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Lime Soda Process in Caustic Soda Production: Principles and Applications

Caustic soda, also known as sodium hydroxide, is a crucial chemical in various industries.  In this article, we'll delve into the details of one of the oldest methods, its advantages, and limitations, and compare it with other available technologies.

What is the Lime Soda Process?

It is developed by a chemical reaction that involves reacting calcium hydroxide (Ca(OH)2) with sodium carbonate (Na2CO3) to produce sodium hydroxide:

Na2CO3 + Ca(OH)2 → 2NaOH + CaCO3

This is also known as the causticizing process.

How Does the Lime Softening Work?

Here's a step-by-step overview:

  1. Dissolving Tank: Sodium carbonate (Na2CO3) with a concentration of 20% is added to a dissolving tank, and mixed with recycled weak liquor from the rotary filter.

  2. Causticizing: This is where the magic happens, and we transform sodium carbonate (Na2CO3) into caustic soda (NaOH). The process starts by mixing the sodium carbonate solution with slaked lime (Ca(OH)2) in just the right proportions. Think of it like baking a cake - you need to get the ingredients just right for it to turn out perfectly! Once the mixture is ready, we heat it up to 80-90°C using steam injection. This is where the chemical reaction really takes off! The slaked lime reacts with the sodium carbonate to form caustic soda and calcium carbonate (CaCO3). The resulting mixture is then left to settle, allowing the calcium carbonate to precipitate out. After that, we filter the mixture to separate the caustic soda from the calcium carbonate, and voilĂ ! We're left with a strong solution of caustic soda, ready to be used in a variety of industries, from paper manufacturing to soap making. It's a pretty cool process, and it's amazing to think about how this one reaction can have such a big impact on our daily lives.

  3. Agitation and Reaction: Air is used for additional agitation, and the reaction is carried out for 2-3 hours until equilibrium is attained.

  4. Thickening: Next up, we've got the Thickening step! After the Causticizing reaction, we're left with a mixture of caustic soda and calcium carbonate, along with some excess water. The goal here is to separate the solids (calcium carbonate) from the liquids (caustic soda solution), and that's where the Dorr thickener comes in. Imagine a giant, circular tank with a rotating rake at the bottom - that's basically what a Dorr thickener is! The slurry from the Causticizing step is pumped into the thickener, where the solids slowly settle to the bottom. As they settle, the rake at the bottom of the tank gently stirs the solids to help them compact and thicken. Meanwhile, the clear liquid (overflow) rises to the top and is skimmed off, leaving behind a thick, concentrated slurry of calcium carbonate. This thickened slurry is then sent off for further processing, while the overflow is recycled or sent to the next step in the process. It's a clever way to separate the solids from the liquids, and it's a crucial step in producing high-quality caustic soda.

  5. Evaporation: Now that we've separated the solids from the liquids, it's time to concentrate the caustic soda solution through Evaporation! The overflow from the Thickening step, containing around 10-11% NaOH, is sent to a triple-effect vacuum evaporator. This is where the magic happens, and we boost the concentration of NaOH to a whopping 50%!. The triple-effect vacuum evaporator is a clever piece of equipment that uses a combination of heat, vacuum, and clever design to evaporate the water from the solution. Here's how it works: the solution is heated in a series of vessels, each operating at a lower pressure than the last. This creates a vacuum effect that helps to boil off the water at a lower temperature, reducing energy costs and preventing damage to the equipment. As the water evaporates, the concentration of NaOH in the solution increases, eventually reaching the desired level of 50%. This concentrated solution is then cooled, filtered, and packaged for distribution to customers. It's an important step in the production process, as it allows us to create a high-quality product that meets the needs of a wide range of industries. And that's the power of Evaporation.

  6. Filtering: The sludge from the thickener is washed and sent to a rotary drum vacuum filter to remove calcium carbonate (CaCO3) in solid form.



Caustic Soda Production Flow Diagram: Lime Soda Process
Sodium Hydroxide Production: Lime Soda Process Flow diagram



Advantages 

  • Simple and cost-effective
  • No cell technology required
  • Can be used for small-scale manufacturing

Some limitations:

  • High cost of sodium carbonate
  • Not suitable for large-scale chemical production
  • Energy-intensive

An Overview of Other Manufacturing Technologies

NaOH production involves several manufacturing methods. Let's take a look at the other two main methods used by chlor-alkali chemical companies:

1. Electrolytic Procedure

This involves the electrolysis of brine (sodium chloride solution) to produce caustic soda. There are three types:

  • Diaphragm Electrolytic Cell: It uses a diaphragm to separate the anode and cathode compartments.
  • Mercury Electrolytic Cell: This method uses mercury as a catalyst.
  • Membrane Type: This is a more modern and efficient technique that uses a membrane to separate the anode and cathode compartments.


2. Chlorine Procedure

This involves the reaction of chlorine with other chemicals to produce Lye. There are three types:

  • HCl – Air Oxidation: This involves the oxidation of hydrogen chloride (HCl) with air.
  • HCl – Air – Cl2 (Oxychlorination Procedure): This procedure involves the reaction of HCl with air and chlorine.
  • HNO3 – NaCl – Air: In this method the reaction of nitric acid (HNO3) with sodium chloride (NaCl) and air.

Comparison of various sodium hydroxide-chemical units:


 Types

 Current Efficiency (%)

 Energy Consumption (kWh/kg NaOH)

 Sodium hydroxide Concentration (%)

 Yield (%)

 Diaphragm Electrolytic Cell

 85-90

 2.5-3.0

 30-35

 -

 Mercury Electrolytic Cell

 90-95

 2.0-2.5

 40-50

 -

 Membrane

 95-98

 1.8-2.2

 30-35

 -

 HCl – Air Oxidation 

 -

 1.5-2.0

 20-30

 80-90

 HCl – Air – Cl2  (Oxychlorination)

 -

 1.2-1.8

 30-40

 90-95

 HNO3 – NaCl – Air 

 -

 1.5-2.5

 20-30

 80-90

 Lime Soda 

 -

 0.5-1.0

 10-20

 70-80


The efficiency of sodium hydroxide large-scale routes can vary significantly, as shown in our comparison table for certain range values they fit in. Electrolytic technology, such as the diaphragm, mercury, and membrane cells, offer high current efficiencies ranging from 85% to 98%. However, they also consume more energy, with values between 1.8 and 3.0 kWh/kg NaOH. On the other hand, chlorine-based techniques like the HCl-air oxidation and oxychlorination have lower energy consumption (1.2-2.5 kWh/kg NaOH), but their yields range from 80% to 95%. The lime soda route stands out for its low energy consumption (0.5-1.0 kWh/kg NaOH), but its yield is relatively lower at 70-80%. Understanding these trade-offs is crucial for optimizing Lye production and minimizing environmental impact. However, actual values may vary depending on specific plant operations, equipment, and conditions.

Consumption Patterns and Uses 

Lye flakes and solutions are essential ingredients that empower a wide range of industries:  

  • Consumer chemicals and consumables  
  • Organic chemicals  
  • Textile industry  
  • Paper and pulp  
  • Alumina  
  • Soap and detergents  
  • Inorganic chemicals  
  • Dyes  


The lime soda technology is an older method, but it's still used for small-scale facilities. While it has its advantages, the high cost of sodium carbonate and the energy-intensive nature of the plant make it less suitable for large-scale production. Nevertheless, understanding this inorganic chemical synthesis can provide valuable insights into the handling and design methodology of Sodium Hydroxide.

Sulphuric Acid Manufacturing by Chamber Process: A Technical Review of the Process and Flow Sheet

Chamber Process Technique for Sulphuric Acid Production: Process Description and Flow Sheet Analysis
Chamber Process for Sulphuric Acid Production
Process Overview

The Chamber Process is a traditional method for producing sulphuric acid, which involves the oxidation of sulphur dioxide (SO2) to sulphur trioxide (SO3) in the presence of nitrogenous oxides and a catalyst. The SO3 is then absorbed into water to produce sulphuric acid.

Process Description

  1. Sulphur Burning: Sulphur is burned with air to produce SO2 gas.
  2. Gas Purification: The gas mixture is filtered to remove solid particles.
  3. Nitre Pots: The gas mixture is passed through nitre pots, where NO2 and NO are mixed.
  4. Glower's Tower: The gas mixture is passed through Glower's Tower, where it is cooled and scrubbed with dilute sulphuric acid.
  5. Lead Chambers: The acid scrub is passed through lead chambers, where it is further concentrated and purified.
  6. Gay-Lussac's Tower: The unabsorbed gases are passed through Gay-Lussac's Tower, where they are reacted with dilute HNO3 to produce NO2 and H2SO4.

Chemical Reactions

1. Sulphur Burning: 2S + O2 → 2SO2
2. Oxidation: 2SO2 + O2 → 2SO3
3. Absorption: SO3 + H2O → H2SO4
4. Nitre Pots: 2NO + SO2 + H2O → 2H2SO4 + NO + NO2
5. Glower's Tower: SO2 + NO2 + H2O → H2SO4 + NO
6. Gay-Lussac's Tower: HNO3 + NO.HSO4 → 2NO2 + H2SO4

Process Flow Sheet

The process flow sheet for the Chamber Process is as follows:

1. Sulphur Burning
2. Gas Purification
3. Nitre Pots
4. Glower's Tower
5. Lead Chambers
6. Gay-Lussac's Tower

Operating Conditions

The operating conditions for the Chamber Process are as follows:

- Temperature: 450-650°C (Glower's Tower), 70-80°C (Lead Chambers)
- Pressure: Atmospheric pressure
- Feed composition: Sulphur, air, water

Product Specifications

The product specifications for the Chamber Process are as follows:

- Sulphuric acid concentration: 50-60% H2SO4
- Purity: High purity sulphuric acid

Safety Considerations

The safety considerations for the Chamber Process are as follows:

- Handling of corrosive and toxic chemicals
- High temperature and pressure conditions
- Explosion and fire hazards

Environmental Considerations

The environmental considerations for the Chamber Process are as follows:

- Emissions of SO2 and NOx
- Disposal of waste acid and chemicals
- Water pollution from acid spills and leaks


Some general design and dimension guidelines for the chambers used in the Chamber Process for sulphuric acid production:


Lead Chambers

  • Shape: Rectangular or square shape with a flat roof and walls.
  • Material: Lead-lined or ceramic-lined to prevent corrosion.
  • Size: Typically 10-15 meters (33-49 feet) in length, 5-7 meters (16-23 feet) in width, and 6-8 meters (20-26 feet) in height.
  • Volume: Around 300-500 cubic meters (10,600-17,700 cubic feet).
  • Inlet and Outlet: Gas inlet at the top, acid outlet at the bottom.


Glower's Tower

  • Shape: Cylindrical or rectangular shape with a conical or flat roof.
  • Material: Brick, stone, or concrete with acid-resistant lining.
  • Size: Typically 10-20 meters (33-66 feet) in height, 2-5 meters (6-16 feet) in diameter.
  • Volume: Around 50-200 cubic meters (1,800-7,100 cubic feet).
  • Inlet and Outlet: Gas inlet at the bottom, acid outlet at the top.


Nitre Pots

  • Shape: Small, cylindrical or rectangular vessels.
  • Material: Ceramic, glass, or acid-resistant materials.
  • Size: Typically 1-5 meters (3-16 feet) in height, 0.5-2 meters (1.6-6.6 feet) in diameter.
  • Volume: Around 0.5-10 cubic meters (18-350 cubic feet).
  • Inlet and Outlet: Gas inlet and outlet at the top.


Gay-Lussac's Tower

  • Shape: Cylindrical or rectangular shape with a conical or flat roof.
  • Material: Brick, stone, or concrete with acid-resistant lining.
  • Size: Typically 10-20 meters (33-66 feet) in height, 2-5 meters (6-16 feet) in diameter.
  • Volume: Around 50-200 cubic meters (1,800-7,100 cubic feet).
  • Inlet and Outlet: Gas inlet at the bottom, acid outlet at the top.


Please note that these are general guidelines, and actual dimensions may vary depending on the specific plant design, capacity, and operating conditions. 

Sulphur Recovery: A Game-Changer for the Energy Industry


As the world grapples with the challenges of climate change, industrial pollution control has become a critical concern. One of the most significant pollutants in industrial processes is hydrogen sulfide (H2S), a toxic and flammable gas that can have devastating environmental and health impacts.

The Problem of Hydrogen Sulfide Pollution

Hydrogen sulfide is a byproduct of various industrial processes, including oil refining, natural gas processing, and chemical manufacturing. When released into the atmosphere, H2S can react with oxygen to form sulfur dioxide (SO2), a potent greenhouse gas that contributes to acid rain, air pollution, and climate change.

The Solution: Sulphur Recovery

One of the most effective ways to mitigate H2S pollution is through sulphur recovery, a process that converts H2S into elemental sulphur. This process not only reduces the environmental impact of H2S but also produces a valuable commodity that can be used in various industries, including agriculture, pharmaceuticals, and construction.

The Process Flow Diagram

Here is a simplified process flow diagram (PFD) that illustrates the sulphur recovery process:

                         

                                     

                                     

Process flow diagram of sulfur recovery from H2S gas
 From Toxic to Treasure: The Art of Sulphur Recovery

                                     

Process Conditions and Operation Procedure

The sulphur recovery process involves several unit operations, including scrubbing, oxidation, reduction, condensation, and storage. The process conditions and operation procedure are critical to ensuring safe and efficient operation.

Block diagram of sulfur recovery method
Block diagram of sulfur recovery process

Oxidation

2H2S + 3O2 ↔ 2SO2 + 2H2O   -247.89 Kcal

 Reduction

4H2S + 2SO2 ↔ S6 + 4H2O       -42.24 Kcal 

The above reactions are exothermic in nature. On the surface of the bauxite catalyst, the reaction is carried forward yielding about 70-80% conversion.

Benefits of Sulphur Recovery

The benefits of sulphur recovery are numerous:

- Reduced environmental impact: Sulphur recovery reduces the amount of H2S released into the atmosphere, minimizing the formation of SO2 and other pollutants.

- Valuable commodity: Elemental sulphur is a valuable commodity that can be used in various industries.

- Improved process safety: Sulphur recovery reduces the risk of H2S-related accidents and improves process safety.

- Compliance with regulations: Sulphur recovery helps industries comply with increasingly stringent environmental regulations.

Sulphur recovery is a critical process that can help industries reduce their environmental footprint, improve process safety, and comply with regulations. By investing in sulphur recovery technologies, industries can turn a pollutant into a valuable commodity, contributing to a more sustainable future.