| HS Code | 214826 |
| Product Name | Super Soft and Smooth Silicone Oil RH-NB-8602 |
| Model | RH-NB-8602 |
| Product Type | Silicone oil |
| Appearance | Colorless to light yellow transparent liquid |
| Ionicity | Weak cationic |
| Ph 1 Aqueous Solution | 5.0-7.0 |
| Solid Content | 90% ± 2% |
| Viscosity | 1000-3000 mPa·s |
| Solubility | Soluble in water |
| Function | Imparts super soft and smooth hand feel |
| Application | Textile finishing for cotton, polyester, and blends |
| Suitable Fibers | Cotton, polyester, and blends |
| Shelf Life | 6 months |
| Storage | Store in a cool, dry, ventilated place; avoid direct sunlight |
| Packaging | 120 kg plastic drum |
As an accredited Super Soft and Smooth Silicone Oil RH-NB-8602 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | RH-NB-8602 is supplied in 200 kg plastic drums or 1,000 kg IBC totes, securely sealed for safe storage and transport. |
| Container Loading (20′ FCL) | Non-hazardous RH-NB-8602 Super Soft and Smooth Silicone Oil loaded in 20′ FCL as palletized, shrink-wrapped, strapped drums, secured for export. |
| Shipping | Ship as a non-hazardous silicone oil in sealed plastic drums or IBC totes. Store in a cool, dry, ventilated area away from direct sunlight, heat, moisture, and contamination. Handle with appropriate PPE and follow the SDS and local transport regulations. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat sources, sparks, and open flames. Keep containers tightly closed, upright, clearly labeled, and protected from physical damage. Avoid contact with strong acids, alkalis, and oxidizing agents. Maintain the recommended storage temperature, prevent freezing, and follow local regulations and SDS guidance. |
| Shelf Life | Store in original sealed container in a cool, dry, ventilated place; shelf life is typically 12 months under proper storage conditions. |
During exhaust finishing of cotton terry towelling in low-liquor-ratio soft-flow jet machines, RH-NB-8602 is emulsified with a nonionic surfactant system and introduced as a fine aqueous dispersion after the last reactive dye soaping cycle and before the final clear overflow rinse. Residual fabric alkali must be below 0.10 g/L NaOH and the bath adjusted to pH 5.0–5.5 with acetic acid; at pH above 6.5, the emulsion destabilises on the fabric surface and generates non-reworkable silicone spots. Addition at 1.5–3.0% owf is circulated for 18–25 min at 35–40°C in a machine with liquor ratio 1:5–1:8, using a dosing pump that injects the diluted softener at 1:10 into the circulation stream rather than directly onto the rope to prevent shock demulsification. After hydroextraction to 50–60% residual moisture, tumble drying at 80–95°C initiates silicone film orientation, and stenter finishing at 110–120°C is limited to dimensional stabilisation. Anionic fluorescent whitening agents and high-electrolyte reactive dye baths must not be co-dosed; incompatibility appears as uneven film deposition on seams and terry loops. Finished fabric is verified against Oeko-Tex Standard 100 Annex 4 Class II extractable limits and ZDHC MRSL v3.1, with colourfastness to laundering tested to AATCC TM61-2A and dimensional change to AATCC TM135. Terminal output comprises terry bath towels, bathrobes, and bath mats where circular bending stiffness is measured by ASTM D4032-08.
Because residual alkali and starch hydrolysate persist on denim garments after stone washing, RH-NB-8602 is applied only after buffered neutralisation brings the final rinse to pH 5.5–6.0. The addition window is further constrained by metal drum baffles: if residual alkalinity remains above pH 6.0, the silicone emulsion cracks on the drum surface and forms a tacky deposit that transfers to pockets, seams, and rivet areas during tumble drying. The softener is dosed at 1.0–2.5% owg in a front-loading industrial washer rotating at 28–32 rpm, diluted inline at 1:10 with demineralised water, and circulated for 12–18 min at 30–40°C. Extraction to 60–70% moisture and tumble drying at 70–85°C for 20–30 min set the silicone film and reduce garment-to-garment slip to a level compatible with folding, pressing, and laser marking. Overdosing above 2.5% owg depresses crockfastness on indigo-dyed twill and increases seam slippage risk in stone-washed constructions. Compliance is judged against ZDHC MRSL v3.1, REACH Annex XVII entries applicable to siloxanes, and Oeko-Tex Standard 100 Appendix 6 limits for solvent transfer in garment finishing. Finished goods include denim jeans, jackets, skirts, and workwear where tensile retention is monitored by ASTM D5034-09 and seam slippage by ISO 13936-1:2004.
Sequentially, pad-dry-cure finishing of cotton-polyester sheeting imposes a different constraint: the silicone film is formed on open-width fabric at high stenter speed. RH-NB-8602 is padded at 10–30 g/L in the finishing bath with a pneumatic pad mangle set to 65–80% wet pickup; pad-roll pressure is adjusted so that edge-to-centre concentration drift remains below 5% of the nominal bath concentration. Drying in the first two stenter chambers is capped at 110°C to prevent silicone migration towards the face before coalescence; curing at 150–170°C for 60–90 s completes film coalescence and reduces migration after laundering. Cure temperatures above 180°C are excluded on white goods because thermal yellowing becomes measurable after 120 s exposure, unless optical brightener compatibility has been validated on a production lot. The bath is held at pH 5.0–5.5 with a non-volatile organic acid buffer; hard water above 150 ppm CaCO₃ must be softened before dosing because calcium salts deposit on the pad rolls and reduce silicone transfer efficiency. Compliance instruments include ASTM D5034-09 for breaking strength retention, ISO 13934-1:2013 for strip tensile, AATCC TM8 for crocking, and Oeko-Tex Standard 100 Class II Annex 4 extractable limits. Terminal products include bed linen, duvet covers, and shirting, where pilling resistance after domestic laundering is evaluated by ISO 12945-2:2020.
Yarn-level application is specified when piece-level processing would entrap the softener in the fabric construction before final fabric formation. On high-speed precision cone winders, RH-NB-8602 is applied by a rotating kiss roller at 0.5–2.0% by weight of yarn, diluted to 8–15% active emulsion and metered through a peristaltic pump with a flow feedback loop tied to winding speed. Winding tension is maintained at 0.08–0.15 cN/tex for spun polyester and 0.05–0.10 cN/tex for corespun polyester-cotton; deposition above 2.5% raises cone rewinding friction sufficiently to produce sloughing during downstream unwinding on embroidery machines and sewing heads. Package density is held between 0.35–0.45 g/cm³ for spun polyester and 0.40–0.50 g/cm³ for corespun yarns; cone hardness above 75 Shore A restricts interior moisture removal and creates a tacky core after radio-frequency drying. Drying is carried out by radio-frequency or hot-air yarn conditioning at 55–65°C for 20–40 min, depending on package density and cone hardness. Published third-party data for RH-NB-8602 on high-speed polyamide texturising winders is limited; process capability is established on the specific winder by tensile retention and cone unwinding trials before lot release. Compliance with REACH Annex XVII and ZDHC MRSL v3.1 applies at the spin-finish stage. Verification uses ISO 2062:2009 for yarn breaking force, ASTM D204 for sewing thread breaking strength, and ASTM D3108-07 for yarn-to-metal friction; coefficient of friction values above 0.25 trigger package reconditioning. Terminal products include industrial sewing threads, embroidery threads, and technical knitting yarns used in mattress ticking, automotive seat panels, and filtration media.
In coated synthetic leather production, RH-NB-8602 is introduced into the polyurethane topcoat at 0.3–1.5 wt% on total wet topcoat solids. The topcoat is applied over release paper by knife-over-roll coating with a gap of 0.15–0.30 mm, then laminated to the transfer-coated base layer and cured in a three-zone tunnel at 90–130°C; the second zone is set to 105–115°C to flash off volatile carriers before the final crosslinking zone. At addition levels above 1.5 wt%, intercoat peel adhesion measured by ISO 11644:2009 falls below the typical 2.5 N/cm acceptance limit for automotive seating, and foil print adhesion on embossed surfaces becomes inconsistent. The cured film is embossed at 120–140°C under a hydraulic press with a dwell time of 3–5 s; surface slip is then verified by a friction sled test against the release paper transfer side. Pot life of the silicone-modified topcoat is monitored by Brookfield viscosity at 25°C; an increase beyond 30% within 4 h indicates destabilisation or premature silanol condensation. The formulation must not combine RH-NB-8602 with amine-based crosslinkers in the same topcoat; premature viscosity rise in the pot has been observed when both amino-functional and melamine-formaldehyde species are present. Regulatory compliance follows REACH Annex XVII, RoHS Directive 2011/65/EU, and automotive OEM VOC method VDA 278 for emissions. Terminal products include automotive seat upholstery, footwear uppers, and bags, where flex endurance is tested by ISO 5402-2:2015 and surface rub fastness by ISO 17704:2004.
Where low-cure temperature is mandated by heat-sensitive elastane cores, exhaust application on nylon-elastane warp-knit fabrics requires a shifted process envelope. RH-NB-8602 is dosed at 2.0–4.0% owf into a soft-flow dyeing machine at pH 5.0–5.5 and 40–45°C, with a residence time of 15–20 min; the lower temperature avoids loss of retractive power in the elastane filament, but requires a longer dwell than cellulosic substrates to achieve film deposition. Extraction to 55–65% moisture precedes tenter drying at 120–130°C for 45–60 s, which is the upper thermal boundary for chlorine-free elastane in most commercial warp-knit constructions. For polyamide-elastane containing chlorine-resistant elastane, cure may be raised to 135°C only after retractive power testing confirms less than 5% loss in stretch recovery. Stretch growth is measured by ASTM D2594-04 and dimensional stability by ISO 6330:2021 after three home-laundering cycles; wet crocking is tested to AATCC TM8. The finish must remain within Oeko-Tex Standard 100 Class I Annex 4 extractable limits for infant and next-to-skin garments. Terminal output includes seamless activewear, lingerie, shapewear, and elasticated medical compression textiles where surface friction reduction is a quality-control variable monitored on a dynamometer sled.
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Super Soft and Smooth Silicone Oil RH-NB-8602 is a tertiary amine-functional polydimethylsiloxane fluid supplied as a clear to slightly turbid viscous liquid for exhaust and pad finishing of cotton, regenerated cellulose, polyester/cellulosic blends, and synthetic knit structures. The model designation RH-NB-8602 identifies a linear aminoalkyl-modified dimethylsilicone that is non-ionic in concentrated form and develops weakly cationic bath behavior after acidification at pH 5.5–6.5. Manufacturer batch certificates list an active content of ≥98 % by mass according to ISO 3251 and a rotational viscosity at 25 °C of 800–1500 mPa·s when measured by ISO 2555. The product is typically diluted to a 10–30 g/L pad liquor or applied at 0.5–2.0 % o.w.f. in exhaust equipment; curing is carried out at 150–170 °C on a stenter frame. Representative specifications are consolidated in Table 1. Published independent data for this specific configuration is limited; the entries below derive from manufacturer batch certificates and should be confirmed against each delivered lot.
| Property | Test method | Typical range | Unit |
|---|---|---|---|
| Appearance at 25 °C | Visual | Clear to slightly hazy liquid | — |
| Active content | ISO 3251 | ≥98 | % by mass |
| Rotational viscosity at 25 °C | ISO 2555 | 800–1500 | mPa·s |
| Density at 25 °C | ISO 2811-3 | 0.97–1.00 | g/cm³ |
| pH at 10 g/L aqueous dilution | ISO 787-9 | 7.0–9.0 | — |
| Amine value | ASTM D2074-based titration | 0.15–0.40 | meq/g |
Bath stability for RH-NB-8602 is controlled by pH, water hardness, shear history, and the order of addition in the finishing liquor. In a jet dyeing machine or overflow softener operated at a liquor ratio of 1:8 to 1:15, the bath is adjusted with 0.5–1.0 g/L acetic acid 60 % to reach pH 5.5–6.5. At pH values above 8.0, the aminoalkyl groups remain insufficiently protonated and bath substantivity decreases; at pH values below 4.5, over-protonation increases cationicity to the point where fibre rewet time may exceed 10 s in AATCC TM79 vertical wicking and residual anionic dyes in the bath may coacervate.
Water hardness above 150 ppm CaCO3 destabilizes the emulsion because divalent cations bridge anionic groups present in sizes and cellulosic surfaces. Production lines using hard water should add a polycarboxylate sequestrant before the silicone is introduced; the sequestrant dose is determined by complexometric titration, and the final bath is checked for sedimentation after 30 min at 40 °C. High-shear pumping above 1500 rpm during stock emulsion preparation can also reduce particle size below the target range and create a viscous inversion that deposits on pad mangle rollers.
The addition sequence on a range with multiple chemical stations should place RH-NB-8602 after the acid but before any cationic fixative; anionic softeners, acrylic binders, and high-electrolyte antistats are withheld from the same bath unless a compatibility trial with a 100 mL jar test shows no phase separation after 24 h. In padding lines, wet pickup is maintained between 65 % and 80 % on a horizontal two-roll padder with roller hardness 70–75 Shore A; lower pickup produces uneven deposition on dense cotton twill and higher pickup extends drying time and migrates the silicone film toward the fabric surface.
In unmodified polydimethylsiloxane, the absence of amine anchoring groups limits exhaustion onto cotton and produces poor wash durability under ISO 6330 machine washing at 40 °C. RH-NB-8602 contains tertiary aminoalkyl side chains that become positively charged at pH 5.0–6.5, permitting electrostatic deposition onto negatively charged cellulosic fibres. The same charge mechanism distinguishes this product from conventional dimethylsilicone oils that require external emulsifiers and from primary aminopropyl silicones that exhibit stronger protonation but also greater thermal yellowing. After padding and curing, the fluid forms a low-surface-energy film; fabric handle is assessed by panel evaluation after five ISO 6330 washes, bending hysteresis by Kawabata KES-FB2, and whiteness retention by ISO 105-B02 daylight exposure.
Stock emulsions are prepared by charging water at 20–30 °C to a stainless steel or high-density polyethylene mixing vessel, adding acetic acid to pH 5.5–6.0, and then feeding RH-NB-8602 under a propeller mixer at 300–500 rpm. The mixture is stirred for 15–20 min and passed through a 150 µm filter before entering the pad trough. A concentric-tube homogenizer is not required and may impart excessive shear; if an inline rotor-stator mixer is used, the tip speed should not exceed 5 m/s. Batch-to-batch variation is controlled by measuring the pad bath pH and viscosity at 25 °C before the first lot and after each 4 h of running time.
In exhaust application on softflow or overflow jets, the fibre load is wetted at 40 °C, the bath is set to pH 5.5–6.5 with acetic acid, and RH-NB-8602 is added at 0.5–2.0 % o.w.f. over 10 min. The bath is circulated for 20–30 min; exhaust of the silicone is monitored by measuring residual turbidity at 600 nm. Residual turbidity above 50 NTU after 30 min may indicate insufficient bath substantivity, high hardness, or anionic interference. The fabric is hydro-extracted and dried at 110–130 °C; no additional curing is required for exhaust application unless durable press resins are present.
On knit cotton, rope marks and crease formation are controlled by reducing loading per chamber to 80 % of nominal capacity and maintaining fabric speed below 300 m/min in overflow machines. Softening with RH-NB-8602 at 1.0–1.5 % o.w.f. lowers cross-machine bending rigidity but does not fully replace mechanical compacting or resin stabilization. Fabric width is checked by AATCC TM135 or the buyer’s dimensional stability protocol; the finish contributes less than 2 % weight change at normal dosage.
On cotton/polyester blends, differential deposition can occur because the cellulosic component carries anionic hydroxyl groups while polyester exhibits a lower surface charge. RH-NB-8602 is typically applied at 10–20 g/L on 65/35 polyester/cotton shirting weight and 15–30 g/L on cotton-heavy knits to compensate for the hydrophobic polyester surface. The pad-dry-cure cycle is set at 110–130 °C for moisture removal followed by 150–170 °C for 45–90 s. Curing below 150 °C leaves an incompletely coalesced film that is removed by subsequent ISO 6330 washing; curing above 180 °C may increase the yellowness index of the finish, particularly on optical brightened cotton.
Deposition uniformity is checked by dyeing the finished fabric with a drop of 0.5 % methylene blue solution; uneven areas appear darker because cationic dye binds preferentially to exposed cellulose. This method is qualitative and is supplemented by measuring silicone add-on through inductively coupled plasma optical emission spectrometry after extraction with xylene; the acceptable add-on range for woven cotton shirting is 0.5–1.0 % silicon on mass of fabric.
Because the tertiary amine in RH-NB-8602 is less nucleophilic than primary aminopropyl groups, the product exhibits lower thermal yellowing in high-temperature cure cycles. Primary amino silicones can undergo amine oxidation at 170–180 °C, producing chromophoric imine and azomethine species; RH-NB-8602, with an amine value of 0.15–0.40 meq/g, limits this pathway. Textile mills that cure at 170 °C for 90 s report whiteness retention values that are acceptable under ISO 105-B02 when optical brightener is applied in a separate step; however, visible yellowing must still be checked on each fibre/dye combination because residual high-temperature processing oils can migrate from polyester and react with amino groups.
Hydrophilic silicone softeners based on polyether-modified siloxanes maintain a wicking time of 3–5 s by AATCC TM79 but typically exhibit lower surface smoothness than aminoalkyl grades. RH-NB-8602 is not selected when the fabric must retain high absorbency; its low-surface-energy film can increase vertical wicking time to 10–20 s. Where both softness and absorbency are required, a blend of RH-NB-8602 with a hydrophilic silicone is evaluated at a ratio of 1:1 to 1:3 by mass, with the mixture checked for clarity after 24 h to rule out phase separation.
When the finishing range operates above 175 °C to accommodate durable-press resins or pigment printing binder crosslinking, the low-yellowing character of the tertiary amine group becomes the primary selection criterion. The product can be co-applied with dimethyloldihydroxyethyleneurea resin at 30–60 g/L and magnesium chloride catalyst at 6–12 g/L, provided the pad bath is cooled below 30 °C and used within 4 h because acid catalysis can slowly protonate the amino groups and raise bath viscosity. The fabric is cured at 160–170 °C for 60–90 s; extended dwell above 120 s should be validated against ISO 105-B02 and ISO 105-X18 phenolic yellowing because yellowing from amine oxidation becomes time-dependent beyond 180 s.
For bright white goods, a two-stage pad sequence with optical brightener in the first pad and RH-NB-8602 in the second reduces yellowing compared with single-bath co-application. The whitening agent is fixed at 120–130 °C, then the silicone is padded at 5–10 g/L and dried at 130–150 °C. This separation prevents quenching of the optical brightener by the amino groups. Whiteness retention is assessed by ISO 105-B02 daylight exposure and phenolic yellowing by ISO 105-X18. A tertiary amine grade is recommended when the same fabric will be stored in polyethylene film for periods exceeding 90 days.
| Regulatory framework | Documentation | Applicable threshold/method |
|---|---|---|
| REACH | Regulation (EC) No 1907/2006, Article 31 safety data sheet | SVHC < 0.1 % w/w |
| RoHS | Directive 2011/65/EU and Commission Delegated Directive (EU) 2015/863 | Pb, Hg, Cd, Cr(VI), PBB, PBDE, DIBP < 0.1 % w/w; Cd < 0.01 % w/w |
| ZDHC MRSL | Version 3.1 manufacturer declaration | Flame retardants, APEOs, chlorinated carriers below detection limit |
| Oeko-Tex Standard 100 | Certificate of compliance for textile auxiliaries | Product class conformity for baby articles optional |
Storage at 5–35 °C in sealed high-density polyethylene or stainless steel vessels prevents moisture ingress and gel formation. Freeze-thaw cycles below 0 °C may increase haze; the product should be remixed at 20–25 °C before use. Containers opened for partial withdrawal should be purged with nitrogen if storage exceeds 30 days. Diluted emulsions are not self-preserving; prepared pad baths should be consumed within 24 h to avoid microbial growth and shear-induced coalescence. The fluid is incompatible with strongly alkaline solutions above pH 10, concentrated hypochlorite bleach, and anionic silicone emulsions; contact with such materials in mixing lines can form a rubbery precipitate that blocks filters with base diameter less than 75 µm.