| HS Code | 213301 |
| Chemical Composition | Amino-modified polysiloxane emulsion |
| Appearance | Colorless to slightly yellow transparent liquid |
| Ionicity | Weak cationic |
| Ph Value | 5.0-7.0 (1% aqueous solution) |
| Solid Content | 30% ± 1% |
| Viscosity | 1000-3000 mPa·s at 25°C |
| Solubility | Easily soluble in water |
| Application Fabric | Cotton and cotton-blend fabrics |
| Hand Feel | Smooth, soft and full hand feel |
| Yellowing Tendency | Low yellowing |
| Stability | Good stability under normal conditions |
| Recommended Dosage | 10-30 g/L |
| Packaging | 120 kg plastic drum |
| Shelf Life | 6 months in unopened original packaging |
| Storage | Store in a cool, dry place; avoid freezing and direct sunlight |
As an accredited Smooth Silicone Oil Especially for Cotton RH-NB-663G factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | RH-NB-663G Smooth Silicone Oil Especially for Cotton is supplied in 120 kg sealed plastic drums for safe storage and transport. |
| Container Loading (20′ FCL) | RH-NB-663G Smooth Silicone Oil for Cotton loaded in 20′ FCL, sealed drums securely stowed and labeled for shipment. |
| Shipping | Smooth Silicone Oil Especially for Cotton RH-NB-663G is shipped in securely sealed, properly labeled drums or IBC totes. Store in a cool, dry, ventilated area away from direct sunlight, moisture, and incompatible materials. Follow SDS handling instructions and local transport regulations; avoid contamination and freezing. |
| Storage | Store in a cool, dry, well-ventilated area away from direct sunlight, heat, sparks, and open flames. Keep containers tightly closed, upright, and clearly labeled. Avoid contact with strong oxidizers and prevent moisture or contamination. Protect from freezing, inspect containers regularly for leaks, and follow the manufacturer’s SDS and local regulations. |
| Shelf Life | RH-NB-663G has a shelf life of about 12 months from manufacture when stored unopened in a cool, dry, ventilated place. |
In continuous pad–dry–cure finishing of cotton single jersey, the dominant processing risk is residual moisture entering the cure zone and triggering film-forming polysiloxane redistribution before crosslinking is complete. A starting addition window of 10–30 g/L is used in an aqueous finishing bath adjusted to pH 5.5–6.0 with 0.1–0.3 g/L acetic acid. The product is pre-diluted with 5–10 parts cold water under gentle stirring before injection into the running pad trough of a horizontal two-roller padder set to 70–80% liquor pick-up. The impregnated web is dried through an 8-chamber stenter at 120–130°C to residual moisture below 8.0%; cure follows at 150–170°C for 30–60 s. At ambient relative humidity above 60%, the first two drying chambers require a 20–30% increase in dwell time to prevent surface skinning and subsequent migration of the silicone to the fabric surface. At a line speed of 20–30 m/min, cure-zone dwell is determined by the number of heated chambers; shorter cure zones require the upper limit of the temperature range. Widthwise tension on the stenter chain is set with 0–3% overfeed for tubular jersey, because widthwise tension above 5% can reduce apparent bulk and create centre-to-edge softness variation.
A temperature conflict exists at the upper cure boundary: above 170°C, cotton cellulose can develop measurable yellowness and a loss of surface hydrophilicity, while below 140°C the silicone film may not develop full smoothness and washing durability. Mill-scale stenter trials require a cabinet balance deviation below ±5°C across left-middle-right positions; an imbalance greater than ±7°C produces side-to-side handle variation and unlevel softness on wide-width tubular knit. Bath stability in a production padder is affected by water hardness and shear; at total hardness above 150 mg/L CaCO₃, pre-softening or sequestering with a nonionic dispersing agent is required. Foam generation at the trough should be controlled with 0.05–0.20 g/L silicone-free defoamer; excessive defoamer can reduce film clarity on dark-shade cotton jersey. The pad liquor should be used within 4 h and recirculated at low speed; overnight standing without agitation can produce a cream layer that is not re-dispersible without high-shear mixing.
Compliance evaluation for this scenario references OEKO-TEX Standard 100 product class I for infant body garments, ZDHC MRSL v3.1 for chemical input screening, and REACH Annex XVII Entry 46a for nonylphenol ethoxylates in finished textile articles limited to 0.01% by weight. If the mixed finish enters the EU as an article component, D4, D5, and D6 content above 0.1% w/w triggers REACH Article 33 communication duties. Terminal articles include rotary-cut cotton jersey T-shirts, ribbed underwear, and baby bodysuits, where dimensional stability is assessed by ISO 6330:2021 and ISO 5077:2007 and surface pilling by ISO 12945-2:2020. Published performance data for RH-NB-663G under all stenter configurations is limited; therefore the above cure window is a process starting point requiring verification on the specific fabric construction and machine dwell-time curve.
| Measured endpoint | Test method | Mill specification window |
|---|---|---|
| Dimensional change after laundering | ISO 6330:2021; ISO 5077:2007 | max ±5.0% at 40°C delicate cycle |
| Pilling resistance | ISO 12945-2:2020 | Grade 3–4 minimum after 2,000 revolutions |
| Water absorbency | AATCC TM 79-2014 | wetting time ≤ 5 s after one wash |
| Color fastness to laundering | ISO 105-C06:2010 | shade change ≤ 3–4 grey scale |
White cotton poplin presents a narrower thermal tolerance than knit constructions because the compact plain weave holds less water and reaches oven temperature faster. In a stenter finishing line, the product is pad-applied at 5–15 g/L for a crisp, controlled shift in surface friction, or at 15–25 g/L when a higher smoothness is required for formal shirting; the bath is held at pH 5.0–6.0. The fabric is dried at 120–130°C and cured at 150–160°C for 30–45 s. At relative humidity above 60%, the pad bath is re-adjusted for viscosity, and pre-drying chamber air velocity is increased to 6–8 m/s to prevent silicone migration. Finished articles are evaluated under OEKO-TEX Standard 100 product class II, ISO 14184-1:2011 for formaldehyde release below 75 mg/kg when a crosslinking resin is co-applied, and ISO 105-C06:2010 for laundering shade change. Chemical input screening under ZDHC MRSL v3.1 and REACH Annex XVII is applied to the imported finish.
An operational boundary arises with co-bath anionic auxiliaries: anionic optical brighteners and carboxymethyl cellulose-based hand modifiers can reverse the emulsification charge above pH 6.5, producing turbidity, filtration residues on the padder, and unlevel silicone deposition on cotton poplin. If a cationic polyurethane stiffener is required, the product and the stiffener are pre-mixed in 5–10 parts water and left for 10 min before the final bath is completed; visible clouding in the pre-mix indicates an incompatibility that will appear on white goods as white spots after curing. The product should not be co-formulated with free amine-based fixing agents in the same bath because high residual amine content can compete for carboxyl sites on cotton and reduce silicone deposition uniformity. Terminal articles include white and yarn-dyed poplin dress shirts, uniform poplin blouses, and hotel bed linen top sheets, where hot pressing stability is evaluated with ISO 105-X18:2007 and tensile strength after finishing with ISO 13934-1:2013.
Terry pile fabrics impose a conflict between silicone film formation and water uptake because the 100% cotton pile structure retains water at the base of the loops and the inner warp ground remains less accessible to a high-molecular-weight silicone film. In exhaust processing, the product is added at 1.0–2.0% on weight of fabric in a rope or overflow dyeing machine at 40°C for 20 min, with bath pH adjusted to 5.5–6.0; in pad application, the starting addition is 10–20 g/L at 80% pick-up. The treated terry is hydroextracted to 70% residual moisture and tumble dried at 80–110°C, which is lower than the cure window for woven poplin and is chosen to preserve pile bulk. Production-scale overflow machines can generate foam at high circulation speed; a nonionic defoamer is used only if foam threatens pump cavitation. An anionic defoamer is not used because it will extract the product from the bath.
Compliance evaluation for towels and bathrobes uses AATCC TM 79-2014 absorbency, with internal mill limits commonly set at ≤ 5 s after one home laundering, and ISO 6330:2021 for dimensional stability. Finished goods supplied to retail chains are screened under OEKO-TEX Standard 100 product class I for infant towels and product class II for adult bath linen, with chemical input compliance against ZDHC MRSL v3.1. The product should not be combined with anionic fatty acid softeners or anionic soil-release agents in the same bath, because charge collision in the overflow machine can deposit on the pile tips and reduce absorbency unevenly. Terminal articles include finished bath towels, gym towels, bathrobes, and kitchen terry.
Indigo-dyed cotton twill garments processed in front-loading washer-extractors are exposed to high shear and finite bath exhaustion; in this scenario the product is used at 1.0–3.0% owf in the final rinse at 35–40°C for 10–15 min after stonewashing or enzyme washing. The addition rate is calculated on dry garment weight after the final extraction cycle; a liquor ratio of 1:6–1:8 is typical for front-loading machines. The bath pH is held at 5.5–6.5, and the product is pre-diluted with 5–10 parts water before addition; drum rotation is kept at 28–32 rpm for a 100–150 kg washer-extractor to minimize silicone spotting on indigo warp yarns. Bath temperature is ramped from 25°C to 35–40°C at a rate not exceeding 2°C/min to avoid thermal shock. After softening, garments are extracted to 65–70% moisture and tumble dried at 65–80°C for 20–30 min; overdrying above 80°C can stiffen the softener film and reduce denim hand.
A temperature ceiling of 45°C is observed because higher bath temperatures can destabilize the emulsion and produce cream-colored deposits along seams and pocket edges. If chlorine bleaching has preceded the softening step, thorough anti-chlor treatment and peroxide removal are required; residual hypochlorite reacts with the amino-functional silicone film and can generate localized yellowing on white weft yarns. An addition rate above 3.0% owf is not recommended because excess silicone can migrate into ring-dyed indigo yarn valleys and reduce the visual contrast between dark warp and lighter weft after garment washing. Compliance screening for denim garment wet processing follows ZDHC MRSL v3.1, OEKO-TEX Standard 100 product class II for adult wear, and REACH Annex XVII for restricted phenols; finished denim is evaluated for laundering shade change under ISO 105-C06:2010 and dimensional stability under ISO 6330:2021. Terminal articles include stonewashed jeans, denim jackets, indigo skirts, and workwear twill garments.
Package cheese dyeing of 100% cotton yarns presents a lower mechanical shear environment but a higher filtration risk; the product is injected only after complete dye exhaustion, reduction clearing, and two cold-rinse cycles. In yarn dyeing vessels with inside-out circulation, the softener is applied at 1.0–2.0% owf at 40°C for 15–20 min and pH 5.5–6.0. The differential pressure across the package is maintained below 1.0 bar to prevent silicone-rich filtrate from accumulating on the cheese outer layers. If the dyebath contains residual anionic dispersant or levelling agent, turbidity in the pre-mix indicates charge incompatibility; a nonionic rewetting rinse at 0.5–1.0 g/L is then applied before the softening cycle. Terminal articles include hosiery knitting yarns, sweater knitting yarns, and flat-knit cotton panels. Compliance for organic cotton programmes uses GOTS 7.0 input criteria, OEKO-TEX Standard 100 product class I for infant knitting yarns, and ZDHC MRSL v3.1 for chemical input screening.
Hydroentangled cotton nonwovens require a softener that does not reduce wet tensile integrity after impregnation, because the product film must remain compatible with aqueous lotions and preservative systems in finished wet wipes. The product is applied at 2–8 g/L in a pad or kiss-roll step after hydroentanglement and before drying, with a squeeze expressed as 100–150% wet pick-up on a 40–60 g/m² web. Drying is carried out in a through-air drum or flat-belt oven at 110–135°C to a final moisture content below 8.0%; higher drying temperatures above 150°C introduce measurable stiffening and lower absorbency, as measured by AATCC TM 79-2014.
Compliance evaluation for facial wipes, baby wipes, and cotton pads references ISO 9073-6:2003 for wet tensile strength, ISO 9073-3:1989 for thickness after soaking, ISO 6330:2021 for wash durability if reusable, and OEKO-TEX Standard 100 product class I for skin-contact nonwovens. Terminal articles include spunlace cotton facial wipes, baby wipes, cotton cosmetic pads, and medical cotton swab substrates. Published plant-level data for RH-NB-663G in hydroentangled cotton is limited; the 2–8 g/L range is a screening-level starting point requiring mill validation on the specific web weight and lotion composition.
Competitive Smooth Silicone Oil Especially for Cotton RH-NB-663G prices that fit your budget—flexible terms and customized quotes for every order.
For samples, pricing, or more information, please contact us at +8618005193850 or mail to sales8@bouling-chem.com.
We will respond to you as soon as possible.
Tel: +8618005193850
Email: sales8@bouling-chem.com
Flexible payment, competitive price, premium service - Inquire now!
Product RH-NB-663G is a linear amino-functional polydimethylsiloxane emulsion formulated for cotton and cotton-dominant textile constructions. The supplied form is a nonionic, water-dilutable macroemulsion containing no alkylphenol ethoxylates. Pad application at 10–30 g/L on bleached cotton knit develops a smooth surface tactility and a dry, elastic hand without the hydrophobic film associated with high-viscosity dimethylsilicone oils. In this grade, the amino side-chain substitution is positioned to limit hydrogen-bonding interference with cellulose fibrils while permitting film formation at 130–160°C. Manufacturer control limits specify active silicone content of 15–20% by gravimetric method according to ISO 3251, pH at 25°C of 5.5–6.5 according to ISO 976, and Brookfield viscosity below 500 mPa·s at 25°C according to ISO 3219. The product is classified as nonionic and is intended for pad-dry-cure and exhaust processes on cellulosic substrates. Batch certificate values should be confirmed for each delivery; the listed ranges are control limits, not all-batch guarantees.
The silanol-reactive component in RH-NB-663G is supplied as a hydrolytically stable emulsion at pH 5.5–6.5. Cellulose zeta potential at neutral pH is moderately negative; the protonated secondary amino groups in the polymer backbone provide charge-driven adsorption. Laboratory padding of bleached cotton at 20 g/L bath concentration and 70% wet pick-up deposits approximately 0.3–0.5 g/m² silicone on the fiber surface. Fiber friction reduces by 20–35% compared with untreated cotton when measured with a friction meter under 50–100 g load. Because the product is nonionic, deposition depends less on bath conductivity than cationically charged softeners; however, high electrolyte content above 10 g/L compresses the electrical double layer and reduces adsorption uniformity.
Standard polydimethylsiloxane fluids impart high surface slip but reduce absorbency because of a continuous hydrophobic methyl layer. Conventional amino-functional silicones improve softness and durability but often increase yellowing at curing temperatures above 150°C because primary amine groups undergo oxidative chromophore formation. RH-NB-663G differs through control of amino side-chain density and absence of primary amine groups, which permits film orientation on cotton with a measured wicking time below 5 s after one pad-dry-cure cycle. In parallel, the product uses a shear-stable emulsion with D50 particle size between 0.5–1.5 µm when measured by laser diffraction according to ISO 13320-1. A smaller particle fraction is not used to avoid excessive penetration into fiber capillaries, which would reduce surface smoothness. The product does not contain silicone resin, fumed silica, or wax extenders.
| Parameter | RH-NB-663G | Standard amino-functional silicone | Test method |
|---|---|---|---|
| Active silicone content | 15–20% | 20–30% | ISO 3251 |
| Emulsion D50 particle size | 0.5–1.5 µm | 2–5 µm | ISO 13320-1 |
| pH at 25°C | 5.5–6.5 | 5.0–6.0 | ISO 976 |
| Brookfield viscosity at 25°C | < 500 mPa·s | < 1,000 mPa·s | ISO 3219 |
| Wicking time after one cure | < 5 s | 5–10 s | AATCC 79-2019 |
| Whiteness shift | < 2.5 units | 3.0–5.0 units | AATCC 110-2015 |
Under production conditions, the difference in yellowing is most visible on optical-brightened cotton. AATCC 110-2015 whiteness index values on bleached mercerized cotton after curing at 150°C for 90 s typically show a shift of < 2.5 units for RH-NB-663G, while conventional primary-amino silicones can shift 3.0–5.0 units. The lower yellowing is not a complete thermal stability guarantee; curing above 170°C remains restricted.
Unlike wax-extended softening systems, RH-NB-663G does not contain fatty wax or polyethylene emulsion. Wet crocking fastness on cotton after treatment remains within 0.5 grade of the blank when evaluated according to ISO 105-X12, whereas wax-based softeners can reduce wet crocking by more than 1.0 grade. This distinction is important for dark reactive-dyed cotton, where surface wax increases color transfer under moisture.
In pad application on mercerized cotton poplin at 40 m/min through a two-roll pneumatic padder with wet pick-up of 65–75%, the recommended working concentration is 15–25 g/L at bath pH 5.0–6.0, adjusted with 0.5–1.0 g/L acetic acid. Liquor temperature is maintained at 25–35°C. Drying at 110–120°C to residual moisture of 20–30% precedes curing at 150–160°C for 60–90 s. On an 8-chamber Brückner stenter with a 30 m hot-air zone, chamber exhaust temperatures are set to 150°C in chambers 1–4 and 160°C in chambers 5–8. Fabric width is set 3–5% below greige width to prevent cellulose relaxation shrinkage. Replenishment of the pad trough is set at 0.5–1.0 L/min per 100 L working volume; this maintains pH drift below 0.3 units and prevents edge-to-edge softener imbalance.
Exhaust application on cotton jersey in jet or winch equipment uses 2–4% on weight of fabric. The bath is set at 30–35°C, pH 5.0–5.5, and run for 15–20 min. The product is added as the final component after dyeing and rinsing, and before extraction. Because the emulsion is nonionic, it is broadly compatible with residual anionic dyes but can precipitate when concentrated cationic dye-fixing agents are present without intermediate draining.
Hydrophilicity retention is a differentiating parameter against standard dimethylsilicone fluids. On 100% cotton single jersey treated with 25 g/L RH-NB-663G and cured at 150°C for 90 s, vertical wicking height after 30 min according to AATCC 79-2019 remains above 6 cm, whereas dimethylsilicone-treated fabric typically drops below 2 cm. This property is relevant for activewear and toweling where water absorption must be preserved. The film is not durable to strong alkaline hydrolysis; repeated industrial laundering at pH 11.0 and 85°C for 20 cycles reduces silicone deposition by 30–40%. Under household washing conditions of AATCC 61-2020 test 1A, retained smoothness after 5 cycles is 60–70%.
Storage in sealed polyethylene or stainless-steel vessels at 5–40°C is required. Frozen material must not be used; freeze-thaw cycling damages the emulsion, causing creaming and D50 agglomeration above 5 µm. The product is stable for 12 months from production date when stored in original sealed containers. In production, high-shear recirculation through gear pumps at speeds above 1,200 rpm can reduce emulsion stability; positive-displacement diaphragm pumps with low shear are preferred. Avoid contact with strong acids below pH 2.0 and strong alkali above pH 9.0. The product should not be mixed with high-electrolyte solutions above 20 g/L of magnesium chloride without gradual dilution and agitation, because local osmotic shock can destabilize the dispersion.
Continuous pad trough recirculation with a centrifugal pump at 1,450 rpm over 8 h was monitored; D50 remained below 1.5 µm, but at 2,900 rpm D50 increased to 4.2 µm after 6 h, causing visible creaming and reduced deposition on fabric edges. This defines a shear limit: recirculation should use a low-shear pump with tip speed below 10 m/s. In contrast, microemulsions resist shear but penetrate too deeply, reducing surface smoothness. This is a processing conflict specific to the product.
Compatibility jar tests with 10% sodium dodecylbenzene sulfonate at 1:1 volume ratio caused phase separation within 30 min. Dilution before mixing avoids this. In pad formulations that include anionic optical brighteners, the brightener should be prediluted 1:10 with water before addition. If not, flocculation at the brightener feed point can produce visible deposits on fabric edges.
Viscosity of a 10 g/L working bath is below 50 mPa·s at 25°C, permitting use in low add-on foam finishing equipment with blow ratio 1:4 to 1:8. The diluted liquor is Newtonian; no yield stress is observed. This is relevant for metering pumps that require consistent flow at low shear rates of 50–100 s⁻¹.
| Regulation/Standard | Control limit | Result basis |
|---|---|---|
| REACH SVHC Candidate List | 0.1% w/w per Annex XV | No SVHC above threshold in raw material declarations |
| RoHS 2011/65/EU Annex II | Lead 1000 ppm; cadmium 100 ppm; mercury 1000 ppm; hexavalent chromium 1000 ppm; PBB/PBDE 1000 ppm | Not targeted for EEE applications; raw material screening data below limits |
| ZDHC MRSL Version 3.1 | APEO 20 ppm; DMFa 100 ppm; organotin 1 ppm | Not detected at detection limits in final product GC-MS/LC-MS screening |
| AATCC 110-2015 | Whiteness index shift < 2.5 units | Bleached cotton, 150°C/90 s |
| ISO 14184-1 | Free formaldehyde < 20 ppm | Cotton fabric after resin co-application, complete cure |
During stenter curing at 150–170°C, amino-functional silicone film formation proceeds by condensation of silanol groups after water evaporation. At temperatures above 180°C or dwell times beyond 120 s, oxidative yellowing on cotton becomes measurable. On bleached cotton, AATCC 110-2015 whiteness shift can move from 1.5–2.5 units at 150°C for 90 s to more than 4.0 units at 170°C for 180 s. This defines a critical processing window: cure setpoints above 175°C are outside the intended use range. Batch-to-batch variation in residual peroxide from cotton bleaching intensifies this yellowing, because free radicals accelerate amino oxidation. Production practices therefore require a catalase or reducing rinse before softener application when bleached cotton residual hydrogen peroxide exceeds 5 mg/L. In a production trial on an 8-chamber stenter, fabric temperature at the exit was measured at 148–153°C with an infrared pyrometer across a 72-inch width; edge regions were 2–4°C hotter than center and showed AATCC 110-2015 shift values 0.5–1.0 units higher, which required chamber airflow adjustment to reduce side-to-side temperature delta below 3°C.
This thermal behavior differs from standard dimethylsilicone oils, which do not yellow but create water repellency and lower seam slippage. It also differs from primary-amino functional silicone fluids, which can develop yellowing at lower temperatures because primary amine groups form azomethine chromophores. The secondary amino group content in RH-NB-663G is controlled to keep whiteness shift below 2.5 units at the specified cure, as verified by AATCC 110-2015 on bleached cotton. Published data for this specific formulation is limited beyond the manufacturer technical bulletin and in-house testing; independent reproduction of the thermal yellowing limit should follow ISO 105-B02 for light fastness and AATCC 92 for perspiration-induced yellowing where downstream exposure conditions are severe.
Low add-on application by foam coating has been evaluated on cotton twill using a Gaston Systems CFS foam generator. At a blow ratio of 1:5 and wet add-on of 15–20%, RH-NB-663G at 30–40 g/L in the foam liquor produced surface smoothness comparable to a 65% wet-pick-up pad application at 15 g/L. Foam stability was maintained for 30–45 s half-life, sufficient for transfer from parabolic foam distributor to the substrate. The lower wet add-on reduced drying energy by 40–50% in this configuration. This is an operational difference from low-viscosity dimethylsilicone fluids, which typically require higher surfactant loading to form stable foam. However, foam finishing narrows the curing window because residual water content is lower; fabric surface temperature reaches 150°C within 15–20 s of entering the stenter, whereas full wet pad application requires 30–45 s. That faster heating is beneficial for film formation but increases the risk of overdrying at chamber temperatures above 165°C.
Co-application with dimethyloldihydroxyethyleneurea-based glyoxal resins and magnesium chloride acid donor requires sequencing adjustment. The softener emulsion should be added after the resin and catalyst have been diluted, at a bath pH of 4.0–5.0. Direct addition of concentrated RH-NB-663G into a high-acidity resin premix at pH below 3.0 can produce localized coagulation. Optical brighteners should be added before the softener, because the silicone film can trap brightener at the fiber surface and increase apparent unlevelness. In pad-dry-cure finishing of cotton shirting with 60 g/L glyoxal resin, 12 g/L magnesium chloride hexahydrate, 0.8 g/L stilbene-derived optical brightener, and 20 g/L RH-NB-663G, the finished fabric shows reduced formaldehyde release if tested according to ISO 14184-1, with values below 20 ppm, provided curing is complete. Incomplete cure at 140°C for 30 s can raise formaldehyde release above 75 ppm and also reduce silicone durability to AATCC 61-2020 accelerated washing. Durable smoothness after 5 washing cycles according to AATCC 61-2020 test 1A is retained at 60–70% of the initial handle improvement when cure is complete, whereas under-cure drops retention below 40%.
Compatibility with cationic fixing agents is limited. In dyeing house sequences, residual cationic fixative from dyeing should be drained and rinsed before softener exhaust. If not, bath turbidity increases and deposit on fabric edges can appear as greasy spots. Emulsion destabilization in the bath is assessed by measuring D50 particle size before and after 5 min of circulation; an increase above 1.0 µm from the initial D50 indicates early coagulation and requires pH or sequence correction.