NaOH production process in industry

NaOH (caustic soda NaOH) production – Current status, electrolysis technology & market trends

Production of NaOH plays a pivotal role in the global chlor-alkali chain. The world produces an average of 45–50 million tons of caustic soda each year, of which the US and Western Europe account for about 80% of the output; the US is the largest producer with a capacity of ~18,5 million tons/year.

NaOH production capacity by region in 2002
NaOH production capacity chart by region (reference 2002).

Current status of NaOH production in the world

About 94% of NaOH traded internationally is in liquid form, usually at a concentration of 50% by mass. Each year ~2 million tons of caustic soda are transported by sea (for alumina refining), and ~5 million tons are transported by road.

Solid caustic soda

The price of solid caustic soda is usually higher than that of liquid caustic soda by ~100–200 USD/ton (dry basis). The market is mainly located in developing countries due to limited infrastructure for using liquid caustic soda. As the infrastructure improves (China, CIS), the demand for solid caustic soda decreases, gradually shifting to liquid caustic soda.

Global caustic soda trade is around 400.000 tonnes/year and is decreasing by ~8%/year; ~225.000 tonnes are supplied by Europe. In Asia, Indonesia is an important market for caustic soda.

Liquid caustic soda

The Australian aluminium industry is the largest customer of seaborne caustic soda, consuming ~50% of seaborne caustic soda. Australia uses about 1,2 million tonnes of NaOH each year to produce ~13 million tonnes of alumina. Other major consuming markets include Brazil, Venezuela, Surinam, Jamaica, Guinea, South Korea, Colombia, etc.

NaOH price & floor-ceiling mechanism

Caustic soda prices are affected by both the demand for NaOH and the demand for its associated product, chlorine. Unlike chlorine, caustic soda prices have a “floor” and a “ceiling” due to its replacement by soda ash (Na2CO3).

  • Floor price: When the price of caustic soda is too low (for example, during the 1997 crisis, below 80 USD/ton), businesses convert NaOH into soda by carbonation (~130 USD/ton), creating a "cushion" to prevent the price of caustic soda from falling further.
  • Ceiling price: When caustic soda became too expensive, some industries turned to soda ash as a partial substitute.
Caustic soda price developments in the US 2001–2002 (USD/ton)
Caustic soda price developments in the US over several years (USD/ton).

Because chlorine is difficult to store safely, when the demand for chlorine (PVC) decreases, businesses are forced to reduce their chlor-alkali capacity, causing the supply of caustic soda to decrease and caustic soda prices to increase. Construction cycles, import taxes, exchange rates, etc. also significantly affect the supply-demand and price of NaOH.

Production costs by ECU in some regions in 1999
Production cost in ECU (1 ECU = 1,0 ton Cl2 + 1,1 tons of NaOH) in some areas (1999).

NaOH production & regional painting

Asia Pacific

Overall, Asia is not self-sufficient in chlorine, nor is it consuming all the caustic soda it produces domestically. High electricity prices reduce its competitive advantage in exporting caustic soda compared to the US and the Middle East; Australia remains a major 50% liquid caustic soda market due to the alumina industry.

CountryOutput (thousand tons/year)
Chinese8.230
Japanese2.755
Indian2.552
Korean990
Indonesia806
Taiwan756
Thailand508
Australia125
Malaysia100
Philippines28
Singapore22
Total16.872

Europe

In 2001, total chlorine production in Western Europe reached 9,26 million tons (capacity utilization rate ~85,6%). In the same year, total caustic soda production reached 9,62 million tons.

CountryChlorine production 2001 (thousand tons/year)
Germany3.640
French1.500
British780
Italy750
Belgium700
Spanish650
Netherlands580
Total8.600
CountryCaustic soda output 2002 (thousand tons/year)
Germany4.167
French1.812
Belgium889
Spanish792
Italy700
British661
Netherlands561
Switzerland325
Norway143
Finland140
Shirt66
Switzerland60
Total10.316

Demand & consumption trends

Total global caustic soda demand (2002 reference) ~46 million tonnes. Major consumption sectors include NaOH in water treatment, textile dyeing, pulp - paper, chemicals... Demand is forecast to increase by ~3%/year, while capacity only increases by ~1%/year, creating pressure to expand or upgrade technology.

NaOH usage rate by consumption sector
NaOH usage rates by industrial sectors (reference 2002).

NaOH production technology (electrolysis of table salt)

NaOH – Cl products2 - H2 appear simultaneously in the NaCl electrolysis tank. Three main electrolysis technologies: mercury (Hg) electrode, diaphragm and ion exchange membrane.

Mercury electrode technology

Advantages: very pure caustic soda product (Rayon grade), concentration 50–52% immediately after electrolysis. Disadvantages: strict safety-environmental management requirements due to mercury.

ImpuritiesContent (typical)Content (maximum)
NaCl10 ppm30 ppm
NaClO30,5 ppm1 ppm
Na2CO30,02% (wt)0,06% (wt)
Na2SO410 ppm20 ppm

Converted power consumption: ~3600 kWh/ton NaOH.

Diaphragm technology

Electrolysis bath gives 12–14% NaOH and contains a lot of salt; requires 3–4 concentration steps to reach 49–52%. “Technical grade” quality, NaCl/NaClO impurities3 higher.

ImpuritiesContent (typical)Content (maximum)
NaCl~1% (wt)1-3%
NaClO30,15% (wt)0,3%
Na2CO30,1% (wt)0,2%
Na2SO40,01% (wt)0,02%

Total converted consumption: ~5000 kWh/ton NaOH.

Ion exchange membrane technology

Is the main trend in NaOH production modern: lowest energy consumption, extremely low impurities. The solution leaves the tank at 33–35%, then concentrated to 50% for transport.

ImpuritiesContent (typical)Content (maximum)
NaCl< 30ppm75 ppm
NaClO3< 3ppm5 ppm
Na2CO30,03% (wt)0,05% (wt)
Na2SO415 ppm20 ppm

Converted power consumption: ~3360 kWh/ton NaOH.

Diagram of ion exchange membrane electrolyzer in NaOH production
Large membrane electrolyzers for modern chlor-alkali plants.

Safety and environmental notes: NaOH production requires chlorine & hydrogen gas control, alkali and corrosion resistant materials; brine pretreatment (Ca/Mg) to protect membranes; brine circulation and concentrated heat recovery.

Technology conversion trends in NaOH production

Many European plants still operate on Hg technology due to the age of the equipment and the large capital investment for conversion. However, increasingly stringent environmental requirements are accelerating the transition to membrane.

NaOH production capacity ratio by technology in Europe
Development of NaOH production capacity ratio by technology in Europe.
Tech Notes: Hg, Diaphragm, Membrane, Other
Tech Notes: Hg, Diaphragm, Membrane, and other.

Comparison of three technologies in NaOH production

CriteriaMercury electrodeDiaphragmIon exchange membrane
NaOH qualityVery high (Rayon grade); NaCl ~10 ppm, NaClO3 ~0,5 ppmTechnical; NaCl ~1%, NaClO3 Up to 0,15%Very high; NaCl <30 ppm, NaClO3 <3 ppm
Concentration after electrolysis50-52%12-14%33-35%
Total energy (DC converted)~3600 kWh/ton~5000 kWh/ton~3360 kWh/ton
Environment & SafetyHg risk – strict management requiredAsbestos/diaphragm problemMost friendly – ​​requires super clean salt water

Technical conclusions: Membrane is optimal in terms of energy and quality; Hg gives the highest quality but is environmentally stressed; Diaphragm is suitable when low CAPEX is a priority and concentrate costs are acceptable.

To know How much is NaOH? and choose the product configuration (50% liquid caustic soda, caustic soda flakes, caustic soda granules) suitable for your process, please contact Loc Thien for detailed advice.

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