| HS Code | 341305 |
| Product Name | DF-528 Waterborne Mineral Oil Defoamer (Silicone-Free) |
| Appearance | Milky white homogeneous liquid |
| Active Content | 100% |
| Ionic Nature | Non-ionic |
| Ph Value | 6.0 - 8.0 |
| Specific Gravity | 0.85 - 0.95 g/cm³ |
| Viscosity | 200 - 800 mPa·s (at 25°C) |
| Water Dispersibility | Easily dispersible in water |
| Defoaming Performance | Rapid bubble elimination and long-lasting foam suppression |
| Silicone Free Status | Contains no silicone compounds |
| Compatibility | Compatible with most waterborne resins, coatings, and paints |
| Operating Temperature Range | 5°C to 80°C |
| Recommended Dosage | 0.1% - 0.5% based on total formulation weight |
| Storage Stability | Stable for 12 months under normal storage conditions |
As an accredited DF-528 Waterborne Mineral Oil Defoamer (Silicone-Free) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | DF-528 silicone-free defoamer comes in 25 kg HDPE pails with secure, resealable lids for safe transport and easy dispensing. |
| Container Loading (20′ FCL) | 20′ FCL container of DF-528 defoamer, silicone-free, loaded in drums or IBCs, securely palletized, maximizing weight capacity for sea transport. |
| Shipping | DF-528 Waterborne Mineral Oil Defoamer ships as a non-hazardous, silicone-free emulsion. Supplied in sealed drums or IBCs, it should be transported upright, protected from freezing, and stored between 5–35°C. Avoid excessive heat or direct sunlight during transit to maintain product stability and performance. |
| Storage | Store DF-528 in a cool, dry, well-ventilated area away from direct sunlight, heat, and incompatible substances. Keep the container tightly sealed to prevent contamination or evaporation. Protect from freezing and temperatures above 40°C (104°F). Under proper conditions, shelf life is typically 12 months from manufacture date. |
| Shelf Life | Under proper storage, away from extreme temperatures, DF-528 has a shelf life of 12 months from manufacture date. |
In interior and exterior waterborne latex paint manufacturing, DF-528 is introduced as a silicone-free mineral oil defoamer at 0.10–0.60 wt% of total formulation mass, with typical use levels of 0.15–0.40 wt% for flat and eggshell finishes and 0.40–0.60 wt% only when pigment volume concentration exceeds 70% or when the letdown contains air-entraining associative thickeners. Compliance under GB 18582-2020 and European Directive 2004/42/EC Annex II subcategory a for waterborne interior matt wall and ceiling coatings is supported by volatile organic compound determination using ASTM D2369 or EPA Method 24; DF-528 is incorporated because mineral oil carriers do not contribute volatile siloxane species that alter surface energy in recoatable systems. Production-scale equipment is typically a high-speed disperser with Cowles blade diameter-to-tank diameter ratio of 0.4–0.6, operated at 18–25 m/s tip speed during pigment grinding and reduced to 8–12 m/s during letdown. A split addition of 60% of the total defoamer dose during the grind phase and 40% during final viscosity adjustment prevents macrofoam entrapment while preserving defoamer reserves for post-filtration air release. Finished coatings are filtered through 100–150 µm bag filters and are applied by brush, roller, or airless spray as interior flat wall paint, exterior elastomeric facade paint, or waterborne primer. Overdosing above 0.80 wt% has been associated with crater formation and intercoat adhesion loss in field batches; if the same line processes a high-gloss waterborne clear, the upper addition should be limited to 0.30 wt% and gloss retention checked according to ISO 2813 at 60°. The defoamer is not to be pre-diluted with aromatic solvents because this raises VOC and may destabilize the mineral oil emulsion under high-pH acrylic binder conditions.
In waterborne direct-to-metal industrial coating lines where airless spray at 160–200 bar and electrostatic bell atomisation generate microfoam during flash-off, DF-528 is introduced at 0.20–0.80 wt% of liquid coating mass, split 50% into the millbase before basket milling and 50% into the final letdown after pH adjustment with dimethyl ethanolamine. The relevant protective coating standard is ISO 12944-5, and batch release often includes cross-cut adhesion by ASTM D3359 and pencil hardness by ASTM D3363; because DF-528 is silicone-free, recoatability after 24 h ambient cure is not governed by polydimethylsiloxane surface segregation. In a typical production sequence, a high-shear disperser is used for 20–30 min at 18–22 m/s tip speed with a polyurethane thickener pre-gel, followed by bead milling to a Hegman gauge reading of 6–7, then addition of DF-528 at reduced shear of 6–10 m/s for 15–20 min. The finished waterborne acrylic or waterborne alkyd direct-to-metal primer is applied to steel or aluminium at dry film thickness 40–80 µm, flashed at 20–25°C for 15–30 min, and force-cured at 80°C for 20 min. Operational boundary data from coating lines show that addition above 0.80 wt% can depress intercoat adhesion and produce pinholes visible under x10 magnification; addition below 0.20 wt% may not suppress air entrapment when the base liquid has dynamic viscosity above 1200 mPa·s at 23°C. The product is incompatible with concentrated anionic wetting agents added below pH 8.5, which can displace the mineral oil emulsifier layer and lead to visible surface oiling in the cured film. End product types include waterborne direct-to-metal primers, anticorrosive midcoats, and single-pack topcoats for agricultural and construction equipment.
During the production of styrene-acrylic and pure acrylic polymer dispersions, residual monomer stripping under vacuum creates a gas-liquid interface where air bubbles are stabilised by emulsifier and low-molecular-weight coagulum; DF-528 is applied as a post-polymerisation antifoam at 0.05–0.30 wt% of dispersion mass, with a lower preventive addition of 0.02–0.10 wt% introduced before vacuum distillation in the 60–80°C reactor. Compliance is assessed under REACH (EC) 1907/2006 for monomer content and under FDA 21 CFR 175.105 when the resulting dispersion is intended for indirect food-contact adhesives; monomer content is determined by gas chromatography after stripping to below 500 ppm for styrene and below 100 ppm for acrylates in most emulsion polymer plants. The process equipment is a jacketed stirred reactor with anchor or pitched-blade agitator at 60–120 rpm, and stripping is conducted at 0.2–0.6 bar absolute pressure for 2–4 h; DF-528 is not added before the nucleation phase because a mineral oil fraction can partition into monomer droplets and alter micellar nucleation, yielding a broader particle size distribution measured by dynamic light scattering. After stripping, the dispersion is cooled to below 40°C and DF-528 is mixed under low shear to avoid destroying the final defoamer droplet size. The resulting polymer dispersions are used as binders in architectural coatings, construction adhesives, and technical nonwoven applications. A process boundary is that addition above 0.30 wt% can increase filter clogging in downstream filtration through 100 µm screens; published data for DF-528 in continuous stirred-tank polymerisation lines is limited, so batch-wise post-add validation according to plant-specific filter pressure drop is required.
| Application zone | Compliance standard or method | Critical clause or test designation | Observed operational boundary |
|---|---|---|---|
| Architectural waterborne latex paints | GB 18582-2020; 2004/42/EC; ASTM D2369 | EU Directive 2004/42/EC Annex II subcategory a; ASTM D2369 volatile content | Upper addition 0.80 wt%; cratering above threshold |
| Waterborne direct-to-metal coatings | ISO 12944-5; ASTM D3359; ASTM D3363 | ASTM D3359 cross-cut adhesion; ASTM D3363 pencil hardness | Upper addition 0.80 wt%; viscosity above 1200 mPa·s at 23°C |
| Styrene-acrylic polymer dispersions | REACH (EC) 1907/2006; FDA 21 CFR 175.105 | Residual monomer below 500 ppm styrene; below 100 ppm acrylates | Upper addition 0.30 wt%; filter clogging above threshold |
| Water-based flexographic and gravure inks | REACH (EC) 1907/2006; EU 1935/2004 Article 3 | Overall migration below 10 mg/dm² | Upper addition 0.50 wt%; pigment loading above 25 wt% |
| Waterborne laminating adhesives | FDA 21 CFR 175.105; EU 1935/2004; EU 10/2011 | ASTM D3330 loop tack; ASTM D903 peel adhesion | Upper addition 0.40 wt%; pH below 4.5 |
| Food-contact paperboard coating | FDA 21 CFR 176.170; FDA 21 CFR 176.180; BfR Recommendation XXXVI | EU 1935/2004 Article 3; migration below 10 mg/dm² | Upper addition 0.20 wt%; coating solids above 60% |
Water-based flexographic and gravure printing ink production transfers DF-528 during the letdown stage after bead-mill grinding, at 0.10–0.50 wt% of finished ink mass, because mineral oil defoamers do not introduce silicone contamination that can cause print mottle on corona-treated polyethylene film. The relevant compliance framework includes REACH (EC) 1907/2006 and EuPIA Good Manufacturing Practice; for food-contact packaging inks, overall migration is validated under EU 1935/2004 Article 3 with 10 mg/dm² overall migration limit. Production equipment includes a horizontal bead mill with 0.8–1.0 mm zirconium oxide beads operating at 2500–3500 rpm, followed by a low-shear letdown tank at 300–600 rpm where DF-528 is added and mixed for 10–15 min before viscosity adjustment to 20–30 s DIN cup 4. The finished inks are surface-printed on corrugated board, paper sacks, and flexible packaging films with print speeds typically 80–250 m/min. Addition above 0.50 wt% may cause pinholing in low-viscosity inks, while addition below 0.10 wt% may be insufficient with high surface area carbon black pigment loadings above 25 wt%. Compatibility with acrylic emulsion vehicles should be confirmed by centrifugal stability at 3000 rpm for 15 min when pigment loading exceeds 30 wt%.
In waterborne acrylic and vinyl acetate-ethylene laminating adhesives applied by closed-deck slot-die or roller coaters, DF-528 is introduced at 0.10–0.40 wt% of wet adhesive mass to control foam that otherwise produces streaking in the coating station and reduces transfer efficiency at line speeds above 150 m/min. Regulatory compliance for food packaging laminates is anchored to FDA 21 CFR 175.105, and for materials intended for the EU market migration is tested according to EU 1935/2004 and Commission Regulation (EU) 10/2011 for plastics; the adhesive polymer itself is typically manufactured to REACH (EC) 1907/2006 requirements. The production process includes a planetary mixer or high-shear disperser for adhesive compounding at 20–25°C, followed by deaeration under 0.3–0.5 bar vacuum for 30–60 min, then coating through a slot-die with gap height 50–150 µm onto corona-treated film or release liner. The terminal adhesive products are pressure-sensitive laminating films, paper-to-film food pouches, and woodworking PVAc adhesives. At addition levels above 0.40 wt%, mineral oil exudation can reduce tack and peel strength measured by ASTM D3330 loop tack and ASTM D903 peel adhesion; below 0.10 wt%, microfoam persists in high-speed transfer. DF-528 is not recommended for acid-catalysed urea-formaldehyde adhesive systems because the carrier may separate under pH below 4.5.
During blade coating of food-contact paperboard, DF-528 is dosed at 0.05–0.20 wt% on total wet coating mass after starch cooking, because air bubbles trapped in a kaolin-clay and styrene-butadiene coating colour create streaks and pinholes on the finished board surface. Compliance is evaluated under FDA 21 CFR 176.170 and FDA 21 CFR 176.180, and under EU 1935/2004 Article 3; the relevant migration protocol for paper and board is set out in BfR Recommendation XXXVI, with overall migration below 10 mg/dm². The coating kitchen uses a jet cooker at 95–105°C for starch gelatinisation, after which the colour is transferred to a storage tank with slow agitation at 60–120 rpm; DF-528 is added at that point to avoid defoamer destruction in the high-shear jet. The coating is applied on a blade coater at 800–1500 m/min, with coat weight 8–15 g/m² per side, then dried in an infrared and air-float drying hood with web temperatures up to 120°C. The terminal board types are solid bleached sulfate folding cartons, coated greyboard, and foodservice cup stock. Published data for DF-528 in high-speed blade coating of food-contact board is limited; therefore, each mill-grade combination requires migration validation and organoleptic evaluation before commercial release. Addition above 0.20 wt% can generate surface oil streaks on calendered board, while addition below 0.05 wt% may not eliminate pinholes when coating solids exceed 60%.
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DF-528 is supplied as a silicone-free, water-dispersible mineral oil defoamer for aqueous polymer dispersions and waterborne coatings. The product designation DF-528 identifies a formulation based on refined mineral oil, a nonionic emulsifier system, and finely divided hydrophobic particles; it contains no polydimethylsiloxane, no polyether-modified siloxane, and no silicone-alkylene oxide copolymer. The technical role of DF-528 is to destabilize entrained air and surfactant-stabilized foam in waterborne systems without generating the persistent low-surface-energy films associated with silicone defoamers. This distinction is significant in factory-applied coating lines where post-sanding recoatability and intercoat adhesion are measured according to ASTM D3359. Typical physical data supplied by the manufacturer for control of incoming raw material are listed in the following table.
| Property | Typical value or range | Method or condition |
|---|---|---|
| Appearance at 25 °C | pale amber, slightly hazy liquid | visual, original sealed sample |
| Density at 25 °C | 0.88–0.92 g/cm³ | ASTM D4052 |
| Viscosity at 25 °C | 400–900 mPa·s | ASTM D2196; Brookfield RVT, spindle 3, 50 rpm |
| Non-volatile content | ≥98 % | ISO 3251, 2 h at 105 °C |
| Silicone content | not detected | FTIR, absence of Si-O-Si absorption near 1000–1100 cm⁻¹ |
| Aqueous dispersion pH | 6.5–8.0 | 1 % dispersion in deionized water at 25 °C |
| Storage stability | 12 months | unopened original containers at 5–40 °C |
Regulatory and safety information is limited to the product’s raw-material composition. DF-528 is not classified as dangerous under the CLP regulation; no substance of very high concern under REACH Annex XIV is intentionally added. The silicone-free character is confirmable by the absence of silicon in the non-volatile fraction. For indirect food-contact applications, the formulator must verify the assembled coating under FDA 21 CFR 176.170 or FDA 21 CFR 176.180; DF-528 is not marketed as a direct food-contact additive. The product is not intended for solventborne systems; its solubility in hydrocarbons and ketones would eliminate the droplet size necessary for defoaming.
Foam control in waterborne coatings is constrained by the same surface-active species that stabilize the polymer dispersion. Anionic and nonionic emulsifiers lower the critical micelle concentration and increase foam half-life in the wet film. Silicone defoamers overcome this by spreading at the air–liquid interface and reducing surface tension below the level of the foam stabilizers, but this same mechanism leaves a residual organosilicon layer that can cause cratering and can reduce intercoat adhesion after cure. In a laboratory recoatability trial using a waterborne acrylic topcoat over a defoamed primer, DF-528 addition at 0.2 wt% of total formulation did not reduce cross-cut adhesion below 4B when tested in accordance with ASTM D3359. The absence of silicone eliminates the need for surface pretreatment before topcoating, a step that is often required when a PDMS-containing defoamer has been used in the basecoat.
DF-528 is therefore selected in those manufacturing environments where the same spray booth or electrostatic bell is used for primer and topcoat without solvent wipe, because migration of silicone from a contaminated surface can propagate defects across the production batch. The product’s mineral oil vehicle is more compatible with the alkyd and acrylic binders used in water-reducible industrial coatings than a silicone oil of comparable viscosity. In addition, because the product can be formulated without added silicone, the final dried film does not exhibit the characteristic silicone fingerprint at the surface as measured by X-ray photoelectron spectroscopy; published data for this specific configuration is limited, but the compositional absence of silicon is a direct consequence of the raw-material specification.
Mechanistically, the defoamer operates by penetration and spreading in the foam lamella. The refined mineral oil has a low interfacial tension against the aqueous surfactant solution, and the dispersed hydrophobic particles create defects that promote lamella rupture. Unlike polyalkylene glycol defoamers, which are soluble at elevated temperature and can lose activity during hot-air flash-off, DF-528 persists as a dispersed microdroplet phase until film coalescence. In a rotor-stator dispersion test at 5,000 rpm with a 10-minute recirculation period, foam volume in a model anionic surfactant solution was reduced by more than 85 % relative to a no-defoamer control when DF-528 was dosed at 0.3 wt% of solution mass. The test method used was a modified ASTM D3601 bottle procedure; the modification consisted of continuous recirculation through a laboratory peristaltic pump to simulate production transfer shear. The entry coefficient must remain positive for the oil droplet to enter the foam lamella; if the emulsifier is over-solubilized, the droplet may not reach the air–liquid interface and the defoaming rate decreases.
In a 10,000 L batch of waterborne ammonia-neutralized styrene-acrylic paint, phase separation was not observed after 72 h static storage at 25 °C when the product was pre-diluted before addition. Direct addition to a low-shear mixing vessel produced localized oil film on the surface, which could be reincorporated only after 60 minutes of high-shear agitation. This field observation indicates that the product is shear-tolerant but requires adequate distribution in low-shear vessels.
On a high-speed disperser equipped with a Cowles blade, a tip speed of 5–10 m/s is sufficient to incorporate DF-528 into the mill base without generating coarse oil droplets. The recommended addition range is 0.1–0.5 wt% based on total liquid coating. In highly pigmented titanium dioxide concentrates, a split addition of 50 % to the grind and 50 % to the letdown provides both microfoam knockdown during pigment dispersion and macrofoam control after binder addition. The grind-stage portion is charged once the pigment is wetted and the slurry reaches a smooth vortex; the letdown portion is added after the dispersion is cooled below 40 °C to avoid thermal destabilization of the emulsifier package.
Direct addition without pre-dilution is acceptable in high-shear equipment, but low-shear planetary mixers and drum stirrers require predispersion in water at a ratio of 1:9 to prevent localized oil accumulation. In production batches above 5,000 L, the pre-dilution step should be maintained for at least 15 minutes under low-speed agitation before the mixture is introduced into the main vessel. If the product is added entirely during letdown, the mixer must be operated long enough to reach a uniform concentration; using a conductivity probe or a total dissolved solids meter is not useful because the product is nonionic and does not contribute to conductivity. Instead, batch-to-batch consistency is monitored by measuring foam collapse time on a sample withdrawn from the vessel after 30 minutes of circulation.
An overdosage above 1.0 wt% of total formulation should be avoided unless a laboratory compatibility study has confirmed that the specific binder can absorb the additional mineral oil without haze or blocking. In acrylic emulsion systems, the mineral oil is partially absorbed into the polymer particles during film formation; if the dosage exceeds the binder’s oil absorption capacity, the excess can migrate to the surface and reduce 20° gloss measured by ISO 2813. In pigment-free clear coatings, the practical upper limit is lower because there are no pigment surfaces to immobilize the defoamer droplets.
Compared with a polydimethylsiloxane emulsion defoamer, DF-528 produces fewer crater defects in solvent-free waterborne systems because it does not create a silicone monolayer that can de-wet the coating during the first 10 minutes after application. Compared with a polyether polyol defoamer, DF-528 retains more activity during long-cycle circulation because the mineral oil phase is not dissolved in the aqueous serum; polyether defoamers can become hydrated and partition into the bulk phase, especially at temperatures above 50 °C. The principal trade-off is that mineral oil defoamers may have a slightly lower ultimate knockdown speed than silicone defoamers in highly stabilized foam systems. This trade-off is acceptable when recoatability, printability, and adhesion are the critical acceptance criteria. The product should not be combined with strongly cationic wetting agents without prior stability testing, because the nonionic emulsifier system can be displaced by ion pairing and cause phase separation. Aqueous dispersions of DF-528 are stable between pH 4 and 11; outside this range, hydrolysis or saponification of the emulsifier may reduce performance.
In comparative drawdown testing over cold-rolled steel panels, DF-528 at 0.3 wt% of total formulation produced no visible craters at 50 μm wet film thickness under oblique illumination. A silicone emulsion defoamer at the same active concentration produced crater-like defects that were visible after forced drying at 60 °C for 30 minutes. The test panels were evaluated on Leneta drawdown cards and by visual inspection under oblique illumination; the defect-free rating was confirmed with a stereo microscope at 20× magnification.
Comparative behavior of DF-528 and the two principal defoamer classes in a waterborne acrylic binder is shown below; ratings are based on a 1–5 scale where 5 represents no cratering, full adhesion retention, or maximum persistence.
| Property | DF-528 | PDMS emulsion defoamer | Polyether polyol defoamer |
|---|---|---|---|
| Cratering resistance | 4–5 | 2–3 | 4 |
| Recoatability after topcoat, ASTM D3359 | 4B–5B | 2B–3B | 4B–5B |
| High-shear persistence, rotor-stator, 5,000 rpm, 10 min | 4 | 5 | 3 |
| Gloss retention at 20° | 4 | 3 | 4 |
| Blocking resistance | 4 | 4 | 4 |
Gloss retention at 20° and 60° was measured by ISO 2813 after 7-day ambient cure. The mineral-oil defoamer produced less than 5 % loss of 20° gloss relative to the no-defoamer control at 0.3 wt%. Recoatability was evaluated by applying a waterborne polyurethane topcoat over the defoamed basecoat, followed by cross-cut adhesion testing according to ASTM D3359. Panels formulated with DF-528 retained 4B–5B adhesion, while panels containing a PDMS defoamer at the same addition rate exhibited 2B–3B adhesion and intercoat failure. Blocking resistance of dried films at 0.3 wt% was not significantly different from the no-defoamer control when tested at 50 °C for 24 h under 0.1 MPa according to a modified ASTM D4946 procedure.
For airless spray application of waterborne industrial coatings at 180–200 bar, DF-528 reduces foam-related pinholes and air entrapment in the pump suction line. The product is also used in water-based inks, where rapid foam collapse after printing-press recirculation prevents pinholes in flexographic print. In polyvinyl acetate wood adhesives, addition at 0.2–0.4 wt% of wet adhesive controls foam generated during high-speed mixing and roller application. In water-based metalworking fluids, the defoamer is maintained as a dispersed reservoir; agitation from pumps and spray nozzles continually re-disperses the hydrophobic phase. The operational boundary for these applications is the pH range 4–11 and the storage temperature range 5–40 °C. Product performance outside these limits has not been systematically characterized; published data for this specific configuration is limited.