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Ascent Petrochem Holdings Co., Limited

SLES 28% – Liquid Detergent & Dishwash Base

    • Product Name: SLES 28% – Liquid Detergent & Dishwash Base
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: sales4@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 324139
    Product Name SLES 28% – Liquid Detergent & Dishwash Base
    Chemical Name Sodium Lauryl Ether Sulfate (SLES)
    Appearance Clear to slightly hazy viscous liquid
    Active Matter Content 28% by weight
    Ph 7.0 – 9.0 (as is)
    Viscosity Moderately viscous, pourable liquid
    Odor Mild characteristic odor
    Solubility Fully soluble in water
    Foam Property High foaming and stable foam
    Detergency Excellent grease-cutting and cleaning action
    Biodegradability Readily biodegradable under aerobic conditions

    As an accredited SLES 28% – Liquid Detergent & Dishwash Base factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing SLES 28% supplied in 220 kg HDPE drums, securely sealed, labelled with product and safety details for detergent and dishwash manufacturing.
    Container Loading (20′ FCL) 20′ FCL: palletized IBCs/drums, secure bracing, spill containment. SLES 28% liquid loaded safely, maximizing cube, ensuring stability.
    Shipping SLES 28% ships in 220kg HDPE drums or 1,000L IBCs. Classified as non-hazardous for road/sea freight, but labeled as an irritant. Store sealed, cool, and dry; avoid freezing or excessive heat. Use spill containment and proper handling equipment.
    Storage Store in a cool, dry, well-ventilated area away from direct sunlight, heat sources, and open flames. Keep containers tightly closed when not in use to prevent contamination or evaporation. Ideal storage temperature is 10–30°C; avoid freezing. Ensure area is spill-contained and compatible with oxidizers. Use corrosion-resistant equipment and follow local chemical storage regulations.
    Shelf Life Shelf life: 12 months from manufacture date when stored sealed, away from sunlight, heat, and freezing.
    Application of SLES 28% – Liquid Detergent & Dishwash Base

    Manual hand dishwashing detergent represents the largest single downstream use for SLES 28% in the household cleaning segment, and the formulation behavior of this base is dominated by a salt-thickening threshold that is substantially narrower than for linear alkylbenzene sulfonates. In a typical high-foam manual dishwash liquid, SLES 28% is incorporated at 18–25% w/w as-supplied, equivalent to 5.0–7.0% active anionic matter in the finished formula; active matter is verified by two-phase titration per ISO 2271 or the supplier certificate of analysis. The feed is pre-diluted with demineralized water at 25–30 °C before addition to the main vessel to avoid localized gel formation that occurs when concentrated ether sulfate contacts hard water or a high-electrolyte brine stream. A 316L stainless steel mixing vessel equipped with a low-shear axial turbine, 30° pitched-blade impeller, and wall baffles is used; impeller tip speed is held below 1.5 m/s during anionic addition because excessive shear entrains air and produces metastable foam that persists through filling and reduces apparent density. Cocamidopropyl betaine is added at 2.0–4.0% as foam stabilizer and secondary surfactant, and lauramine oxide at 0.5–1.5% contributes viscosity response and cold-water grease emulsification. The batch is adjusted to pH 6.5–7.5 with 50% citric acid solution, since the as-supplied SLES 28% has a 1% aqueous pH in the range 7.0–9.0 when measured per ISO 4316. Preservative selection is restricted to non-cationic systems such as methylchloroisothiazolinone/methylisothiazolinone at 0.05–0.10% or sodium benzoate at 0.3–0.5% only when pH is below 5.5; benzalkonium chloride at 0.1% causes immediate anionic-cationic complexation, visible as a white precipitate within 20 min under low shear. Sodium chloride is added as a 20% w/w aqueous solution after pH correction and co-surfactant incorporation. The salt curve is non-linear: at 0.5% NaCl, Brookfield viscosity measured at 20 °C using spindle 3 at 12 rpm per ASTM D2196-20 is approximately 150–250 mPa·s; at 1.0% NaCl the viscosity rises to 400–700 mPa·s; the maximum is typically reached at 1.2–1.5% NaCl with 800–1,200 mPa·s. Addition beyond 1.8% NaCl causes a sharp viscosity collapse to below 300 mPa·s, a cliff-edge that is not reversible by simple dilution and generally requires reformulation with a higher chain-length alkyl ether sulfate or an alkanolamide. The final product must remain clear at 5 °C and 40 °C for 72 h; clouding at low temperature often results from insufficient betaine level, residual free fatty alcohol from the ethoxylation route, or hard-water cations above 150 ppm as CaCO3. Foam performance is evaluated with ASTM D1173-07 using a 0.1% active solution at 25 °C in 150 ppm hard water; a high-foam manual dish product typically produces an initial foam height of 120–180 mm and retains at least 60% of initial height after 10 min. Grease removal is assessed with ASTM D4009-92 under controlled soiled-plate conditions; formulations with a betaine:SLES active ratio above 0.35:1.00 show faster emulsification of lard and vegetable oil soils, but betaine above 3.5% active may suppress the salt-thickening response and require an additional polymeric thickener such as PEG-120 methyl glucose dioleate at 0.2–0.5%. Filling lines use positive-displacement heads rather than gravity filling because the shear-thinning rheology of salt-thickened SLES causes variable fill weights when line speed exceeds 40 units/min. Degassing is not required if impeller tip speed remains below 1.5 m/s, but air bubbles introduced during powder salt addition remain visible for 24–48 h in clear bottles and are a common batch rejection on high-speed lines. For export detergent formulations, Regulation (EC) No 648/2004 Annex VII A requires ingredient declaration for enzymes, preservatives, and fragrance allergens; REACH Regulation (EC) No 1907/2006 Annex VIII exposure scenarios apply to the neat SLES 28% feed and require eye and skin protection during bulk transfer. Biodegradability of the anionic component is typically confirmed against OECD 301B ready biodegradability criteria, with the 10-day window pass reported on the supplier certificate of analysis.

    Representative laboratory panel for a manual dishwash base, measured 24 h after mixing with a Brookfield LVT viscometer; freeze-thaw stability was evaluated at the stated temperatures for 72 h.

    SLES 28% feed (wt%)Cocamidopropyl betaine (wt%)NaCl (wt%)Brookfield LVT viscosity at 20 °C (mPa·s, spindle 3, 12 rpm)Freeze-thaw stability 5 °C / 40 °C, 72 h
    1820.8200–300Clear, no separation
    2031.2600–900Clear, no separation
    2031.8250–350Slight haze at 5 °C
    2240.6150–250Clear, low viscosity

    What Changes When SLES 28% Replaces Linear Alkylbenzene Sulfonate in Built Liquid Laundry Detergents?

    In built liquid laundry formulations, SLES 28% is introduced not as a primary viscosity builder but as a low-smear anionic component that remains phase-stable at pH 8.0–9.5 and tolerates sodium citrate and sodium tetraborate better than in-situ neutralized alkylbenzene sulfonic acid. A typical heavy-duty liquid would contain 5.0–12.0% SLES 28% as-supplied, corresponding to 1.4–3.4% active anionic matter, combined with 5.0–8.0% C12–C15 alcohol ethoxylate 7–9 EO and 2.0–5.0% sodium citrate builder. The substitution of SLES for linear alkylbenzene sulfonate reduces the monoethanolamine demand by up to 60% compared with an LAS acid-based formulation, because SLES 28% is supplied as the sodium salt and does not require in-line neutralization exotherms. Addition sequencing is critical: the alcohol ethoxylate is first dissolved in water at 30–35 °C, propylene glycol at 2.0–4.0% is added as hydrotrope and enzyme stabilizer, and only after full nonionic solubilization is SLES 28% charged under low shear. Charging SLES before the nonionic produces a viscous, stringy gel phase at the feed zone, particularly when tap water hardness exceeds 200 ppm as CaCO3; in one common failure mode, the gel blocks the recirculation pump inlet and necessitates a 24-h warm-water soak before the batch can be recovered. Enzymes are added after the batch is cooled below 30 °C. Protease and amylase are stable for 90 days at 25 °C only if free water content remains above 45% and pH is held between 8.0 and 9.5; above pH 10.0 or in the presence of more than 2.0% free ethanol, protease autolysis accelerates and stain removal on standardized swatches degrades by 20–40%. Optical brighteners such as disodium diaminostilbene disulfonate are incorporated at 0.10–0.20% and must be pre-dissolved in warm water before addition to the anionic/nonionic micellar phase; direct powder addition creates insoluble agglomerates that redeposit on cotton as bright specks. Low-temperature phase stability is measured at 5 °C for 14 days; a well-formulated built liquid remains clear or slightly opalescent, while a visible electrolyte layer indicates insufficient hydrotrope. Stain removal is assessed according to ASTM D4265-14 using sebum, clay, and grape juice on cotton/polyester panels in a tergotometer with six 1-L stainless steel pots and a 40-rpm oscillation cycle at 30 °C and 150 ppm hard water. Viscosity for built liquid laundry is targeted at 300–600 mPa·s at 20 °C, spindle 2 at 20 rpm per ASTM D2196-20; unlike dishwash formulas, this viscosity is normally achieved with a polymeric rheology modifier such as carbomer or hydrophobically modified alkali-swellable emulsion at 0.1–0.5%, not with sodium chloride, because the electrolyte load from builders would push the salt curve beyond its maximum. The high water content of the 28% feed also makes it unsuitable for polyvinyl alcohol unit-dose detergent film, because final water activity above 0.6 causes film softening at 30 °C. For European markets the formulation must meet Regulation (EC) No 648/2004 Annex VI limits for phosphates and Annex VII ingredient disclosure for enzymes and preservatives, while the bulk SLES 28% feed should be accompanied by a REACH extended safety data sheet with derived no-effect levels for freshwater discharge.

    Alkaline Degreasing of Polymerized Food Soil at pH 9.0–10.5

    Food-processing hard-surface cleaners formulated with SLES 28% operate in a pH band where the ether sulfate linkage remains hydrolytically stable while the formula contains sufficient alkalinity to saponify polymerized fats. A concentrated exhaust-hood and fryer-deck cleaner contains 8.0–15.0% SLES 28% as-supplied, 1.0–3.0% sodium metasilicate pentahydrate, 1.0–2.0% tetrasodium EDTA, 2.0–4.0% sodium citrate, and 1.0–3.0% dipropylene glycol methyl ether. The builder is dissolved first at 35–40 °C; SLES 28% is added only after the metasilicate is fully dissolved, because simultaneous charging of concentrated metasilicate and ether sulfate generates a localized gel that can take several hours to re-homogenize. The pH is adjusted with sodium hydroxide or citric acid to 9.0–10.5; above pH 12.0 the sulfate ester bond undergoes measurable hydrolysis at 40 °C within 72 h, reducing anionic active matter by more than 10% and dropping foam height. Dilution at the point of use ranges from 1:10 to 1:30 with potable water, yielding 0.3–1.5% as-supplied product or 0.08–0.42% active SLES. Soil removal on stainless steel 304 panels is evaluated gravimetrically in a 40 °C immersion cell with continuous recirculation at 0.5 m/s using a lard/mineral oil/microparticulate soil; there is no single ASTM method for this specific food-processing substrate, so plant trials often include a 5-min contact time followed by a 20-psi potable-water rinse. The recirculation pump should be a centrifugal unit with a SS316 impeller rather than a positive-displacement pump, because the high-viscosity gel formed during sequential addition can dead-head a progressive-cavity pump. Foam profile must remain moderate for manual spray-and-squeegee use, with ASTM D1173-07 initial height below 50 mm for a 0.1% active solution at 25 °C; this is achieved by selecting an alcohol ethoxylate with 5–6 EO as the nonionic co-surfactant at 1.0–2.0% rather than a high-foam betaine. For food-contact surfaces, the cleaner is not a sanitizer and must be followed by a potable-water rinse; sanitizing steps are regulated separately under applicable biocide or FIFRA provisions. The use concentration must be verified for pH below 11.5 to avoid caustic labeling under transport and supply regulations.

    Unlike manual dish products, vehicle shampoos built on SLES 28% do not share the salt-thickening target of dish liquids, because trigger-foam and touchless pre-soak products are diluted at the nozzle from 1:50 to 1:100 and must remain pumpable as low-viscosity concentrates. A pH-neutral car shampoo concentrate typically uses 10.0–20.0% SLES 28% as-supplied, 1.0–3.0% cocamidopropyl betaine, 0.5–1.5% lauramine oxide, and 0.2–0.5% sodium citrate. The dilution at 1:100 gives 0.1–0.2% as-supplied product, which is sufficient for wetting road film and providing lubricity on clear-coat surfaces. Sodium chloride is omitted entirely; the concentrate viscosity is kept below 50 mPa·s at 20 °C to allow reliable draw through a foam lance venturi with an orifice diameter of 1.0–1.2 mm. Foam stability is measured with ASTM D1173-07 at 0.1% active and 25 °C, with an initial height of 80–120 mm and complete drainage within 10 min preferred for rinsing without residue. The pH is maintained at 6.5–7.5 with citric acid; more alkaline conditions above pH 9.0 accelerate gloss loss on clear-coat panels after repeated washes, while pH below 5.0 begins to remove wax from polymer sealants. Water hardness tolerance of the diluted vehicle shampoo remains acceptable up to 300 ppm as CaCO3 when sodium citrate is present; without citrate, a hazy precipitate forms within 24 h in hard-water regions. No globally harmonized test method exists for car shampoo lubricity; production-scale validation typically uses a linear friction sled on painted clear-coat panels at 25 °C and 60% relative humidity to compare the diluted formula against water, with the target coefficient of friction at least 30% lower than water without added surfactant. Preservative levels follow the same anionic compatibility rules as manual dishwash: isothiazolinones at 0.05–0.10% are effective, while quaternary ammonium compounds are excluded because they precipitate sodium laureth sulfate and reduce foam height within 48 h.

    When a High-Active Ether Sulfate Is Diluted to 7% for Trigger Spray, Phase Stability Dictates Solvent Choice

    Trigger-spray laundry pre-spotters differ from the built liquids described above because they require Newtonian or near-Newtonian discharge through a fine orifice and must remain clear in the presence of water-miscible solvents. A typical pre-spotter uses 5.0–10.0% SLES 28% as-supplied, equivalent to 1.4–2.8% active anionic matter, combined with 2.0–5.0% dipropylene glycol n-butyl ether, 1.0–2.0% sodium citrate, and optionally 0.5–2.0% ethanol or isopropanol. The solvent is pre-blended with water and sodium citrate before SLES 28% is added, because direct injection of polar solvent into a concentrated surfactant phase can thin the micellar structure and produce a temporary two-phase haze that persists for several hours. Viscosity is targeted at 10–50 mPa·s at 20 °C, spindle 1 at 60 rpm per ASTM D2196-20, measured after 24 h to confirm equilibrium. No thickening salt is used; the built-in electrolyte from sodium citrate is sufficient to give Newtonian flow, and additional NaCl would create the same viscosity spike seen in dishwash but without the mechanical strength required in a trigger-spray system. The trigger dispenser delivers 1.0–1.2 mL per stroke through a 0.6-mm orifice; above 100 mPa·s the spray becomes intermittent and droplet size increases beyond 200 µm, reducing penetration into cotton interstices. Phase stability is evaluated at 5 °C and 40 °C for 72 h, with cloud point adjusted by the ratio of dipropylene glycol n-butyl ether to ethanol; an excess of ethanol above 2.0% lowers flash point below 60 °C, triggering flammable-liquid storage classification under GHS. Preservative selection for this water-rich trigger-spray system is typically methylchloroisothiazolinone/methylisothiazolinone at 0.05%; DMDM hydantoin may be used only if the released formaldehyde is declared under Regulation (EC) No 648/2004 Annex VII. Stain removal on cotton/polyester is assessed according to ASTM D4265-14 using dirty motor oil, tomato, and grass soil; the pre-spotter is applied at 4 mL per 100 cm², left for 5 min, then laundered at 30 °C. For products containing enzymes, the EU detergent regulation requires enzyme labeling regardless of concentration, and fragrance allergens above 0.01% must be declared.

    For general-purpose trigger-bottle cleaning, a ready-to-use all-purpose cleaner is produced by diluting SLES 28% to 1.0–2.0% as-supplied with potable water and adding 0.5–1.0% C9–C11 alcohol ethoxylate; no additional thickener, salt, or co-surfactant is required, and pH is adjusted to 8.0–9.5 with sodium carbonate or citric acid before filling into trigger bottles.

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    Certification & Compliance
    More Introduction

    The product identified as SLES 28% – Liquid Detergent & Dishwash Base is an aqueous anionic surfactant solution of sodium lauryl ether sulfate, INCI Sodium Laureth Sulfate, CAS 9004-82-4, with a nominal active matter of 28% by mass. The model designation used throughout this technical description is SLES-28 LDD; manufacturer-specific commercial codes vary but refer to the same 28% active ether sulfate platform. The material is supplied as a clear to slightly hazy, pale yellow liquid with a mild fatty alcohol odour and is positioned for direct incorporation into manual dishwash liquids, hard-surface cleaners, and liquid laundry detergents. The product is already neutralised and does not require the caustic neutralisation step associated with alkylbenzene sulfonic acid.

    Specifications are typically grouped around an active matter window of 27.5–28.5%, a pH of 7.0–9.0 as received, and a residual sulfate content controlled to prevent viscosity drift. The presence of approximately 2 mol ethylene oxide per mole of fatty alcohol distinguishes the ether sulfate from straight sodium lauryl sulfate: the ethoxy chains raise tolerance to hard-water calcium ions and lower the Krafft point, reducing precipitation in cold liquid formulations. These properties directly affect use as a base for dishwash liquids in which clarity at 5°C and viscosity control with sodium chloride are process-critical.

    What Distinguishes the 28% Active Grade from 70% SLES Pastes During Bulk Transfer and Storage?

    Bulk receiving and process design for the 28% grade differ from 70% SLES paste primarily because of rheological behaviour at ambient temperature. A 70% paste typically requires heated storage at 30–40°C or an inline dilution skid to become pumpable, whereas the 28% grade can be transferred at 10–35°C using standard rotary lobe, progressive cavity, or centrifugal pumps. Supplier technical bulletins commonly report Brookfield viscosity below 2,500 mPa·s at 20°C for the 28% grade; the corresponding 70% paste frequently exceeds 15,000 mPa·s under identical spindle conditions. The handling benefit is therefore the elimination of heat tracing and heated storage for some production lines, but the delivered mass per active kilogram is higher.

    The dilution economics should be evaluated on a dry-active basis. Formulating to 12% active anionic matter in a 1,000 kg batch requires 428.6 kg of SLES-28 at 28% active, compared with 171.4 kg of SLES-70 at 70% active. The resulting volumetric increase affects storage tank sizing and freight mass. In exchange, the 28% grade avoids the metered hot dilution step and reduces the risk of gel-phase stratification that can occur when 70% paste is added too rapidly to cold water without sufficient shear.

    Storage should be in closed tanks constructed from 316L stainless steel or high-density polyethylene. Carbon steel is not recommended because the surfactant may promote metal surface wetting and under-deposit corrosion. Recirculation lines should be sized for low-shear or laminar flow; continuous high-shear recirculation can entrain air and produce stable foam blankets in the headspace. At 5°C, the product may become slightly turbid, but a short recirculation at 10–15°C typically restores visual clarity without active matter loss.

    Product Specification Ranges and Analytical Test Methods

    The table below summarises commonly reported certificate-of-analysis parameters. Limits may vary by supplier and should be fixed in the purchasing specification rather than inferred from generic data.

    ParameterTypical range or limitTest method
    AppearanceClear to pale yellow liquidVisual at 20–25°C
    Active matter27.5–28.5% w/wISO 2271
    pH as received7.0–9.0ISO 4316
    Sodium sulfate1.5%ISO 6844
    Density at 20°C1.03–1.07 g/cm³ISO 758
    Brookfield viscosity at 20°C1,000–3,000 mPa·sISO 2555
    Hazen colour50 HazenISO 2211

    In a 5,000 L jacketed mixing vessel fitted with a turbine agitator, the addition sequence for a dishwash base should place SLES-28 after neutralized LABSA and before amphoteric betaine. This sequence prevents exposure of the ether sulfate to concentrated acid. At pH below 4.0, acid-catalysed hydrolysis of the ether sulfate linkage can reduce active matter and generate fatty alcohol ethers, which may appear as haze or cause odour drift. Neutralized LABSA, typically pH 7–9 after sodium hydroxide addition, should be cooled to below 45°C before SLES-28 is added; higher temperatures accelerate oxidation and can deepen colour, especially in the presence of trace iron.

    The product can be used as the sole anionic surfactant in economy manual dishwash but is more commonly co-formulated with linear alkylbenzene sulfonate at an active matter ratio of 1:1 to 3:1 SLES-28:LABSA. The ratio balances foam volume, grease-cutting, and skin mildness. Production-scale batch records show that final viscosity depends more on the salt response of the mixed anionic system than on the viscosity of the individual raw materials.

    Sodium sulfate is not merely a diluent in this product; it contributes to the initial ionic strength of the batch. Because the salt curve in a mixed anionic/amphoteric system is sensitive to total electrolyte, the sulfate content of each incoming batch should be subtracted from the sodium chloride budget. A batch produced with a high-sulfate supplier lot at 1.5% sodium sulfate may require 0.2–0.4% less sodium chloride than a low-sulfate lot at 0.5%, even if active matter remains constant. This lot-to-lot shift is a common cause of viscosity deviation in production when the purchasing specification lacks an upper sulfate limit.

    When SLES 28% Replaces Sodium Lauryl Sulfate Powder in a Cold-Mix Dishwash Line

    Conversion from sodium lauryl sulfate powder to the 28% ether sulfate changes material handling from a dust-controlled powder induction unit to a liquid metering system. SLS powder is typically supplied at ≥90% active matter and requires a high-shear disperser to prevent lump formation; SLES-28 can be introduced through a positive-displacement metering pump directly into the main mix vessel. The cost per active kilogram is higher for the liquid grade because water and freight are included, but the elimination of dust extraction, wetting time, and powder bridging can reduce batch cycle time on an existing liquid line.

    Formulation differences extend beyond handling. SLS powder tends to produce a lower initial foam volume in hard water and can precipitate as the calcium salt; SLES-28 maintains clarity at water hardness up to 150–300 mg/L CaCO₃ depending on concentration and temperature. In manual dishwash liquids, the ether sulfate is selected when a denser, less irritant foam profile is required. The trade-off is that the 2 mol EO distribution shifts the micellisation behaviour; no universal critical micelle concentration value should be applied across suppliers because the alkyl chain distribution and ethylene oxide distribution vary among feedstock sources.

    FeedstockPhysical formActive matterpH as suppliedHandling requirement
    SLES 28% LDDAqueous liquid27.5–28.5%7.0–9.0Direct liquid metering
    SLS powderPowder or needles90%7.5–10Dust control, high-shear induction
    SLES 70% pasteViscous paste or gel68–72%7.0–9.0Heated storage or dilution
    LABSA 96%Viscous acid96%<1Neutralisation before use

    In a transfer from powder to liquid, the most frequent production defect is overshooting final viscosity due to the preconceived salt requirement. Because the liquid grade already contains water and can carry sodium sulfate from the sulfation process, the effective salt content of the raw material must be included in the thickening calculation. A batch that performed at 1.8% added sodium chloride with SLS powder may require only 1.0–1.4% added salt with SLES-28 when the same total active matter is used. The adjustment is made by preparing a 25% NaCl stock solution and dosing it under agitation at 0.1% increments, with Brookfield LVT viscosity checked at 25°C, spindle 2, 12 rpm after deaeration.

    Process conflicts arise when the salt curve is approached from the high side. Beyond the plateau maximum, further salt addition can cause viscosity collapse or gel formation, depending on betaine ratio and perfume type. Reversing an over-thickened batch is possible only by dilution and rebuild with additional surfactant, which shifts active matter and may require re-preservation. Published data for this specific configuration is limited; therefore, each production site should generate a salt-response curve for its fixed perfume and preservative system.

    Viscosity after manufacture should be measured at 25°C after deaeration because entrained air can suppress the reading by 10–30% in low-viscosity dishwash bases. The result is compared against a production control chart based on Brookfield LVT, spindle 2, 12 rpm, with a defined immersion depth and beaker diameter. Without fixed spindle, speed, and temperature, viscosity values are not transportable between batches or plants.

    In manual dishwash performance testing, foam stability is evaluated under soil load using modifications of DIN 53902 or internal panel tests. The ether sulfate often shows lower initial flash foam than sodium lauryl sulfate but better foam retention in the presence of oily soil at comparable active matter. This behaviour is formulation-dependent; published comparative data for the 28% liquid base versus other feedstocks is limited, so process development should rely on standardised foam measurements with the target perfume and water hardness.

    Relative to alpha-olefin sulfonate at equivalent active matter, SLES-28 has lower colour and milder odour but lower stability in strongly alkaline builders. In a liquid laundry application in which the finished pH is maintained above 10.5, alpha-olefin sulfonate or secondary alkane sulfonate may be preferred because the ether sulfate may undergo gradual hydrolysis. Conversely, in transparent dishwash at neutral pH, SLES-28 can deliver lower-temperature clarity and better compatibility with betaines than secondary alkane sulfonates.

    Because the 28% grade contains approximately 72% water, it is not intrinsically self-preserving in bulk storage. Storage tanks should be vented through 0.2 µm filters or nitrogen blanketed. In-drum shelf life is typically 12 months at 5–35°C; lower temperatures may produce temporary turbidity, while repeated freeze-thaw cycles are not recommended. Microbiological stability of the finished product should be confirmed by ISO 11930 challenge testing when preservatives are selected. The anionic active matter by ISO 2271 should be measured on every received batch, and the pH should be re-checked after prolonged storage above 30°C because ester hydrolysis can lower pH gradually.

    Regulatory data for the ether sulfate class indicate ready biodegradability under OECD 301F; however, finished-product claims depend on the full formulation and regional detergent regulation. Suppliers should provide REACH registration numbers for the exact substance and tonnage band. The 1,4-dioxane residual should be controlled through the sulfation process and specified as needed for the target market; if the finished product is covered by cosmetic or personal care limits, a limit of ≤30 mg/kg is commonly requested, but the detergent grade is not automatically certified to cosmetic monograph limits.