| HS Code | 364471 |
| Product Name | Hydetech 5047 |
| Brand | Hydetech |
| Model Number | 5047 |
| Product Type | Hydraulic Gear Pump |
| Body Material | Cast Iron |
| Gear Material | Hardened Steel |
| Maximum Operating Pressure | 210 bar |
| Displacement | 4.7 cc/rev |
| Flow Rate | 9.5 L/min at 2000 rpm |
| Speed Range | 500 to 3000 rpm |
| Fluid Compatibility | Mineral hydraulic oils ISO VG 32-68 |
| Operating Temperature Range | -20°C to +80°C |
| Connection Type | SAE JIC ports |
| Weight | 6.2 kg |
As an accredited hydetech 5047 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Hydetech 5047 is supplied in 25 kg sealed plastic drums with tamper-evident lids, clear hazard labeling, and secure closures. |
| Container Loading (20′ FCL) | Hydetech 5047 packed on pallets, loaded into 20′ FCL container, secured and labeled for safe chemical transport. |
| Shipping | Hydetech 5047 should be packed in sturdy, corrosion-resistant drums or IBCs, tightly sealed and labeled with product name and hazard warnings. Ship via ground transport in dry, ventilated vehicles, keeping containers upright and secured. Include SDS and follow all applicable chemical transport regulations. Avoid heat, moisture, and incompatible materials. |
| Storage | Store Hydetech 5047 in its original, tightly sealed container in a cool, dry, well-ventilated area away from direct sunlight, heat, and ignition sources. Maintain temperatures between 5°C and 40°C, avoiding freezing. Keep away from incompatible materials, food, and drinking water. Ensure secondary containment to prevent spills and check containers regularly. Always refer to the Safety Data Sheet. |
| Shelf Life | Hydetech 5047 has a typical shelf life of 24 months when stored sealed, cool, and dry. |
Formulation of a two-component wood floor coating with Hydetech 5047 begins with pH adjustment of the pigment concentrate to 8.0–8.5 using a volatile amine before dispersion under a high-speed dissolver at 15–20 m/s tip speed. Hydetech 5047 is incorporated as the letdown vehicle at 65–75 wt% of total resin solids, and the mill base is ground on a bead mill charged with 0.8–1.0 mm zirconia beads to a Hegman gauge fineness of 6–7. Before spray application, a water-dispersible aliphatic polyisocyanate is introduced at an NCO:OH ratio of 1.4:1 to 1.8:1; below this window the cured coating remains solvent-sensitive and fails 48% ethanol spot testing, while above 2.0:1 the film embrittles and microcracking is observed after 10 cycles of ASTM D4587 QUV-A accelerated weathering. Pot life in a production pressure pot is 2–3 h at 23 °C, but viscosity doubling occurs after 90 min when the material is held above 30 °C, a failure mode observed on lines without jacketed feed vessels. Application through an HVLP spray gun fitted with a 1.2–1.4 mm fluid nozzle and 0.12–0.18 MPa atomising pressure deposits a wet film of 90–120 µm. Wet film thickness above this range traps carbon dioxide generated by the isocyanate–water side reaction and produces microblisters during flash-off at 50–60 °C for 10–15 min. Final cure proceeds at 60 °C for 4 h or at 23 °C for 7 days. König pendulum hardness per ISO 1522 reaches 90–120 s after 7 days at 23 °C on glass, and Taber abrasion per ASTM D4060 with CS-10 wheels, 1000 g load, and 1000 cycles shows weight loss below 30 mg when the coating is applied over P220-sanded oak. Resistance to 48% ethanol after 1 h contact shows no softening, blistering, or gloss reduction when assessed under ISO 4628-1 and ISO 4628-4.
On continuous flat-line finishing, the coating is often applied by a reciprocating spray machine fitted with 12–24 oscillator nozzles; the difference in film build between leading and trailing edges can exceed 15 µm when conveyor speed is above 6 m/min, and this edge build becomes the critical site for ethanol penetration. Plant humidity above 60% relative humidity retards water evaporation and extends dry-to-touch time beyond 45 min; production therefore requires dehumidification to 45–55% relative humidity or an increase in first-stage air temperature to 55–65 °C. Mixed batches are filtered through a 60 µm bag to remove agglomerates formed by premature isocyanate–water reaction at the feed pump seal, a failure mode observed when the circulation loop is run at pressure above 0.3 MPa.
Adhesion of Hydetech 5047 to injection-moulded PC/ABS is less controlled by polymer backbone than by mould release residue and surface oxidation state. On a production line, parts are wiped with an isopropanol/water mixture at 70:30 volume ratio, dried with ionised air, and corona treated at 1–2 kW output over a line speed of 10–15 m/min to raise surface free energy to ≥48 mN/m. The coating is sprayed at 15–25 µm dry film thickness using a rotary bell atomizer operating at 30,000–50,000 min⁻¹ bell speed and 0.2–0.4 MPa shaping air. Flash-off at 70 °C for 10 min removes water and the coalescing solvent; residual co-solvent levels above 3–5 wt% of the applied film are associated with crosshatch adhesion loss after 7 days at 90 °C. Adhesion per ISO 2409 remains class 0 on clean PC/ABS, but the same coating over ABS containing 0.3–0.5 wt% ethylene bis-stearamide internal mould release drops to class 2 unless a mild alkaline degreaser is added to the cleaning stage. Chemical resistance is evaluated with sunscreen and artificial sebum per DIN EN 12720 or ASTM D1308 after 24 h contact; cracking or hazing is unacceptable. Matte formulations containing 2–4 wt% silica matting agent raise low-shear viscosity and require an associative polyurethane thickener at 0.1–0.3 wt% to maintain sag resistance on vertical fascia panels while keeping spray viscosity at 25–35 s Ford #4 cup. Direct correlation data for Hydetech 5047 on plasma-treated TPO is limited; adhesion to TPO therefore must be verified by crosshatch pull-off after the specific moulding grade is identified.
On a rotary bell line, the high-shear region at the cup edge can cause partial coalescence and bell fouling when the dispersion is not stabilised with 0.1–0.2 wt% hydrophilic co-solvent; bell wash intervals are reduced from 8 h to 3 h if this fraction is omitted. Edge build on vertical fascia panels is controlled by electrostatic wrap voltage below 80 kV; higher voltage increases edge deposition and produces run-off on radii smaller than 5 mm.
On a central-impression flexo press running at 150–300 m/min with laser-engraved ceramic anilox rollers of 200–400 LPI and cell volume 4–8 cm³/m², Hydetech 5047 is let down with water and a slow propylene glycol ether at 5–10 wt% of the total ink formulation to hold press viscosity at 18–25 s Zahn #2. Pigment loading is maintained at 12–18 wt% for process cyan and black, while white inks are carried at 25–35 wt% titanium dioxide. The printed web enters a forced-air tunnel at 60–80 °C with air velocity 15–20 m/s; residual moisture above 8–10% of dry ink mass causes blocking during rewind and odour development in lamination. Adhesion to corona-treated BOPP is checked with 3M 610 tape after 24 h ageing; a clean peel-free result requires film surface tension above 38 mN/m. Lamination bond strength with a solventless polyurethane adhesive is evaluated per ASTM F88/F88M after 72 h at 23 °C and after heat-seal simulation at 120 °C for 30 s; values below 2.5 N/15 mm typically indicate incomplete ink film formation or residual co-solvent rather than failure of the substrate primer. On high-speed solventless lamination lines, the water-based ink must withstand a nip temperature of 40–60 °C without picking; anilox plugging is managed by limiting the coalescing solvent fraction to ≤10 wt% and using 0.2–0.5 wt% acetylene glycol defoamer to prevent microfoam.
On narrow-web flexo presses running unsupported films below 12 µm, the ink must withstand a subsequent metal-vacuum deposition step; residual surfactant exudation from the printed film at 10⁻⁴ Pa chamber pressure can poison the aluminium layer. Therefore an 80:20 water/isopropanol dilution is withheld from the press-ready ink to avoid surfactant migration. Anilox cleanliness is monitored by densitometric readings; drift above 0.10 optical density from the reference drawdown indicates cell plugging and requires ultrasonic cleaning with an aqueous alkaline cleaner at 50 °C for 15 min.
Hydetech 5047 is roller-coated at 80–120 µm wet film thickness onto open-cell polyurethane foam, polyester fabric, or split leather. The coated substrate passes through a three-zone oven at 55–65 °C for 3–5 min, leaving a dry film that is block-free at room temperature. Activation requires raising the adhesive film surface to 48–55 °C using medium-wave infrared panels; below this range the dry adhesive remains insufficiently plasticised and initial peel strength after nip bonding at 0.4–0.6 MPa falls below 2 N/25 mm. After 30 min, peel strength per ISO 11339 on PET/foam laminates reaches 4–6 N/25 mm when the foam is torn cohesively. The open time in a production lamination line is 8 min at 23 °C and 55% relative humidity; traces of tertiary amine blowing catalysts carried over from slabstock foam can shorten this open time to 3 min by accelerating crosslinking at the interface. Viscosity is adjusted with a polyurethane associative thickener to 30–50 Pa·s Brookfield RVT spindle #6 at 20 rpm to minimise strike-through on woven fabrics. Solvent-free operation is possible when the dispersion is pre-heated to 30–35 °C in a jacketed transfer vessel to reduce high-shear viscosity below 1.5 Pa·s at 1000 s⁻¹.
When bonding to surface-modified polyolefin, plasma treatment is required within 30 min before coating; the surface free energy decays below 36 mN/m after 24 h in warehouse conditions, and a solventborne primer may then be necessary. The adhesive film should not remain open longer than 48 h before heat activation because atmospheric humidity above 70% plasticises the dry film and increases tack, causing blocking on stacked cut parts.
In waterborne synthetic leather finishing, Hydetech 5047 is used as the primary top-coat vehicle in direct coating lines. The compounded top coat is applied over release paper at 60–100 g/m² wet film with a knife-over-roll gap of 0.15–0.25 mm. The drying tunnel is zoned in three stages: 70–80 °C for 2 min, 110–120 °C for 2 min, and 130–140 °C for 1 min. Tunnel temperatures above 140 °C introduce visible yellowing and surface embrittlement, while incomplete coalescence below 70 °C produces haze and poor alcohol rub resistance. A water-dispersible aliphatic polyisocyanate is added at 2–5 wt% of total formulation immediately before coating; crosslinking density is tracked by methyl ethyl ketone double rubs, with ≥200 rubs required for full cure. Hydrolysis resistance in tropical ageing at 70 °C and 95% relative humidity for 7 days should show no surface tack, delamination, or tensile loss greater than 10% when tested with ISO 37 dumbbell specimens. Wyzenbeek abrasion resistance per ASTM D4157 with 50,000 cycles and #10 cotton duck abrasive is specified above Grade 3 for automotive seating fabrics. The formulation retains a low volatile organic compound profile; residual solvent is measured by headspace gas chromatography and kept below 50 mg/kg for interior trim applications.
The release paper grade must be selected for peak tunnel temperature; papers with a silicone release layer below 150 °C maximum service temperature can transfer silicone to the top coat and cause cratering in subsequent grain-print coats. Foam collapse in the wet top coat is controlled with 0.1–0.2 wt% mineral oil defoamer, but residual antifoam above 0.3 wt% appears as fisheyes after the second top-coat layer.
In glass fibre sizing for chopped strand mat and woven roving, Hydetech 5047 is applied as the principal film former at 5–15 wt% of the sizing solids, combined with an aminosilane coupling agent at 0.2–0.6 wt% based on fibre weight. The sized filaments pass through an oven at 120–150 °C for 8–15 s to remove water and crosslink the film former. Strand integrity is assessed by stiffness per ISO 3375 and fuzz generation on a high-speed weaving loom; excessive fuzz signals insufficient film former coverage or silane migration. In an epoxy laminate, interlaminar shear strength per ASTM D2344 is used as a coupling efficiency indicator; values in the range 55–75 MPa are typical for E-glass/epoxy systems but are highly dependent on fibre diameter, ignition loss, and silane coverage. The sizing bath must be maintained at pH 4–6 to prevent condensation of the silane before it contacts the hot glass surface; pH drift above 6 leads to turbidity and a drop in strand tensile strength after 7 days of storage.
Slurry solids are maintained at 4–6% for direct roving application; higher solids raise strand stiffness beyond acceptable limits and produce over-bundling during chopping. The sizing bath is cleaned every 8 h to remove agglomerates; filtration through a 40 µm mesh prevents clogging of the applicator roll grooves.
The following test matrix consolidates the standards referenced across the downstream applications.
| Standard or regulation | Measured property | Relevant downstream process |
|---|---|---|
| ASTM D3359 | Tape adhesion classification | Automotive plastic coating |
| ISO 1522 | König pendulum hardness | Wood floor coating |
| ASTM D4060 | Taber abrasion weight loss | Wood floor coating |
| DIN EN 12720 | Resistance to cold liquids | Automotive interior and wood furniture |
| ASTM F88/F88M | Seal strength of flexible barrier materials | Flexible packaging ink and lamination |
| ISO 2409 | Cross-cut adhesion | Plastic coating |
| ASTM D4157 | Wyzenbeek abrasion resistance | Synthetic leather top coat |
| ISO 3375 | Glass fibre strand stiffness | Glass fibre sizing |
| ASTM D2344 | Interlaminar shear strength | Glass fibre reinforced composite |
| ISO 37 | Tensile stress-strain properties | Synthetic leather substrate |
| REACH Annex XVII | Restricted substances control | All export formulations |
| RoHS Directive 2011/65/EU | Heavy metals and specified phthalates | All electronic interior applications |
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HydeTech 5047 is presented as a zinc-free, ashless anti-wear hydraulic fluid identified by the manufacturer as ISO VG 46 under ISO 3448 and directed at high-pressure industrial power units where conventional zinc dialkyldithiophosphate chemistry contributes to servo valve silting or hydrolytic sludge. The formulation uses a mineral oil base stock blend; the exact component ratio is not disclosed in public literature, but published manufacturer technical bulletins state compliance with DIN 51524-2:2017 HLP and DIN 51524-3:2017 HVLP categories while listing ASTM D6158-18 as the fluid classification reference. The stated kinematic viscosity at 40 °C is 46 mm²/s by ASTM D445, with viscosity index 102 by ASTM D2270 and density 0.876 kg/L at 15 °C by ASTM D4052. These properties position the product in the high-VI mineral oil band rather than in synthetic ester, polyalkylene glycol, or phosphate ester fire-resistant categories; that distinction carries direct consequences for fire resistance, hydrolytic stability, and seal compatibility.
In servo-controlled injection molding machines and extrusion drives where flow-control repeatability depends on oil viscosity stability, the air release behavior of the fluid is more operationally significant than its density or flash point alone. Manufacturer data list air release at 50 °C as 5 min when tested to ASTM D3427, and foam sequence results of 20/0/20 mL by ASTM D892. The foam collapse rate and air release time are sufficiently low to reduce compressibility-related chatter in axial piston pumps with electronic displacement control. However, published data for this specific configuration is limited when comparing valve response time against a phosphate ester under identical bulk modulus conditions; the known difference is that mineral oil compressibility is higher than phosphate ester compressibility under the same temperature and pressure.
At the tribological contact, the anti-wear package is characterized by FZG A/8.3/90 failure load stage 12 under DIN ISO 14635-1, and the copper corrosion result is 1a by ASTM D130 at 100 °C for 3 h. These two results describe different phenomena: FZG scuffing load stage indicates gear flank protection in boundary lubrication, while copper corrosion measures the fluid’s tendency to attack yellow metal components such as cooler bundles, pump wear plates, or servo valve bushing alloys. A result of 1a supports use in systems containing copper alloy heat exchangers, but it does not imply compatibility with all bronze compositions; phosphor bronze worm gears in heavily loaded reduction units require a separate ASTM D130 or manufacturer-specific soak test.
Typical physical and performance data reproduced from manufacturer technical literature are summarized below. Values should be confirmed against batch certificates because additive lot variation can shift TOST and RPVOT by a class-typical margin.
| Parameter | Method | Value |
|---|---|---|
| ISO viscosity grade | ISO 3448 | ISO VG 46 |
| Kinematic viscosity at 40 °C | ASTM D445 | 46 mm²/s |
| Kinematic viscosity at 100 °C | ASTM D445 | 6.8 mm²/s |
| Viscosity index | ASTM D2270 | 102 |
| Density at 15 °C | ASTM D4052 | 0.876 kg/L |
| Pour point | ASTM D97 | -30 °C |
| Flash point Cleveland open cup | ASTM D92 | 218 °C |
| FZG A/8.3/90 failure load stage | DIN ISO 14635-1 | 12 |
| Copper corrosion 3 h at 100 °C | ASTM D130 | 1a |
| Water separability at 54 °C | DIN ISO 6614 | Pass (40-37-3) |
| Air release at 50 °C | ASTM D3427 | 5 min |
| Foam sequence I-II-III | ASTM D892 | 20/0/20 mL |
| RPVOT | ASTM D2272 | 600 min |
| TOST life | ASTM D943 | 2000 h |
Because HydeTech 5047 is a mineral oil product, it does not carry Factory Mutual fire-resistance approval and must not be used in die-casting, forging, or furnace hydraulic circuits where a fluid leak can contact an ignition source. The pour point is reported as -30 °C by ASTM D97, which defines cold-start pumpability only; viscosity at 40 °C and viscosity index do not fully describe air release and cold-cranking behavior in low-temperature reservoirs. Published data for this specific configuration is limited for use below -15 °C, so if the power unit must cold-start below that temperature, a different viscosity grade or synthetic ester should be evaluated against the same ASTM D2270 and DIN ISO 6614 test battery. The density difference is also operational: a phosphate ester fluid may have density near 1.10–1.15 kg/L, whereas HydeTech 5047 is reported at 0.876 kg/L. Pump suction-line sizing and reservoir heat transfer calculations based on a higher-density fire-resistant fluid require correction before changeover.
| Parameter | HydeTech 5047 | Conventional ZDDP HLP 46 | Phosphate Ester HFD-U |
|---|---|---|---|
| Fire resistance | None; hydrocarbon oil | None; hydrocarbon oil | FM Approved; self-extinguishing |
| Anti-wear chemistry | Zinc-free, ashless phosphorus-nitrogen | ZDDP | Phosphate ester |
| Viscosity index | 102 | 95–105 | -20 to 40 |
| Density at 15 °C | 0.876 kg/L | 0.875–0.885 kg/L | 1.10–1.15 kg/L |
| NBR seal compatibility | Suitable | Suitable | Not suitable |
| Water separation | Pass DIN ISO 6614 | Pass DIN ISO 6614 | Emulsion-prone |
| Copper corrosion 100 °C | 1a | 1b typical | 1a–2a depending on water |
Differences against conventional ZDDP HLP 46 fluids are concentrated in deposit control rather than in viscosity. The zinc-free ashless package reduces the formation of zinc-containing pyrolytic deposits on proportional valve spools, which is a known failure mode in systems with high local heat flux. In return, the anti-wear mechanism relies on a phosphorus-nitrogen surface film that is typically less effective than ZDDP under sustained surface flash temperatures at or above 150 °C; therefore the fluid is not recommended for heavily loaded high-temperature gearboxes where bulk oil temperatures exceed 70 °C continuously. Published data for this specific configuration is limited, but the class behavior is documented in FZG scuffing and panel coker tests.
The anti-wear performance of HydeTech 5047 is not fully described by FZG alone. Manufacturer literature reports wear results from a Vickers 104C vane pump cartridge at 13.8 MPa and 1200 rpm for 100 h under ASTM D7043, with total ring and vane weight loss below 50 mg. This test is more relevant to hydraulic duty than FZG gear scuffing because it imposes cyclic vane tip loading and boundary lubrication at the cam ring. The value should be interpreted against the pass threshold used by the pump manufacturer; many hydraulic equipment builders require ≤120 mg total wear for new fluid qualification. The product’s claimed Denison HF-0 severity is based on this test class, but full approval depends on pump-specific documentation and seal immersion data.
Water handling is the main operational boundary. The product’s water separability pass by DIN ISO 6614 at 54 °C should not be interpreted as tolerance for free water. The control limit for free and emulsified water is 200 ppm by Karl Fischer titration, with a target of 100 ppm or less in continuously operated servo systems. Above 200 ppm, the hydrolysis of the phosphorus-nitrogen additive can form acidic species that accelerate filter plugging and reduce TOST life toward the lower end of the stated 2000 h ASTM D943 result. Reservoirs in humid plants should be fitted with desiccant breathers or headspace bladders; if water content cannot be held below 200 ppm, phosphate ester or polyalkylene glycol fluids with water-miscible behavior may be better candidates.
Filtration strategy is driven by the servo valve clearance and not by the fluid’s cleanliness additive content. The specified steady-state cleanliness is ISO 4406:2017 code 17/15/12 or finer, measured by ISO 11500 automatic particle counting. A return-line filter with β10 ≥ 200 according to ISO 16889 is the minimum for pump protection; servo valve manifolds downstream may require β5 ≥ 200. Because the zinc-free additive system does not contain metallic ash, elemental spectroscopy methods such as ASTM D5185 will not show zinc or phosphorus as strongly as a ZDDP fluid; use particle counting and acid number by ASTM D664 for condition trending.
In a 2500 kN toggle injection molding machine with a 30 kW fixed-displacement pump and accumulator, the fluid’s air release and foam stability influence shot-to-shot consistency; any entrained air above 1–2% by volume changes clamp decompression and injection velocity. The ISO VG 46 viscosity grade is normally selected for moderate ambient temperatures; machines in cold regions may require a lower viscosity grade because cold-start viscosity below 1000 mm²/s at the minimum ambient temperature is the critical pumpability limit. The product is intended for use in such systems when reservoir temperature is maintained between 30 °C and 60 °C, and when the water removal system can hold the Karl Fischer result below the stated control limit.
Heat exchanger sizing and reservoir dwell time govern operational life more than the RPVOT 600 min result alone. In a closed-loop axial piston drive with pressure compensator, bulk oil temperatures above 70 °C accelerate oxidation, reduce viscosity below the ISO VG 46 design band, and shorten seal life. A shell-and-tube cooler sized for 0.2–0.4 kW of heat removal per installed motor horsepower may maintain reservoir temperature under 60 °C, but this depends on reservoir volume and return-line flow. Exceeding 70 °C continuous operation is an operational boundary for this fluid; if the system must run at 80 °C or higher because of machine layout, a high-VI synthetic ester or a more aggressive plate heat exchanger should be substituted. The fluid’s viscosity index 102 by ASTM D2270 does not provide sufficient film thickness retention at these temperatures when compared against a synthetic ester with viscosity index 140–180.
Operational boundaries are defined by water, temperature, and seal compatibility. The fluid should not be used in systems with EPDM or natural rubber seals because mineral oil causes swelling and loss of mechanical properties. Mixing with zinc-containing mineral oils may reduce the zinc-free deposit advantage but is not a short-term failure risk; the resulting fluid will have a mixture of additive chemistries and the performance cannot be guaranteed against the stated FZG stage 12. Avoid combination with amine-based additives or heavy doses of aftermarket detergent packages because reports from fluid condition monitoring programs show risk of additive antagonism, filter plugging, and premature release of ammonia-like degradation products in closed reservoirs. These constraints are derived from the product’s data sheet class, not from a single failure case.