SLES 70% – сертифицированный класс RSPO

Dilution of 70% active Sodium Laureth Ether Sulfate into a rinse-off personal cleansing base is governed by the viscosity phase behaviour of the paste rather than by simple pump transfer. The paste is received at 25°C with a typical rotational viscosity of 5,000–15,000 mPa·s and must be pre-heated or diluted with demineralized water at 35–40°C before in-line addition. A final shampoo or body wash is commonly formulated to 7–10% active SLES, corresponding to 10–14.3 parts of SLES 70% per 100 parts finished product. The water phase is charged first, then the paste is added under low-speed axial agitation; high-shear rotor-stator dispersion is avoided at this stage because excessive shear can entrain air into the thick paste and produce persistent foam that alters specific gravity readings. After the paste is fully dispersed, the pH is adjusted downward to 5.5–6.0 with 50% citric acid solution; concentrated acid must not be added directly to the paste because localized pH below 4.0 accelerates hydrolysis of the sulfate ester group and generates a measurable increase in unsulfated matter. Cocamidopropyl betaine is introduced at an active ratio of SLES to CAPB between 2:1 and 3:1, which is the working window where wormlike micelle formation becomes responsive to sodium chloride. Sodium chloride is added as a 25% aqueous solution only after pH correction; at 8% active SLES the viscosity peak usually occurs between 0.8% and 1.2% NaCl, and further salt addition reduces viscosity sharply. Line experience on 5,000 kg batches shows that localized salt addition above 40°C can separate the ethoxylated sulfate from the water phase and create translucent gel domains that are slow to clear. Preservative selection follows ISO 11930:2019 challenge testing and the limits in EU 1223/2009 Annex V; phenoxyethanol with ethylhexylglycerin is typically processed at 1.0–1.5% in the finished product when pH exceeds 5.5. The RSPO Supply Chain Certification Standard 2020 requires batch-level mass balance reconciliation for any RSPO MB on-pack claim involving this feedstock. These bases are used for shampoos, body wash, hand soap, bubble bath, and pet grooming rinse-off formulations.

How Does SLES 70% Reduce Hard Water Foam Collapse in Manual Dishwash Concentrates?

Manual dishwash systems are built at higher active matter than personal cleansing because the formulation must emulsify food oils while retaining foam in wash water that contains hardness ions. SLES 70% RSPO certified grade is routinely combined with neutralized linear alkylbenzene sulfonic acid at SLES-to-LABSA active ratios of 1:1 to 2:1, with the LABSA neutralized separately by 50% sodium hydroxide or triethanolamine before the SLES phase is added. The total anionic active matter in a hand dishwashing liquid is most often controlled between 12% and 18%, which maintains foam volume under ASTM D1173-23 conditions at 300 mg/L CaCO₃ hardness; unlike LAS, SLES does not form visible calcium sulfonate precipitates under the same hardness conditions. A foam stabilizer such as cocamide DEA or CAPB is added at 2–4% active matter, and the finished pH at 20°C is measured neat at 6.5–8.0 using ISO 4316:1977. Viscosity adjustment in this segment is more sensitive than in shampoo because the electrolyte concentration is already high from LABSA neutralization; sodium chloride is added as a 0.2% increment after the batch is below 35°C. At 16% active anionic matter, total salt content above 2.0% can rapidly invert the viscosity and produce a non-pourable gel, so the batch is checked on an ISO 2555 rotational viscometer at 20 rpm between increments. Foam retention in 300 mg/L hard water is used as an in-process control because commercial manual dishwash products must maintain foam at the end of a sink wash; the batch is passed only when the foam volume after 5 min remains above 300 mL at 0.1% active surfactant. Ready biodegradability of the finished surfactant system is verified under OECD 301B, and the EU Detergents Regulation 648/2004 imposes surfactant biodegradability and phosphorous restrictions on the marketed liquid. The RSPO MB chain of custody requires that the mass of certified SLES 70% entering the batch is balanced against the mass of RSPO MB manual dishwash sold under claim within the same trading period.

Solvent-Surfactant Coupling Limits in Alkaline Trigger Spray Degreasers

In concentrated industrial and institutional hard surface degreasers, SLES 70% functions as the anionic wetting component in solvent-loaded systems, not as the primary foam generator. The material is dosed at 0.5–5% active surfactant in finished trigger spray or mop-and-bucket concentrates, where the solvent phase is typically a glycol ether such as diethylene glycol monobutyl ether or propylene glycol n-butyl ether at 3–8% by mass. Phase stability is maintained by hydrotropes such as sodium xylene sulfonate at 2–4%, and the pH is elevated to 8.0–11.0 with sodium hydroxide or monoethanolamine. Water is charged first; solvent and hydrotrope are blended, then SLES 70% is added under low-shear axial flow. High-shear rotor-stator dispersion is not required if the water temperature is held at 30–40°C, but a 3,000 rpm batch homogenizer may be used for 5–10 min when the solvent load exceeds 10%. The alkaline environment accommodates builder chelants such as tetrasodium EDTA or trisodium MGDA, but quaternary ammonium biocides must not be combined with this anionic surfactant in an unbuilt formulation because the sulfate head group forms an oil-insoluble complex. The finished concentrate is evaluated for phase clarity after three freeze-thaw cycles between -5°C and 40°C, and viscosity is held below 200 mPa·s for trigger spray recovery. End products built on this platform include kitchen degreasers, vehicle wash presoaks, enclosed parts washers, and low-foam floor scrubber detergents. Under EU Detergents Regulation 648/2004, the surfactant system must be ultimately biodegradable; SLES 70% RSPO certified grade is readily biodegradable under OECD 301B, with mineralization reported above the 60% threshold within the 10-day window for this surfactant class, but the final formulation must be tested as a whole because solvents and hydrotropes can alter biodegradation kinetics.

Liquid laundry detergent processing differs from personal care because the formulation contains protease, amylase, and mannanase enzymes that are incompatible with the low pH and high electrolyte levels used in manual dishwash systems. SLES 70% RSPO certified grade is introduced into the built detergent base at 2–8% active surfactant, often below the level used for dishwash because machine laundry requires controlled foam rather than persistent foam. The surfactant is blended with a non-ionic C₁₂–C₁₅ alcohol ethoxylate, neutralized LAS, fatty acid soap, and a builder system based on sodium citrate or methylglycinediacetic acid at pH 7.5–8.5. The finished viscosity using ISO 2555 at 20°C is typically maintained at 200–600 mPa·s; SLES 70% contributes shear-thinning response when the total active matter exceeds 12%, but elastic gel formation is avoided by limiting electrolyte release from builder neutralization. In production, the order of addition places enzymes after the anionic surfactant has been diluted and the pH is buffered above 7.5; direct contact between concentrated SLES 70% and liquid enzyme preparations can strip calcium ions from protease and reduce storage stability. Hypochlorite bleach must not be combined directly with SLES in a concentrated liquid at elevated temperature because the ether sulfate group can be oxidized and the formulation may generate chlorinated by-products; oxygen-based bleach systems are added only after pH buffering below 8.5. Machine laundry liquids based on this architecture require a silicone defoamer or fatty acid soap regulator because the sulfate ether is a strong foam source; foam breakout in a horizontal-axis washer is measured under defined agitation using a calibrated drum test and maintained below 10 mm overflow height. The RSPO MB documentation remains batch-linked for the SLES input, but the finished detergent product claim requires reconciliation against sold volumes according to RSPO SCCS 2020.

When Cotton Scouring Liquors Operate at 60°C, SLES 70% Wets and Emulsifies Residual Spinning Oils

At 60°C in a continuous open-width scouring range, SLES 70% is applied as a wetting and emulsifying component in textile pretreatment auxiliaries, but only when formulated with a defoamer or a low-foam non-ionic co-surfactant because high-shear jet machines can cavitate from generated foam. The scouring bath is prepared at 0.5–2.0 g/L active SLES, with sodium hydroxide at 2–5 g/L and hydrogen peroxide 50% at 2–4 g/L for a one-bath prepare-for-dye treatment. Under these conditions the ether sulfate remains stable for the 30–60 min residence time at 60–80°C, though prolonged alkaline holding above 90°C can hydrolyse the sulfate ester group and reduce wetting efficiency. The SLES 70% emulsifies paraffin-based coning oils and polyalkylene glycol lubricants; bath turbidity after 20 min is used as a line control parameter to verify emulsification before hydrogen peroxide decomposition becomes excessive. Finished textiles intended for Oeko-Tex or ZDHC conformance require that the auxiliary formulation be screened for restricted aromatic amines and APEO; SLES 70% RSPO certified grade is APEO-free by design. Do not use SLES 70% as a levelling agent for cationic dyes in acrylic dyeing because the anionic charge precipitates with cationic dye molecules. The material is used in pad-batch pretreatment, continuous open-width scouring ranges, and rope processing of knitted fabric; the final wetting agent content is verified by the Draves skein wetting method or the drop absorption test on greige cotton.

Primary Emulsifier Behaviour in Styrene-Acrylic Latex Synthesis at 0.5–1.5 phm

During the pre-emulsion stage, SLES 70% RSPO certified grade serves as the anionic primary surfactant in styrene-acrylic or vinyl acetate-ethylene latex synthesis. The technical material is charged at 0.5–1.5 phm based on monomer mass, which is above the critical micelle concentration of SLES in deionized water reported in the 100–200 mg/L range at 25°C. The monomer pre-emulsion is prepared by first dissolving SLES 70% in warm deionized water at 35–40°C, then feeding the monomer blend into a rotor-stator mixer at 2,000–3,000 rpm for 15 min. The resulting emulsion is dosed to a jacketed reactor maintained at 80–85°C with ammonium persulfate initiator at 0.3–0.5 phm. Particle size distributions measured by ISO 22412:2017 commonly show z-average diameters below 200 nm for stable commercial latexes made with SLES as the sole anionic emulsifier; coagulum is screened through a 100-mesh filter and kept below 0.1% of wet latex mass. Residual SLES at the particle surface reduces water resistance in the dried film; post-polymerization addition of divalent salts can destabilize the anionic latex. Do not use this emulsifier with cationic monomers unless the system incorporates a non-ionic steric stabilizer because charge-induced agglomeration occurs rapidly. These latexes are used in architectural coating binders, pressure-sensitive adhesives, paper coatings, and nonwoven binders. RSPO certified latex inputs require supplier mass balance documentation for the surfactant used in the polymerization record, and the downstream latex manufacturer retains that documentation for audit under RSPO SCCS 2020.

Unlike high-foam manual dishwash or personal cleansing systems, gypsum wallboard production uses SLES 70% as a dilute foaming surfactant to reduce board density while maintaining core strength. The material is first diluted to 5–10% active solution with softened water and metered into a continuous foam generator at addition rates normally kept below 0.1% of dry stucco mass; excessive surfactant input produces unstable coarse bubbles and poor nail pull resistance, so the foam generator air-to-liquid ratio is adjusted to produce a foam density in the 80–150 g/L range. The generated foam is blended with the stucco slurry after the accelerator and before the forming plate, where shear must be low enough to avoid bubble collapse but sufficient to distribute the foam uniformly across the board width. Calcium sulfate and hard water ions compete with the sulfate head group and reduce foam volume; therefore softened water with hardness below 50 mg/L CaCO₃ is used for the dilution tank. The surfactant stream is kept separate from set retarders and certain polycarboxylate dispersants until the foam distribution manifold; premixing at high concentration can cause phase separation before the foam reaches the slurry mixer. Published dosage-response curves for gypsum foam density are often limited to proprietary board line studies, but field observation confirms that small changes in dilute surfactant feed rate produce measurable core density shifts. Finished boards are evaluated under EN 520 or ASTM C1396/C1396M for flexural strength and nail pull. RSPO MB documentation remains with the surfactant purchase and is not automatically transferred to the gypsum board product claim unless the board manufacturer maintains separate supply chain certification covering the surfactant input.