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SLES 70% – Low Dioxane Grade (≤10ppm)
- Product Name: SLES 70% – Low Dioxane Grade (≤10ppm)
- Factroy Site: Yudu County, Ganzhou, Jiangxi, China
- Price Inquiry: sales4@ascent-chem.com
- Manufacturer: Ascent Petrochem Holdings Co., Limited
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- In terms of specification, SLES 70% – Low Dioxane Grade (≤10ppm) is supplied with 70% active matter and 1,4-dioxane content ≤10 ppm, making it suitable for mild personal care rinse-off formulations.
| HS Code | 631511 |
| Product Name | SLES 70% – Low Dioxane Grade (≤10ppm) |
| Chemical Name | Sodium Lauryl Ether Sulfate |
| Cas Number | 9004-82-4 |
| Molecular Formula | CH3(CH2)11(OCH2CH2)nOSO3Na |
| Appearance | Clear to slightly hazy viscous liquid |
| Active Matter Content Percent | 70 ± 2 |
| Ph 1 Percent Solution | 7.0 - 9.5 |
| Dioxane Content Ppm | ≤ 10 |
| Sodium Sulfate Content Percent | ≤ 1.5 |
| Color Apha | ≤ 50 |
| Odor | Characteristic faint fatty odor |
| Density At 20c G Per Cm3 | 1.05 |
| Viscosity At 20c Mpa S | 500 - 3000 |
| Cloud Point C | 0 - 5 |
As an accredited SLES 70% – Low Dioxane Grade (≤10ppm) factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.
| Packing | SLES 70% Low Dioxane Grade (≤10 ppm) is packaged in 220 kg polyethylene-lined steel drums, ensuring secure containment. |
| Container Loading (20′ FCL) | 20' FCL loading of SLES 70% (Low Dioxane ≤10ppm) in drums/IBCs, secured palletized cargo for safe transport. |
| Shipping | SLES 70% – Low Dioxane Grade (≤10 ppm) ships in sealed HDPE drums, IBC totes, or isotanks, depending on volume. Transport must follow hazardous goods regulations, with proper labeling, ventilation, and moisture protection. Store away from heat and oxidizers. Ensure containers are secured upright to prevent leakage during transit. |
| Storage | Store SLES 70% – Low Dioxane Grade (≤10ppm) in tightly sealed, corrosion-resistant containers (e.g., stainless steel or HDPE), in a cool, dry, well-ventilated area away from direct sunlight, heat, and moisture. Maintain temperatures between 10–30°C, avoid freezing, and segregate from strong oxidizers and acids. Under proper conditions, shelf life is typically 6–12 months. |
| Shelf Life | Shelf life: 1 year from manufacture if stored sealed, protected from extreme heat/cold, and kept in original container. |
Low-dioxane SLES 70% (sodium lauryl ether sulfate, approximately 2 moles of ethylene oxide, 70% active matter, 1,4-dioxane ≤10 ppm) is specified in rinse-off detergent systems where residual 1,4-dioxane control is a sourcing constraint rather than a post-formulation correction. The paste has shear-thinning flow at 25–35 °C; bulk storage in insulated 316L stainless steel or polypropylene tanks is held at 28–32 °C to maintain transfer viscosity, while drums stored below 20 °C require tempering before positive-displacement transfer. Certificates of analysis include headspace gas chromatography–mass spectrometry quantification of 1,4-dioxane with a reporting limit at or below 2 ppm. The applications below are restricted to rinse-off detergents and wet-cleaning processes where the ether sulfate contributes detergency, foam, and salt-responsive viscosity.
Liquid hand-dishwashing compounds based on low-dioxane SLES 70% are manufactured as high-active concentrates at 35–45 °C in sealed stainless-steel mixing vessels fitted with side-scraped agitators, then let down with demineralized water to a final active anionic range of 10.5–17.5% w/w (15–25% w/w SLES 70% as supplied). The surfactant blend is fixed at a total active ratio of ether sulfate to cocamidopropyl betaine/lauryl amine oxide of 1:0.25–1:0.45, and tetrasodium glutamate diacetate is added at 0.5–1.0% w/w to buffer hard-water calcium and magnesium cations without precipitating at 300–400 ppm water hardness. Sodium chloride is post-dosed as a 25% brine solution at 1.2–2.0% w/w after the batch pH is corrected to 6.5–7.2 with 50% citric acid solution; in-line static mixers containing 6–12 elements handle the rapid salt-induced viscosity transition from approximately 150–250 mPa·s to 1,800–3,000 mPa·s without mechanically aerating the finished gel. For compliance, the residual 1,4-dioxane level ≤10 ppm on the raw material certificate of analysis is reconciled with EU Detergent Regulation (EC) No 648/2004 biodegradability and labeling obligations, and the surfactant is registered under REACH (EC) No 1907/2006 with ready biodegradability data generated to OECD 301B. Terminal product types include manual dishwashing liquids, pumpable commercial pot-wash liquids, and flexible refill-pouch concentrates; process controls at the filler must cap back-pressure below 4 bar because the salt-thickened product exhibits pseudoplastic yield and can cavitate rotary fillers if the suction line diameter is below 50 mm.
What Limits Salt-Thickening Margin in Personal Cleansing Systems Based on SLES 70%?
In transparent shampoo and body wash manufacture, the thickening limit is set by the weight fraction of SLES 70% that can be salted into a shear-thinning lamellar network without phase separation; added active matter from SLES 70% is typically 8.0–12.0% w/w active (11.5–17.0% w/w as supplied), and the final total active matter including cocamidopropyl betaine or lauryl hydroxysultaine reaches 12.0–15.0% w/w. The production sequence reverse-adds the betaine into demineralized water at 30–35 °C, then slowly introduces low-dioxane SLES 70% preheated to 35 °C through a ring manifold at the vessel wall; direct injection into the vortex of a center-mounted agitator creates persistent gel lenses that reduce batch turnover and require post-filtration. The batch is acidified to pH 5.3–5.8 with lactic acid or citric acid, and sodium chloride is added at 1.0–1.5% w/w to reach 4,000–8,000 mPa·s on a Brookfield LV viscometer using spindle 3 at 12 rpm and 25 °C per ASTM D2196-20. Cosmetic compliance is structured around ISO 22716:2007 manufacturing controls and EC 1223/2009 Article 17 trace management for 1,4-dioxane; because 1,4-dioxane is classified as Carc. 1B H350 under CLP (EC) No 1272/2008, the ≤10 ppm raw material specification and batch-specific headspace GC-MS release are reviewed within the cosmetic product safety assessment rather than treated as optional quality data. Terminal product types include clear shampoos, pearlized body washes, sulfate-based shower gels, and daily-use liquid hand soaps; the main manufacturing failure mode is a viscosity plateau below 1,200 mPa·s when the total active matter drops under 10% w/w, which cannot be corrected solely by additional sodium chloride without destabilizing the lamellar network.
At manual car-wash stations where high-foam detergents are applied through 0.8–1.2 mm orifice foam lances and then recovered through wash-water reclamation systems, low-dioxane SLES 70% is incorporated into super-concentrates at 22–28% w/w as supplied, yielding 15.4–19.6% active anionic in the concentrate and 0.08–0.30% active anionic in the final foam-lance dilution. The batch is prepared in stainless-steel mixers with sawtooth disperser blades operated at 900–1,200 rpm for 20–30 min; high-foam additives are introduced after the surfactant is fully hydrated, and the pH is buffered to 7.0–7.5 with sodium citrate rather than caustic soda to protect long-term color stability in clear trigger spray packaging. Ready biodegradability of the finished blend is confirmed under OECD 301F, and the ≤10 ppm 1,4-dioxane specification is carried into the Section 3 composition disclosure for EU Detergent Regulation (EC) No 648/2004; for professional carwash operators, the raw material supports low-impurity profiles in recycled wash-water systems where non-readily-biodegradable residues are already restricted by local discharge permits. Terminal product types include snow foam, touchless pre-wash, hand-wax car shampoo, and motorcycle/cycle rinse-off cleaning concentrates; the main process failure mode on high-speed fillers is air entrainment when the concentrate is transferred by centrifugal pump above 1,500 L/h, which is corrected by switching to a lobe pump with 0.5–1.0 bar back-pressure control.
When a Low-Dioxane Ether Sulfate Is Specified for Sensitive-Skin Foaming Cleansers
Low-dioxane SLES 70% is selected in sensitive-skin and infant rinse-off formats at lower active loadings than standard personal cleansers: 5.0–8.0% w/w as supplied in body washes (3.5–5.6% active) and 2.5–5.0% w/w as supplied in baby wash and junior shampoo (1.75–3.5% active). At these active levels, the salt-thickening reserve of SLES collapses, so PEG-120 methyl glucose dioleate at 1.0–1.5% w/w is pre-hydrated in cold water for 45–60 min under slow agitation before the surfactant addition to provide pseudoplastic yield without sodium chloride. The batch is acidified to pH 5.0–5.5 with lactic acid, and amphoteric/amino-acid co-surfactants are introduced at an active ratio of 1:0.6–1:1.0 to the ether sulfate to lower protein-binding and ocular sting. Cosmetic compliance is structured around ISO 22716:2007 manufacturing controls and EC 1223/2009 Article 17 trace management for 1,4-dioxane; because 1,4-dioxane is classified as Carc. 1B H350 under CLP (EC) No 1272/2008, the ≤10 ppm dioxane specification is reviewed in the cosmetic product safety assessment as a toxicological threshold rather than a commercial differentiator. Terminal product types are fragrance-free baby wash, hypoallergenic hand foam, extra-mild facial cleanser, and sulfate-containing intimate wash bases; the main manufacturing constraint is that final viscosity below 2,500 mPa·s may require a second post-homogenization hydration rest of 4–6 h at 25 °C to eliminate air bubbles, especially in transparent pump-foamer bottles with dip-tube diameters below 2 mm.
Liquid Laundry Detergent Stability and Residual 1,4-Dioxane Control
Heavy-duty liquid laundry detergents include low-dioxane SLES 70% at 6.0–12.0% w/w as supplied to provide anionic detergency and to stabilize nonionic-loaded microemulsions without contributing to fabric encrustation. The batch is built at 25–30 °C in glass-lined or 316L stainless vessels; linear alkylbenzene sulfonic acid is neutralized in situ with monoethanolamine or sodium hydroxide to pH 7.5–8.5, then the SLES 70% is pumped into the neutralized LAS phase and followed by nonionic ethoxylates, propylene glycol, and sodium cumene sulfonate as hydrotrope at 1.0–3.0% w/w. Alkaline builders including sodium citrate and sodium carbonate are dissolved before enzyme addition, and protease/amylase liquids are dosed after the batch temperature drops below 40 °C to preserve activity at 80–95% of declared enzyme content. Regulatory compliance rests on EU Detergent Regulation (EC) No 648/2004 for ultimate aerobic biodegradability and on REACH (EC) No 1907/2006 for the registered SLES substance; the ≤10 ppm 1,4-dioxane level is retained in the final formulation below 1.2 ppm when the addition fraction does not exceed 12% w/w as supplied, producing a low-impurity profile suitable for AISE Charter for Sustainable Cleaning reporting. Terminal product types are standard liquid laundry detergents, compact liquid detergents, pre-spotter laundry gels, and fragranced laundry emulsions; the main production failure is gelling in the premix when LAS neutralization temperature exceeds 45 °C before SLES addition, which is avoided by maintaining neutralization below 40 °C and by sequencing the hydrotrope before ether sulfate injection.
For neutral-pH institutional floor detergents used in healthcare, long-term care, and food-processing wet areas, low-dioxane SLES 70% is incorporated at 8–12% w/w as supplied to deliver wetting on vinyl, sealed concrete, and epoxy-coated floors without leaving tenacious anionic residues that attract black heel marks. The process blends the ether sulfate with dipropylene glycol monobutyl ether solvent at 2–4% w/w, sodium citrate at 1–2% w/w, and a silicone defoamer emulsion at 0.05–0.10% w/w under low-shear propellers at 400–600 rpm; the finished concentrate is diluted at 1:80 to 1:120 through wall-mounted proportioning systems to a use solution of 0.06–0.12% active anionic. Compliance is anchored to EU Detergent Regulation (EC) No 648/2004 for surfactant biodegradability and to OECD 301B ready biodegradability of the formulated detergent; the ≤10 ppm 1,4-dioxane raw material specification supports occupational exposure documentation where prolonged dermal contact occurs during manual floor mopping. Terminal products include no-rinse floor detergents, daily cleaning concentrates for automatic scrubbers, and low-foam hard-surface detergents for rotary brush machines; the practical limit is that SLES-based formulas above 12% w/w as supplied generate flash foam in cylindrical brush decks, requiring an increase in defoamer to 0.20% w/w or a switch to a narrower ethylene oxide distribution ether sulfate.
Competitive SLES 70% – Low Dioxane Grade (≤10ppm) prices that fit your budget—flexible terms and customized quotes for every order.
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- SLES 70% – Low Dioxane Grade (≤10ppm) is manufactured under an ISO 9001 quality system and complies with relevant regulatory requirements.
- COA, SDS/MSDS, and related certificates are available upon request. For certificate requests or inquiries, contact: sales4@ascent-chem.com.
Product designation SLES70-LD10 is supplied as an aqueous sodium lauryl ether sulfate concentrate with a nominal ethoxylation degree of 2 mol EO, an active matter content of 70 ± 1 wt%, and a residual 1,4-dioxane concentration not exceeding 10 mg/kg in the as-received raw material. The material is identified by CAS 68891-38-3 and INCI name Sodium Laureth Sulfate. It appears as a clear to slightly hazy pale liquid at 25°C. The product functions as an anionic surfactant in rinse-off and leave-on cleansing systems, providing detergency, foam generation, and electrolyte-responsive viscosity build. SLES70-LD10 is not a chemically modified surfactant relative to conventional SLES 70%; it is the same lauryl ether sulfate backbone with tighter impurity control on 1,4-dioxane.
Chemically, the product is represented as R(OCH₂CH₂)nOSO₃Na, where R is predominantly C12–C14 and n averages 2. The hydrophobic chain distribution follows the feedstock alcohol; lauryl alcohol cuts commonly contain 68–75% C12 and 22–28% C14. The anionic sulfate head group provides foaming and emulsification, while the ethoxy spacer improves hard-water tolerance relative to sodium lauryl sulfate. The supplied concentrate contains approximately 28–30 wt% water, with the balance comprising active matter, sodium chloride, sodium sulfate, and minor unsulfated matter.
| Parameter | Method | Specification |
|---|---|---|
| Active matter | ISO 2271 | 69.0–71.0 wt% |
| 1,4-Dioxane | Headspace GC-MS with isotope dilution | ≤10 mg/kg |
| pH (5% aqueous, 25°C) | ISO 4316 | 7.0–9.5 |
| Sodium sulfate | ISO 4322 | ≤1.5 wt% |
| Unsulfated matter | ISO 8799 | ≤2.0 wt% |
| Colour | ISO 6271 | ≤30 Hazen |
Release testing for the ≤10 mg/kg dioxane limit uses isotope-dilution headspace GC-MS; the reporting limit should be no higher than 5 mg/kg to support reliable pass/fail decisions. Published standard methods specific to 1,4-dioxane in ethoxylated surfactant matrices are limited; quality control laboratories may adapt US EPA 8260D or equivalent isotope-dilution protocols. Because 1,4-dioxane is volatile, sample handling must minimize evaporative loss before injection. Active matter is determined by anionic titration in a two-phase system under ISO 2271; pH is measured in 5% aqueous solution at 25°C per ISO 4316.
How Does the ≤10 ppm 1,4-Dioxane Limit Affect Surfactant Processing?
1,4-Dioxane is not added to the product. It is formed as a side reaction during ethylene oxide insertion onto the lauryl alcohol backbone, with concentration influenced by catalyst type, ethylene oxide/alcohol molar ratio, reactor temperature, and neutralization pH. Conventional SLES 70% grades may leave the sulfation plant with 1,4-dioxane levels from 20 mg/kg to above 100 mg/kg depending on feedstock and process age. SLES70-LD10 is therefore processed through additional post-neutralization stripping. In production-scale equipment, the neutralized paste is fed to a wiped-film or falling-film stripper operated under vacuum with nitrogen or steam sparging. Typical stripping conditions reported in surfactant process literature include feed temperatures of 80–100°C, absolute pressure below 150 mbar, and controlled residence time to transfer 1,4-dioxane into the vapour phase. Because 1,4-dioxane forms a minimum-boiling azeotrope with water, stripping is often performed before final water adjustment to avoid excessive viscosity and to maintain active matter at 70%.
Removal of 1,4-dioxane from a high-viscosity surfactant paste is mass-transfer limited. The stripper must balance temperature, vacuum, and residence time against colour formation and active-matter preservation. If the paste is held too long at elevated temperature, the sulfate ester can undergo hydrolysis, generating free alcohol and lowering active matter. The stripping operation is therefore typically performed under vacuum 50–150 mbar at the lowest effective temperature, and the product is cooled immediately after discharge. Production plants monitor stripper condensate for 1,4-dioxane to verify removal efficiency rather than relying only on finished product testing. Published equipment-specific removal efficiency data for this exact product matrix is limited; release testing on each batch is required rather than relying solely on fixed process settings.
Batch-to-batch control at the ≤10 mg/kg limit requires upstream ethoxylate dioxane load to be constrained and stripper vacuum stability to be maintained. On continuous sulfation lines, variation arises from upstream ethoxylate quality and from fluctuations in steam sparging rate. In-process verification at the paste stage is used to divert nonconforming material before dilution to final concentration. The product is stored in closed, nitrogen-blanketed vessels to limit atmospheric CO₂ ingress and pH drift. Hydrolysis of the sulfate ester accelerates below pH 5.0 and at temperatures above 50°C. 316L stainless steel or high-density polyethylene are suitable wetted materials; unlined carbon steel is not recommended for prolonged storage.
Viscosity Build and Electrolyte Response in Clear Cleansing Formulations
In rinse-off personal-care formulations, SLES70-LD10 is typically used at 5–20 wt% as supplied, corresponding to 3.5–14 wt% active surfactant. The product does not produce significant viscosity in water alone; final viscosity is developed by electrolyte addition. Sodium chloride at 0.5–2.5 wt% is the most common modifier, and the response curve passes through a maximum. In a representative shampoo base containing 10 wt% SLES70-LD10, 3 wt% cocamidopropyl betaine, and 1 wt% cocamide DEA, viscosity after sodium chloride addition can be tuned from approximately 2,000 mPa·s to 12,000 mPa·s at 25°C depending on salt concentration. Overdosing beyond the peak causes viscosity collapse due to micelle structural changes and eventual phase separation in the presence of co-surfactants. The exact peak depends on the co-surfactant ratio, pH, and temperature. Rotational viscosity is measured by Brookfield RV at 20°C and 20 rpm, with method alignment to ASTM D2196-20.
Production-scale mixing of SLES70-LD10 requires slow agitation or low-shear blending during dilution to avoid air entrainment. High-shear dispersion is not necessary for complete hydration and may generate stable foam that requires vacuum deaeration. The product should be added to water at 30–40°C to reduce viscosity and improve pump transfer. After combining with co-surfactants, pH is adjusted to 5.0–7.0 with citric acid or sodium hydroxide. Preservative is added below 40°C where the preservative is temperature-sensitive. SLES70-LD10 is compatible with amphoteric surfactants such as cocamidopropyl betaine, nonionic alkyl polyglucosides, and alkanolamides in clear shampoo and body wash systems. Cationic conditioning polymers may be included at low charge density; strong complexation with high-charge cationic polymers can reduce foam and form precipitates. Preservative selection should follow challenge testing under ISO 11930; the unpreserved surfactant feed must not be assumed to protect finished formulations.
When the Low-Dioxane Grade Replaces Conventional SLES in Leave-On Applications
Replacement of a conventional SLES 70% with SLES70-LD10 is primarily a risk-control measure rather than a change in surfactant activity. For a formulation containing 10 wt% of a conventional 70% grade with 50 mg/kg 1,4-dioxane, the contributed residual is 5 mg/kg in the finished product. The same formulation using SLES70-LD10 at ≤10 mg/kg contributes ≤1 mg/kg. This difference is relevant in leave-on cleansers, baby care, facial wipes, and other products where dermal exposure time is longer and where retailers or regulators request trace CMR control. The grade does not remove 1,4-dioxane from other ethoxylated raw materials; formulators must sum contributions from all ethoxylates. Under California Proposition 65, 1,4-dioxane is listed as a carcinogen, and the no significant risk level for oral exposure is 30 µg/day. Low-dioxane SLES reduces the surfactant contribution but does not by itself confer compliance.
Under EU CLP, 1,4-dioxane is classified as Carcinogenicity Category 1B; under IARC it is Group 2B. EU Cosmetic Regulation 1223/2009 does not establish a numerical limit for 1,4-dioxane as an impurity in finished cosmetics, but control in practice occurs through raw material quality and trace CMR management. The low-dioxane grade is therefore used when the surfactant contribution must be minimized before final product testing or exposure assessment is performed.
| Parameter | SLES70-LD10 | Conventional SLES 70% |
|---|---|---|
| 1,4-Dioxane | ≤10 mg/kg | 20–100 mg/kg grade dependent |
| Active matter | 69.0–71.0 wt% | 69.0–71.0 wt% |
| Colour (Hazen) | ≤30 | ≤30–50 |
| Unsulfated matter | ≤2.0 wt% | ≤2.0–3.0 wt% |
| Sodium sulfate | ≤1.5 wt% | ≤1.5–2.0 wt% |
The principal operational difference is analytical and process-related rather than a shift in foaming or detergency. Because the low-dioxane grade receives additional stripping, the odour profile may be slightly lower in volatile ethoxylate residuals, but the active surfactant functionality is not altered. In manufacturing trials, no reformulation is required when substituting at equal active matter; however, the viscosity response curve should be revalidated because trace electrolyte and unsulfated matter differences between suppliers can shift the salt peak by 0.2–0.5 wt% sodium chloride.
In high-foaming manual dishwash concentrates, SLES70-LD10 is commonly combined with linear alkylbenzene sulfonic acid neutralized with sodium hydroxide or triethanolamine. The final pH is adjusted to 7.0–8.5, and hydrotropes such as sodium xylene sulfonate are used to maintain clarity. The low-dioxane grade does not alter enzyme stability or builder compatibility; however, the contribution of alcohol ethoxylates and other ethoxylated nonionics to the total 1,4-dioxane burden must still be evaluated. Published data for finished detergent matrices is limited; final product testing is required when a downstream specification is imposed.
Bulk storage of SLES70-LD10 should avoid freezing and temperatures above 40°C. If separation or viscosity stratification occurs after long static storage, gentle recirculation or low-shear mixing should be used to homogenize the batch before sampling. The product is not intended for use under strongly acidic conditions below pH 4.0, because acid-catalyzed hydrolysis of the sulfate ester will reduce active matter and generate free fatty alcohol. Strong oxidizing agents and high concentrations of cationic surfactants should also be avoided in concentrated systems because of incompatibility and potential precipitation.
