| HS Code | 339703 |
| Productname | 77-2 Metal Cleaning Agent and Anti-rust Agent |
| Model | 77-2 |
| Productcategory | Water-based metal cleaning and anti-rust agent |
| Appearance | Light yellow to colorless transparent liquid |
| Odor | Slight characteristic odor |
| Phvalue | 8.0-10.0 (1% aqueous solution) |
| Density | 1.00-1.10 g/cm3 at 20°C |
| Watersolubility | Completely soluble in water |
| Applicationmaterials | Steel, cast iron, aluminum, copper, and their alloys |
| Cleaningmethods | Immersion, spraying, ultrasonic cleaning, and manual wiping |
| Workingconcentration | 3%-10% by volume in water |
| Workingtemperature | Room temperature to 60°C |
| Antirustperiod | 1-6 months under indoor dry conditions |
| Packaging | 25 kg plastic drum or 200 kg iron drum |
| Shelflife | 12-24 months in original sealed packaging |
| Storageconditions | Store sealed in a cool, dry, ventilated place; avoid freezing and direct sunlight |
As an accredited 77-2 Metal Cleaning Agent and Anti-rust Agent factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | 77-2 Metal Cleaning Agent and Anti-rust Agent is supplied in sealed 25 kg plastic drums with clear hazard and handling labels. |
| Container Loading (20′ FCL) | 77-2 Metal Cleaning Agent and Anti-rust Agent loaded in a 20-foot full container load (FCL) for safe sea transport. |
| Shipping | 77-2 Metal Cleaning Agent and Anti-rust Agent is shipped in sealed, properly labeled chemical containers with SDS and transport documents. Confirm hazardous classification and packaging per applicable regulations before shipment. Keep upright, dry, away from heat and incompatible materials; handle with suitable PPE. |
| Storage | Store **77-2 Metal Cleaning Agent and Anti-rust Agent** in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Keep containers tightly closed, upright, clearly labeled, and in original or compatible corrosion-resistant packaging. Use secondary containment where required. Separate from acids, oxidizers, food, and feed. Follow the SDS and local regulations. |
| Shelf Life | 77-2 Metal Cleaning Agent and Anti-rust Agent typically has a shelf life of about two years when stored sealed in a cool, dry, ventilated place. |
77-2 Metal Cleaning Agent and Anti-rust Agent functions as an aqueous alkaline cleaning and interstage corrosion-inhibitor fluid for ferrous metal manufacturing. The working bath is prepared by diluting the concentrate with deionized or reverse-osmosis water having conductivity below 50 µS/cm; water hardness above 150 mg/L CaCO₃ reduces anti-rust film uniformity and produces scale on heating coils. The product is supplied as a liquid concentrate and is applied only to ferrous substrates unless specific compatibility testing on aluminium, zinc, magnesium, or copper alloys has been completed. Bath preparation, replenishment, and discharge must follow the safety data sheet and local wastewater permits. The application scope covers machined automotive components, high-strength fasteners, precision bearing elements, cold-formed transmission parts, steel packaging, and maintenance-overhaul components. The following scenarios describe process conditions, compliance anchors, addition ratios, and terminal products for specific downstream processes.
On automotive powertrain machining lines producing grey cast iron caliper bodies, 42CrMo4 steel wheel hubs, and differential bearing caps, aqueous cutting fluid residues are removed before assembly-facing surfaces are milled and before final rust-preventive oil is applied. In immersion cells, the 77-2 working bath is controlled at 6–8 vol% concentration, pH 9.2–9.7, and temperature 55–65 °C; contact time is 4–7 min. Spray-washer stages for the same part families operate at 3–5 vol%, 50–60 °C, and 1.5–2.5 bar nozzle pressure. The production sequence consists of loading baskets onto an overhead monorail, primary wash, drain zone, second spray rinse at conductivity below 25 µS/cm, air-knife blow-off at 4 bar, and dry-off at 80–90 °C for 6–10 min. Terminal products include brake calipers, wheel hubs, steering knuckles, and differential bearing caps. Compliance for exported assemblies follows IATF 16949:2016 clause 8.6.1.1 cleanliness requirements, while corrosion protection is validated under ISO 9227:2022 neutral salt spray for 24–48 h or ISO 6270-2:2022 condensation humidity at 40 °C and 100% RH for 72 h without red rust. Process limits observed on production-scale immersion lines show that concentrations above 9 vol% can leave visible white inhibitor residue in blind M8 tapped holes after dry-off, while concentrations below 4 vol% allow flash rust on machined cast iron within 2 h in unheated staging bays. Baskets containing stacked parts require incremental rotation at 3 rpm for blind-hole drainage; otherwise localized pitting is found at internal threads after field returns. The bath is skimmed with a belt oil separator and filtered through 25 µm bag filters to prevent redeposition of metal fines.
High-strength steel fasteners of property classes 10.9 and 12.9 for automotive chassis joints are cleaned and given interstage anti-rust protection before zinc phosphate conversion. The 77-2 bath is charged at 5–7 vol% in the first stage of a five-stage power spray tunnel at 60–70 °C; stage-one contact time is 2–3 min. Stage two rinses with mains water at 25–35 °C and conductivity below 30 µS/cm. Stages three and four apply zinc phosphate per ISO 9717:2024 and a cold water rinse; stage five applies a chromate-free passivation. Terminal products include M10–M20 hex flange bolts, wheel bolts, stabilizer link studs, and steering rack bolts. Compliance anchors include ISO 898-1:2013 for mechanical properties, ISO 9227:2022 for phosphate-plus-seal salt spray resistance over 72 h, and REACH Regulation (EC) No 1907/2006 Annex XVII for restricted substances in EU export. A process conflict occurs at the cleaner-to-phosphate transition: drag-out from stage one raises free acid in the phosphate bath when carry-over exceeds 0.3 L/100 kg of fasteners, shifting coating weight and crystal morphology. Operators titrate the cleaner bath at 12–18 mL total alkalinity and 6–9 mL free alkalinity; if free alkalinity drifts below 5 mL, rinse corrosion appears on washer internal surfaces. The anti-rust component permits 4–6 h transfer time from stage two to phosphate without red rust. Foam generation above 2.5 bar spray pressure at 7 vol% requires defoamer addition, which shortens oil-skimmer interval. Published data for the exact foam collapse rate under this specific phosphate-line configuration is limited; lot release is therefore controlled by a bench-top spray cell test using a 10 mL/L sample.
| Application mode | Concentration (vol%) | Temperature (°C) | Contact time | Typical ferrous substrate |
|---|---|---|---|---|
| Immersion | 6–8 | 55–65 | 4–7 min | grey cast iron, 42CrMo4 steel |
| Spray tunnel | 2–7 | 40–70 | 20 s–3 min | fasteners, can sidewall, pail bodies |
| Ultrasonic | 4–6 | 45–55 | 3–5 min | bearing rings, ground raceways |
| Rotary drum | 6–10 | 65–75 | 8–12 min | synchronizer sleeves, CV joint cages |
| Manual / parts washer | 5–10 | 40–55 | 5–10 min dwell / 10–20 min circulation | pump casings, gear reducer housings |
Residual film interference on rolling bearing vibration signatures has been investigated on DIN 625-1 deep-groove ball bearing rings and linear guide rails before preservative oil application. The 77-2 fluid is used in ultrasonic immersion cells at 4–6 vol%, pH 9.0–9.5, and 45–55 °C for 3–5 min, followed by two counterflow rinses with deionized water at 40 °C. Cleaning performance is verified by particle count according to ISO 16232:2018; the acceptance limit for high-precision bearing rings is ≤100 particles ≥5 µm per component. The anti-rust effect is validated under ISO 6270-2:2022 condensation conditions for 48 h. Terminal products include 62-series electric motor bearings, bicycle hub bearings, spindle bearing races, and linear motion blocks. A critical threshold arises when the working concentration exceeds 7 vol%: residual inhibitor film thickness on raceways increases roughness by 0.02–0.05 µm Ra, and vibration velocity measured under ISO 15242-1:2015 elevates by 10–25 µm/s in the medium-frequency band from 50–300 Hz on finished assembled bearings. Below 3 vol%, flash rust on ground raceways appears within 30 min at relative humidity above 60%. Shielded or sealed bearing rings must be tilted 15° during ultrasonic treatment to release trapped air; otherwise the anti-rust film is absent behind the shield. Rinse tank conductivity is maintained below 20 µS/cm because residual salts contribute to electrical impedance changes in motor bearings. The production constraint is not solubility but film uniformity on superfinished surfaces; load density above 15 kg per 20 L ultrasonic bath leads to non-uniform film and requires reduction to 10 kg/20 L.
Transmission synchronizer sleeves, gearshift forks, and CV joint inner races formed with chlorinated or phosphate-ester lubricants are processed through a rotary drum washer before controlled atmosphere quench hardening. In this configuration the 77-2 bath is charged at 6–10 vol% at 65–75 °C, pH 9.2–10.0, with cycle time 8–12 min in a continuous rotary drum and countercurrent rinse. Rinsing uses tempered water below 25 µS/cm and is followed by 90 °C hot air drying for 8–12 min. Terminal products include synchronizer hubs, gearshift forks, CV joint inner races, and bearing cages. Compliance is linked to CQI-9 heat treatment system assessment and AMS 2750F pyrometry; surface chloride before heat treatment is checked by ISO 8502-2:2005 with acceptance limit <10 mg/m² to avoid stress corrosion and furnace liner attack. The main process conflict is thermal: the anti-rust film breaks down at approximately 110 °C, but undried pockets at blind bores carry cleaner residue into the quench furnace, where carbonate residues reduce furnace atmosphere carbon potential and produce non-uniform case depth. Bath concentration is therefore held in the lower half of the range, 6–7 vol%, for parts with blind holes, accepting a shorter humidity protection interval. At 10 vol%, drain time must be extended by 2 min to avoid residue bridging. Data from production-scale rotary washers indicate that bath life declines when tramp oil exceeds 5% by volume as measured by refractometer; the cleaning rate for chlorinated forming oil drops by half and leads to localized soft spots in gear teeth after carburizing. The recommended oil skimming and centrifuge loop is 0.5–1.0 bath turnover/h. This fluid is not suitable for aluminium synchronizer rings above 45 °C due to alkaline etching.
Steel aerosol can bodies and 20-L pail sidewalls coming from tandem welding and necking lines are cleaned and given temporary rust protection before exterior base coating or powder coating. The 77-2 bath is sprayed at 2–4 vol% and 40–50 °C; contact time is limited to 20–40 s in a high-speed in-line washer with 1.0–1.5 bar fan nozzles. The process sequence includes pre-rinse, cleaner stage, municipal water rinse at 20–30 °C, forced ambient air blow-off, and dryer zone at 70–80 °C. Terminal product types are decorated aerosol containers for automotive paints and lacquers, steel pails for solvent-based adhesives and sealants, and tinplate drum closures. Compliance references include UN 1A2 package certification for steel pails and closures, REACH Regulation (EC) No 1907/2006 for chemical restrictions, and RoHS Directive 2011/65/EU for exported packaging components where applicable. A lower concentration is required because can sidewall coverage at high line speeds would otherwise leave inhibitor streaks that interfere with lacquer adhesion; a cross-cut tape adhesion test per ISO 2409:2013 is used after coating, and values fall from Gt 0 to Gt 2 when cleaner concentration exceeds 5 vol%. Foam generation in the high-shear nozzle system is controlled by liquid level rather than defoamer; the bath tank is fitted with a low-level float switch at 150 mm from pump suction. Bath temperature above 60 °C accelerates corrosion protection but causes lacquer blistering on unrinsed seams. The anti-rust component provides 24–48 h indoor storage protection at 20–25 °C and 50% RH when verified by ISO 6270-2:2022, sufficient between washing and coating shifts.
| Standard / requirement | Scope | Acceptance criterion |
|---|---|---|
| ISO 9227:2022 | Temporary anti-rust film on ferrous components | No red rust after 24–72 h depending on substrate |
| ISO 6270-2:2022 | Interstage protection in condensation humidity | No red rust at 40 °C / 100% RH for 48–72 h |
| ISO 8502-2:2005 | Soluble salts on cleaned steel before heat treatment or painting | <10 mg/m² chloride |
| ISO 16232:2018 | Component cleanliness for precision bearing and hydraulic parts | ≤100 particles ≥5 µm per component |
| ISO 9717:2024 | Zinc phosphate conversion coatings on ferrous fasteners | Coating weight per customer drawing; salt spray per ISO 9227:2022 |
| REACH Regulation (EC) No 1907/2006 Annex XVII | Restricted substances in EU export components | SDS declared substances below applicable concentration limits |
Maintenance overhaul of API 610 centrifugal pump casings and gear reducer housings uses the compound as a cold cleaner and flash-rust inhibitor during teardown and reassembly. In open parts washers, concentration is 5–10 vol% at 40–55 °C; for manual brushing, the same dilution is applied with an acid brush, allowed 5–10 min dwell, then rinsed with water below 30 µS/cm. The process begins with removal of old grease by scraping, followed by circulation through a 100 L stainless steel parts washer with 50 µm strainer, rinse, compressed air blow-down at 3 bar, and application of a heavier preservative oil for long-term storage. Terminal products include overhauled centrifugal pumps, gear reducers, fan shaft assemblies, and valve bodies. Compliance for industrial maintenance uses ISO 12944-2:2017 corrosivity category C2 indoor protection; surface salts are measured by ISO 8502-2:2005 and limited to <10 mg/m² for painted assemblies. Operational boundaries include avoiding copper alloy shafts and bronze impellers at concentration above 7 vol% and temperature above 55 °C; brass and copper components can tarnish. Cast iron housings with absorbed oil require replenishment at 1.5–2.0 vol% per 8 h shift because the cleaner emulsifies tramp oil and reduces active alkalinity. The anti-rust film is intentionally thin and provides 24 h indoor protection; extended storage beyond 48 h without preservative oil application is outside the validated operating window. Published data for humidity resistance on machined cast iron in unheated tropical sheds is limited; field verification at 35 °C and 85% RH is recommended before relying on the compound as a sole preservative.
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77-2 Metal Cleaning Agent and Anti-rust Agent is supplied as a water-dilutable alkaline liquid concentrate intended for ferrous metal components. The model designation identifies a single-package chemistry that combines emulsification of light-to-medium machining oils, drawing lubricants, and shop soils with temporary flash-rust inhibition on steel and cast iron. Representative physical specifications from the current supplier’s technical data sheet include a density of 1.08–1.15 g/cm³ at 20 °C by ASTM D4052-18a, a pH of 9.0–10.5 at 3 vol% dilution in deionized water at 25 °C by ASTM D1293-18, and a closed-cup flash point above 100 °C under ASTM D93-20. The concentrate is packaged in 25 kg, 200 kg, and 1,000 kg containers and stored between 5 °C and 45 °C. Dilution water should be softened or deionized to total hardness below 150 ppm as CaCO₃ because calcium and magnesium cations precipitate anionic surfactant components, reduce bath clarity, and form scale on heat exchanger surfaces.
Chemical composition is based on anionic and nonionic surfactants, alkaline builders, and a polar organic corrosion inhibitor. The exact proportion is proprietary; the safety data sheet identifies hazardous components under EU CLP. The organic inhibitor adsorbs on ferrous surfaces through polar head groups and is not a nitrite-based system. Raw material compliance should be confirmed against current REACH Annex XVII restrictions and regional industrial wastewater discharge permits before bulk use.
Before charging an immersion bath, the tank should be cleaned of accumulated rust sludge and metallic fines because suspended iron particles consume inhibitor and can cause dark deposits on parts. The concentrate is added to cold or warm water under agitation; addition to water above 60 °C may produce localized meringue-like foam that is slow to disperse. On agitated immersion lines, the recommended working concentration is 5–10 vol% at 50–70 °C, with contact time of 5–20 min depending on oil loading and part geometry. In low-pressure spray washers operating at 0.2–0.5 MPa, the working concentration is reduced to 1–3 vol% and bath temperature held at 40–60 °C; higher concentrations in spray configuration generate foam that can reduce pump suction pressure. Agitation may be provided by recirculating eductor nozzles, low-frequency ultrasonics at 25–40 kHz, or part rotation. Mechanical action reduces the thermal energy required to remove water-miscible cutting fluids but does not fully substitute for temperature below 40 °C, where emulsification rate and oil splitting capacity decline.
Rinsing immediately after cleaning removes loosened soil and excess alkalinity. A single-stage overflow rinse at 20–40 °C with conductivity below 150 µS/cm is usually sufficient for interstage storage; harder water may leave white mineral film after drying. Drying is performed in forced-air ovens or tunnel dryers at 80–120 °C until surfaces reach ambient temperature. Drying air above 150 °C can darken the protective film and reduce humidity resistance. The residual film is intentionally thin, typically below 0.5 µm dry film thickness; it is not a substitute for oil-based long-term preservatives or barrier coatings.
In high-pressure spray washers, bath life is governed less by surfactant depletion than by the accumulation of emulsified oil and suspended metallic fines. When oil loading exceeds 8–12 g/L, redeposition of oily soils appears on downward-facing surfaces and the cleaning window narrows. Unlike conventional emulsifying cleaners that hold oil indefinitely, 77-2 permits free oil to separate after quiescent standing; this aids oil skimming but requires recirculation before the bath is returned to service. Ultrafiltration side-stream loops or coalescing plate separators extend bath life by removing free oil, but alkaline cleaners cannot remove dissolved oil fractions; a portion of the bath must be drained and replaced at intervals defined by oil titration and pH drop. Biodegradation of surfactants can occur at pH below 8.5 or after extended shutdowns, producing odor and reducing detergency. Biological control is maintained by keeping pH above 9.0, ensuring circulation during idle periods, and avoiding prolonged storage of diluted baths.
Titration against 0.1 N hydrochloric acid to a phenolphthalein or pH 8.3 endpoint is used to estimate free alkalinity; the target free alkalinity is typically 12–20 mL for immersion baths and 5–10 mL for spray baths under the supplier’s method. When the consumed alkalinity is replenished by additions of 77-2, the cleaner-to-inhibitor ratio remains balanced only if the bath is not excessively diluted by drag-out. Make-up additions should be based on titrated alkalinity, not visual appearance alone. A pH electrode is not a substitute for free alkalinity titration because the buffer system can hold pH nearly constant while effective surfactant concentration has already collapsed. Automated dosing based on free-alkalinity titration improves batch-to-batch consistency; manual additions based on bath colour produce wider variation in residual inhibitor concentration.
Process pumps and seals should be selected for alkaline media. EPDM, 316L stainless steel, and polypropylene are generally compatible, while aluminum pump housings, galvanized piping, and brass fittings are not. Heat exchangers should be sized to maintain the specified temperature band because high heat flux surfaces can accelerate scale deposition when using water with hardness above 150 ppm even after softening.
| Parameter | Representative range | Test method or equipment |
|---|---|---|
| Appearance | Clear to slightly hazy amber liquid | Visual inspection |
| Density at 20 °C | 1.08–1.15 g/cm³ | ASTM D4052-18a |
| pH at 3 vol% | 9.0–10.5 | ASTM D1293-18 |
| Flash point | >100 °C closed cup | ASTM D93-20 |
| Immersion concentration | 5–10 vol% | Supplier titration or refractometer |
| Spray concentration | 1–3 vol% | Supplier titration |
| Immersion bath temperature | 50–70 °C | In-tank RTD |
| Spray bath temperature | 40–60 °C | In-tank RTD |
| Rinse water conductivity | <150 µS/cm | ASTM D1125-23 |
| Rinse water temperature | 20–40 °C | In-line RTD |
| Drying air temperature | 80–120 °C | Forced convection |
| Storage temperature | 5–45 °C | Supplier stability data |
Concentrations above 10 vol% in immersion may become difficult to rinse and leave a tacky film that interferes with gauging or adhesive bonding. Concentrations below 5 vol% may clean light soils but provide insufficient rust inhibition in humid environments. This concentration-response relationship creates a process window that should be verified on the actual production line rather than extrapolated from laboratory coupon tests. The flash-rust inhibitor does not require a post-rinse dewatering oil; parts can be welded without removal if film thickness is controlled. Resistance welding may show increased contact resistance if film mass exceeds 0.3 mg/cm², so spot-welding trials are required before high-volume joining.
Substitution of 77-2 for solvent degreasing changes the cleaning mechanism from dissolution in a nonpolar solvent to emulsification and alkaline saponification of fatty acid soils. Chlorinated solvent degreasers dry rapidly and can remove heavy oils from blind holes, but they carry VOC, fire or decomposition hazards, and require sealed equipment. 77-2 reduces solvent handling but adds an aqueous rinse and forced-air drying step and leaves a thin polar inhibitor film. The product is not intended to remove heavy greases on gearboxes with viscosity above ISO VG 320, baked-on carbon deposits, or dry-film lubricants; solvent pre-wiping or high-pressure alkaline cleaning may be required for those soils.
Acid phosphate stages produce inorganic conversion layers that improve paint adhesion by increasing surface area and anchoring the organic coating. 77-2 does not form a phosphate crystal network and is not a paint-base pretreatment. Its anti-rust action is temporary and derived from adsorbed polar inhibitors; under high humidity or condensation, the film can be leached and loses protection. Published data for outdoor exposure with 77-2 alone is limited. In indoor interstage storage at 20–25 °C and relative humidity below 60 %, protection is typically limited to 24–72 h on low-carbon steel; parts stored beyond that period require additional preservative oil or a conversion coating.
Compared with ordinary alkaline cleaners without corrosion inhibition, 77-2 leaves steel surfaces less reactive to flash rust. Most alkaline cleaners remove soils but leave active metal surfaces that can rust within minutes in humid air. The inhibitor package in 77-2 adsorbs preferentially on ferrous surfaces; the deposited amount increases with concentration and residence time. This difference means that 77-2 is not a direct drop-in for a cleaner alone when the line lacks controlled rinsing or drying, because the residual film requires adequate rinse removal and thermal drying to avoid tackiness.
| Property | 77-2 | Chlorinated solvent degreaser | Acid phosphate stage |
|---|---|---|---|
| Cleaning mechanism | Emulsification and saponification | Solvent dissolution | Acid pickling and conversion |
| Operating temperature | 50–70 °C | 40–60 °C vapour condensing | 40–65 °C |
| Rinse stage | Required | Not required | Required |
| Flash-rust protection | Yes, temporary | No | No, but conversion layer passivates |
| Paint adhesion | Not designed as paint base | Not designed as paint base | Yes, conversion layer |
| Waste treatment | Oil splitting and pH neutralization | Solvent recovery or incineration | Acid neutralization and sludge dewatering |
Compliance claims should be verified under current REACH Annex XVII and the EU CLP classification; the safety data sheet is controlling for worker exposure and disposal. VOC content should be determined by ASTM D2369-20; because the product is water-based, the method may require exclusion of water and exempt solvents as defined by the regional regulation. Cleaning performance may be evaluated by water-break-free surface after drying under ASTM F22-13; corrosion-inhibiting properties by humidity exposure under ISO 6270-2:2018 and neutral salt spray under ISO 9227:2022. Because temporary rust-preventive films are sensitive to contact marks, parts should be handled with gloves after treatment.
Avoid combining 77-2 with acidic descalers, cationic polymer quench baths, or amine-cured epoxy wash water because charge neutralization can produce suspended solids and reduce cleaning. Do not use on magnesium, zinc, or unsealed anodized aluminum; the alkaline pH can etch those substrates and generate hydrogen on reactive metals. Parts with deep blind holes or shielded internal cavities require air blow-off and rotation after rinsing to prevent cleaner retention and subsequent staining. Waste baths should be treated by oil splitting at pH 2–3, followed by neutralization and precipitation according to local discharge permits; the oily phase may be removed by skimming or coalescing filtration before discharge to biological wastewater treatment.