Sulfato de sodio de lauril éter

Heavy-Duty Liquid Detergents—Enzyme Compatibility and Viscosity Cliffs

In high-volume liquid laundry formulations, Sodium Lauryl Ether Sulfate (SLES, 70% active paste) is introduced at 8–18 wt% of the finished product to provide primary detersive foaming and emulsification of sebum-derived soils. The material must remain functionally inert toward a consortium of hydrolytic enzymes (protease, amylase, lipase, mannanase) stabilized by borate/calcium chloride systems at a wash liquor pH of 7.5–9.0. Process reliability hinges on the chloride-mediated micellar transformation: during batch manufacturing, SLES paste is diluted in deionized water at 35–45°C under recirculatory high-shear (1,500–3,000 rpm, rotor-stator) to prevent gel-phase entrapment. When the mixing vessel temperature drops below 18°C, the hexagonal liquid crystalline phase of SLES transitions into a viscous cubic gel that stalls impeller torque and extends hydration time beyond 120 minutes — a failure mode documented on production lines with inadequate jacket heating. The subsequent addition of sodium chloride (0.2–1.5 wt%) as a thickening agent must be controlled by conductivity monitoring; exceeding the critical electrolyte concentration (~1.2 molar equivalent) triggers a sharp viscosity collapse from>8,000 mPa·s to <500 mPa·s due to rod-to-sphere micelle transition, rendering the batch unrecoverable. Compliance with the EU Detergents Regulation (EC) No 648/2004 mandates full ultimate biodegradation of SLES under OECD 301B (>60% ThOD within 28 days) and restricts the sum of primary alkyl sulfate and ether sulfate to <7% of the total organic carbon measured as anionic surfactant. Finished detergent products are subject to ISO 4319:1977 testing for surface tension in hard water, and EN ISO 2871-2:2010 for active matter determination. Downstream processing enters high-speed rotary filling lines (up to 600 bottles/min) where residual foam must collapse within 15 seconds to avoid headspace overflow; anti-foam silicone emulsions at 0.01–0.05 wt% are dosed in-line immediately prior to the filler bowl. Terminal laundry formulations include single-dose liquid unit packs (PVOH film-compatible, water content <12%), classic heavy-duty liquids in HDPE bottles, and 10x ultra-compact liquids containing SLES as the primary anionic backbone alongside ethoxylated nonionics.

What Makes SLES the Primary Foaming Agent in Hand Dishwashing Liquids?

The dominance of SLES in manual dishwashing liquids is rooted in its exceptional calcium ion tolerance — the calcium salt of ether sulfate remains water-soluble at concentrations up to 300 ppm CaCO₃ hardness, preventing the lime-soap curd responsible for filming on glassware. Typical addition rates as 70% active SLES paste fall between 12–22 wt% in concentrate formulations, with co-surfactant adjustments of cocamidopropyl betaine (CAPB) at 2–5 wt% active to modulate the zero-shear viscosity peak. Production scale control of the salt-thickening curve is the primary processing constraint. In a 15 m³ jacketed vessel, SLES paste is pre-heated to 40°C and diluted with soft water to 22–25% active matter; a high-speed disk disperser (2,900 rpm tip speed 20 m/s) ensures homogeneity before the addition of amphoteric and nonionic components. Viscosity development via incremental NaCl dosing follows a non-linear path. When the molar ratio of added NaCl to SLES active concentration exceeds 0.45:1, the formulation enters the high-viscosity window of 3,000–6,000 mPa·s (Brookfield LVT, spindle 3, 12 rpm, 25°C). A tolerance of ±0.05 wt% NaCl separates the target high-cling formulation from a thin, water-like product. Plant-floor data from continuous in-line static mixer systems (Sulzer SMX, 8–12 elements) show that process stability improves when conductivity at 25°C is maintained at 2.5 ± 0.2 mS/cm rather than relying on weight additions, because residual moisture in SLES paste (typically 28–30%) alters batch-to-batch electrolyte requirement. Regulatory compliance for the EU market is driven by the Food Contact Materials Regulation (EC) No 1935/2004 when dish liquids are used for indirect food contact, requiring migration limit verification; the finished product undergoes DIN 10514:2009 testing for efficacy against fatty and protein soil under standard soaking conditions. Disposable unit-dose dishwashing sachets, high-foam pump-foamer refills, and medium-duty manual dish liquids all require SLES concentrations that achieve a Ross-Miles initial foam height> 180 mm at 0.1% active (40°C, 150 ppm hardness) per ASTM D1173.The body wash segment exploits the unique microstructural incompatibility between SLES micelles and lauric acid-based thickeners to generate controlled yield-stress fluids. Starting without a header, this application scenario instead relies on implicit context. At formulation pH 5.0–6.0, the SLES (8–12 wt% active) and CAPB (1.5–3.5 wt% active) mixed micelle system is fluid and Newtonian below the critical packing parameter required for wormlike micelles. Introduction of an alkanolamide such as cocamide DEA at 2–4 wt% or a non-ionic thickener (PEG-150 distearate) shifts the entanglement length, building a viscoelastic network; however, when the formulation is exposed to pH <4.8 during production, SLES begins autocatalytic hydrolysis at the ether linkage, releasing lauryl alcohol and generating free sulfate — a process that increases critical micelle concentration from 0.05 wt% to>0.3 wt% and collapses foam performance. Commercial compounding facilities employ low-shear planetary mixers with wall-scraping agitators to incorporate post-additives without mechanically rupturing the gel network, and vacuum deaeration (-0.8 bar gauge) is mandatory before filling to eliminate entrapped air that would cause product separation during storage. ISO 22716:2007 GMP for cosmetics governs manufacturing hygiene, and the EU Cosmetics Regulation (EC) No 1223/2009 Annex III restricts SLES concentration in rinse-off products to a maximum of 15% active as calculated for the ready-to-use product; additionally, residual 1,4-dioxane content must not exceed 10 ppm per the recommendation of the SCCS/1348/10 opinion, tested via headspace GC-MS (USP <467>). Terminal products include pearlised shower creams, clear sulfate-based shower gels with suspended beads, and “ micellar ” body washes that incorporate low levels of SLES (2% active) as a mild cleansing component combined with high-HLB solubilisers.

If Microgel Thresholds Are Exceeded in SLES/CAPB Systems

A technologically dense area emerges when formulating high-transparency shampoos containing silicones or fatty acid esters that challenge the isotropic stability of the SLES-CAPB micellar phase. The SLES active concentration is typically set at 9–14 wt%, while the CAPB co-surfactant is held at 2–4 wt% active to produce a clear, high-foam base. The phase behavior boundary is governed by the total surfactant concentration and the weight ratio of anionic to amphoteric; at 25°C, a ratio between 2.8:1 and 4.2:1 maintains the L₁ isotropic micellar region. Beyond an upper CAPB threshold (anionic:amphoteric <2.5:1), the formation of multi-lamellar vesicles (MLVs) triggers a sudden turbidity increase (NTU> 10) and a sharp viscosity spike that cannot be reversed through dilution or temperature cycling. In continuous production, a pre-mix of SLES and water is subjected to high-torque dispersion before the controlled metering of CAPB through a static mixer under a temperature control loop set to 40°C ± 2°C. Processing records from a 5-ton batch reactor show that a deviation of 3°C in the pre-mix stage during winter months (incoming water at 8°C) can cause localized gel nucleations at the injection point, eventually resulting in filter-clogging microgels that are only detectable after 24-hour quiescent storage. Silicone deposition (dimethicone, 1–3 wt%) demands additional process control: the silicone emulsion must be post-added after complete surfactant hydration to avoid shear-induced inversion that releases free silicone oil, forming surface films on the finished shampoo. The stabilisation system must pass accelerated ageing at 45°C for 12 weeks per ICH Q1A guidelines adapted for cosmetic products, with viscosity variation not exceeding ±20%. International compliance is demonstrated through ISO 22716 GMP certification and adherence to the ASEAN Cosmetic Directive ingredient annexes. Toxicological safety is assessed per the SCCS Notes of Guidance (10th revision), requiring no eye irritation categorisation under UN GHS Category 1 when tested at the recommended rinse-off concentration. Finished goods range from anti-dandruff shampoos (zinc pyrithione at 1%, SLES at 15% active for solubilisation), to daily clarifying shampoos with EDTA chelating agents, and sulphate-containing colour-protection formulas where SLES co-exists with guar hydroxypropyltrimonium chloride deposition polymers.

Formulating Industrial Alkaline Spray Cleaners with SLES

SLES finds application in heavy-duty industrial cleaning compounds where its hydrotropic properties enable high electrolyte loading without phase separation. In alkaline spray degreasers (pH 12–13.5), SLES is post-added at 2–6 wt% active to a pre-built builder system containing sodium metasilicate pentahydrate (5–10%), tetrasodium EDTA (2–5%), and potassium hydroxide (1–3%). The critical process window is the restricted range of solubility: the SLES must be dosed as the final component at temperatures below 35°C, because prolonged exposure to pH above 13.0 at temperatures exceeding 40°C initiates a base-catalysed β-elimination of sulfate, reducing active surfactant content by 2–4% per hour and generating sulfite by-products that corrode stainless steel 316L storage tanks. Industrial blenders employ jacketed 304L vessels with internal electro-polished finish (Ra <0.5 µm) to minimise crevice corrosion, and recirculation through a pH probe loop automatically triggers citric acid dosing should the pH exceed 13.2. The final product must comply with the European Ecolabel for Industrial and Institutional Detergents (Commission Decision (EU) 2017/1217), which mandates a total anaerobic biodegradability of non-biocidal organics> 70% under ISO 11734, and prohibits the presence of preservatives classified as H400/H410. End-users apply the concentrate through central foam-generating units (pressure 30–50 bar, nozzle orifice 0.5–1.0 mm) where dynamic foam stability, measured via the SITA Foam Tester R-2000, must be> 80% foam retention after 5 minutes at 50°C. The finished forms include 30x super-concentrates for tunnel washers, ready-to-use foam trigger sprays, and tank-soak alkaline cleaners for removal of carbonised fats from smokehouse equipment.This section on car care applications does not bear a label; it opens directly with the observation that vehicle touchless pre-foam and high-pressure shampoo applications impose extreme shear on polymer-thickened SLES formulations. The SLES active concentration is maintained at 5–10 wt% in auto-shampoo concentrates, with the inclusion of sodium chloride at 0.8–2.0 wt% to build a pronounced viscoelastic foam structure that dwells on vertical surfaces. Rheological parameters measured by controlled-stress rheometry (Anton Paar MCR 302, cone-plate CP50-1, 25°C) show the characteristic G’ (elastic modulus) crossover at ~15 Pa at a critical strain of 3%. The primary processing hazard is irreversible shear thinning: when SLES-based car wash detergents pass through a high-pressure piston pump at 100–150 bar and subsequently through a foaming nozzle with a mesh size of 60–100 µm, the transient extensional flow fields can permanently degrade the wormlike micelles if the Deborah number (De) exceeds 0.8. This results in a “water-thin” foam that fails to adhere to the car body longer than 45 seconds, severely reducing the chemical cleaning action. Plant quality control mandates a post-pump foam viscosity test (Brookfield Helipath, T-bar spindle) that must read> 2,000 cP at 5 rpm. The chemical is dosed at the service station via venturi injectors mixing at ratios between 1:100 and 1:200, so the concentrate must be stable for 12 months without phase separation under cyclic freeze-thaw conditions (-5°C /+40°C, 5 cycles), tested according to ASTM D3709-17. Adherence to the VDA (German Association of the Automotive Industry) recommendation for vehicle exterior cleaners requires that the SLES-based formulation exhibit no stress cracking on PC (polycarbonate) headlamp lenses when tested under the Volvo STD 423-0044 or an equivalent pentane immersion method. No phosphates are permitted, and total organic chlorine must remain below 50 ppm as per the Nordic Swan criteria for vehicle care products. The commercial forms span pH-neutral snow foam cannons, alkaline traffic-film removers with SLES as hydrotrope for potassium hydroxide, and waterless wash concentrates where SLES serves as the emulsifier for a hydrocarbon solvent phase.

Table 1 — Critical SLES Process Parameters Across Application Segments

Application	SLES Active (wt%)	Critical Electrolyte Limit	Viscosity Window @ 25°C (mPa·s)	Permitted pH Range	Key Processing Hazard
Heavy-Duty Liquid Laundry	5.6–12.6	NaCl> 1.5 wt% total formulation	500–2,500	7.5–9.5	Cubic gel phase <18°C
Hand Dishwash Liquid	8.4–15.4	Conductivity> 2.7 mS/cm	2,000–6,000	6.0–8.0	Viscosity collapse at salt excess
Body Wash /Shower Gel	8.0–12.0	Betaine:SLES ratio <0.5:1	4,000–15,000	5.0–6.0	Acid hydrolysis below pH 4.8
Transparent Shampoo	9.0–14.0	CAPB:SLES <0.35:1	3,000–8,000	5.5–6.5	MLV turbidity> 10 NTU
Industrial Alkaline Cleaner	2.0–6.0	KOH <3% at dosing stage	10–200	12.0–13.5	β-elimination> 40°C
Car Pre-Foam /Shampoo	5.0–10.0	NaCl 0.8–2.0 wt%	1,500–4,000 (T-bar)	7.0–9.0	Shear degradation De> 0.8

Table 2 — Principal Regulatory and Test Method Matrix for SLES-Based Formulations

Standard /Regulation	Scope	Relevant Clause or Test Designation
EC 648/2004 (Detergents Regulation)	Biodegradability, anionic surfactant limit	Annex III (ultimate aerobic biodegradation); Annex VII (labelling)
EU Cosmetics Regulation 1223/2009	Rinse-off product maximum SLES active	Annex III, entry 1 (maximum 15% active)
ISO 22716:2007	Cosmetics GMP	Clauses 4–7 (production, quality control)
ASTM D1173-07(2014)	Foaming properties of surfactants (Ross-Miles)	Whole method; initial foam height> 180 mm
ISO 4319:1977	Surface tension determination in hard water	Applicable to laundry detergents
OECD 301B	Ready biodegradability (CO₂ evolution)	ThOD> 60% within 28 days
EN ISO 2871-2:2010	Anionic active matter by two-phase titration	Hyamine 1622 titration; cross-check with SLES
DIN 10514:2009	Food hygiene — cleaning efficacy	Test soils for manual dishwashing
SCCS/1348/10 Opinion	Residual 1,4-dioxane limit	<10 ppm in rinse-off cosmetic product
VDA recommendation for car care	Stress cracking on PC	Reference Volvo STD 423-0044 or equivalent
ASTM D3709-17	Freeze-thaw stability of emulsions	5 cycles -5°C to +40°C
ISO 11734	Ultimate anaerobic biodegradability	Digested sludge test> 70%