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CA2174169A1 - Process for removing waterborne and oil base paints from water - Google Patents

Process for removing waterborne and oil base paints from water

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Publication number
CA2174169A1
CA2174169A1 CA 2174169 CA2174169A CA2174169A1 CA 2174169 A1 CA2174169 A1 CA 2174169A1 CA 2174169 CA2174169 CA 2174169 CA 2174169 A CA2174169 A CA 2174169A CA 2174169 A1 CA2174169 A1 CA 2174169A1
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Prior art keywords
paint
ppm
spray booth
water
polymer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Abandoned
Application number
CA 2174169
Other languages
French (fr)
Inventor
Howard B. Agree
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Veolia WTS USA Inc
Original Assignee
Betz Laboratories Inc
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Filing date
Publication date
Application filed by Betz Laboratories Inc filed Critical Betz Laboratories Inc
Publication of CA2174169A1 publication Critical patent/CA2174169A1/en
Abandoned legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

A process for detackifying oil base paint and for coagulating and flocculating waterborne paint in water. In the processes a dimethylamine/
ethylenediamine/epichlorohydrin polymer, aluminum chlorohydrate and an alkaline material are added to water to detackify oil base paint and to coagulate and flocculate waterborne paint. The conditioned paint solids can then be removed from the water. The process is particularly useful for removing paint from paint spray booth water.

Description

- 217~169 PROCESS FOR REMOVING WATERBORNE AND
OIL BASE PAINTS FROM WATER

FIELD OF THE INVENTION

The ~r~sen~ invention relates to processes for treating paint wastes and paint oversprays in water. More particularly, the present invention re-lates to a process which employs a polymeric composition and aluminum chJorohydrate to detackify oil base paint and to coagulate and flocculate 5 waterborne paint in water.

BACKGROUND OF THE INVENTION

The spray painting of automobile bodies, truck parts, appliances 10 and other industrial goods is typically carried out in enclosed areas called paint spray booths. These booths act to contain solvent fumes and over-sprayed paint and reduce the chances of dust contamination in order to protect the paint spray booth operators and the painted articles. These booths vary in size, but are somewhat basic in their design and opera-15 tion. A typical booth consists of a work area, back section with misteliminators and a sump.

~ 7~l~9 The articles to be painted generally pass through the work area where an air flow makes oversprayed paint contact water either in the sump or in the spray from the water curtain. The air is scrubbed with the water curtain, passes through mist eliminators and is removed by an ex-5 haust fan. The water from the water curtain, containing the oversprayedpaint, is recirculated.

Even though paint transfer efficiencies have increased through im-proved application technologies, roughly one half of all paint sprayed 10 does not reach its intended article. As a result, significant concenlralions of paint buildup in the system and paint agglomeration can occur. When solventborne paints are used, the resultant mass is a sticky, tacky mater-ial which can plug mist eliminators, shower heads, and even recirculating pumps. When waterborne paints are used, they do not cause the same 15 type of clumping and tackiness problems as are c~ ~sed by solventborne paints. Instead, waterl,o~"e paints remain dispersed in the spray booth water. Failure to remove walerbor"e paints results in increasing COD
(carl,o" oxygen demand) levels, increasing suspended solids, and in-creasing levels of foam. All of these conditions decrease water quality.
20 When water quality decreases, scrubbing efficiency decreases leading to conditions of unchecked paint emissions being discharged into the at-mosphere. Such conditions may also present safety hazards to paint spray booth operators.

It is therefore desirable to treat paint spray booth water systems so as to reduce the agglG,neralion and deposition of oversprayed paint on critical paint spray booth operating parts and to facilitate removal of the entrained paint from the system.

217416~ .

Generally waterborne paints will disperse in an aqueous medium while solventborne paints agglGmerate into a tacky mass and adhere to paint spray booth operating parts. Bec~use of the difrerences in their be-havior in water the chemical treal",ent processes differs for each type of 5 paint. In order to remove waterborne paint from an aqueous medium waterborne paints have been considered as hydrophilic polymeric col-loids which must be rendered hydrophobic. The stability of the colloids in water arises from the surface charge generated from carboxylic aliphatic or aromatic hydroxyl groups on the polymer backbone. The process of 10 destabilizing such solutions is termed coagulAtion. The process whereby the destabilized particles are induced to come together make contact and form large agglo" ,eranls is termed floccul~tion. The floc formed is generally buoyant which facilitates removal of the floc containing the paint solids from the treated water. Solventborne paints are hydrophobic 15 and their treatment has involved partially dispersing the paint particles in the ~gueous medium via an anionic dispersan~. The partially hydrophilic particles can then be lrea(ed to render them non-tacky. This process is referred to as detackification. The detackified paints can then be treated with a flocculant to facilitate their removal.
Due to the differences in the l,eal",ent methods of waterborne paint and oil base paints it is often necessAry to use separate treatments to detackify oil base paint and to co~3~ te and flocculate waterborne paint. Treat",ents which are effective for both detackifying oil base paint 25 and for co~ulAting and floccul~ting waterbor"e paint are highly desirable since they provide paint spray booth operdtor~ with the ability to use a single treatment to remove captured paints from the paint spray booth water.

~1 741 6q Therefore, a need exists for treatments which effectively detackify oil base paints and which also co~gul~tR and floccul~te waterborne paints to form conditioned paint solids which can be removed from paint spray booth water. As used herein the term "conditioned paint solids" is used to 5 mean detackified oil base paint solids and/or coa3ul~ted and flocculated waterborne paint solids.

Thus, it is an object of this invention to provide a process for detackifying oil based paint and for co~gul~ting and flocculating 10 walert,Gr~ ,e paint to facilitate removal of conditioned paint solids from paint spray booth water.

PRIOR ART

Numerous paint detackification and coagulation compositions are known. Paint overspray removal has been achieved with clays, cationic polyelèctrolytes, metal salts, urea, and melamine formaldehyde resins.
For example, U.S. Patent No. 4,637,824 to Pominville discloses a paint spray booth detackifier where the pH of the washwater is adjusted be-20 tween 7 and 12 by an alkali metal silicate. Pominville requires the addi-tion of an amphoteric metal salt and a polydiallyldimethylammonium hal-ide. Mizutani et al., U.S. Patent No. 4,600,513 discloses a paint spray booth detackifier consisting of an alkali metal zincate added to the wash-water along with a cationic polyamine including polycondensates of poly-25 ethylene glycol/hexa"~ethylenediamine, ethylenediamine/ethylenedichlo-ride and a"~monia/ethylenedichloride, etc. Also included are polyethyl-ene polyamine; polycGndensates having a molecular weight of at least 1000 of epichlorohydrin and precondensates of polyalkylene polyamines and polyoxyalkylene glycol chlorides; and condensation products of ~ ~ 74 ~ -6~

hexamethylene diamine, polyethylene glycol, epichlorohydrin and 1,4-dichloro-2-butene. U.S. Patent No. 5,060,682 to Merrell discloses a process for detackifying paint cG,nprising forming stable colloid solutions consisting of weakly ele(A,opositive metals. The metals are activated by 5 various anionic or cationic polymers including condensation products of dimethylamine/epichlorohydrin or polydiallyldimethylammonium chloride or blends thereof.

U.S. Patent No. 5,073,205 to Morse discloses an improved method 1 0 for detackifying over:jprayed paint, l~c~uer or enamel entrained in paint spray booth water comprising maintaining a small amount of N-methylo-acrylamide copolymer with methyldiallylamine in the water. Also disclos-ed is the use of a polymer flocculant to promote formation of a buoyant floc to facilitate the removal of paint solids.
U.S. Patent No. 5,143,624 to Morse discloses that poly (diallyl-amine) blended with poly (N-methylolacrylamide) effectively detackifies over-spray paint in the circulating water of a wet paint spray booth. After detackification, the dispersed paint is flocculated with hydrolyzed poly-20 acrylamide and the waste paint is removed. Morse also discloses thatboth solvent-based and water-based paints can be detackified, floccu-lated and removed by the process and that alkalinity, particularly carbon-ate alkalinity, ~ssists in floating the flocculated paint particles to the sur-face of the water system treated.

217~169 U.S. Patent 4,440,647 to Puchalski discloses compositions and methods for treating water containing water based and oil based paints - using a combination of a water dispersible polyamide-epichlorohydrin resin, a water dispersible ethylene dichloride-hexamethylenediamine 5 condensation polymer, and an amphoteric metal salt.

U.S. Patent 5,250,189 to Rey discloses a method for treating circu-lating water containing waterborne paint with aluminum salts, including aluminum chlorohydrate, and a floccu'~nt to remove sludge from the 1 0 water.

U.S. Patent 5,147,557 to Purnell discloses a process for the de-tackification and co~gl ~'-tion of oversprayed waterborne-paint and mixed waterborne and oil based paint particles in the water collection system of 15 a paint spray booth comprising adding a unitary blend of an inorganic an-ion and a cationic polymer. The sodium, potassium and ammonium salts of metal alu",inate (A102-) are among the disclosed sources of inorganic anions and a cG"clensation product of dimethylamine/ethylene diamine/
epichlorohydrin is among the disclosed cationic polymers.
SUMMARY OF THE INVENTION

To achieve the foregoing objects, the present invention provides a process for detackifying oil base paint and for coagulating and flocculat-25 ing waterborne paint in paint spray booth water. The process consistsessentially of adding to the paint spray booth water dimethylamine/ethyl-enediamine/epichlorohydrin polymer, aluminum chlorohydrate and an alkaline material selected from the group consisting of sodium hydroxide, ~174~q potassium hydroxide and sodium silicate. The polymer, aluminum chloro-hydrate and alkaline material is added in an amount sufficient to detackify oil base paint and to co~gul~te and floccul~te waterborne paint solids.
The conditioned paint solids can then be removed from the paint spray 5 booth water.

When only waterborne paint is in the paint spray booth water, the addition of an alkaline material may be optional depending on the particu-lar waterborne paint solid present in the paint spray booth water.
DETAILED DESCRIPTION OF THE INVENTION

The present inventor has discovered that dimethylamine/ethylene-diamine/epichlorohydrin (DMA/EDA/EPI) polymer, aluminum chlorohy-15 drate and an alkaline material, when added to water containing oil basepaint effectively detackifies oil base paint. The inventor has also discov-ered that a DMA/EDA/EPI polymer, aluminum chlorohydrate and option-ally an alkaline material effectively co~glJ~^tes and flocculates waterborne paint, when added to water containing waterborne paint.
Detackified oil base paint and coagulated and floccul~ted water-borne paint, termed collectively "conditioned paint solids", can then be easily removed from the water by any conventional method such as by skimming or by filtration. The invention is particularly useful for removing 25 paint from paint spray booth water.

~1 74 ~ 6q The DMA/EDA/EPI polymer (also called 1,2-ethanediamine poly-mer with (chloron)etllyl)oxirane and N-methylmethanamine) is a conden-sation product of dimethylamine plus epichlorohydrin plus ethylene diamine, prepared as taught in U.S. Pat. Re 28808 to Panzer et al., the S disclosure of which is incorporated herein by reference. DMAJEDA/EPI
polymers are available commercially from Betz Laboratories, Inc.

The polymer and aluminum chlorohydrate can be added sepa-rately to paint spray booth water or mixed together with a water carrier 10 and then added to the paint spray booth water. When water is used to mix polymer and aluminum chlorohydrate, the water can make up to 30%
by weight of the mixture. An alkaline material activator selected from the group consisting of sodium hydroxide, potassium hydroxide and sodium silicate can also be added to the polymer and aluminum chlorohydrate 15 mixture or added directly to the paint spray booth water as an ionicity source.

The prefer,ed ratio range of polymer to aluminum chlorohydrate is from about O.S to 1 to about 1 to 0.5 and the most preferred ratio is about 20 1 to1.

The amount of polymer and aluminum chlorohydrate (absent carrier) effective to coagulate and to floccul-te waterborne paint is from about 50 ppm to about 500 ppm of polymer and from about 50 ppm to 25 about 500 ppm of aluminum chlorohydrate.

21 741 bq The amount of polymer and aluminum chlorohydrate (absent a carrier) effective to detackify oil base paint is from about 50 ppm to about 500 ppm of polymer and from about 50 ppm to about 500 ppm of aluminum chlorohydrate.

When an activator is utilized the amount of activator added to paint spray booth water is up to about 2000 ppm and most preferably from about 1000 ppm to about 1600 ppm.

In the preferred embodiment of the invention a water carrier is used to mix the polymer and aluminum chlorohydrate. In the most pre-ferred embodiment of the invention a 35% by weight dimethylamine/
ethylenediamine/epichlorohydrin polymer, 35% by weight aluminum chlorohydrate and 30% by weight water mixture, in an amount of from about 250 ppm to 1000 ppm, and sodium hydroxide, potassium hydroxide or sodium silicate, in an amount of up to 1600 ppm, are added to paint spray booth water to produce conditioned paint solids in the paint spray booth water. The conditioned paint solids can then be removed from the paint spray booth water by any known removal method.
In order to show the efficacy of using the invention compositions to detackify oil base paint and to co~g~ te and flocculate waterborne paint, various tests were performed. The results are presented herein for pur-poses of illustration and not limitation.

ExamPles Jar Testin~ Procedure A standard jar test procedure is used to determine the functional 5 dosage levels and proper combinations of polymeric compositions and activator required to detackify, and coagul^te and flocculate paint. The general procedure is to add 100 milliliters (ml) of tap water to a 120 ml jar. The polymeric composition, activator and optionally a flotation poly-mer are added (either premixed or fed separately), and the bottle is 10 capped and shaken to mix the contents. One milliliter of a paint (oil based or waterborne) is then added to the jar. After vigorous shaking for 30 secG, Ids a wooden tongue depressor is immersed in the solution and then removed for examination. The following guidelines are used for evaluating the detackification performance of the treatment.
Kill Ratino. Definition Paint forms large tacky globules and/or coating which adheres to the e)~osed surfaces of the jar and tongue depressor.
2 Paint forms agglo",er~es which are slightly tacky to touch, or upon crushing. Paint sludge coats the tongue depressor.
3 Paint forms granular flocs which adhere to less than 10% of the exposed surface area of the jar or depressor. Sludge may be smeary, but not tacky.
4 Paint forms particles, some of which appear as specks on less than 1% of the exrosed sur~ace area of the jar or depressor. Sludge is neither smeary nor tacky.

Paint forms particles which do not adhere to the exposed surfaces of the jar or depressor. The paint sludge may float, sink, or be dispersed in the water.

Where "+" indicates a rating between the number shown with the "+" and the next highest number and "-" indicates a rating between the number shown with the "-" and the next lowest number.

Water clarity was judged on a scale of 1 to 5, where "1" was poor/
10 opaque and "5" was excellenVsubslanlially clear.

Water ClaritY Deterrnination To determine a rating of water clarity a black "X" is marked on the 15 base of a standard glass 100 mL graduated cylinder. The jar test sample (including paint, treatment chemicals and sludge) is then added to the gradll~ted cylinder. The solution is added until the "X" can no longer be seen. The following scale is then used to rate the water clarity.

20 Ratina Definition Opaque - cannot view "X" at 0.1 mL - 5 mL
2 Cannot view "X" at 6 mL - 25 mL
3 Cannot view "X" at 26 mL - 50 mL
4 Cannot view "X" at 51 mL - 75 mL
Clear, colorless - can view "X" at 100 mL

~1 741 ~9 Example I

Invention Composition A, a mixture containing 35% by weight dimethylamine/ethylenediamine/epichlorohydrin (DMA/EDA/EPI) polymer, 5 35% by weight aluminum chlorohydrate and 30% by weight water was tested against comparative Composition B, a mixture containing 35% by weight, 1,6-hexanediamine polymer with 1,2-dichloroethane, 35% by weight aluminum chlorohydrate and 30% by weight water. Compositions A and B
were used to treat water containing waterborne paints, with and without 10 alkaline activators. The results are shown in Table 1.

TABLE I
Composition Activator- Floc Water Sample Paint Concentration Conce~t~tion Size ClaritY
(ppm) (ppm) 1 Laurence-David A-250 0 large 4 (acrylic) 2 Laurence-David A400 0 large 4/4+
(acrylic) 3 Laurence-David A400 KOH-1000 small 4-(acrylic) 4 Laurence-David A-750 KOH-1000 large 4-(acrylic) 5 Laurence-David A-600 sodium silicate- large 4+
(acrylic) 1000 6 Laurence-David A-750 NaOH; pH=9 large 4/4+
(acrylic) 7 Laurence-David B400 0 large 4/4+
(acrylic) 8 Dupont (acrylic/ A400 0 large 4+
polyester) 13 2174!69 . .

TABLE I (cont'd) CompositionActivator- Floc Water Sample Paint Concentration Concentration Size Clarity (ppm) (ppm) 9 Dupont (acrylic/ A-750 KOH-1000 medium 2+
polyester) Dupont (acrylic/ A-1000 KOH-1000 medium 2+
polyester) 11 Dupont (acrylicl A400 sodium silicate - none polyester) 1000 12 Dupont (acrylic/ A-750 sodium silicate - large 4+
polyester) 1000 13 Dupont (acrylic/ A-750 NaOH; pH=9 none polyester) 14 Dupont (acrylic/ B400 0 none polyester) Dupont (acrylic/ B-750 0 large 4/4+
polyester) 16 Dupont (acrylic/ B-750 KOH-1000 none polyester) 17 Dupont (acrylic/ B-750 sodium silicate - none polyester) 1000 18 Desoto (acrylic) A400 0 none 19 Desoto (acrylic) A-750 0 large 4+
20 Desoto (acrylic) A-400 KOH-1000 none 4+
21 Desoto (acrylic) A-750 KOH-1000 none 22 Desoto(acrylic) A-400 sodium silicate - none 23 Desoto (acrylic) A-750 sodium silicate - none 24 Desoto (acrylic) A-750 NaOH; pH=9 small 2 25 Desoto (acrylic) A-1000 NaOH; pH=9 large 3 26 Desoto(acrylic) B400 0 none 27 Desoto (acrylic) B-750 0 none 28 Desoto (acrylic) B-400 KOH-1000 none 21 7~1 6q TABLE I (cont'd) Composition Activator- Floc Water SamPle Paint Concenl(alion Concenlralion Size Claritv (ppm) (PPm) 29 Desoto (acrylic)B-750 KOH-1000 none 30 Desoto (acrylic)B400 sodium silicate- none 31 Desoto (acrylic)B-750 sodium silicate- none 32 General Polymer A400 0 medium 2 (acrylic) 33 General Polymer A-750 0 medium 2 (acrylic) 34 General Polymer A400 KOH-1000 none (acrylic) 35 General Polymer A-750 KOH-1000 medium 2 (acrylic) 36 General Polymer A-1000 KOH-1000 medium 4+
(acrylic) 37 General Polymer A400 sodiumsilicate- none (acrylic) 1000 38 General Polymer A-750 sodium silicate- small 2 (acrylic) 1000 39 General Polymer A400 NaOH; pH=9 none (acrylic) 40 General Polymer A-750 NaOH; pH=9 large 3 (acrylic) 41 General Polymer B400 0 none (acrylic) 42 General Polymer B-750 0 medium 4/4+
(acrylic) 43 General Polymer B400 KOH-1000 none (acrylic) 217416q TABLE I (cont'd) CompositionActivator- Floc Water SamPlePaint Concenlr~lion Conce"lralion Size ClaritY
(~Pm) (ppm) 44 General Polymer B-750 KOH-1000 none (acrylic) 45 General Polymer B400 sodium silicate- none (acrylic) 1000 46 General Polymer B-750 sodium silicate- none t (acrylic) 1000 47 Spraylat (acrylic) A400 0 none 48 Spraylat(acrylic) A-700 0 none 49 Spraylat (acrylic) A-400 KOH-1000 poor 50 Spraylat (acrylic) A-800 KOH-1000 poor 51 Spraylat (acrylic) A-1000 KOH-1000 small 2 52 Spraylat (acrylic) A400 sodium silicate - poor 53 Spraylat(acrylic) A400 sodiumsilicate- small 4+

54 Spraylat(acrylic) A400 NaOH; pH=9 poor 2 55 Spraylat (acrylic) A400 0 none 56 Spraylat (acrylic) B-750 0 none 57 Spraylat (acrylic) B-750 KOH-1000 small 4 58 Spraylat(acrylic) B-800 KOH-1000 small 4 59 Spraylat(acrylic) B400 sodiumsilicate- small 4~

Table I shows that the invention Composition A was effective for coagulating and floccul~ting waterborne paints and, depending upon the 30 paint treated, can be effective without the need for an alkaline activator.

21 741 6'1 ExamPle 11 Compositions A and B of Example I were used to treat water con-taining oil based paints. The results are shown in Table ll.

TABLE ll Composition Activator SamPle Paint Concentration Conce,)lralion Kiil (ppm) (ppm) 1 PPG (melamine- A400 KOH-1000 3+
formaldehyde) 2 PPG (melamine- A-1000 KOH-1000 4/4+
formaldehyde) 3 PPG (melamine- A-750 sodium silicate-1000 4 formaldehyde) 4 PPG (melamine- A-750 sodium silicate-1600 4+
formaldehyde) PPG (melamine- B400 KOH-1000 3+
formaldehyde) 6 PPG (melamine- B-1000 KOH-1000 4-formaldehyde) 7 PPG (melamine- B400 sodium silicate-1000 4+
formaldehyde) 8 Dupont (polyester- A400 KOH-1000 melamine) 9 Dupont (polyester- A-750 KOH-1000 4 melamine) 10 Dupont (polyester- A400 sodium silicate-1000 4-melamine) 11 Dupont (polyester- A-750 sodium silicate-1000 4 melamine) 12 Dupont (polyester- A-750 sodium silicate-1600 4+
melamine) 13 Dupont (polyester- B400 KOH-1000 melamine) 217~169 TABLE ll (cont'd) Composition Activator SamPle Paint Concer,l,alion Conce"l,ation Kill (ppm) (DPm) 14 Dupont (polyester- B-1000 KOH-1000 melamine) 15 Dupont (polyester- B-750 sodium silicate-1000 2 melamine) 16 Dupont (polyester- B-750 sodium silicate-1600 4 melamine) 17 Lily (polyester) A400 KOH-1000 2 18 Lily (polyester) A-1000 KOH-1000 2 19 Lily (polyester) A-1000 KOH-1500 4 Lily (polyester) A-750 sodium silicate-1000 21 Lily (polyester) A-750 sodium silicate-1600 4 22 Lily (polyester) B-750 KOH-1000 23 Lily (polyester) B-750 sodium silicate-1000 3 24 Lily (polyester) B-750 sodium silicate-1600 4 25 Dupont (melamine) A-400 KOH-1000 3 26 Dupont (melamine) A-750 KOH-1500 4 27 Dupont (melamine) A-1000 KOH-1500 4 28 Dupont (melamine) A400 sodium silicate-1000 3 29 Dupont (melamine) A-750 sodium silicate-1600 4 30 Dupont (melamine) B400 KOH-100 4-31 Dupont (melamine) B-750 KOH-1500 4 32 Dupont (melamine) B-750 sodium silicate-1000 4 33 Dupont (melamine) B-1000 sodium silicate-1600 4 Table ll shows that Composition A also effectively detackifies (kills) oil base paint in water.

- ~1 7 ~

Example lll A comparison of particle size between Compositions A and B of Example I was conducted. The results are shown in Table lll.
TABLE lll Population Volume Treatment Median (um) Mean (um) Neat A 1.18 2.61 10% A in water1.17 3.00 Neat B 1.69 6.93 10% B in water1.70 6.75 Table lll shows the particle size for Composition A has a smaller 15 particle size than Composition B. The smaller size of Composition A
allows for a greater amount of surface area to contact the paint solid particle and thus enhances the detackification or coagulation and flocculation process.
20 ExamPle IV

Composition A of Example I was used to detackify oil based paints in the presence of various activators. The results are shown in Table IV.

TABLE IV
Composition A Activator Sample PaintConcentrationConcentration Kill (PPm) (pPm) Vemco 600 0 2 Vemco 600 sodium silicate-1000 3+
3 Vemco 600 sodium silicate-1600 4/4+
4 Vemco 750 sodium silicate-1600 4+
Vemco 600 KOH-1000 3 6 Vemco 600 KOH-1500 3+

217416~

TABLE IV (cont'd) Composition A Activator SamPle PaintConcer,lralionConcenlralion Kill (ppm) (PPm) 7 Vemco 750 KOH-1500 4-8 Vemco 600 NaOH; pH=9 3 9 Vemco 750 NaOH; pH=9 3+
Mazda 600 NaOH; pH=9 2 11 Mazda 750 NaOH; pH=9 2 12 Mazda 750 sodium silicate-1000 4 13 Mazda 750 sodium silicate-1600 4+
14 Mazda 750 KOH-1000 3+
Mazda 750 KOH-1500 3+

Thus, the invention provides a process effective for detackifying oil based paint and for coagulating and flocculating waterborne paint in water so as to condition the paint solids and thereby facilitate removal of the conditioned paint solids from the water.

The inventor also believes that since the invention compositions effectively detackify oil base paint and coagulate and flocculate water-borne paint separately that mixtures of oil base paint and waterborne paint in paint spray booth water would be effectively conditioned by the invention process.
While this invention has been described with respect to particular embodiments thereof, it is apparent that numerous other forms and modi-fications of the invention will be obvious to those skilled in the art. The appended claims and this invention generally should be construed to cover all such obvious forms and modifications which are within the true spirit and scope of the present invention.

Claims (10)

1. A process for detackifying oil base paint and for coagulating and flocculating waterborne paint in paint spray booth water, said process consisting essentially of adding to said paint spray booth water a sufficient amount for the purpose of dimethylamine/ethylenediamine/epichlorohydrin polymer, in combination with a sufficient amount for the purpose of alumi-num chlorohydrate and in selective combination with an amount sufficient for the purpose of an alkaline salt selected from the group consisting of sodium hydroxide, potassium hydroxide, and sodium silicate to form de-tackified oil base paint solids and coagulated ted and flocculated waterborne paint solids, wherein the weight ratio of said polymer to said aluminum chlorohydrate is from about 0.5 to 1 to about 1 to 0.5.
2. A process according to claim 1 wherein said polymer is add-ed to said paint spray booth water in an amount of from about 50 ppm to about 500 ppm, said aluminum chlorohydrate is added to said paint spray booth water in an amount of from about 50 ppm to about 500 ppm and said alkaline salt is added to said paint spray booth water in an amount of up to about 2000 ppm.
3. The process of claim 1 wherein said polymer and said alu-minum chlorohydrate are added to said paint spray booth water as an aqueous mixture comprising about 35% by weight polymer, about 35% by weight aluminum chlorohydrate and about 30% by weight water.
4. A process for detackifying oil base paint in paint spray booth water, said process consisting essentially of adding to said paint spray booth water a sufficient amount for the purpose of dimethylamine/ethyl-enediamine/epichlorohydrin polymer, in combination with a sufficient amount for the purpose of aluminum chlorohydrate and in selective com-bination with an amount sufficient for the purpose of an alkaline salt selected from the group consisting of sodium hydroxide, potassium hy-droxide, and sodium silicate to form detackified paint solids, wherein the weight ratio of said polymer to said aluminum chlorohydrate is from about 0.5 to 1 to about 1 to 0.5.
5. The process of claim 4 wherein said polymer is added to said paint spray booth water in an amount of from about 50 ppm to about 500 ppm, said aluminum chlorohydrate is added to said paint spray booth water in an amount of from about 50 ppm to about 500 ppm and said alka-line salt is added to said paint spray booth in an amount of up to about 2000 ppm.
6. The process of claim 4 wherein said polymer and said alu-minum chlorohydrate are added to said paint spray booth water as an aqueous mixture comprising about 35% by weight polymer, about 35% by weight aluminum chlorohydrate and about 30% by weight water.
7. A process for coagulating and detackifying waterborne paint in paint spray booth water, said process consisting essentially of adding to said paint spray booth water a sufficient amount for the purpose of di-methylamine/ethylenediamine/epichlorohydrin polymer, in combination with a sufficient amount for the purpose of aluminum chlorohydrate and optionally adding an amount sufficient for the purpose of an alkaline salt selected from the group consisting of sodium hydroxide, potassium hy-droxide and sodium silicate to form coagulated and detackified paint solids, wherein the weight ratio of said polymer to said aluminum chloro-hydrate is from about 0.5 to 1 to about 1 to 0.5.
8. The process of claim 7 wherein said polymer is added to said paint spray booth water in an amount of from about 50 ppm to about 500 ppm, said aluminum chlorohydrate is added to said paint spray booth water in an amount of from about 50 ppm to about 500 ppm and said alka-line salt is added to said paint spray booth in an amount of up to about 2000 ppm.
9. The process of claim 7 wherein said polymer and said alu-minum chlorohydrate are added to said paint spray booth water as an aqueous mixture comprising about 35% by weight polymer about 35% by weight aluminum chlorohydrate and about 30% by weight water.
10. A process for removing paint solids from paint spray booth water containing oil base paint, waterborne paint or mixtures of oil base and waterborne paint, said process consisting essentially of:

a) adding to said paint spray booth water from about 50 ppm to about 500 ppm of dimethylamine/ethylenediamine/epichlorohydrin polymer, from about 50 ppm to about 500 ppm of aluminum chloro-hydrate and up to about 2000 ppm of an alkaline material selected from the group consisting of sodium hydroxide, potassium hydrox-ide and sodium silicate, to detackify oil base paints and to coagu-late and flocculate waterborne paints, so as to produce conditioned paint solids wherein the weight ratio of polymer to aluminum chlorohydrate is from about 0.5:1 to about 1:0.5; and b) removing the resulting conditioned paint solids from said paint spray booth water.
CA 2174169 1995-12-06 1996-04-15 Process for removing waterborne and oil base paints from water Abandoned CA2174169A1 (en)

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US56806695A 1995-12-06 1995-12-06
US08/568,066 1995-12-06

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006056022A1 (en) * 2004-11-26 2006-06-01 Hardman Australia Pty Ltd Water treatment process

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006056022A1 (en) * 2004-11-26 2006-06-01 Hardman Australia Pty Ltd Water treatment process

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