CN109706441A - Aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration - Google Patents

Abstract

The present invention discloses aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration, and non-mobile water washes a group slot differential concatenation 1# degreasing tank；5# drains slot, pump 1 and 4# chromium-free deactivation slot differential concatenation；Contain hydrofluoric acid and phosphonobutane tricarboxylic acid in 1# degreasing tank；Contain fluotitanic acid, fluorine zirconic acid and phosphonobutane tricarboxylic acid in 4# chromium-free deactivation slot.Degreaser brings after 4# chromium-free deactivation slot the stability and ability to work for not influencing 4# chromium-free deactivation slot into.The present invention chelating and corrosion inhibiting ability superpower to the compatible unique design of 4# chromium-free deactivation slot medicament and PBTCA using 1# degreasing tank, chelated mineral cation, 1#-5# slot is not muddy, does not precipitate, and by degreasing tank ejected wash water differential concatenation to degreasing tank, recycles degreaser；5# drains slot and collects chrome-free tanning agent, is recycled to 4# chromium-free deactivation slot；It realizes waste water and dregs zero-emission, production and environmentally friendly cost is greatly reduced.

Description

Aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration

Technical field

The present invention relates to aluminium alloy spraying chromium-free deactivation preconditioning technique field more particularly to aluminium alloy spraying pretreatment nothings Chromium passivating line waste water and dregs zero-emission configuration.

Background technique

For a long time, it has been recognized that technology containing chromium passivating is from aluminum profile production, use and waste treatment full mistake The serious pollution of chromium of journey realizes that aluminium section surface chromium-free Passivation Treatment is the target that aluminium manufacturing industry is pursued.To meet industry Demand to chromium-free deactivation technology, researcher have carried out a large amount of research work, in nearly 30 years aluminium and its alloy surface In the technology research of chromium-free deactivation, the result of study of a variety of aluminium and aluminium alloy non-chromium Passivation Treatment is produced, such as zirconium titanium system Chromium-free deactivation, molybdenum salt system chromium-free deactivation, rare-earth salts system chromium-free deactivation, organosilicon methane series chromium-free deactivation etc..These have both at home and abroad Although report or only carried out laboratory research or carried out pilot scale, abandoned since result is undesirable.At present There are no the scale applications that a kind of result of study can be realized architectural aluminum section.

(1) zirconium titanium system chromium-free deactivation technology

It is proposed first by U.S. Amchem Products Inc. etc. in early 1980s, subsequent Germany Henkel, The companies such as Japanese Parker have carried out numerous studies.Zirconium titanium system chrome-free tanning agent mainly contains H₂ZrF₆And H₂TiF₆.Aluminium alloy exists A series of chemical reaction occurs for the treatment fluid and hydrolysis, the conversion film of generation are by aluminum oxide, zirconium, titanium and fluorine The mixing field trash film of the compositions such as complex compound, to enhance the binding force of coating and matrix, and improves corrosion resistance.

The corrosion resistance of its chemical composition coating is close with chromate film when zirconium titanium system handles aluminium alloy, can prevent aluminium from closing The corrosion of gold.The zirconium chrome-free tanning agent of the five or nine Research Institute of weapons portion shows paint film and aluminium to aluminium alloy wheel hub plated film The binding force of substrate reaches level-one, the 500h of resistance to neutral salt spray test.Guo Rui light etc. has studied metatitanic acid salting liquid and turns in aluminum alloy surface Change the Corrosion Protection of film.Aluminium alloy through titanium-based Passivation Treatment occurs by the salt mist experiment rear surface of 336h without spot corrosion, table Bright titanate chemical composition coating has good corrosion protection effect to aluminum alloy surface.

It is current studies have shown that when zirconium or titanium system inorganic salts are used alone, because passivating solution is fluorine-containing system, in production process It is unstable, the easy decomposition failure of tank liquor；Need further to be studied as scale chromium-free deactivation film technique processing architectural aluminum section.

(2) molybdate series chromium-free deactivation technology

Molybdenum and chromium belong to Group VIA, have similar physicochemical properties.Molybdate is a kind of less toxic inorganic acid salt, is utilized Molybdate substitution traditional chromium hydrochlorate has carried out numerous studies.Hinton etc. in sodium molybdate solution, generates aluminium alloy dipping A kind of blue Molybdate Conversion Film of golden yellow band, to improve the protective performance of aluminium alloy.King is existed at equal using same infusion process LY₁₂Aluminum alloy surface obtains the anti-corrosion conversion film of molybdate of buff.Extent of corrosion is significantly in 3.5wt.%NaCl solution It reduces, occurs after impregnating within 21 days without spot corrosion.Yang Yuxiang etc. has studied the molybdate black conversion film of cast aluminium alloy.Potassium bichromate point Drop experiments have shown that, the corrosion resistance of film is 40s.

Although these are research shows that molybdate substitution chromate film forming has certain anti-corrosion effect, and chromate conversion coating Technology is compared, and it is poor that molybdate film forming protective performance is used alone, and molybdenum salt system chromium-free deactivation cost is very high, the army of being only used for With equal special materials preparation, it is unsuitable for the surface passivating treatment of scale architectural aluminum section.

(3) rare-earth salts chromium-free deactivation technology

Australian Hintom and Arnott etc. uses Ce³⁺As corrosion inhibiter of the AA7075 aluminium alloy in NaCl solution, The corrosion rate of AA7075 aluminium gold is reduced to original 1/10.If sample is put into 1g/L CeCl in advance₃It is impregnated in solution Certain time is handled, then is transferred in 0.1mol/L NaCl solution, the corrosion of sample equally considerably reduces.Without cerium salt processing The corrosion rate of AA7075 aluminium alloy is 5.9 μ g/ (m²It s), is only 0.2 μ g/ (m after cerium salt is handled²S), this is because aluminium Alloy surface is passivated, and forms the reason of corrosion resistant rare-earth salt passive film.The Mansfeld etc. in the U.S. has developed cerium-molybdenum Joint passivation process, the aluminium alloy through this process are not sent out still for continuous dipping 60 days in 0.5mol/L NaCl solution Raw spot corrosion, corrosion resistance have been more than traditional chromating processing.In AA2014 aluminium alloy, AA2024 aluminium alloy, AA5083 Research on aluminium alloy, AA2090 and AA8090 aluminium alloy also demonstrates rare-earth conversion coatings to the effective of these material corrosion protection Property.Aluminium alloy through rare earth Passivation Treatment, not only the ability of anti-homogeneous corrosion significantly increases, but also the ability of anti-local corrosion It significantly improves.Research of the country in terms of aluminum alloy rare earth passivation is started late.Li Jiuqing etc. develops P5, SRE and T2/T7 aluminium Three kinds of rare earth passivation technologies of alloy.After SRE process, corrosion resistance can be subjected to the neutral salt spray test of 360h.Through T2/T5 The commercial-purity aluminium and LF of process₆The corrosion polarization resistance of aluminium alloy than it is untreated when improve more than ten times, in 3.5wt.% 21d is impregnated in NaCl solution, spot corrosion does not occur, and can bear the neutral salt spray test of 504h or more, and usually after chromic acid salt treatment Aluminium alloy at most only require bear 336h neutral salt spray test, therefore through the rare earth passivation technology handle aluminium alloy be more than The corrosion resistance standard of chromating processing.Shi Tie etc. forms the neutral salt that can bear 400h or more on the surface LF21 The cerium-based conversion coating of mist experiment.The research of rare earth secondary passivity is carried out to LY12 aluminium alloy in promoting culture etc., rare earth obtained is double The corrosion resistance of tunic is substantially better than the monofilm being once passivated.

Although rare earth chromium-free deactivation technology achieves certain progress, due to the toxicity to inorganic salt of rare earth and its to environment Influence the problems such as can not effectively solve always.

(4) organosilicon methane series chromium-free deactivation technology

Skin covering of the surface caused by the processing of organosilicon methane series is better than chromate film.Beccaeia etc. contains pure Al at 80 DEG C 15min is impregnated in the aqueous solution of the inclined oxygen propyl group methylphosphine acyl silanes (MAOS) of 0.5wt.%, improves the general corrosion to Al With the inhibition of local corrosion.Wang Xiuhua etc. is successfully prepared methyl triethylphosphine acyl silanes in LY12 aluminium alloy matrix surface (MTEOS)/ethyl orthosilicate (TEOS) hybridized film.The hybridized film has excellent corrosion resistance, and n (MTEOS): n (TEOS)=3:1 when, the corrosion resistance of coating is best.Su Honglai etc. has studied different silane treatment LY12 aluminium alloy corrosion resistances Energy.Point out that silane improves the Corrosion Protection of film Yu aluminum substrate binding force and aluminium alloy.The researchs such as Chu find that GPTMS can be with Increase the density of film and improves the binding force between polymeric matrix.Metrok etc. studies GPTMS-TEOS film, it is indicated that organic matter contains Amount and hydrolysing rate have a major impact the corrosion resisting property of the silicate films (Ormosil film) of organic modification.But spot corrosion makes film Hydrophilic radical is formd, the salt spray resistance of silane film is poor.It is denser that Van Ooij etc. thinks that addition crosslinking agent can be formed Silicone film, reduce and reacted with moisture.Zandi-zand etc. with bisphenol-A crosslinking agent agent obtain it is uniform, flawless, Dense GPTMS-TEOS film, improves the corrosion resistance of aluminium alloy.

It is current studies have shown that since there are at high cost, solvent be volatile or corrosivity for organosilicon methane series chrome-free tanning agent Many reasons such as strong, final industrialization are also faced with many difficulties and need to solve.

(5) the compound chromium-free deactivation technology of organic matter-inorganic salts

Organic-inorganic composite passivating solution can effectively improve corrosion resisting property compared with the passivating solution for using one-component.Deck Etc. having studied the influence of acrylic acid and Acrylic polymer to the corrosion resisting property of fluotitanic acid and fluorine zirconic acid conversion film.The result shows that The corrosion current for mixing the passivating film obtained with fluorine zirconic acid with 7:3 acrylic acid/acrylamide polymer is minimum, and corrosion resisting property is suitable In phosphorus chromium film.The researchs such as Smit point out that polyacrylic acid is added in fluotitanic acid and fluorine zirconic acid or tannic acid can get preferable corrosion resistance Energy.Paloumpa etc. reports the fluotitanic acid that polyvinyl pyrrole is added and fluorine zirconic acid and can get fabulous corrosion and inhibit.But at present The studies above is still in the laboratory research stage.

(6) manganate chromium-free deactivation technology

Lin Shengling etc. has studied the chemically composited conversion film of fine aluminium and LY12 aluminum alloy surface manganate and molybdate.As a result The Corrosion Protection of Al, LY12Al in 3.5wt.%NaCl solution greatly improves.Old east is elementary to be made with molybdate, permanganate For the oxidant that forms a film, the corrosion resisting property of aluminium alloy LY12 chemical composition coating is had studied, conversion film is rotten in 3.5wt.%NaCl solution It loses and there was only a small amount of pitting in medium after 70h impregnates.Aluminium alloy is in KMnO₄By suitable in the solution mixed with zirconium titanium system inorganic salts When processing can also form good conversion film.Japanese Patent Laid-Open 11236082, which describes, can provide good corrosion resistance and painting The aluminium alloy inactivating treatment liquid of layer adhesive force, main component are permanganate, water-soluble zirconium compound and water-soluble titanium compound. The inorganic compounding passivation of two or more heavy metal element compound containing manganese etc. can be formed after Passivation Treatment, on alloy matrix aluminum Film.Inventor is it is thought that the key that passivating film corrosion resistance is further improved.

Following aluminum alloy surface chromium-free deactivation technological development direction will turn to the inorganic multiple of research various metals salt formation It is organic based on organic-inorganic compounding conversion film, organic matter such as silane coupling agent that conjunction conversion film, organic matter and metal salt are formed Compound conversion film etc..But applicant thinks: for comparing the compound conversion film of inorganic salts, although organic matter passivating film is a kind of The directionality technology of the following surface preparation, becoming mainstream technology, there is also cost, solvent volatilization pollution etc. are a variety of Factor restricts, and has a long way to go.Develop the organo-mineral complexing conversion film new technology formed by various metals salt to be more suitable for The current national conditions in China.

Summary of the invention

It is an object of the invention to propose aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration, utilize 1# the degreasing tank chelating and corrosion inhibiting ability superpower to the compatible unique design of 4# chromium-free deactivation slot medicament and PBTCA, chelating gold Belong to cation, 1#-5# slot is not muddy, does not precipitate, and by degreasing tank ejected wash water differential concatenation to degreasing tank, recycles degreaser；5# drip The chrome-free tanning agent that dry slot is collected, is recycled to 4# chromium-free deactivation slot；It realizes waste water and dregs zero-emission, production and environmental protection is greatly reduced Cost.

To achieve this purpose, the present invention adopts the following technical scheme:

Aluminium alloy spraying pretreatment the waste water and dregs zero-emission of chromium-free deactivation line configuration, which is characterized in that including 1# degreasing tank, The washing trough of 2# non-mobile water, the washing trough of 3# non-mobile water, 4# chromium-free deactivation slot and 5# drain slot, and aluminium alloy spraying pretreatment is successively passed through 1# degreasing tank, the washing trough of 2# non-mobile water, the washing trough of 3# non-mobile water, 4# chromium-free deactivation slot and 5# drain slot；1# degreasing tank, 2# do not flow Dynamic rinsing bowl and 3# non-mobile water washing trough differential concatenation are used for the moisturizing of 1# degreasing tank and recycling degreaser；4# chromium-free deactivation slot And 5# is drained and is provided with pump between slot, pump is pumped into 4# chromium-free deactivation slot for 5# to be drained the tank liquor in slot；

Contain degreaser in 1# degreasing tank, 4# chromium-free deactivation slot has included chrome-free tanning agent；

The chemical constituent of degreaser includes hydrofluoric acid and PBTCA, hydrofluoric acid (50wt.%): PBTCA (50wt.%)=3: 1, degreaser concentration 20-30g/L, acidity value 0.5-1.0 equivalent；

The chemical constituent of chrome-free tanning agent includes fluotitanic acid, fluorine zirconic acid and PBTCA, fluotitanic acid (50wt.%): fluorine zirconic acid (50wt.%): PBTCA (50wt.%)=0.5:0.5:1, chrome-free tanning agent concentration 5.0-8.0g/L；

1# degreasing tank is compatible to 4# chromium-free deactivation slot medicament, when the ingredient of degreaser brings 4# chromium-free deactivation slot by aluminium alloy Afterwards, 4# chromium-free deactivation slot is stable.

It further explains, in degreaser, hydrofluoric acid (50wt.%) concentration is 15-22.5g/L, PBTCA (50wt.%) concentration is 5-7.5g/L.

It further explains, in chrome-free tanning agent, fluotitanic acid (50wt.%) concentration is 1.25-2.0g/L, fluorine zirconic acid (50wt.%) concentration is 1.25-2.0g/L, and PBTCA (50wt.%) concentration is 2.5-4.0g/L.

It further explains, 3# non-mobile water washing trough is connected with running water pipe, and running water pipe is for making tap water enter 3# Non-mobile water washing trough supplements liquid level.

It further explains, in 1# degreasing tank and 4# chromium-free deactivation slot: PBTCA is as corrosion inhibiter, phosphono and three Carboxyl is adsorbed on aluminum alloy surface, for tank liquor to be isolated, delays to corrode, reduces molten aluminum amount, tank liquor is kept to stablize.

It further explains, in degreasing tank and chromium-free deactivation slot, PBTCA is kept as chelating agent, chelated mineral cation Tank liquor is stablized；In chromium-free deactivation slot, PBTCA combines the metal ion of chelating into chromium-free passivating film, shape as phosphorization filming agent At phosphatization-chromium-free passivating film, metal cation and PBTCA are consumed；The butane group of phosphorization filming agent PBTCA is combined into powder spray Layer.

It further explains, the chromium-free deactivation temperature of 4# chromium-free deactivation slot is 5-35 DEG C.

It further explains, aluminium alloy is 30-120 seconds in the chromium-free deactivation time of 4# chromium-free deactivation slot.

It further explains, in 4# chromium-free deactivation slot, the pH value operation interval of 4# chromium-free deactivation slot is 2.5-4.5.

It further explains, the washing trough of 2# non-mobile water is equipped with No. five valves to the 1# degreasing tank, and the 3# non-mobile water is washed Slot to the 2# non-mobile water washing trough be equipped with No. four valves, the 3# non-mobile water washing trough be equipped with No. three valves, the 5# drain slot with The pipeline of the 4# chromium-free deactivation connection is equipped with No. two valves, pump, No.1 valve；The tap water of supplement from No. three valves enter 3# slot, Through 3# slot → 2# → 1# degreasing tank reverse flow, 1# degreasing tank liquid level is supplemented, recycles degreaser；The 5# drains slot and 4# Chrome-free Deactivation slot differential concatenation drains liquid through 5# slot → No.1 valve → pump → No. bis- valve → 4# chromium-free deactivation slot reverse flow, recycles nothing Chromium passivating liquid；Whole chromium-free deactivation line does not set discharge outlet, waste water and dregs zero-emission.

The invention has the benefit that

1, determine that fluorine zirconic acid-PBTCA chelating agent-PBTCA corrosion inhibiter-PBTCA phosphorization filming agent is compound matches for fluotitanic acid-for the first time Side, establishes chromium-free deactivation new system, new process, has found passivation film forming changing rule, thoroughly solves the prior art to building Build the pollution problem of aluminium shape surface processing bring Cr VI；

2, it directly selects fluotitanic acid and fluorine zirconic acid as main film-forming components for the first time, the stability of tank liquor is significantly increased. The present invention eliminates fluotitanate and fluozirconate from the stability of passivating solution, directly selection fluotitanic acid and fluorine zirconic acid, keeps away Exempt to generate the risk that villiaumite precipitates；

3, special chelating agent PBTCA is selected for the first time, on the basis of 1# degreasing tank is compatible to 4# chromium-free deactivation slot medicament, only The non-mobile water washing trough of 2#, 3# slot is selected, traditional 5#, 6# flowing rinsing bowl is rejected, substantially shortens process flow.PBTCA, which is removed, to be had Effect blocks the decomposition of aluminium, zirconium, titanium to be precipitated, holding tank liquor runs outer Ca also effectively in chelating tap water steadily in the long term²⁺、Mg²⁺ Plasma, 2#, 3# are abandoned traditional pure water cleaning, are cleaned using not flowing running water, two slot water for cleaning differential concatenations, supplement Tap water enters from 3# slot, through 3# → 2# → 1# slot reverse flow, recycles degreaser, saves water for cleaning；The present invention drips 5# The chrome-free tanning agent that dry slot is collected is pumped into 4# chromium-free deactivation slot with pump, recycles chrome-free tanning agent, be greatly reduced production and environmental protection at This；

4, special corrosion inhibiter PBTCA is selected for the first time, is adsorbed on using its electronegative phosphono and three carboxyls positively charged Aluminum alloy surface, the function of tank liquor is isolated, slow down corrosion, reduce molten aluminum amount, holding tank liquor stable operation；

5, special phosphorization filming agent PBTCA is selected for the first time, makes full use of the phosphorization filming function of the component phosphono, by The bridge joint of PBTCA acts on, and the metal ion of chelating and PBTCA are combined into passivating film, passivating solution aging is effectively prevent；4# slot is raw At passivating film, be fluotitanic acid and fluorine zirconic acid passivation, PBTCA phosphono phosphatization formed composite membrane, be organic matter machine composite membrane, Its butane group binding force superpower with spraying resin determines that aluminium after Non-water washing, meets national standard, substantially after the passivation of 4# slot Process flow is shortened in water-saving saving；

6, chelating agent, corrosion inhibiter and phosphorization filming agent are selected as same component PBTCA for the first time, are waste water and dregs zero-emission It puts and takes a firm foundation.Phosphino- and carboxyl chelating aluminium ion, titanium ion, zirconium ion and the Ca of phosphonobutane tricarboxylic acid²⁺、Mg²⁺ Plasma stablizes tank liquor；Part carboxyl and phosphono are adsorbed on aluminium alloy matrix surface, and tank liquor is isolated, reduces molten aluminum amount, are formed Inhibition；Phosphono is combined into passivating film, forms film forming matter, and the aluminium in deactivation slot is kept away as carrier in conjunction with film forming by PBTCA Aluminium ion and PBTCA accumulation are exempted from；Hydrofluoric acid, the PBTCA of 1# slot addition, fluotitanic acid, fluorine zirconic acid, the PBTCA of 4# slot addition are equal For film-forming components, after water for cleaning zero-emission, 4# slot absolutely not due to individual components progressive poisoning dead slot risk；The aluminium of dissolution from The Ca that son, tap water are brought into²⁺、Mg²⁺Ion is acted on by the chelating and bridge joint of PBTCA, through phosphono phosphatization into passivating film, Risk without progressive poisoning；1# slot, the medicament of 4# slot addition, dissolution aluminium, the Ca that brings into of 3# slot supplement tap water²⁺、Mg²⁺Deng Ion can be combined in 4# slot into passivating film, it is ensured that 1#-5# flute length phase production run, it is not muddy, do not precipitate, the aluminium of production Meet national standard；

7, degreasing tank medicament is designed as the first time completely compatible to chromium-free deactivation slot medicament, prevents to bring passivation into except oil component To the damage of deactivation slot ability to work and stability after slot.The present invention simplifies by selecting meticulously and removes oil ingredient, reject those drops Low deactivation slot ability to work or influence deactivation slot stability component, degreasing tank component is designed as it is completely compatible to deactivation slot, The risk except oil ingredient damage deactivation slot is thoroughly released, lays solid theoretical basis for waste water and dregs zero-emission；

8, passivation temperature lower limit is greatly reduced for the first time.Traditional chromium-free deactivation temperature is room temperature, due to special film-forming components The selection of PBTCA, greatly improves passivation ability, and chromium-free deactivation new process of the present invention normally forms the blunt of qualification at 5 DEG C or more Change film, it is energy saving when being lower than room temperature without heating, reduce production cost；

9, substantially shorten passivation time for the first time.Traditional chromium-free deactivation time is 120-240 seconds, due to special film-forming components The selection of PBTCA greatly improves passivation ability, and passivation time is shorten to 30-120 seconds by the present invention, substantially shortens passivation time, Work efficiency is provided；

10, pH value operation interval is substantially widened for the first time.It is 3.0-4.0 during traditional chromium-free deactivation slot pH value work, due to The selection of special inhibition and cheating components PBTCA, is expanded downwards pH value with hydrofluoric acid to 2.5 and to be not concerned about molten aluminum amount too big, Passivating solution is influenced to stablize；With ammonium hydroxide be improved upwards to 4.5 and be not concerned about fluoride decompose precipitating, the steady of passivating solution greatly improved It is qualitative.

Detailed description of the invention

Fig. 1 is research and development content graph of the invention；

Fig. 2 is research and development technology route schematic diagram of the present invention；

Fig. 3 is PBTCA molecular structure；

Fig. 4 is Al alloy powder spraying film layer schematic diagram；

Fig. 5 is aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration of the present invention；

Contain in Fig. 5: the valve 5 of valve 4, five of valve 3, four of valve 2, three of No.1 valve 1, two.

Specific embodiment

With reference to the accompanying drawing and specific embodiment further illustrates technical solution of the present invention.

Chinese patent CN201610185885.6 " aluminium alloy non-chromium entirety medicament compatible processing and wastewater zero discharge system ", CN201610186144X " aluminium alloy non-chromium passivator and its processing system of application ", " aluminium alloy is gone CN201610186179.3 Burr degreasing tank medicament and its use and its chromium-free deactivation processing system ", CN 201610186876.9 " aluminium alloy non-chromium passivation Slot medicament compatible processing system " propose 1# deburring degreasing tank and the compatible method of 7# chromium-free deactivation slot, two pharmacy slots at The stability and ability to work of split-phase is same, compatible, medicament is independent of each other after bringing into pharmacy slot, on this basis, configuration is not Rinsing bowl is flowed, realizes waste water and dregs zero-emission.Wherein, 1# degreasing tank working index are as follows: fluotitanic acid (50wt.%) and fluorine zirconic acid (50wt.%) (1:1) concentration 20-30g/L, polyacrylic acid (30wt.%) concentration 4-6g/L, phosphonobutane tricarboxylic acid (50wt.%) 40-60g/L, 5-35 DEG C of temperature, acidity value 1.5-2.0 equivalent (with 50% hydrofluoric acid tune acidity value)；7# Chrome-free slot Working index are as follows: fluotitanic acid (50wt.%) and fluorine zirconic acid (50wt.%) (1:1) concentration 2.0-3.0g/L, polyacrylic acid (30wt.%) concentration 0.4-0.6g/L, phosphonobutane tricarboxylic acid 4.0-6.0g/L, 5-35 DEG C of temperature, pH2.0-5.0.Production Operation shows that the fluotitanic acid and fluorine zirconic acid of 1# flowing current separation 20-30g/L, production cost are too high；1# slot adds to stablize titanium and zirconium Add phosphonobutane tricarboxylic acid (50wt.%) 40-60g/L, cost is too high；1# slot adds polyacrylic acid (30wt.%) concentration 4- 6g/L, 7# slot add polyacrylic acid (30wt.%) concentration 0.4-0.6g/L, after selecting non-mobile water washing trough wastewater zero discharge, gather Acrylic acid is not involved in film forming, and aluminium ion and polyacrylic acid constantly accumulate, and gradually reduces the passivation ability of 7# slot and dead slot；Whole spray It applies pretreatment line and is configured with 10 slot positions, process is too long, influences working efficiency.This set series of patents needs to do following improvement:

1, by the etching component fluotitanic acid and fluorine zirconic acid of 1# degreasing tank, hydrofluoric acid is replaced with, reduces production cost；

2, the dosage for reducing phosphoryl butane tricarboxylic acid (PBTCA), is greatly reduced production cost；

3, the polyacrylic acid for rejecting 1# slot and 7# slot avoids adding ingredient from accumulating and the risk of dead slot；

4, under the critical conditions of water for cleaning zero-emission, the aluminium ion of degreasing tank and deactivation slot dissolution is found in deactivation slot In conjunction with the Consumption into passivating film, the risk of 4# slot dead slot because of aluminium ion accumulation is avoided；

5, cleaning slot number is reduced, production efficiency is improved.

The present invention still selects fluotitanic acid and fluorine zirconic acid is the main component of chromium-free deactivation, still uses fluorine-containing system.Add After entering PBTCA chelating agent, PBTCA corrosion inhibiter and PBTCA film forming agent, it is adsorbed on by the negatively charged phosphono of PBTCA and three carboxyls The corrosion inhibition properties on positively charged aluminum substrate surface are isolated tank liquor, reduce molten aluminum amount；Using the powerful sequestering power of tri- carboxyl of PBTCA, Chelated metal ions stablize tank liquor；Using the powerful phosphorization capacity of PBTCA phosphono, together by metal ion and PBTCA, knot It closes into passivating film, eradicates deactivation slot tank liquor degradation risk, greatly improve the passivation ability of deactivation slot；Utilize passivating film containing PBTCA The mechanism that middle butane group and the powder spray resin same sex mix, greatly improves passivating film to the adhesive force of organic coating.In determination On the basis of chromium-free deactivation slot formula, the present invention has studied in detail influence of the degreasing tank to deactivation slot, selects appropriate degreasing tank The formula compatible to deactivation slot, is greatly reduced damage of the oil removing to deactivation slot ability to work and stability, it is ensured that spraying pretreatment System is run steadily in the long term.

One, chromium-free deactivation slot formula designs

The present invention proposes and establishes a kind of architectural aluminum section chromium-free deactivation new technology, which, which uses, contains fluotitanic acid-fluorine zirconium Acid-chelating agent-corrosion inhibiter-bonderite compound prescription, Chrome-free in formula, to solve architectural aluminum section industry for a long time universal Surface passivating treatment bring pollution of chromium problem is carried out using chromate-fluorine ion passivation liquid system.Aluminium through the technical treatment Profile is entirely capable of reaching national standard (GB/T5237.4-2017) to passivation film thickness, resisting salt fog corrosion, humidity resistance, boiling, punching It hits, the requirement of the indexs such as cupping test.

1, present invention research and development content

Present invention research chrome-free tanning agent is newly formulated, new process, explore the dynamics of chromium-free deactivation process, PASSIVATION MECHANISM and The factor (temperature, concentration, time etc.) of product quality is influenced, determines and optimizes aluminum non-chromium passivation technology, assess new technology The indexs such as cost, sewage discharge complete the pilot scale verifying of new technology, optimize new process and blunting line configuration on the basis of lab scale, It proposes production decision and pushes new process to industrialization.Research contents is as shown in Figure 1.

2, the key technology difficulty that the present invention solves

(1) by exploring chromium-free deactivation mechanism and passivating process dynamics, determine in passivating solution the effect of each component and Chromium-free deactivation theoretical basis is established and is improved in influence to Chromating Film On Zn Deposits, instructs the screening of chromium-free deactivation formula.

(2) by the screening of Chrome-free formula, fluotitanic acid-fluorine zirconic acid-chelating agent-corrosion inhibiter-bonderite compound prescription is established System；By influencing the research of the factor of Chromating Film On Zn Deposits on temperature, concentration, time etc., passivation film forming changing rule is found, is built Vertical chromium-free deactivation new process.

(3) method for establishing Fast Monitoring Chromating Film On Zn Deposits makes production operation personnel regulate and control production process in time, guarantees to produce Quality.

(4) the wide chromium-free deactivation new process of temperature applicable range is established, remains to obtain qualification at 5-35 DEG C of operation temperature Passivating film, without heating, solves the problems, such as passivating process consumption mass energy.

(5) new chromium-free deactivation compound prescription tank liquor is stablized, and technological operation is simple, energy conservation and environmental protection, and wastewater treatment is easy, and is easy to Large-scale production.

(6) it establishes and improves chromium-free deactivation theoretical basis, instruct the screening of Chrome-free formula.

3, the economic and technical norms that the present invention reaches

The present invention develop fluotitanic acid-fluorine zirconic acid-chelating agent-corrosion inhibiter-bonderite chromium-free deactivation be newly formulated and Chrome-free it is blunt Change new process, new formula is free of Cr VI, and operation temperature is in 5-35 DEG C, pH value in 2.5-4.5 range；It is passivated tank liquor to stablize, work Skill is easy to operate, energy conservation and environmental protection, and wastewater treatment is easy, and is easy to be mass produced.

Implementation of the invention has very great strategic importance.Firstly, thoroughly finish architectural aluminum section surface treatment, Using the pollution of chromium with waste treatment process, real chromium-free deactivation pretreatment is realized, the world solved in decades is difficult Topic, the status being technically in a leading position, and go abroad for the aluminium product in China, it takes part in international competition and takes a firm foundation. Secondly, this technology will bring huge economic benefit, annual about 10,000,000 tons of aluminum profile of the spray treatment in the whole nation is got rid of due to chromium dirt Bring embarrassment condition is contaminated, profit will be considerably beyond existing level.

4, method, technology path and process flow that present invention research uses

The present invention researchs and develops chromium-free deactivation new technology for architectural aluminum section, and technology path is as shown in Figure 2.

5, chromium-free deactivation slot formulation selection of the present invention

In research and development of the invention, pilot scale and process of producing product, it is all made of fluotitanic acid-fluorine zirconic acid-chelating agent-corrosion inhibiter- The passivating solution of bonderite compound prescription, passivating solution are recycled, reduce the discharge of pollution, prevent the production of pollutant from source It is raw.

(1) the new formulating of chrome-free tanning agent

Fluotitanic acid-fluorine zirconic acid-compound new formula of chelating agent-corrosion inhibiter-bonderite is studied, chromium dirt is thoroughly eliminated from source Dye.The present invention selects fluotitanic acid and fluorine zirconic acid as main passivation ingredient, and ionization, hydrolysis and passivation reaction are (fluorine zirconic acid It is similar):

1, fluotitanic acid ionizes

H₂TiF₆=2H⁺+TiF₆ ^2- (1)

2, fluotitanic acid hydrolyzes

3TiF₆ ^2-+6H₂O=Ti (OH)₃F₃ ^2-+Ti(OH)₂F₄ ^2-+Ti(OH)F₅ ^2-+6H⁺+6F^- (2)

By (2) formula, the aqueous solution of fluotitanic acid and fluorine zirconic acid is unstable, and facile hydrolysis is at monohydroxy, dihydroxy and trihydroxy fluorine Metatitanic acid and fluorine zirconic acid root, while releasing H⁺And F^_, decline tank liquor pH value, F^_Concentration increases；If improving pH value, (2) formula is pressed, React mobile to the right.When pH value is greater than 4.5, trihydroxy fluotitanic acid and fluorine zirconic acid are further hydrolyzed, and turbidity and precipitation occur:

3, fluotitanic acid decomposes, titanium hydroxide is precipitated

Ti(OH)₃F₃ ^2-+H₂O=Ti (OH)₄↓+H⁺+3F^- (3)

When being put into aluminium alloy in tank liquor, following reaction occurs for fluotitanic acid and reactive aluminum:

4, passivating film is dissolved, and pH value increases

Al₂O₃+12F^-+3H₂O=2AlF₆ ^3-+6OH^- (4)

5, Ti is reduced

4Al+3Ti(OH)₃F₃ ^2-+9H⁺=3Ti+AlF₆ ^3-+3F^-+3Al³⁺+9H₂O (5)

6, aluminium is dissolved, and generates fluoaluminic acid root

6Al³⁺+21F^-+15H₂O=AlF₆ ^3-+Al(OH)F₅ ^3-+Al(OH)₂F₄ ^3-

+Al(OH)₃F₃ ^3-+Al(OH)₄F₂ ^3-+Al(OH)₅F^3-+15H⁺ (6)

Chromium-free passivating film is hydroxyl fluotitanic acid aluminium, hydroxyl fluorine zirconic acid aluminium, Titanium, metal zirconium, hydroxyl fluoaluminic acid titanium, hydroxyl The composite membrane of the material compositions such as base fluoaluminic acid zirconium.

In order to guarantee that aluminium alloy is used for a long time, it is necessary to be passivated and spray treatment.The purpose of passivation spraying is to mention The corrosion resistance of high aluminium, its surface anti-pollution ability and its color and fast light, weatherability, therefore the adhesive force being passivated is very Important technical indicator.The technique generally used both at home and abroad at present is the Cr VI passivating solution based on chromic anhydride, passivation technology Condition are as follows:

PH value: 1.8-2.2

Temperature: 25-35 DEG C

Time: 120-240s

CrO₃: 2.0-4.0g/L (7)

It is passivated using fluotitanic acid and fluorine zirconic acid, is deposited into and is divided into titanium and zirconium, it is thoroughly nontoxic, just adapt to aluminium alloy increasingly Go deep into the main trend of mankind's daily life various aspects.But fluotitanic acid and fluorine zirconic acid how are made good use of, technical difficulty is very big.

By (3) formula, pH is increased, and fluotitanic acid and fluorine zirconic acid decomposite titanium hydroxide, and tank liquor is muddy；By (2) formula, fluotitanic acid and Fluorine zirconic acid hydrolysis, ionizes out F^-；Fluorine aluminium complex is generated by (4), the reaction of (5) formula, discharges OH^-, pH is increased, when pH value is more than 4.5 When, it generates Ti (OH)₄And Al₂(OH)₃F₃Mixture, Surface of profile generate pollen, and tank liquor is muddy.

By (5) and (6) formula, after aluminium alloy enters fluotitanic acid and fluorine zirconic acid tank liquor, aluminium is dissolved, and forms fluoaluminate, titanium It is replaced reduction, is deposited on aluminum alloy surface, forms the composite membrane of Titanium, completes passivation.

As described above, titanium and zirconium in fluotitanic acid and fluorine zirconic acid, can be used as the main component of passivator, and be passivated speed completely Degree is fast, and passivation temperature is low.But the following fatal problem encountered in research and development:

1), in terms of molecular formula, fluotitanic acid and fluorine zirconic acid, fluorine is too high, easily knot pollen；

2), fluotitanic acid and fluorine zirconic acid are unstable, and when pH value is greater than 4.5, tank liquor is decomposed, and form titanium hydroxide and hydroxide Zirconium precipitating, passivation optimization section can only be between 3-4；

3), fluorine is high, and pH value is low, and aluminum alloy surface is easily corroded；

4), fluorine is high, and pH value is low, and molten aluminum amount is too big, and tank liquor is easily muddy, the easily upper powder of aluminium alloy.

Only solve aluminium alloy under high fluorine, low ph value be corroded, powder on surface, the problem of tank liquor muddiness could effectively make With fluotitanic acid and fluorine zirconic acid, chromium-free deactivation is realized.

For this purpose, corrosion inhibiter, chelating agent and film forming agent is selected to solve under high fluorine, low ph value with fluotitanic acid and fluorine zirconic acid compatibility Powder and tank liquor muddiness problem on aluminium alloy.

Corrosion inhibiter refers to a kind of medicament that fluotitanic acid and fluorine zirconic acid corrosive power can be effectively reduced.In view of passivating film band Positive charge, the present invention select electronegative carboxyl to be adsorbed on aluminum alloy surface, and tank liquor is isolated, slows down corrosion.The selection of corrosion inhibiter, Must satisfy four requirements: first is that reducing the meltage of aluminium alloy, it is clean to enable aluminum alloy to surface, no pollen；Second is that can actively join With film forming, corrosion inhibiter building up in deactivation slot is avoided, passivation ability is influenced；Third is that do not decompose, it is severe in high fluorine, low ph value Under the conditions of homeostasis；Fourth is that meeting requirements of the national standard after passivation.

Chelating agent, refer to can effectively chelated mineral cation, be allowed to be not easy to decompose a kind of medicament of precipitation from tank liquor.It presses (3)-(6) formula, after chelating agent is added, Ti (OH)₄And Al₂(OH)₃F₃Not easily generated, tank liquor is stablized, and aluminium alloy is not easy powder.? Under the constantly raised mal-condition of low ph value, high fluorine, aluminium ion, to keep tank liquor clear, chelant ties live in Al³⁺And Ti⁴⁺, Difficulty is not really small.When analyzing alkaline etching and oxidation tank liquor, in order to analyze Al³⁺Concentration generally plus potassium fluoride uses F^-Open Al³⁺ With the complex bonds of ligand, aluminium ion concentration is just measured.So in fluotitanic acid and fluorine zirconic acid tank liquor, since fluorine is too high, generally Complex compound and chelate, bond energy is inadequate, is not enough to chelate Al³⁺And Ti⁴⁺, tank liquor is easily muddy.It is available in high F^-Under the conditions of chela Share Al³⁺And Ti⁴⁺Chelating agent, selection is limited in scope.

By many experiments, following several big serial chelating agents can be selected:

(1), acetic acid system, such as triethanolamine, ethylenediamine tetra-acetic acid etc.；

(2), phosphate, such as sodium tripolyphosphate, sodium pyrophosphate, sodium metaphosphate, aminotrimethylene phosphate (ATMP)；

(3), phosphate carboxylic serials, such as phosphonobutane tricarboxylic acid (PBTCA).

The selection of chelating agent, it is necessary to meet four requirements: first is that effectively chelated mineral cation, it is dry to enable aluminum alloy to surface Only, no pollen, does not corrode；Second is that tank liquor is clear, do not decompose, does not precipitate；Third is that film forming can be actively engaged in, avoid chelating agent blunt Change building up for slot, influences passivation ability；Fourth is that meeting requirements of the national standard after passivation.

Film forming agent, the present invention refer to moieties participate in film forming, the organic group that is partially free on passivation film surface can be with A kind of medicament that spraying resin mixes.This kind of film forming agent can greatly improve Chromating Film On Zn Deposits, shorten passivation time, reduce passivation temperature Degree enhances passivating film adhesive force.

The present invention is selected by fluotitanic acid, fluorine zirconic acid, chelating agent phosphonobutane tricarboxylic acid (PBTCA), corrosion inhibiter phosphono Butane tricarboxylic acid (PBTCA) and film forming agent phosphonobutane tricarboxylic acid (PBTCA) form chrome-free tanning agent and are newly formulated, chelating agent, Corrosion inhibiter and film forming agent select same component phosphonobutane tricarboxylic acid, are done based on PBTCA special molecular structure (Fig. 3) Ingenious selection out.

In Fig. 3, phosphono and three carboxyls are in electronegativity, and there are three types of functions for this structure tool.1, three carboxyls have superpower Sequestering power, cation can be chelated, solids is avoided to be precipitated, stablize tank liquor；2, three carboxyls and phosphono can be adsorbed on and be in Electropositive aluminum alloy surface is isolated tank liquor using organic moiety, there is superpower corrosion inhibiting ability；3, cation has been chelated PBTCA, can be used as carrier, phosphono can also with positively charged alloy matrix aluminum phosphorization filming, organic moiety on the outside of film, with The spraying resin same sex mixes, and the adhesive force of passivating film can be significantly increased (see Fig. 4).A kind of only component of PBTCA has both inhibition, chela Conjunction and three kinds of functions of phosphorization filming, can greatly improve the passivation ability of chrome-free tanning agent, greatly improve adhesive force, greatly improve slot The stability of liquid, is greatly reduced reagent cost.PBTCA is not easy that it is long-term to be able to maintain tank liquor by other chemical agents or bacterial decomposition Stablize；In addition, phosphonobutane tricarboxylic acid in addition to chelating aluminium ion, titanium ion, zirconium ion, also chelates, shields water for cleaning band The Ca entered²⁺、Mg²⁺Cations are waited, the water for cleaning before and after deactivation slot can replace pure water with tap water, production cost is greatly reduced.

(2) chromium-free deactivation process dynamics

(1)-(6) formula display is passivated dynamic (dynamical) overall process.(1) formula shows that fluotitanic acid and fluorine zirconic acid are ionized into tank liquor 2H⁺+TiF₆ ^2-；(2) formula shows that fluotitanic acid and fluorine zirconic acid root are hydrolyzed into Ti (OH) in tank liquor₃F₃ ^2-+Ti(OH)₂F₄ ^2-+Ti(OH) F₅ ^2-, and discharge 6H⁺+6F^-；(3) formula shows that fluotitanic acid is unstable, is easy to be hydrolyzed into titanium hydroxide, needs to add chelating agent, surely Determine metal cation；(4) formula shows F^-With passivation film reaction, OH is released^-, improve the pH value in tank liquor；(5) formula show aluminium with Ti(OH)₃F₃ ^2-Reaction generates passivation goods and materials Ti, is deposited on aluminum alloy surface, forms film forming matter；(6) formula shows that deactivation slot is molten The aluminium of solution, with the complex status of fluoaluminic acid and hydroxyl fluoaluminic acid, is present in passivating solution under conditions of tank liquor is stablized, and utilizes The chemical bond of fluoaluminic acid participates in forming a film, and in deactivation slot, the dissolution of aluminium and the film forming containing aluminium fluoride carry out simultaneously, avoid aluminium Ion and building up for chelating agent and dead slot.

(3) chromium-free deactivation regulation rule is studied

1), influence of the passivation time to passivation quality

Passivation time directly determines passivation quality.Time is too short, and not exclusively, the time is too long for passivation, and aluminum alloy surface plays ash Seriously, the adhesive force of passivating film is influenced；Passivation time is the embodiment of passivator passivation ability, by temperature, pH value, passivator ingredient With being affected for concentration, additive component and concentration.Under equal conditions, compared with chromic anhydride, fluotitanic acid and fluorine zirconic acid it is blunt Strong three times of change ability or so.That is the passivation time of fluotitanic acid and fluorine zirconic acid is the 1/3 of chromic anhydride.

2), influence of the passivation temperature to passivation quality

Temperature influences chemical reaction velocity, and usually every to increase 10 DEG C of l times of chemical reaction velocities raisings, passivation time can contract It is short by 1 half.According to the passivation test under different temperatures, the changing rule of fluotitanic acid and fluorine zirconic acid passivation quality and temperature can be obtained. When the temperature increases, ion diffusion velocity is accelerated, and hydrolysis rate is accelerated, Ti (OH) in tank liquor₃F₃ ^2-Concentration increase, with aluminium close Gold reaction is accelerated, and the Ti of generation increases, and passivation speed improves.Experiment shows when other Con trolling index are in working range, fluorine titanium The relationship of the passivation temperature and passivation speed of acid and fluorine zirconic acid are as follows: temperature is at 5-10 DEG C, passivation time 180-240s；Temperature exists At 10-15 DEG C, passivation time 120-180；Temperature is at 15-20 DEG C, passivation time 60-120s, and 20 DEG C or more at this moment of temperature When, passivation time can be lower than 60s.

3), influence of the pH value to passivation quality

Influence according to pH value to passivation quality is tested, and can obtain pH value to the affecting laws of passivation quality.With tank liquor pH value Rising, press (2) formula, fluotitanic acid and fluorine zirconic acid hydrolysis increase, be passivated Quality advance；But pH value is too high, and Surface of profile is easy to produce Raw lime, this is primarily due to fluotitanic acid and fluorine zirconic acid loss of stability, a large amount of to hydrolyze；PH value is too low, is not enough to cause fluorine titanium Acid and fluorine zirconic acid hydrolysis, are not achieved passivation effect.PH value is to the chemistry that the action principle of passivation is by (2) (3) (4) (5) (6) formula Reaction, the hydrolysis of fluotitanic acid and fluorine zirconic acid, the Ti deposition aluminium surface of generation achieve the purpose that passivation, and Ti deposition number Directly affect the effect of passivation.PH value deposition of Ti between 2.5-4.5 is more, can reach the purpose of passivation, and pH value exists Passivation effect is best when 3.0-4.0 or so, and the very good control of acidity at this moment, just flat in the hydrolysis of fluotitanic acid and fluorine zirconic acid Weighing apparatus section, pH value are sufficiently stable.

4), the influence of fluotitanic acid and fluorine zirconic acid concentration to passivation quality

The present invention selects fluotitanic acid and fluorine zirconic acid as main deactivation matter, and fluotitanic acid and fluorine zirconic acid root are to be passivated in tank liquor most One of main ion.Passivation is to be replaced by fluotitanic acid and fluorine zirconic acid root by aluminium, be deposited on what aluminium surface was achieved, blunt Compound matter is mainly made of Ti or Zr, is the synthesis result reacted by (1)-(6) formula.Ti and Zr deposition velocity directly affects passivation Speed, fluotitanic acid and fluorine zirconic acid content influence passivation quality very big.The experimental results showed that fluotitanic acid and fluorine zirconic acid (50wt.%) Concentration controls between 1.25-2.0g/L respectively.

5), influence of the PBTCA density of corrosion inhibitor to passivation quality

PBTCA corrosion inhibiter of the present invention is adsorbed on positively charged aluminum alloy surface by electronegative three carboxyl and phosphono, Tank liquor is isolated, slows down corrosion.Under fluotitanic acid and fluorine zirconic acid passivation system, pH value operation interval 2.5-4.5, slant acidity is pressed (1)- (6) formula, low ph value are conducive to Al₂O₃With F^-Reaction generates AlF₆ ^3-, Al (OH) F₅ ^3-, Al (OH)₂F₄ ^3-, content reaches certain When value, association, hydrolysis and concentration occur for interionic, are finally translated into stable phase complexing aluminum fluoride Al₂(OH)₃F₃；In aluminium alloy table Face, Al₂(OH)₃F₃It is pollen；In tank liquor, Al₂(OH)₃F₃It is muddy object.So the molten aluminum amount of tank liquor is too big, on aluminium alloy is easy Powder, the easily muddy dead slot of tank liquor.The addition of PBTCA corrosion inhibiter reduces molten aluminum amount, extends precisely in order to protecting the not upper powder of aluminium alloy Tank liquor service life.By experimental result, the concentration ranges of PBTCA corrosion inhibiter are 1.25-2.0g/L.

6), influence of the chelating agent concentrations to passivation quality

Chelating agent of the present invention selects phosphonobutane tricarboxylic acid (PBTCA), with its powerful chelating bond energy, stablizes Ti⁴⁺With Al³⁺, it is ensured that tank liquor is not muddy, the not upper powder of aluminium alloy.By (1)-(6) formula, when pH is increased, it is easy to generate Ti (OH)₄And Al₂(OH)₃F₃.These goods and materials, if generating in aluminum alloy surface, as powder；If generating in tank liquor, as muddy object.PBTCA chelating agent It is added, improves Ti (OH)₄And Al₂(OH)₃F₃Generation threshold, aluminium alloy is not easy powder, and tank liquor is not easy muddiness.In addition, Carboxyl and phosphono in PBTCA chelating agent is negatively charged, can be adsorbed on positively charged passivating film, plays corrosion inhibiter, reduces aluminium The meltage of alloy.Experiment shows that appropriate PBTCA chelating agent concentrations are 1.25-2.0g/L.

7), influence of the special film forming agent concentration to passivation quality

Film forming agent of the present invention selects phosphonobutane tricarboxylic acid (PBTCA), by its powerful chelating bond energy, chelates Ti⁴⁺ And Al³⁺, it is ensured that tank liquor is not muddy, the not upper powder of aluminium alloy；Using its electronegative phosphono, chelating body is combined into passivating film, Phosphatization-passivating film is formed, metal ion and PBTCA in deactivation slot are consumed, avoids these ingredient excessive accumulations and dead slot.Phosphorus The formation of change-passivating film greatly improves passivation ability, shortens passivation time, reduces passivation temperature, widens passivation pH value section. Chelating, inhibition, film forming select same component PBTCA, are significant technology innovations of the invention, have both the PBTCA of three kinds of functions Total amount is 2.5-4.0g/L, by fluotitanic acid: fluorine zirconic acid: PBTCA=0.5:0.5:1 weight ratio prepares chrome-free tanning agent, will be passivated Agent concentration 5.0-8.0g/L, as Con trolling index, production requirement can be met.

8), influence of the foreign ion to passivation quality

In process of production, washing constantly brings foreign ion into, causes the accumulation of impurity, such as Na⁺、K⁺、Ca²⁺、Mg²⁺Equal sun Ion increases, and the consumption of PBTCA chelating agent is accelerated.Therefore, it is most important to hold cleaning pass.In addition, ammonia can be used when tank liquor pH is too low Water adjusts pH value to 3.5 or so, not adjusted with sodium hydroxide, can effectively prevent Na in this way⁺Addition, consume PBTCA chela Mixture.Select fluotitanic acid and fluorine zirconic acid rather than fluotitanic acid and potassium fluorozirconate as main passivation ingredient, key reason is K⁺ Consumption to PBTCA chelating agent.

There are many factor for influencing aluminium alloy non-chromium passivation quality, mainly have fluotitanic acid and fluorine zirconic acid concentration, density of corrosion inhibitor, Chelating agent concentrations and film forming agent concentration, this five factors are the key that determine aluminium alloy passivation quality；The pH value of tank liquor, temperature and Passivation time is an important factor for influencing aluminium alloy passivation quality；And improving the cleanliness of tank liquor, reducing the content of impurity is aluminium The important guarantee of alloy passivation quality.

(4) chromium-free deactivation is newly formulated new process

(7) formula gives the technological parameter of chromic anhydride passivating solution, is being to be passivated the nothing of main component with fluotitanic acid and fluorine zirconic acid Under the new formulation condition of chromium passivating agent, technological parameter is varied widely:

H₂TiF₆(50wt.%) 1.25-2.0g/L

H₂ZrF₆(50wt.%) 1.25-2.0g/L

PBTCA (50wt.%) 2.5-4.0g/L (8)

5-35 DEG C of passivation temperature

Passivation speed 30-120s

Tank liquor pH 2.5-4.5

F^-Concentration is that fluotitanic acid and fluorine zirconic acid are included, is not limited specially

Compare (7) and (8) formula, the enhancing of PBTCA post-passivation ability is added, passivation temperature lower limit is widened by 25 DEG C to 5 DEG C, blunt Change speed to improve to 120s, tank liquor pH is improved by 1.8-2.2 to 2.5-4.5, and range is widened.Due to being chelated containing a large amount of PBTCA Agent, new formula is not high to water quality requirement, and washing, fluting use tap water, contained Ca²⁺、Mg²⁺It can be complete by PBTCA chelating agent Full-shield.In fluotitanic acid and fluorine zirconic acid molecular structure, fluorine content is excessively high, for this purpose, corrosion inhibiter PBTCA is specially arranged in formula, drops The corrosive power of low fluorine, therefore F^-By (2) formula, automatic hydrolysis balance, without detecting and controlling.Zirconium in fluotitanic acid and fluorine zirconic acid tank liquor It is not with Zr with titanium⁴⁺、Ti⁴⁺In the presence of, but with Ti (OH)₃F₃ ^2-+Ti(OH)₂F₄ ^2-+Ti(OH)F₅ ^2-In the presence of (zirconium is analogized), therefore select Use H₂TiF₆(50wt.%) and H₂ZrF₆Each 1.25-2.0g/L of (50wt.%) concentration is as detection control interval.

Two, aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration

Degreasing tank generally selects sulfuric acid, phosphoric acid, nitric acid, hydrochloric acid, hydrofluoric acid, sodium fluoride, ammonium fluoride, ammonium acid fluoride, lemon Acid, sorbierite, glycerol, ethylene glycol and proper amount of surfactant oil removing.When aluminium oil removing, aluminium is in the degreaser containing mixed acid and fluorine The middle following chemical reaction of generation:

1, natural oxide film is removed

Al₂O₃+6H⁺=2Al³⁺+3H₂O (9)

2, molten aluminium, deburring

2Al+6H⁺=2Al³⁺+3H₂↑ (10)

3, aluminium is by fluorine complexing, stable degreaser

6Al³⁺+21F^-+15H₂O=AlF₆ ^3-+Al(OH)F₅ ^3-+Al(OH)₂F₄ ^3-+Al(OH)₃F₃ ^3-+Al(OH)₄F₂ ^3-+Al (OH)₅F^3-+15H⁺ (11)

4, it is passivated aluminium surface, reduces molten aluminium

2Al+3NO₃ ^-=Al₂O₃+3NO₂ ^- (12)

By (9) (10) two formula, acid concentration is higher, and molten aluminium speed is faster；By (11) (12) formula, aluminium material surface passivation, molten aluminium Amount is restricted, and the pressure that crystal is precipitated in tank liquor is reduced；The presence of high concentration nitric acid simultaneously, aluminium is with fluoaluminic acid and hydroxyl fluoaluminic acid Form exist, rather than with aluminum fluoride or aluminum phosphate Precipitation, tank liquor is stablized, and does not decompose, non-scaling, can longtime running.

By the chromium-free deactivation tank liquor formula that (8) formula is selected, the tank liquor is kept to run steadily in the long term, the formula pair of degreasing tank The influence of chromium-free deactivation Stability of Bath Solution be can not ignore.When mass production, after aluminium alloy oil removing, generally flows and wash through twice, into Enter the passivation of chromium-free deactivation slot, part degreaser brings chromium-free deactivation slot into, influences passivation ability and tank liquor is stablized.It, must in degreasing tank Those must be rejected and endanger chromium-free deactivation ability to work and the stable component of tank liquor, it is ensured that oil removing and passivation operation steady in a long-term.? Optionally except in oil ingredient, sulfuric acid, hydrochloric acid, phosphoric acid and nitric acid influence the ability to work of chromium-free deactivation slot, it is necessary to reject；Sodium ion The fluorine ion of chromium-free deactivation slot is consumed, generates ice crystal precipitating, it is necessary to reject；Citric acid, sorbierite, glycerol, ethylene glycol are easy It is bacterially decomposed, keeps chromium-free deactivation slot muddiness smelly, it is necessary to reject；Degreasing tank ammonium ion cannot too, and aluminium material surface is easy to hang Ash rejects ammonium acid fluoride；The adhesive force of Surfactant Effect chromium-free deactivation material, it is necessary to reject；In addition, degreasing tank dissolution is a large amount of Aluminium, under conditions of rejecting nitric acid, AlF easy to form₃Precipitating；It is needed by (11 formula) in order to stablize hydroxyl fluoaluminic acid series Chelating agent is added, the generation of aluminum fluoride is blocked；In order to reduce molten aluminum amount, degreasing tank ability to work is kept, it is necessary to add corrosion inhibiter. Integrated suites experimental result simplifies formula to the compatible degreasing tank of chromium-free deactivation slot are as follows:

HF (50wt.%) 10-20g/L

PBTCA (50wt.%) 3.5-7g/L (13)

Time 3-6 minute

Temperature room temperature

By (8) formula, HF and PBTCA contained by (13) formula is completely compatible to chromium-free deactivation slot, the oil removing brought into through rinsing bowl at Point, it will not influence the ability to work and stability of deactivation slot completely.(13) in formula, HF is good etching agent, dissolves aluminium alloy The natural oxide film on surface, deburring, it is ensured that certain etch amount；PBTCA is acidity, it is possible to provide certain acidity value increases Oil removing ability；PBTCA is chelating agent, chelates aluminium ion, blocks the generation of aluminum fluoride, it is ensured that degreasing tank longtime running；Meanwhile PBTCA or corrosion inhibiter, electronegative three carboxyl and phosphono are adsorbed on positively charged aluminum alloy surface, and tank liquor is isolated, Slow down corrosion.PBTCA is used for degreasing tank, can perform to its corrosion inhibiting ability and sequestering power ultimate attainment.

Three, aluminium alloy spraying degreasing tank configures the compatible slot position of chromium-free deactivation slot medicament

Referring to traditional spraying line laying out slot positions, aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission of the present invention Configuration is as shown in Figure 5.

In Fig. 5,1# degreasing tank is the degreasing tank of (13) formula setting, and 4# chromium-free deactivation slot is the chromium-free deactivation of (8) formula setting Slot, 1# degreasing tank are completely compatible to 4# chromium-free deactivation slot；2#, 3# are non-mobile water washing trough, in 1# degreasing tank to 4# chromium-free deactivation On the basis of slot medicament is compatible, the present invention by two slot water for cleaning differential concatenations, the tap water (not being pure water) of supplement from 3# not It flows rinsing bowl to enter, through 3# → 2# → 1# slot reverse flow, reduces water for cleaning, recycle degreaser；The present invention drains 5# The chrome-free tanning agent that slot is collected is pumped into 4# chromium-free deactivation slot with pump, recycles chrome-free tanning agent, reduces production and environmentally friendly cost.

Aluminium alloy rises and hangs drip 30 seconds after the oil removing in 3-6 minutes of 1# degreasing tank, into 2# non-mobile water washing trough, cleans 1 point Clock drip 30 seconds, into 3# non-mobile water washing trough, cleans 1 minute, drip 30 seconds；Into 4# chromium-free deactivation slot, it is passivated 30-240 Second, it rises and hangs drip 30 seconds, drain slot into 5# and drain, complete spraying chromium-free deactivation pretreatment.4# chromium-free deactivation slot contains chelating agent PBTCA, maskable Ca²⁺、Mg²⁺Ion, therefore the washing trough of 2# non-mobile water, 3# non-mobile water washing trough ejected wash water all use tap water, Rather than the pure water that conventional method is all, production cost is greatly reduced.The ingredient of 1# degreasing tank is completely simultaneous to 4# chromium-free deactivation slot Hold, 3# non-mobile water washing trough bring into 4# chromium-free deactivation slot except oil component, do not influence the ability to work of 4# chromium-free deactivation slot.1# is removed Hydrofluoric acid, the PBTCA of oil groove addition, fluotitanic acid, fluorine zirconic acid, the PBTCA of 4# chromium-free deactivation slot addition are film-forming components, cleaning After water zero discharge, 4# chromium-free deactivation slot absolutely not due to individual components progressive poisoning dead slot risk；The aluminium ion of dissolution, originally The Ca that water is brought into²⁺、Mg²⁺Ion is acted on by the chelating and bridge joint of PBTCA, through phosphono phosphatization into passivating film, also without accumulation The risk of poisoning.The passivating film that 4# chromium-free deactivation slot generates is that fluotitanic acid and fluorine zirconic acid passivation, PBTCA phosphono phosphatization are formed Composite membrane, on the outside of phosphating coat, butane group contained by PBTCA, mix with the powder spray resin same sex, the attached of passivating film be significantly increased Put forth effort, therefore aluminium is after the passivation of 4# slot, Non-water washing, is drained after slot drains through 5#, complete spraying pretreatment, meet national standard detection and want It asks.5# drains the passivating solution of slot collection, is recycled to 4# chromium-free deactivation slot through pump, and it is water-saving substantially to save medicine.

1# degreasing tank degreaser recovery method: after dry aluminium enters 1# degreasing tank oil removing, part is taken out of from 1# degreasing tank Degreaser, 1# degreasing tank have liquid level loss, need moisturizing.No. three valves 3 are opened, tap water enters 3# non-mobile water washing trough, through four Number valve 4 enters the washing trough of 2# non-mobile water, then enters 1# degreasing tanks through No. five valves 5, completes the moisturizing of 1# degreasing tank and medicament recycling.

4# chromium-free deactivation slot chrome-free tanning agent recovery method: opening No.1 valve 1 and No. two valves 2, opens pump, 5# is drained slot The chrome-free tanning agent of collection is pumped into 4# chromium-free deactivation slot, completes chrome-free tanning agent recycling.

By the configuration of Fig. 5, it can be ensured that spraying pre-processes production run steady in a long-term.

Aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration of the invention, including 1# degreasing tank, 2# Non-mobile water washing trough, the washing trough of 3# non-mobile water, 4# chromium-free deactivation slot and 5# drain slot, and 1# is successively passed through in aluminium alloy spraying pretreatment Degreasing tank, the washing trough of 2# non-mobile water, the washing trough of 3# non-mobile water, 4# chromium-free deactivation slot and 5# drain slot；The 1# degreasing tank, 2# are not Rinsing bowl and 3# non-mobile water washing trough differential concatenation are flowed, is used for the moisturizing of 1# degreasing tank and recycling degreaser；The 4# Chrome-free Deactivation slot and 5# are drained and are provided with pump between slot, and pump is pumped into 4# chromium-free deactivation slot for 5# to be drained the tank liquor in slot；3# does not flow Dynamic rinsing bowl is connected with running water pipe, the running water pipe, for making tap water enter 3# non-mobile water washing trough supplement liquid level.

The chemical constituent of degreaser includes hydrofluoric acid and PBTCA, hydrofluoric acid (50wt.%): PBTCA (50wt.%)=3: 1, degreaser concentration 20-30g/L, acidity value 0.5-1.0 equivalent；In degreaser, hydrofluoric acid (50wt.%) concentration is 15- 22.5g/L, PBTCA (50wt.%) concentration are 5-7.5g/L.

The chemical constituent of chrome-free tanning agent includes fluotitanic acid, fluorine zirconic acid and PBTCA, fluotitanic acid (50wt.%): fluorine zirconic acid (50wt.%): PBTCA (50wt.%)=0.5:0.5:1, passivating agent concentration 5.0-8.0g/L.In chrome-free tanning agent, fluorine titanium Sour (50wt.%) concentration is 1.25-2.0g/L, and the concentration of fluorine zirconic acid (50wt.%) is 1.25-2.0g/L, PBTCA (50wt.%) concentration is 2.5-4.0g/L；

1# degreasing tank is compatible to 4# chromium-free deactivation slot medicament, when the ingredient of degreaser brings 4# chromium-free deactivation slot by aluminium alloy Afterwards, 4# chromium-free deactivation slot is stable.

In 1# degreasing tank and 4# chromium-free deactivation slot: PBTCA is adsorbed as corrosion inhibiter and chelating agent, phosphono and three carboxyls It reduces molten aluminum amount for tank liquor, inhibition aluminium surface to be isolated in aluminum alloy surface, chelating aluminium ion, stablize tank liquor.In 4# Chrome-free In deactivation slot, as phosphorization filming agent, the metal ion for that will chelate is combined into passivating film PBTCA.

Preferably, the chromium-free deactivation temperature of 4# chromium-free deactivation slot is 5-35 DEG C.Chrome-free of the aluminium alloy in 4# chromium-free deactivation slot Passivation time is 30-120 seconds.In 4# chromium-free deactivation slot, the pH value operation interval of 4# chromium-free deactivation slot is 2.5-4.5.4# without The pH value adjusting of chromium passivating slot is carried out by hydrofluoric acid and ammonium hydroxide.

Embodiment 1

The washing trough of 2# non-mobile water, 3# non-mobile water washing trough are cleaned 60 seconds by tap water, are produced within drip 30 seconds.

Aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration of the invention, including 1# degreasing tank, 2# Non-mobile water washing trough, the washing trough of 3# non-mobile water, 4# chromium-free deactivation slot and 5# drain slot, and aluminium alloy successively passes through 1# degreasing tank, 2# Non-mobile water washing trough, the washing trough of 3# non-mobile water, 4# chromium-free deactivation slot and 5# drain slot；The 1# degreasing tank, 2# non-mobile water are washed Slot and 3# non-mobile water washing trough differential concatenation are used for 1# degreasing tank moisturizing；The 4# chromium-free deactivation slot and 5# are drained between slot It is provided with pump, pump is pumped into 4# chromium-free deactivation slot for 5# to be drained the tank liquor in slot；3# non-mobile water washing trough is connected with tap water Pipe, the running water pipe is for making tap water enter 3# non-mobile water washing trough fluid infusion.

1# degreasing tank Con trolling index are as follows: HF (50wt.%) 18g/L；PBTCA (50wt.%) 6g/L；Time 4 minutes；Temperature Room temperature.

4# chromium-free deactivation slot Con trolling index are as follows: fluotitanic acid (50wt.%) concentration 1.5g/L；Fluorine zirconic acid (50wt.%) concentration 1.5g/L；PBTCA corrosion inhibiter chelating agent concentrations 3.0g/L；Passivation time 150 seconds；Temperature room temperature；PH value 3.5.

It is produced by above-mentioned Con trolling index, spraying material can meet national standard testing requirements.Increase 1# degreasing tank PBTCA concentration To 7.5g/L, degreasing tank reaction speed slows down, and 1#, 2#, 3# slot are apparent；Degreasing tank PBTCA concentration is reduced to 5g/L, degreasing tank Reaction speed is accelerated, and 1# slot is clear, and 2#, 3# slot are slightly muddy, has a small amount of aluminum fluoride to decompose and is precipitated.Block 1# degreasing tank, 2#, 3# The condition that rinsing bowl aluminum fluoride is precipitated is HF (50wt.%): PBTCA (50wt.%)≤3:1 (weight ratio)；In view of medicament at Sheet and the influence to 4# chromium-free deactivation slot, take HF (50wt.%): PBTCA (50wt.%)=3:1, prepare oil removing by this weight ratio Agent, the production Con trolling index by degreaser concentration 20-30g/L, as 1# slot.

In 1# degreasing tank, when PBTCA (50wt.%) concentration is 7.5g/L, HF (50wt.%) 22.5g/L；Work as PBTCA When (50wt.%) concentration is 5g/L, HF (50wt.%) 15g/L.In degreasing tank and chromium-free deactivation slot: PBTCA is as corrosion inhibiter And chelating agent, phosphono and three carboxyls are adsorbed on aluminum alloy surface, for tank liquor to be isolated, reduce molten aluminum amount, chelating aluminium ion, Stablize tank liquor.In chromium-free deactivation slot, as phosphorization filming agent, the metal ion for that will chelate is combined into passivating film PBTCA. The pH value adjusting of chromium-free deactivation slot is carried out by hydrofluoric acid and ammonium hydroxide.

1# degreasing tank degreaser recovery method: after dry aluminium enters 1# degreasing tank oil removing, part is taken out of from 1# degreasing tank Degreaser, 1# degreasing tank have liquid level loss, need moisturizing.No. three valves 3 are opened, tap water enters 3# non-mobile water washing trough, through four Number valve 4 enters the washing trough of 2# non-mobile water, enters 1# degreasing tanks through No. five valves 5, completes the moisturizing of 1# degreasing tank and medicament recycling.

4# chromium-free deactivation slot chrome-free tanning agent recovery method: opening No.1 valve 1 and No. two valves 2, opens pump 1,5# is drained The chrome-free tanning agent that slot is collected is pumped into 4# chromium-free deactivation slot, completes chrome-free tanning agent recycling.

Embodiment 2

The blunting line and embodiment 1 of aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration of the invention It is essentially identical, the difference is that, increase 4# chromium-free deactivation slot PBTCA concentration to 4.5g/L, it is qualified to spray the detection of material national standard；Subtract Few 4# chromium-free deactivation slot PBTCA concentration sprays material national standard detection qualification, 4# slot is slightly muddy, there is a small amount of fluoride to 2.0g/L It decomposes and is precipitated.Not only it had been able to satisfy national standard, reduced cost, but also the condition that 4# chromium-free deactivation slot fluoride can be blocked to be precipitated is (fluorine Metatitanic acid (50wt.%)+fluorine zirconic acid (50wt.%)): PBTCA (50wt.%)=1:1 (weight ratio, wherein fluotitanic acid and fluorine zirconic acid Weight ratio is also 1:1)；In view of the stability of reagent cost and 4# chromium-free deactivation slot, by fluotitanic acid (50wt.%): fluorine zirconic acid (50wt.%): PBTCA (50wt.%)=0.5:0.5:1 weight ratio prepares chrome-free tanning agent, by passivating solution concentration 5.0-8.0g/ L, the production Con trolling index as 4# slot.

In 4# chromium-free deactivation slot, when the concentration of PBTCA (50wt.%) is 4.0g/L, the concentration of fluotitanic acid (50wt.%) For 2.0g/L, the concentration of fluorine zirconic acid (50wt.%) is 2.0g/L；When the concentration of PBTCA (50wt.%) is 2.5g/L, fluorine titanium The concentration of sour (50wt.%) is 1.25g/L, and the concentration of fluorine zirconic acid (50wt.%) is 1.25g/L.

Embodiment 3

The blunting line and embodiment 1 of aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration of the invention It is essentially identical, the difference is that, increase 4# chromium-free deactivation slot passivation time to 240 seconds, national standard detection is qualified；Reduce 4# Chrome-free For deactivation slot passivation time to 20 seconds, national standard detection was unqualified once in a while；Passivation time, but not below 30 can suitably be shortened under room temperature Second；Passivation time can be appropriately extended under low temperature, but do not exceed 240 seconds.

Embodiment 4

The blunting line and embodiment 1 of aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration of the invention It is essentially identical, the difference is that, increase 4# chromium-free deactivation bath temperature degree to 35 DEG C, national standard detection is qualified；Reduce 4# chromium-free deactivation For bath temperature degree to 5 DEG C, national standard detection is unqualified once in a while；At 15-35 DEG C, deactivation slot fluotitanic acid (50wt.%) concentration 1.25-2.0g/ L, fluorine zirconic acid (50wt.%) concentration 1.25-2.0g/L, PBTCA corrosion inhibiter chelating agent concentrations 2.5-4.0g/L, passivation time are 60-240 seconds, spraying material can meet national standard testing requirements；Under low temperature, at 5-15 DEG C, drug concentration capping, passivation time is also taken The upper limit can satisfy national standard testing requirements.

Embodiment 5

The blunting line and embodiment 1 of aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration of the invention It is essentially identical, the difference is that, 4# chromium-free deactivation slot pH to 4.5 is adjusted with ammonium hydroxide, spraying material national standard detection is qualified；With hydrogen fluorine For acid adjustment 4# chromium-free deactivation slot pH value to 2.5, spraying material national standard detection is qualified；Deactivation slot pH is higher than 4.5, and passivating solution has decomposition to analyse The risk of fluoride out；Passivating solution pH value is lower than 2.5, and molten aluminum amount is too big, and passivating solution equally has the risk decomposed and fluoride is precipitated； The stable pH value control interval of passivating solution is 2.5-4.5.

The technical principle of the invention is described above in combination with a specific embodiment.These descriptions are intended merely to explain of the invention Principle, and shall not be construed in any way as a limitation of the scope of protection of the invention.Based on the explanation herein, the technology of this field Personnel can associate with other specific embodiments of the invention without creative labor, these modes are fallen within Within protection scope of the present invention.

Claims (10)

1. aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration, which is characterized in that including 1# degreasing tank, 2# Non-mobile water washing trough, the washing trough of 3# non-mobile water, 4# chromium-free deactivation slot and 5# drain slot, and 1# is successively passed through in aluminium alloy spraying pretreatment Degreasing tank, the washing trough of 2# non-mobile water, the washing trough of 3# non-mobile water, 4# chromium-free deactivation slot and 5# drain slot；The 1# degreasing tank, 2# are not Rinsing bowl and 3# non-mobile water washing trough differential concatenation are flowed, is used for the moisturizing of 1# degreasing tank and recycling degreaser；The 4# Chrome-free Deactivation slot and 5# are drained and are provided with pump between slot, and the pump is pumped into 4# chromium-free deactivation slot for 5# to be drained the tank liquor in slot；It is whole Chromium-free deactivation line only sets water inlet at No. three valves, does not set discharge outlet, does not drain deslagging；

Contain degreaser in the 1# degreasing tank, the 4# chromium-free deactivation slot has included chrome-free tanning agent；

The chemical constituent of the degreaser includes hydrofluoric acid and PBTCA, hydrofluoric acid (50wt.%): PBTCA (50wt.%)=3: 1, the degreaser concentration 20-30g/L, acidity value 0.5-1.0 equivalent；

The chemical constituent of the chrome-free tanning agent includes fluotitanic acid, fluorine zirconic acid and PBTCA, fluotitanic acid (50wt.%): fluorine zirconic acid (50wt.%): PBTCA (50wt.%)=0.5:0.5:1, the chrome-free tanning agent concentration 5.0-8.0g/L；

The 1# degreasing tank is compatible to 4# chromium-free deactivation slot medicament, when by aluminium alloy to bring 4# Chrome-free into blunt for the ingredient of the degreaser After changing slot, the 4# chromium-free deactivation slot is stable.

2. aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration according to claim 1, feature It is, in the degreaser, hydrofluoric acid (50wt.%) concentration is 15-22.5g/L, and PBTCA (50wt.%) concentration is 5- 7.5g/L。

3. aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration according to claim 1, feature It is, in the chrome-free tanning agent, fluotitanic acid (50wt.%) concentration is 1.25-2.0g/L, fluorine zirconic acid (50wt.%) concentration For 1.25-2.0g/L, PBTCA (50wt.%) concentration is 2.5-4.0g/L.

4. aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration according to claim 1,2 or 3, It is characterized in that, the 3# non-mobile water washing trough is connected with running water pipe, and the running water pipe is not flowed for making tap water enter 3# Dynamic rinsing bowl supplements liquid level.

5. aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration according to claim 1, feature It is, in the 1# degreasing tank and 4# chromium-free deactivation slot: the PBTCA is as corrosion inhibiter, phosphono and the absorption of three carboxyls Delay to corrode, reduce molten aluminum amount, tank liquor is kept to stablize for tank liquor to be isolated in aluminum alloy surface.

6. aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration according to claim 1, feature It is, in the degreasing tank and chromium-free deactivation slot, the PBTCA keeps tank liquor steady as chelating agent, chelated mineral cation It is fixed；In the chromium-free deactivation slot, the PBTCA combines the metal ion of chelating into chromium-free passivating film as phosphorization filming agent, Phosphatization-chromium-free passivating film is formed, metal cation and PBTCA are consumed；The butane group of the phosphorization filming agent PBTCA is combined into powder Last spray coating enhances adhesive force.

7. aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration according to claim 1, feature It is, the chromium-free deactivation temperature of the 4# chromium-free deactivation slot is 5-35 DEG C.

8. aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration according to claim 1, feature It is, the aluminium alloy is 30-120 seconds in the chromium-free deactivation time of the 4# chromium-free deactivation slot.

9. aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration according to claim 1, feature It is, in the 4# chromium-free deactivation slot, the pH value operation interval of the 4# chromium-free deactivation slot is 2.5-4.5.

10. aluminium alloy spraying pretreatment chromium-free deactivation line waste water and dregs zero-emission configuration according to claim 1, feature Be, the 2# non-mobile water washing trough to the 1# degreasing tank be equipped with No. five valves, the 3# non-mobile water washing trough to the 2# not It flows rinsing bowl and is equipped with No. four valves, the 3# non-mobile water washing trough is equipped with No. three valves, and the 5# drains slot and the 4# Chrome-free is blunt The pipeline for changing connection is equipped with No. two valves, pump, No.1 valve；The tap water of supplement enters 3# slot, through 3# → 2# → 1# from No. three valves Degreasing tank reverse flow supplements 1# degreasing tank liquid level, recycles degreaser；The 5# drains slot and reversely goes here and there with 4# chromium-free deactivation slot Connection drains liquid through 5# slot → No.1 valve → pump → No. bis- valve → 4# chromium-free deactivation slot reverse flow, recycles chromium-free passivation liquid；It is whole Chromium-free deactivation line does not set discharge outlet, waste water and dregs zero-emission.