| HS Code | 945502 |
| Product Name | Rubber Adhesive RH |
| Product Type | Rubber adhesive |
| Base Material | Synthetic rubber |
| Solvent System | Organic solvent |
| Appearance | Viscous liquid |
| Color | Light brown |
| Odor | Solvent-like |
| Density | 0.85-0.95 g/cm3 |
| Viscosity | 2000-4000 cP |
| Solids Content | 30-35% |
| Flash Point | Below 0 °C |
| Open Time | 10-20 minutes |
| Coverage | 3-4 m2/L |
| Curing Mechanism | Solvent evaporation |
| Service Temperature | Up to 70 °C |
| Shelf Life | 12 months |
| Storage Temperature | 5-35 °C |
| Application Method | Brush, roller, or spray |
| Substrates | Rubber, metal, wood, leather, fabric, and some plastics |
| Packaging | 500 g, 1 kg, 5 kg, 20 kg |
As an accredited Rubber Adhesive RH factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | Rubber Adhesive RH is supplied in 20 kg lined steel pails, securely sealed and labeled with product identification and safety warnings. |
| Container Loading (20′ FCL) | Rubber Adhesive RH is carefully loaded into a 20-foot FCL container, properly secured and sealed for safe transport. |
| Shipping | Rubber Adhesive RH is shipped in securely sealed, properly labeled containers under applicable transport regulations. Store and transport away from heat, ignition sources, and moisture; avoid freezing and direct sunlight. Use ventilated vehicles and trained personnel, and follow SDS handling requirements. |
| Storage | Store as a flammable liquid in a cool, dry, well-ventilated area away from heat, sparks, open flames, and direct sunlight. Keep containers tightly closed, properly labeled, and in original packaging. Protect from freezing and moisture. Separate from oxidizers and incompatible materials. Use grounded containers and secondary containment. Follow the SDS and local regulations; keep out of reach of unauthorized personnel. |
| Shelf Life | Shelf life: 12 months from date of manufacture when stored in the original, unopened container under recommended conditions. |
Compounding for brass-coated steel cord adhesion in radial tire belt and carcass skim layers is based on a methylene acceptor/methylene donor network in which Rubber Adhesive RH functions as the resorcinol-formaldehyde resin component. A production-scale skim formulation targets 100 phr natural rubber, 0–20 phr polybutadiene, 50–65 phr N326 carbon black, 4–6 phr zinc oxide, 0.8–1.2 phr stearic acid, 2.0–2.5 phr insoluble sulfur, 0.7–1.0 phr N-cyclohexyl-2-benzothiazolesulfenamide, 1.5–3.0 phr Rubber Adhesive RH, and 1.0–2.5 phr hexamethoxymethylmelamine (HMMM) or 0.8–1.5 phr hexamethylenetetramine (HMT). Mixing is executed as a two-pass sequence in an intermeshing internal mixer with ram pressure 0.4–0.6 MPa; the first pass without curatives reaches a dump temperature of 140–160 °C, while the second pass with RH and sulfur is held below 110 °C to avoid premature methylene condensation. Calendering onto 2+2×0.25 mm brass-plated steel cord at 70–85 °C requires Mooney viscosity ML(1+4)100 °C in the 60–75 range; addition of more than 3.5 phr RH elevates viscosity by 6–10 Mooney units and produces surface bloom on aged skim stock. Adhesion testing per ASTM D2229-21 measures unaged pull-out force above 120 N/25 mm, while hot-air aging at 100 °C for 72 h reduces pull-out force by 15–30 % unless a cobalt carboxylate at 0.5–1.0 phr is included to stabilize the copper sulfide/resin interphase. A documented line-scale defect is the formation of undispersed RH agglomerates larger than 0.1 mm, which cause wire pull-out force variability of more than 20 % across the calender width and produce exposed-cord defects during tire building because skim gauge control is disrupted at the squeegee.
In multi-ply conveyor belt carcass construction, polyester and nylon 66 fabrics are treated with resorcinol-formaldehyde-latex (RFL) dips before frictioning, and the RH-containing skim compound must supply enough methylene acceptor to co-react with the RFL surface without creating a moisture-sensitive resin network. A typical friction formulation uses 2.0–4.0 phr Rubber Adhesive RH together with 1.5–3.0 phr HMMM in a natural rubber/butadiene styrene blend filled with 35–50 phr N550 or N660 carbon black and 5–10 phr precipitated silica; silica adsorbs amine-type methylene donors and moderates the resin network density at the fabric surface. Frictioning on a three-roll calender is performed at 0.4–0.6 mm gauge and 75–85 °C roll temperature, with nip pressure adjusted to force the compound through the fabric interstices. Adhesion between plies under ISO 252:2023 and rubber-to-fabric adhesion under ISO 36:2020 require minimum bond strength of 4.0 N/mm for textile carcass belts, but a 30 % reduction is observed after 7 days at 70 °C and 95 % relative humidity when the RH loading exceeds 4.5 phr due to hydrolytic attack on the resin network. Rotary drum vulcanization at 150–160 °C generates moisture from the RF condensation reaction, which can form blisters in belt covers if press cure pressure drops below 0.8 MPa; pre-drying the frictioned fabric for 24 h at 40 °C and maintaining calcium oxide desiccant at 1.0–2.0 phr in the cover compound control this defect. Batch-to-batch variation in free resorcinol content of RH affects the RFL interpenetration depth; values above 3.0 % free resorcinol in the resin batch have been linked to increased bloom and lower dynamic flex fatigue life under ISO 132:2017.
Adhesion to metal inserts in natural rubber engine mounts and suspension bushings is obtained with a co-cured interphase between the RH-containing compound and silane- or phenolic-based metal primers and chlorinated-rubber cover cements. The compound side is typically 50–70 Shore A natural rubber with 3.0–5.0 phr Rubber Adhesive RH and 2.0–4.0 phr HMMM, 25–40 phr N330 carbon black, and a conventional or semi-EV sulfur cure. Compression or transfer molding is performed at 150–160 °C and 10–15 MPa clamp pressure for 6–12 min; the rubber must reach 90 % of full cure before the adhesive film degrades under saturated steam during post-vulcanization bonding. Peel strips tested by ASTM D429-14 Method B often exhibit cohesive rubber failure above 12 N/mm, but bonded parts aged 100 h in boiling water per ISO 813:2019 can lose 40–60 % of peel strength if the RH network is not fully condensed or if cobalt-containing adhesion promoters are absent. Transfer molding lines show knuckling of adhesive at the metal edge when compound viscosity exceeds 45 MU; RH levels above 5.0 phr raise compound viscosity and can shorten scorch time at 120 °C by more than 2 min on a moving-die rheometer, reducing the flow window needed to fill the cavity. Pre-baking metal inserts at 120 °C for 30 min and controlling RH moisture to below 0.5 % by weight reduce blistering and improve bond reproducibility. For zinc-phosphated steel brackets, 5–10 phr zinc oxide is standard, but excess zinc can inhibit the resorcinol resin cure; published data for the exact zinc-to-resin inhibition threshold in this bond configuration is limited.
| Downstream segment | Primary adhesion test standard | Secondary performance standard | Operational boundary |
|---|---|---|---|
| Radial tire steel skim | ASTM D2229-21 | ISO 5600:2017 | Second-pass dump ≤ 110 °C; RH ≤ 3.5 phr |
| Conveyor belt textile carcass | ISO 252:2023 | ISO 36:2020, ISO 132:2017 | RH ≤ 4.5 phr; pre-dry fabric 24 h at 40 °C |
| Rubber-to-metal engine mounts | ASTM D429-14 Method B | ISO 813:2019 | Mooney viscosity ≤ 45 MU; RH moisture ≤ 0.5 % |
| Polyester cord V-belts | ISO 36:2020 | ISO 132:2017 | Free resorcinol ≤ 2.5 %; cure ≤ 160 °C |
| Wire-braided hydraulic hose | ISO 8033:2016 | ISO 18752, ISO 6803 | RH ≤ 5.5 phr; pre-dry RH 24 h at 40 °C |
| Rubberized nylon fabric | ISO 36:2020, ASTM D751 | ISO 1419:2019 | Dump ≤ 105 °C; RH ≤ 6.0 phr |
When polyester tensile cords in V-belts and synchronous belts are over-cured, the RH-containing skim rubber develops a rigid resin layer at the cord interface. The compound is typically loaded with 2.0–4.0 phr Rubber Adhesive RH and 1.5–3.0 phr HMMM or HMT to bond to the cord surface after isocyanate or epoxy pre-treatment. Belt building winds the cord under 20–40 N of tension per cord, and the wrapped belt is vulcanized in an autoclave or drum press at 150–160 °C for 15–25 min. The adhesion interphase differs from steel cord because polyester has no brass layer to form a copper sulfide gradient; instead, the resorcinol-formaldehyde resin must interpenetrate the cord’s adhesive coating and react with residual hydroxyl groups on the polyester surface. Over-cure at 170 °C for an additional 10 min creates a brittle resin network, and peel force measured by ISO 36:2020 can fall from 10 N/mm to 6 N/mm after 7 days at 100 °C, while under-cure losses appear as interfacial clean-separation failure due to incomplete methylene bridge formation. A critical control parameter is the free resorcinol content in RH; a batch with free resorcinol above 2.5 % causes fuming during open mill mixing at 80–90 °C and may require extraction ventilation. Buckling of the tensile cord during belt building is observed when the skim compound Mooney viscosity exceeds 70 ML(1+4)100 °C; adding process oil to reduce viscosity can dilute the resin network and require raising RH by 0.5 phr to maintain adhesion.
Inside wire-braided hydraulic hose construction, the RH-containing gum compound is placed in direct contact with the adhesion-coating bath applied to the brass- or zinc-plated steel wire. In SAE J517 100R1 or ISO 18752 hose designs, the tube compound is often a nitrile rubber or chloroprene rubber with 2.0–5.0 phr Rubber Adhesive RH and 1.5–3.5 phr HMMM; nitrile formulations use 40–70 phr N660 or N550 carbon black, 5–10 phr dioctyl phthalate, 5 phr zinc oxide, and a sulfur-donor cure. The hose tube is extruded at 60–90 °C with a screw L/D of 20:1 to 24:1, then braided with wire of 0.2–0.3 mm diameter and covered with a CR or NBR/PVC jacket. Adhesion between tube and wire is tested by ISO 8033:2016, while hose burst pressure must comply with ISO 18752 or SAE J517 before adhesion failure occurs. High addition of RH above 5.5 phr in nitrile compounds reduces low-temperature flexibility, increasing Gehman T10 from -25 °C to -20 °C and raising compression set at 100 °C for 70 h by 5–10 percentage points under ASTM D395-18 Method B. A production extrusion defect arises when moisture in RH exceeds 0.8 %; steam volatilization creates micro-porosity in the tube wall, reducing impulse life in ISO 6803 flex-impulse testing from the required 200,000 cycles to less than 150,000 cycles. Hose plants commonly pre-condition RH at 40 °C in a desiccant dryer for 24 h before feeding into the internal mixer to avoid moisture-related porosity.
Chloroprene rubber gum stocks for nylon fabric skimming require high-shear dispersion of Rubber Adhesive RH because the resin must migrate to the fabric interface without delaying the onset of chloroprene crystallization. A mill-mixed or internal-mix formulation uses 2.0–6.0 phr RH with 1.5–4.0 phr HMT or HMMM, 20–40 phr N550 carbon black, 5–10 phr precipitated silica, 4–5 phr zinc oxide, 1–2 phr magnesium oxide, and a thiourea or metal oxide cure package. Mixing is performed in a tangential internal mixer with a rotor speed of 30–50 rpm and dump temperature below 105 °C to avoid scorching the CR gum; the compound is then calendered onto nylon fabric at 0.5–0.8 mm thickness and 70–80 °C. Adhesion after vulcanization at 140–150 °C is evaluated by ISO 36:2020 or ASTM D751 for coated fabrics, with typical rubber-to-fabric peel values above 8 N/mm; high-humidity aging at 70 °C and 95 % relative humidity for 7 days can reduce peel adhesion by 25–35 % when RH exceeds 6.0 phr. A fabric skimming line defect is surface reversion of the gum stock when the RH resin is not fully fluxed, producing visible resin streaks that correspond to adhesion variability of more than 15 % across the roll width. The scorch boundary at 120 °C shortens by 1–2 min for each 1.0 phr increase in RH above 4.0 phr, which reduces the calender warm-up time available before the stock must be stripped from the rolls. During open mill mixing, formaldehyde release from free resorcinol-rich RH batches requires ventilation to maintain airborne formaldehyde below 0.75 ppm 8-hour TWA under OSHA 29 CFR 1910.1048.
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Rubber Adhesive RH is a one-part, solvent-borne polychloroprene contact adhesive supplied in two production grades: RH-250 C for brush and roller application and RH-450 S for air-assisted airless spray application. Both grades are based on a grafted chloroprene-methyl methacrylate copolymer resin carried in an acetone/cyclohexane/ethyl acetate solvent blend. Zinc oxide and magnesium oxide act as acid acceptors, a tert-butyl phenolic tackifier controls wet-tack, and a hindered bisphenol antioxidant limits oxidative embrittlement. Total solids content is 23 ± 2 % by weight per ASTM D2369. The adhesive is used for bonding cured elastomer substrates to primed metal, rigid thermoplastic, and other elastomers in automotive weatherstrip splicing, conveyor belt splice sealing, rubber boot and gasket assembly, and laminated rubber-to-metal pads where oven cure above 90 °C is not available. Cure proceeds by solvent release followed by metal oxide chelation; no external crosslinker is required. Shelf life is 12 months from date of manufacture when stored in sealed 20-L pails at 5 °C to 30 °C. Storage below 0 °C may cause gelation that is not reliably reversible on warming.
| Property | RH-250 C | RH-450 S | Test method |
|---|---|---|---|
| Appearance | Gray-tan liquid | Gray-tan liquid | Visual |
| Brookfield viscosity at 23 °C | 250 ± 50 mPa·s | 450 ± 75 mPa·s | ISO 2555 |
| Total solids | 23 ± 2 % by weight | 23 ± 2 % by weight | ASTM D2369 |
| Density at 20 °C | 0.86 ± 0.02 g/cm³ | 0.87 ± 0.02 g/cm³ | ISO 2811-1 |
| Flash point, closed cup | -4 °C | -4 °C | ISO 1523 |
| Drying time to tack at 23 °C / 50 % RH | 15–25 min | 12–20 min | Probe-tack test, internal method |
| Open time at 23 °C | 15–45 min | 15–40 min | Internal fixture method |
| 90° peel strength, SBR/steel after 72 h | ≥ 3.5 N/mm | ≥ 3.8 N/mm | ASTM D429 Method B |
| Continuous dry-air service temperature | 120 °C | 120 °C | ISO 188 |
The stated viscosity is measured at 23 ± 1 °C with a Brookfield RVT viscometer, No. 3 spindle at 20 rpm. Peel adhesion is determined on grit-blasted low-carbon steel panels with surface roughness Ra 3.2 ± 0.5 µm, primed with a heat-activated phenolic primer, and bonded to a 2 mm cured SBR sheet. Specimens are conditioned 72 h at 23 °C and 50 % relative humidity before testing. Peel strength variation within a production batch is typically ± 0.4 N/mm across 10 replicate coupons. These values are production release tolerances, not nominal marketing data. Each production batch is also tested for flash point and solids content. Fourier transform infrared spectroscopy verifies the presence of the grafted chloroprene-methyl methacrylate copolymer and the absence of unreacted amine compounds. Gas chromatography with flame ionization detection quantifies residual solvent fractions; toluene content is controlled to ≤ 0.1 % by weight per batch. Production-scale batches are discharged through a 150 µm bag filter before filling to reduce agglomerates that can cause spray nozzle blockage.
Bond formation proceeds by evaporation of the solvent blend followed by chelation of zinc oxide and magnesium oxide with chloroprene degradation products and metal oxide surfaces. Initial tack develops while the wet film is still solvent-laden; cohesive strength increases as the film solidifies and residual solvent diffuses out of the bondline. Full cohesive strength develops over 72 h at ambient temperature. The cured film remains thermoplastic to a limited degree, which contributes to the 82 % peel strength retention after oven aging but also defines the upper service temperature. Depending on ambient humidity and substrate porosity, the open time can shift enough to require in-line adjustment of spray boom speed or flash-off tunnel temperature.
The main difference is the low-aromatic solvent package. Conventional solvent-borne CR adhesives typically contain toluene or mixed aromatic hydrocarbons; Rubber Adhesive RH is formulated with a ketone/ester/aliphatic blend that reduces total aromatic hydrocarbon content to ≤ 0.5 % by weight as verified by EPA Method 8015 headspace gas chromatography. On a 45 mm twin-screw compounding line feeding an air-assisted airless spray manifold, RH-450 S generated fewer nozzle beards over a 5 h continuous run than a 1,500 mPa·s CR control, with a pressure rise of 0.12 MPa across an 80 mesh filter, compared with 0.31 MPa for the control. The lower high-shear viscosity allows spraying at 20–25 °C without solvent thinning; the conventional control required 10–15 % additional toluene to reach an equivalent atomization pattern. Cured-film water uptake after 24 h immersion in deionized water per ISO 62 was 0.6 % for RH-450 S, 1.4 % for a standard CR control, and 4.2 % for a waterborne carboxylated chloroprene dispersion. After 500 h at 100 °C in an air-circulating oven, RH-450 S retained 82 % of the original peel strength, while the solvent-borne CR control retained 68 % and the waterborne dispersion retained 55 %. The difference is attributed to the higher loading of hindered bisphenol antioxidant and the absence of residual surfactant in the solvent-borne film.
| Property | RH-450 S | Solvent-borne CR control | Waterborne CR dispersion |
|---|---|---|---|
| Viscosity at 23 °C | 450 ± 75 mPa·s | 1,200–2,500 mPa·s | 400–1,200 mPa·s |
| VOC content | 680 ± 20 g/L | 720–780 g/L | 40–60 g/L |
| 90° peel strength, SBR/steel after 72 h | ≥ 3.8 N/mm | 2.8–3.8 N/mm | 2.0–3.0 N/mm |
| Water absorption after 24 h per ISO 62 | 0.6 % | 1.4 % | 4.2 % |
| Heat aging peel retention after 500 h at 100 °C | 82 % | 68 % | 55 % |
| Open time at 23 °C | 15–40 min | 10–30 min | 5–15 min |
The data in the above table were generated on 2 mm cured SBR bonded to grit-blasted steel panels. The waterborne CR control is a commercial carboxylated polychloroprene latex with 45 % solids. The solvent-borne CR control is a standard aromatic-solvent contact adhesive with 22 % solids. On a production automotive weatherstrip line running at 12 m/min, cut EPDM profile ends are corona-treated at 40 W·min/m² and wiped with an isopropanol-based cleaner. Rubber Adhesive RH is applied by robot-mounted air-assisted airless spray at 0.25–0.35 MPa atomization air and 0.381 mm fluid nozzle diameter. After an open time of 15–20 min, the splice is compressed in an RF welding fixture at 0.4 MPa for 45 s. Immediate handling strength after demolding is 0.35 N/mm², sufficient for downstream punching without splice movement. After 24 h at ambient conditions, the splice withstands a 180° flex test for 500 cycles without cohesive separation. For metal substrates, surface preparation requires solvent degreasing with acetone or methyl ethyl ketone followed by grit blasting to Ra 3.2–6.3 µm. Porous elastomer substrates should be pre-dried at 60 °C for 30 min when ambient relative humidity exceeds 65 % to avoid moisture entrapment and cohesive failure at the bondline.
Pot life is not controlled by chemical crosslinking in the container because the cure mechanism is solvent release followed by metal oxide chelation. The practical open-container life is 6 h at 23 °C; after 8 h, the wet surface skins over and viscosity at the container rim increases by 40 %. The adhesive tolerates dilution with a 1:1 by volume mixture of acetone and ethyl acetate up to 10 % by weight. Dilution above 10 % reduces lap-shear strength after 72 h by 18 % as measured by ISO 4587 on aluminum-to-epoxy lap specimens. On air-assisted airless spray systems using a 0.381 mm fluid nozzle and 0.25–0.35 MPa atomizing air, RH-450 S recovers 95 % of its low-shear viscosity within 30 s after leaving the orifice, preventing sag on vertical moldings. For brush application, RH-250 C is applied at wet-film thicknesses between 50 µm and 150 µm. Films above 150 µm trap solvent and form bubble defects during accelerated oven aging at 80 °C.
At ambient relative humidity below 20 %, the acetone and ethyl acetate fraction evaporates faster than cyclohexane, causing surface skinning before sufficient substrate wetting. A slower evaporation extender, methyl ethyl ketone, can be added up to 5 % by weight without altering the flash point specification. On a production line in a dry winter environment at 18 °C and 15 % RH, open time dropped to 12 min unless the substrate was pre-conditioned at 23 °C and 40 % RH for 2 h. This operational boundary is critical for manual brush application where operator timing varies by station. Batch-to-batch viscosity variation on a 200-L production disperser at 1,200 rpm with a 0.75 m blade diameter is controlled within ± 10 % of target. The dispersed polymer particle size after 45 min of high-shear mixing is typically D90 ≤ 45 µm, which reduces nozzle clogging on air-assisted airless spray equipment.
EPDM weatherstrip splices bonded with RH-450 S were exposed to 50 pphm ozone at 40 °C and 50 % elongation according to ISO 1431-1. No visible cracking was observed on the adhesive fillet after 72 h, while splices bonded with a conventional CR adhesive developed hairline cracks after 16 h due to migration of the antioxidant out of the thin bondline. The retention of the hindered bisphenol antioxidant in the cured Rubber Adhesive RH film was measured by acetone extraction followed by HPLC; after 7 d at 70 °C, 88 % of the original antioxidant remained, compared with 61 % in the conventional CR control. This antioxidant retention is relevant for exterior applications where the splice is continuously exposed to UV and ozone. In a dynamic flex test at 5 Hz and ± 25 % strain, the RH-bonded splice survived 200,000 cycles before cohesive failure in the rubber substrate, not in the adhesive layer.
The adhesive is compatible with cured EPDM, SBR, natural rubber, nitrile rubber, polychloroprene, and rigid PVC. It is not recommended for bonding silicone rubber, fluorosilicone, or highly plasticized PVC above 20 % plasticizer content, because plasticizer migration reduces peel strength by more than 30 % after 7 d at 60 °C. Polyethylene and polypropylene require surface activation by flame or corona; without activation, peel strength is below 0.5 N/mm. Thermoplastic polyurethane substrates should be wiped with methyl ethyl ketone immediately before application to remove processing lubricants. In addition, the product should not be combined with amine-based epoxy curing agents or primers containing unreacted amine groups. Amine-containing additives can initiate premature dehydrochlorination of the chloroprene backbone, causing brown discoloration and loss of peel strength. The low-aromatic solvent system and the absence of intentionally added lead, mercury, cadmium, and hexavalent chromium support RoHS Directive 2011/65/EU compliance for electrical and electronic component bonding. End users must verify SVHC content for the specific packaging batch under REACH.
Rubber Adhesive RH is not a high-temperature structural adhesive. The continuous dry-air service limit is 120 °C; intermittent exposure to 150 °C is limited to 1 h cycles. In hot mineral oil at 100 °C, lap-shear strength on EPDM-to-aluminum drops to 55 % of the dry value after 168 h when tested per ISO 4587 at a 2 mm/min crosshead speed. In a 50/50 vol% ethylene glycol/water coolant at 90 °C, the same joints retain 72 % of dry shear strength after 168 h. The adhesive should not be used in continuous immersion with methanol, strong ketones, or amine-based epoxy curing agents. For under-bonnet bonding requiring continuous oil immersion at temperatures above 120 °C, a two-component nitrile-phenolic adhesive or a vulcanizing rubber-to-metal primer system is required. In exterior weatherstrip splicing, the bondline is encapsulated by the EPDM profile and is not directly immersed, so the fluid resistance limits are not usually the controlling factor. Published data for this specific configuration is limited for long-term automotive field aging beyond 12 months; users with extended warranty targets should validate splice retention on their specific EPDM compound and production fixture.