Caustic Soda in Soap Making: Complete Guide to Saponification, Safety & Bulk Supply

- Caustic Soda in Soap Making: Complete Guide to Saponification, Safety & Bulk Supply
- Caustic Soda in Soap Making
Grades, dosage and bulk supply for soap manufacturers - How much caustic soda per tonne of soap?
- What caustic soda does in soap making
- SAP values for soap-making oils and fats
- Sizing a caustic soda contract for your soap plant?
- Best caustic soda for soap making: which grade to specify
- Caustic soda flakes, pearls or liquid for soap manufacturing
- How industrial soap is made with caustic soda
- What the finished soap standards actually require
- Handling caustic soda safely in a soap plant
- Buying caustic soda for soap manufacturing: the checklist
- How to get a price for caustic soda for soap making
- Ask for a price directly
- How soap manufacturers actually structure caustic soda supply
- How to choose a caustic soda supplier or exporter for soap manufacturing
- Caustic soda in soap making — FAQ
- Choosing caustic soda for your soap manufacturing operation
- Send the specification. Get a firm offer back.
- References
Caustic Soda in Soap Making
Grades, dosage and bulk supply for soap manufacturers
Caustic soda in soap making is the alkali that converts oil into soap, and roughly 121 kg of it on a 100% basis goes into every tonne of 78% TFM soap you produce. This guide covers the reaction, the SAP arithmetic, which NaOH grade and form each soap type needs, what the finished-product standards demand, and exactly what to specify when you buy caustic soda for soap manufacturing in bulk from an exporter.
- Product
- NaOH · CAS 1310-73-2
- Forms supplied
- Flakes 98% · Pearls 99% · Liquid
- Typical dosage
- ≈121 kg/MT of soap
- HS codes
- 2815.11 · 2815.12
- MOQ
- 25 MT — 1 × 20ft FCL
- Loading
- Mersin · Jebel Ali
- ≈121 kgNaOH per MT of soap
- 98–99%flake & pearl assay
- UN 1823Class 8 · PG II
- 25 MTMOQ, one 20ft FCL
How much caustic soda per tonne of soap?
Set your oil blend, your finished-product TFM and your monthly output, and this returns the sodium hydroxide you actually have to buy — in kilograms, in 25 kg bags and in containers. The arithmetic is the real stoichiometry, shown in full below the result, not a rule of thumb.
Assumes 98% assay flakes and the 1–2% alkali excess plants normally charge, with 2% used here. Recalculate against the saponification value stated on your own oil certificate of analysis — SAP values are ranges, not constants.
Indicative sizing, not a specification. Actual consumption shifts with free fatty acid in the oil, alkali losses, whether part of the alkali is substituted with soda ash on a fatty-acid route, and your own excess policy. Use it to size an enquiry, then confirm against a plant trial.
What caustic soda does in soap making
Caustic soda in soap making supplies the hydroxide ion that splits a triglyceride and converts the released fatty acids into their sodium salts — and a sodium salt of a fatty acid is what soap physically is.
Saponification, step by step
A fat or oil is a triglyceride: three fatty acid chains held on a glycerol backbone by ester bonds. Hydroxide attacks each ester carbon, the bond breaks, and the fatty acid leaves as a carboxylate ion which pairs with sodium.
1 triglyceride + 3 NaOH → 3 sodium soap + 1 glycerolThree points follow from the stoichiometry and they drive everything else on this page. First, the alkali requirement is fixed by the number of ester bonds in the oil, which is what a saponification value measures. Second, the reaction is exothermic — dissolving the caustic soda releases heat, and so does the saponification itself, which is why lye preparation and reaction vessels need cooling and controlled addition. Third, the hydroxide is fully consumed when the dose is correct, which is why correctly made soap contains no free caustic soda.
Glycerol is the co-product, not a waste stream. Around 93 kg of glycerol on a 100% basis is released per tonne of 78% TFM soap, about 11% of the oil charged. On the saponification route it is recovered from the spent lye and refined; in cold-process bars it stays in the soap and is sold as a feature.
Why sodium hydroxide and not another alkali
Because the sodium ion packs the fatty acid chains into a hard crystal. Swap sodium for potassium and the same fatty acids give a soft, water-soluble paste instead of a bar. That single difference divides the industry: caustic soda for solid bar soap and soap noodles, potassium hydroxide for liquid hand soap, soft soap and shaving products.
Two consequences for dosing. Potassium hydroxide SAP values are 1.403 times the sodium hydroxide values for the same oil, because KOH is the heavier molecule. And technical KOH flake is normally supplied at 90% rather than the 98–99% of caustic soda, so the charged weight has to be divided by the purity — a correction of about 11% against roughly 2% for NaOH.
What caustic soda is not doing
It is not a catalyst, though it is often described as one. A catalyst is recovered unchanged; the hydroxide here is a stoichiometric reagent that is consumed and ends up as part of the soap molecule. That distinction is why you buy it by the tonne against output, and why the calculator above works at all.
Where the ≈121 kg per tonne figure comes from
For a standard 80:20 palm / palm kernel blend making soap at 78% total fatty matter:
Blend SV = 0.80 × 199.5 + 0.20 × 242 = 208.0 mg KOH/g NaOH per g oil = 208.0 × 0.71289 / 1000 = 0.1483 g/g Fatty acid yield = 1 − (208.0 × 2.26074e-4) = 0.9530 g FA per g oil Oil per MT soap = 780 / 0.9530 = 818.5 kg NaOH (100%) = 818.5 × 0.1483 = 121.4 kgCross-checked against the fatty-acid neutralisation route, which must give the same answer: 780 kg fatty acid × 39.997 ÷ 257.1 average fatty acid molecular weight = 121.4 kg. The mass balance closes — 818.5 kg oil plus 121.4 kg NaOH minus 93.1 kg glycerol gives 846.7 kg of anhydrous soap, which back-calculates to exactly 78.0% TFM.
Add the 1–2% alkali excess normally charged, and buy 98% flakes rather than pure NaOH, and the practical purchase figure is roughly 124 to 127 kg per tonne of soap — about five 25 kg bags. Figures quoted as high as 140 kg per tonne imply about 15% alkali loss and are not defensible as a general number.
One qualification worth knowing before you size a contract: plants running the fat-splitting route, where the oil is hydrolysed to fatty acids first and the acids are then neutralised, often substitute part of the sodium hydroxide with soda ash. That lowers NaOH consumption below the figures above and changes your raw material mix.
SAP values for soap-making oils and fats
The saponification value is the mass of alkali needed to saponify one unit mass of a given oil. The NaOH figures below are derived from the Codex Alimentarius saponification value ranges for named vegetable oils and animal fats,[1][2] converted to the sodium hydroxide basis. They are ranges, not constants — fatty acid composition moves with cultivar, origin, harvest and refining, which is exactly why Codex publishes ranges in the first place.
| Oil or fat | Codex SV, mg KOH/g | NaOH SAP range, g/g | Midpoint | What it contributes |
|---|---|---|---|---|
| Coconut oil | 248–265 | 0.1768–0.1889 | 0.183 | Hardness and fast, dense lather from lauric acid; usually capped in skin bars |
| Palm kernel oil | 230–254 | 0.1640–0.1811 | 0.173 | The lower-cost lauric oil; the foaming half of a standard 80:20 noodle |
| Palm oil | 190–209 | 0.1354–0.1490 | 0.142 | The industry's structural hard oil; creamy stable lather, predictable supply |
| Beef tallow | 190–202 | 0.1354–0.1440 | 0.140 | Chemically close to palm; hard, long-lasting bars where tallow is cheap locally |
| Lard | 192–203 | 0.1369–0.1447 | 0.141 | White, hard, mild bars; regionally constrained by market acceptance |
| Cottonseed oil | 189–198 | 0.1347–0.1412 | 0.138 | A soft-oil filler where locally milled and priced below palm |
| Soybean oil | 189–195 | 0.1347–0.1390 | 0.137 | Soft oil; conditioning but slows hardening and shortens shelf life |
| Sunflower oil | 187–194 | 0.1333–0.1383 | 0.136 | Soft oil, mild; high-oleic grades keep better than commodity grades |
| Olive oil | 184–196 | 0.1312–0.1397 | 0.135 | Defines Castile soap; mild and conditioning, needs a long cure |
| Rice bran oil | 180–199 | 0.1283–0.1419 | 0.135 | Regional soft oil; the wide SV range makes a batch COA essential |
| Castor oil | 176–185 | 0.1255–0.1319 | 0.129 | Small additions only; lather booster and humectant |
| Shea butter | 160–195 | 0.1141–0.1390 | 0.127 | Premium positioning; the SV range spans ±14%, so never dose from a table |
← Swipe the table sideways to see every column.
Using a SAP value correctly
Multiply each oil weight by its NaOH SAP value, add the results, then multiply by one minus the superfat fraction:
NaOH = Σ (oil weight × SAP) × (1 − superfat)If your figure is published as mg KOH per gram — which is how oil suppliers and Codex state it — divide by 1.403 to convert to the sodium hydroxide basis before using it. Getting this wrong in either direction is the single most common dosing error, and it is a 40% error, not a rounding one.
Superfatting, also called a lye discount, means charging slightly less alkali than the theoretical requirement so that a little oil stays unsaponified. Craft cold-process practice generally runs a 5–10% lye discount,[3] both for skin feel and as a hedge against SAP-value uncertainty. Industrial noodle production works to a specified free fatty acid figure instead, so the superfat concept translates differently and should be set from your own finished-product specification rather than copied from a craft formula.
Dose against the certificate of analysis, not the table
Every number in the table above is a published range for a named oil, not a property of the drum in your warehouse. Rice bran spans 180–199 and shea spans 160–195; at the extremes of those ranges the alkali requirement moves by more than 10%.
Reputable oil suppliers state the actual saponification value on the batch certificate of analysis. Use that figure. Where it is missing, ask for it before contracting — an oil supplier who will not state a saponification value is asking you to guess at your largest process variable.
The same discipline applies on the alkali side: dose from the assay on the caustic soda COA, not the nominal grade on the offer sheet. A batch running 97.6% against a 98% nominal is perfectly normal and perfectly saleable, but it is a 0.4% shortfall in every batch you make from it.
Sizing a caustic soda contract for your soap plant?
Send your monthly soap output and the grade you need, and a firm quotation comes back with the specification, a batch certificate of analysis format, the safety data sheet, packing and container loading options, MOQ and lead time — loading FOB Mersin or FOB Jebel Ali, or CFR, CIF and DAP to a named destination.
Best caustic soda for soap making: which grade to specify
For most soap manufacturers the answer is 98–99% membrane-grade caustic soda in flake or pearl form, and the parameter that separates a good batch from a problem batch is iron, not assay. Assay tells you how much alkali you are paying for. Iron tells you what the bar will look like in six months.
| Soap product | Grade to specify | Form | Critical parameter | Why |
|---|---|---|---|---|
| Laundry bar soap | 98% industrial | Flakes | Assay, Na₂CO₃ | High volume, lean formulation, colour tolerance is wide — cost per unit of active alkali decides |
| Soap noodles for onward sale | 98–99% | Flakes or pearls | Assay consistency | Your customer reformulates around your TFM; batch drift in alkali shows up as drift in their product |
| Toilet soap & bath bars | 99% membrane | Pearls | Iron, chloride | Iron traces catalyse oxidation of the fat phase — discolouration and rancid odour over shelf life |
| Transparent / glycerin soap | 99% membrane | Pearls | Iron, colour | Every impurity is visible by definition; the product's whole claim is optical clarity |
| Antibacterial & medicated bars | 99% membrane | Pearls | Heavy metals | Active-ingredient claims usually bring a tighter raw-material dossier with them |
| Industrial & institutional soap | 98% industrial | Flakes or liquid | Assay, logistics | Concentrate strength dominates; liquid caustic works where the plant has tank capability |
| Liquid & soft soap | Potassium hydroxide | Flakes, 90% | KOH purity | A different alkali entirely — NaOH gives a bar, not a liquid. Dose at 1.403 × the NaOH SAP value |
← Swipe the table sideways to see every column.
The four impurities that matter
- Iron (Fe) — the one that shows in the finished bar. Iron traces catalyse oxidation of the fatty phase, producing yellowing and rancid odour over shelf life. Premium toilet soap buyers specify a low-iron membrane grade for exactly this reason. Ask for the figure in ppm, not a "low iron" adjective.
- Sodium carbonate (Na₂CO₃) — formed when caustic soda meets atmospheric carbon dioxide. It is a weaker alkali than NaOH, so a carbonated batch under-doses your saponification even though the bag weight is unchanged. It is also the reason opened bags degrade.
- Sodium chloride (NaCl) — a residue of the electrolysis. It affects electrolyte balance, and in liquid systems it moves viscosity in ways you did not ask for. Membrane-grade material carries less of it than diaphragm-grade.
- Heavy metals — arsenic, lead, mercury. Only decisive where the finished product carries a cosmetic, food-contact or pharmaceutical claim, but where it applies it is a pass-or-fail dossier item rather than a preference.
What "membrane grade" actually means
Caustic soda is a co-product of chlorine manufacture, and three cell technologies have been used: mercury cell, diaphragm cell and membrane cell. Membrane cell material carries markedly lower chloride and sulfate than diaphragm material and none of the mercury-cell legacy, which is why it has become the reference grade for anything with a purity-sensitive end use.
For a soap manufacturer the practical question is not the cell technology name on the offer but whether the COA carries the numbers. A supplier who writes "membrane grade, 99% min" and stops has told you the marketing; a supplier who states assay, carbonate, chloride and iron per batch has told you what you are buying.
Do you need food or pharmaceutical grade?
Almost never for soap. Food-grade FCC and pharmacopoeial caustic soda exist and carry tighter heavy-metal limits, but soap is a rinse-off product and the finished-product standards that govern it — free caustic alkali, TFM, moisture — are met comfortably with good industrial material. Specify a higher grade only where your own customer's dossier or a specific market registration demands it, and expect to pay for it. Speciality grades are quoted on enquiry.
Caustic soda flakes, pearls or liquid for soap manufacturing
Assay decides soap quality; physical form decides how your plant runs and what your landed cost per unit of active alkali actually is. These three are the same chemical in three delivery formats, and the right one is a function of your handling equipment, your climate and your distance from supply.
| Property | Flakes 98% | Pearls 99% | Liquid 30–50% |
|---|---|---|---|
| Typical assay | 98% min, 96% and 99% traded | 99% min | 30–50% w/w, 50% standard merchant |
| Active alkali per unit cost | Best | Good | Lowest — you freight the water |
| Dust generation | Moderate — enclosed transfer and PPE needed | Low — the main reason plants switch | None |
| Flow in feeders | Irregular shape, can bridge in screw conveyors | Free-flowing — suits automated dosing | Pumped; metering is the simplest of the three |
| Dissolution | Fast; exothermic, needs cooling and controlled addition | Fast and even | Already dissolved — no lye-making step |
| Storage requirement | Dry, sealed, ambient warehouse | Dry, sealed, ambient warehouse | Corrosion-resistant tank; heated in cool climates |
| Cold-weather issue | None — solids are unaffected | None | Crystallises near 12 °C; minimum unloading temperature about 21 °C[4] |
| Packing | 25 kg bags · 500/1,000 kg FIBC | 25 kg bags · FIBC | ISO tank · tank truck · 1,000 L IBC |
| Shelf life sealed | 12–24 months | 12–24 months | Long, but carbonates on air contact |
| Dangerous goods | UN 1823, Class 8, PG II | UN 1823, Class 8, PG II | UN 1824, Class 8, PG II or III by concentration |
| Best fit | Most soap plants; laundry and general bar production | Toilet soap, transparent soap, automated lines | Continuous plants close to the supply point |
← Swipe the table sideways to see all three columns.
How industrial soap is made with caustic soda
Two routes dominate, and which one you run changes what you buy. The saponification route reacts oil directly with caustic soda. The fat-splitting route hydrolyses the oil to fatty acids first, then neutralises them — often with soda ash substituting part of the caustic soda, which lowers your NaOH tonnage.
Where cold process sits in a commercial conversation
Cold process combines lye and oils without external heat, moulds the batch, and lets saponification finish in place. It takes roughly 18–24 hours to complete the reaction and a further 3–4 weeks to cure.[6] It retains the glycerol, accommodates heat-sensitive additives, and needs almost no capital equipment.
It also cannot be verified complete before the bar is wrapped, which is precisely why the SAP arithmetic has to be right the first time and why the alkali assay has to be trustworthy. For a manufacturer choosing a route, the honest framing is that cold process is a premium positioning and low-capital decision, not a throughput or consistency one — and either way the caustic soda specification matters more, not less.
What the finished soap standards actually require
Two numbers connect your caustic soda purchase to your finished-product compliance: total fatty matter, which sets how much alkali you consume per tonne, and free caustic alkali, which proves you dosed correctly. Both are governed by published method standards, not house practice.
Free caustic alkali — the limit that proves your dosing
Free caustic alkali is unreacted sodium hydroxide left in the finished bar. It is a skin-irritation and product-safety parameter, and the limits are tight:
- IS 2888:2004 — toilet soap, all three grades: 0.05% by mass maximum[7]
- IS 13498:1997 — bathing bars: 0.05% by mass maximum[8]
- EAS 186:2011 — East African toilet soap: 0.1% by mass maximum[9]
Note the factor of two between the Indian and East African limits — cite the standard your destination market actually applies rather than assuming a global figure. The measurement method is ISO 456 or the equivalent national method.
The practical link back to procurement: free caustic alkali failures come from over-dosing, and over-dosing usually comes from working off a nominal grade instead of a batch assay, or from a partly carbonated bag that read as full-strength on the label.
TFM — the grade your soap is traded on
Total fatty matter is the proportion of the soap that is fatty acid, determined by splitting the soap with dilute acid, extracting the fatty matter with ether, evaporating and weighing.[10]
Soap noodles are benchmarked in trade at 78% TFM, and the standard blend designation 80:20 means 80% palm oil and 20% palm kernel or coconut oil, with 90:10, 70:30 and 60:40 also traded.[11] Regulatory floors sit below the trading benchmark: IS 2888:2004 requires 76% minimum for Grade 1 toilet soap, 70% for Grade 2 and 60% for Grade 3, and EAS 186:2011 requires 76% minimum.
Why a caustic soda buyer cares: alkali consumption is proportional to fatty matter. Moving a product from 70% to 78% TFM raises your caustic soda requirement per tonne of output by roughly the same proportion — which is a real line in the raw-material budget and a real change in how many containers you book a year.
| Standard | What it determines | Why it matters to your alkali purchase |
|---|---|---|
| ISO 685:2020[15] | Total alkali content and total fatty matter, simultaneously, in soaps including liquid soaps, excluding compounded products | The single method behind both of your headline finished-product numbers |
| ISO 684:1974 | Total free alkali | Catches over-dosing before it becomes a customer complaint |
| ISO 456:1973 | Free caustic alkali | The specific test against the 0.05% and 0.1% regulatory limits |
| ISO 672:1978 | Moisture and volatile matter, oven method | Moisture dilutes TFM; a wet bar fails a grade it should have passed |
| ISO 673:1981 | Ethanol-insoluble matter | Picks up inorganic carry-over, including excess salt from the wash |
| ISO 8212 | Sampling techniques during manufacture | A COA is only as good as the sample behind it — this is the method that makes it defensible |
← Swipe the table sideways to see every column.
Handling caustic soda safely in a soap plant
Solid caustic soda is a Class 8 corrosive. The hazard is not exotic and it is entirely manageable, but it is the one raw material in a soap plant that will cause a serious injury from a single careless minute — and the exposure limits are widely misquoted, so they are set out precisely below.
| Limit | Value | Form — this is the part usually misstated |
|---|---|---|
| OSHA PEL | 2 mg/m³ | 8-hour time-weighted average, not a ceiling — 29 CFR 1910.1000 Table Z-1[12] |
| NIOSH REL | 2 mg/m³ | Ceiling — must not be exceeded at any time[13] |
| ACGIH TLV | 2 mg/m³ | Ceiling |
| NIOSH IDLH | 10 mg/m³ | Immediately dangerous to life or health |
← Swipe the table sideways to see every column.
Personal protective equipment
- Eyes — chemical splash goggles as the minimum. Safety glasses alone are not sufficient. A full face shield is worn over goggles for dissolving, decanting and open-vessel work.
- Hands — chemically resistant gloves in nitrile, neoprene or butyl rubber, inspected before each use. Not latex.
- Body — resistant apron or suit, long sleeves, rubber or PVC boots. Caustic soda destroys leather footwear, so leather boots are not protective equipment here.
- Respiratory — a NIOSH-approved particulate respirator where flake dust is generated in an enclosed area, or during large-scale dissolving. Enclosed transfer beats respirators wherever it is achievable.
- Facilities — an eyewash station and safety shower within ten seconds of the work area, tested on a schedule, with a clear unobstructed path.
First aid and storage
Skin contact — remove contaminated clothing at once and flush with cool running water for at least 20 minutes. Do not attempt to neutralise with acid: that generates additional heat in an already burned tissue. Seek medical attention for any burn larger than a palm.
Eye contact — a medical emergency. Flush at the eyewash station holding the eyelids open for 20–30 minutes and arrange transport to an ophthalmologist. Alkali burns to the eye progress after the exposure ends, which is why the flushing time is so long.
Ingestion — do not induce vomiting; contact poison control immediately.
Storage in the warehouse
Sealed, moisture-proof packaging in a cool, dry, ventilated store. Caustic soda is hygroscopic and reacts with carbon dioxide, so open or damaged bags cake and convert progressively to sodium carbonate. Segregate from acids — including any sulfuric acid or hydrochloric acid held for splitting or cleaning — and from aluminium, zinc and tin, which liberate hydrogen on contact. Bund spill containment to 110% of the largest single container.
Buying caustic soda for soap manufacturing: the checklist
These are the parameters to verify on the batch certificate of analysis and fix in the contract — not target values. Specifications vary by producer, grade and batch, and no published figure, ours included, substitutes for the documentation travelling with your own cargo.
On the certificate of analysis
what to read before you accept
- NaOH assay — the actual batch figure, not the nominal grade. This is what you dose against.
- Sodium carbonate — carbonated material under-doses your saponification at unchanged bag weight.
- Sodium chloride — electrolyte carry-over; matters most in liquid and transparent systems.
- Iron, in ppm — the parameter that decides whether a premium bar yellows on the shelf. Ask for a number, not an adjective.
- Heavy metals — where a cosmetic or food-contact dossier applies.
- Batch spread — ask for COAs from several recent batches. Judge the spread, not whether each one merely sits inside specification. Drift is what forces you to reformulate.
- Traceability — batch numbers that connect the bag in your warehouse to a COA and a production date.
- Production date and shelf life — typically 12–24 months sealed. Confirm you are not being offered aged stock.
On the contract and the cargo
what to fix before you sign
- Packing and net weight — 25 kg bags, 500 or 1,000 kg FIBC, or pallets. Confirm net weight per unit rather than assuming it.
- Bag quality — multi-layer with an inner liner, closure integrity, palletisation and shrink wrap. Bagged caustic soda that gets wet in transit arrives as a solid block.
- Container loading — 25 MT of bagged material in a 20ft is the standard load. Confirm stuffing pattern and dunnage.
- Dangerous goods documentation — UN 1823 Class 8 PG II for solid, UN 1824 for solution with the packing group assigned by concentration. Confirm marking and labelling meet destination requirements.
- SDS language — in the language your destination authority requires, not only English.
- Incoterm — EXW, FOB, CFR, CIF or DAP, and who arranges and pays for inland transport, loading, documentation and destination handling.
- Pre-shipment inspection — whether SGS, Intertek or Bureau Veritas is accepted at your cost.
- Payment terms — T/T, L/C at sight or D/P, matched to the trade history between you.
Container loading and what actually fits
A 20ft container takes 25 metric tons of bagged caustic soda as a standard load — 1,000 bags of 25 kg. That is also our minimum order quantity, and it is not an arbitrary number: it is one full container, which is the point below which the freight cost per tonne rises sharply and the documentation cost stops being proportionate.
Put that against the calculator at the top of this page. At roughly 125 kg of caustic soda per tonne of finished soap, one 25 MT container covers about 200 tonnes of soap production. A plant making 50 tonnes of soap a month is buying roughly one container a quarter; a plant making 500 tonnes a month is on a monthly or contract programme and should be pricing it that way.
Buyers who also take soda ash light for the fatty-acid route, stearic acid for bar hardness, or LABSA and SLES for a detergent line alongside the soap plant can consolidate several products into one shipment rather than booking part-loads separately.
How to get a price for caustic soda for soap making
No price is published on this page. Caustic soda is a traded commodity whose level moves with chlor-alkali operating rates, energy cost, freight and regional supply, and a figure written today would be wrong within weeks and misleading in any market other than the one it was quoted for. Every enquiry is answered individually — by email or on WhatsApp. Indicative current levels for reference grades are maintained on our caustic soda price page.
Ask for a price directly
Send the six lines above and you will have a quotation for caustic soda flakes, pearls or liquid, loading FOB Mersin or FOB Jebel Ali. Soap manufacturers sourcing several raw materials for one production line can consolidate the enquiry into a single shipment.
How soap manufacturers actually structure caustic soda supply
What changes between these is your working capital, your exposure to a price move, and how much warehouse space the alkali occupies.
Spot, container by container
- No contract exposure to a falling market
- Minimal warehouse space tied up
- Fully exposed to a rising market and to lead-time gaps
- Highest cost per tonne over a year
Scheduled programme
- Supply security without pre-paying for the year
- Volume pricing against committed tonnage
- Predictable warehouse and cash planning
- Specification locked once, applied to every lifting
Annual contract
- Best pricing and priority on allocation
- Dedicated batch reservation where required
- Needs a reliable production forecast to sign
- Suits plants selling noodles onward under their own spec
How to choose a caustic soda supplier or exporter for soap manufacturing
For a commodity alkali, supplier selection comes down to consistency and documentation. A supplier who delivers variable assay does far more damage — through reformulation, off-spec batches and customer complaints — than any apparent saving elsewhere recovers.
SUHA International Trading — caustic soda supplier for soap manufacturers
SUHA International Trading L.L.C., trading as Caustic Soda Co, is a supplier and exporter of caustic soda flakes 98%, caustic soda pearls 99% and liquid caustic soda to soap manufacturers, distributors and traders internationally, loading from Mersin in Türkiye and Jebel Ali in the UAE, with a batch certificate of analysis and safety data sheet supplied for every shipment.
Two loading origins is a practical point rather than a slogan: when a route is disrupted, a port congested or a producer on turnaround, the enquiry moves to the other origin instead of stalling. For buyers in Europe, the Black Sea, North Africa and the eastern Mediterranean, Mersin usually lands cheaper; for the GCC, East and West Africa, South Asia and the Indian Ocean, Jebel Ali usually does.
Soap manufacturers sourcing more than one input can consolidate — soda ash light for the fatty-acid neutralisation route, stearic acid for bar hardness, and the detergent surfactants LABSA 96% and SLES 70% for a parallel liquid line — all come from the same source, on one set of documents. The full range is on our products page, and buyers importing into Türkiye specifically can start from the caustic soda supplier Türkiye page.
- CAS
- 1310-73-2
- HS codes
- 2815.11 · 2815.12
- Dangerous goods
- UN 1823 · Class 8 · PG II
- Grades
- Flakes 98% · Pearls 99% · Liquid
- Packing
- 25 kg bags · FIBC · ISO tank
- MOQ
- 25 MT — 1 × 20ft FCL
- Loading
- Mersin · Jebel Ali
- Payment
- T/T · L/C · D/P
- Documents
- COA · SDS · TDS · CO · B/L
Caustic soda in soap making — FAQ
Choosing caustic soda for your soap manufacturing operation
Specify 98–99% membrane-grade caustic soda, choose flakes or pearls on how your plant handles solids rather than on headline price, and buy against the batch assay and the iron figure rather than the nominal grade.
What decides the technical choice
Assay sets your dosing, iron sets your shelf life, and physical form sets your handling. Laundry and general bar production runs comfortably on 98% flakes. Toilet soap, transparent soap and anything judged on colour justifies 99% low-iron pearls, and the premium is small against the cost of a discoloured production run.
What decides the commercial choice
Consistency, documentation and lead time. A supplier whose assay drifts costs you reformulation and complaints; a supplier who cannot produce a batch COA, a current SDS in the right language and correct UN 1823 paperwork costs you at the port. Neither cost appears in the unit price you compared.
Caustic soda is the non-substitutable input of soap manufacturing — there is no soap without a strong alkali, and no bar soap without sodium hydroxide specifically. That makes it a supply-security question as much as a purchasing one, which is why two loading origins and an honest lead time are worth more to a running plant than a marginal saving on a single container.
The practical sequence is short. Work out your tonnage from your own oil blend and TFM using the calculator above, decide the grade and form from the tables, write the specification down including the iron limit, and put the same enquiry to more than one supplier so you are comparing like with like. Then verify what arrives against the COA rather than the offer sheet — every time, not only on the first shipment.
Send the specification. Get a firm offer back.
Grade, tonnage, packaging, destination port and Incoterm — that is all it takes. A quotation comes back with the technical data sheet and the certificate-of-analysis format attached, normally within 24 hours on working days, for caustic soda flakes 98%, pearls 99% or liquid caustic soda, loading from Türkiye and the UAE.
References
- FAO/WHO Codex Alimentarius, CXS 210-1999 — Standard for Named Vegetable Oils (saponification value ranges). fao.org/fao-who-codexalimentarius
- FAO/WHO Codex Alimentarius, CXS 211-1999 — Standard for Named Animal Fats. fao.org (PDF)
- Handcrafted Soap & Cosmetic Guild, Superfatting and the Lye Discount. soapguild.org
- Occidental Chemical Corporation, Caustic Soda Handbook (50% solution crystallisation and minimum unloading temperature). oxychem.com (PDF)
- US Environmental Protection Agency, AP-42, Chapter 6.8 — Soap and Detergents. epa.gov (PDF)
- Adawiyah Jamil et al., cold saponification and curing of handmade soap, PMC6225244. pmc.ncbi.nlm.nih.gov
- Bureau of Indian Standards, IS 2888:2004 — Toilet Soap Specification. law.resource.org (PDF)
- Bureau of Indian Standards, IS 13498:1997 — Bathing Bars Specification. law.resource.org (PDF)
- East African Community, EAS 186:2011 — Toilet Soap Specification. law.resource.org (PDF)
- Bureau of Indian Standards, IS 286:1978 — Methods of Sampling and Test for Soaps (total fatty matter definition and method). law.resource.org (PDF)
- ICIS, Soap Noodles Pricing Methodology (78% TFM benchmark; 80:20, 90:10, 70:30 and 60:40 blend designations). icis.com
- US Occupational Safety and Health Administration, 29 CFR 1910.1000 Table Z-1 — Limits for Air Contaminants. osha.gov
- US National Institute for Occupational Safety and Health, NIOSH Pocket Guide to Chemical Hazards — Sodium hydroxide. cdc.gov/niosh
- Handcrafted Soap & Cosmetic Guild, The Water Discount (published lye concentration practice). soapguild.org
- International Organization for Standardization, ISO 685:2020 — Analysis of soaps: determination of total alkali content and total fatty matter content. iso.org
Technical values on this page are general commercial ranges and published standard figures provided for orientation. Saponification values are ranges rather than constants and vary with the origin, cultivar and refining of the oil; caustic soda specifications vary by producer, grade and batch. Always verify against the certificate of analysis and safety data sheet supplied with your own material, confirm the finished-product standard that applies in your destination market, and validate any formulation change through your own bench and plant trials before production. Nothing on this page constitutes a specification, a warranty or a formulation recommendation for a specific product. Content reviewed .

