 佛山市三水雄鹰铝表面技术创新中心有限公司 The aluminium pre-treatment three-in-one and alkali liquid regeneration of alkalescence and aluminium hydroxide online recycling technique
CN109179357A (en) * 2018-07-27 2019-01-11 佛山市三水雄鹰铝表面技术创新中心有限公司 The configuration of aluminium industry polished and cleaned Sewage treatment compound fertilizer's method and system

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* Cited by examiner, † Cited by third party
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CN103572294B (en) * 2012-07-27 2017-04-12 王润强 Treating method, technology and system for waste aluminum alloy chemical milling solution
CN103590086A (en) * 2013-11-14 2014-02-19 佛山市三水雄鹰铝表面技术创新中心有限公司 Nickel-free hole sealing agent for aluminum alloy and hole sealing treatment process of agent
CN103590086B (en) * 2013-11-14 2016-08-17 佛山市三水雄鹰铝表面技术创新中心有限公司 Aluminium alloy is without nickel hole sealing agent and hole-sealing treatment process thereof
CN106065473A (en) * 2016-07-06 2016-11-02 陈衍旻 Realize iron and steel parts oxidation processing technique and the system of sewage zero-discharge
CN106065473B (en) * 2016-07-06 2019-03-26 陈衍旻 Realize the iron and steel parts oxidation processing technique and system of sewage zero-discharge
CN106367791A (en) * 2016-11-11 2017-02-01 佛山市三水雄鹰铝表面技术创新中心有限公司 Alkaline three-in-one grinding process capable of integrating pretreatment of aluminum with on-line recycle of aluminum hydroxide
CN106367792A (en) * 2016-11-11 2017-02-01 佛山市三水雄鹰铝表面技术创新中心有限公司 Aluminum pretreatment alkaline three-in-one online recycling system for demolding alkaline liquor for extruding mold aluminum material heads and aluminum hydroxide
CN106757268A (en) * 2016-11-11 2017-05-31 佛山市三水雄鹰铝表面技术创新中心有限公司 The aluminium pre-treatment three-in-one and alkali liquid regeneration of alkalescence and aluminium hydroxide online recycling technique
CN106367791B (en) * 2016-11-11 2018-10-02 佛山市三水雄鹰铝表面技术创新中心有限公司 Aluminium pre-treatment and aluminium hydroxide online recycling and the three-in-one frosting technology of alkalinity
CN109179357A (en) * 2018-07-27 2019-01-11 佛山市三水雄鹰铝表面技术创新中心有限公司 The configuration of aluminium industry polished and cleaned Sewage treatment compound fertilizer's method and system
CN109179357B (en) * 2018-07-27 2020-03-24 佛山市三水雄鹰铝表面技术创新中心有限公司 Method and system configuration for recovering compound fertilizer from polishing and cleaning wastewater in aluminum industry

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