Carbonatation is a chemical reaction in which calcium hydroxide reacts with carbon dioxide and forms insoluble calcium carbonate: The process of forming a carbonate is sometimes referred to as "carbonation", although this term usually refers to the process of dissolving carbon dioxide in water.
Concrete
Carbonatation is a slow process that occurs in concrete where lime2 in the cement reacts with carbon dioxide from the air and forms calcium carbonate. The water in the pores of Portland cement concrete is normally alkaline with a pH in the range of 12.5 to 13.5. This highly alkaline environment is one in which the steel rebar is passivated and is protected from corrosion. According to the Pourbaix diagram for iron, the metal is passive when the pH is above 9.5. The carbon dioxide in the air reacts with the alkali in the cement and makes the pore water more acidic, thus lowering the pH. Carbon dioxide will start to carbonatate the cement in the concrete from the moment the object is made. This carbonatation process will start at the surface, then slowly move deeper and deeper into the concrete. The rate of carbonatation is dependent on the relative humidity of the concrete - a 50% relative humidity being optimal. If the object is cracked, the carbon dioxide in the air will be better able to penetrate into the concrete. Eventually this may lead to corrosion of the rebar and structural damage or failure.
Sugar refining
The carbonatation process is used in the production of sugar from sugar beets. It involves the introduction of limewater and carbon dioxide enriched gas into the "raw juice" to form calcium carbonate and precipitate impurities that are then removed. The whole process takes place in "carbonatation tanks" and processing time varies from 20 minutes to an hour. Carbonatation involves the following effects:
The target is a large particle that naturally settles rapidly to leave a clear juice. The juice at the end is approximately 15 °Bx and 90% sucrose. The pH of the thin juice produced is a balance between removing as much calcium from the solution and the expected pH drop across later processing. If the juice goes acidic in the crystallisation stages then sucrose rapidly breaks down to glucose and fructose; not only do glucose and fructose affect crystallisation but they are molassagenic taking equivalent amounts of sucrose on to the molasses stage. The carbon dioxide gas bubbled through the mixture forms calcium carbonate. The non-sugar solids are incorporated into the calcium carbonate particles and removed by natural sedimentation in tanks. There are several systems of carbonatation, named from the companies that first developed them. They differ in how the lime is introduced, the temperature and duration of each stage, and the separation of the solids from the liquid.
Dorr - a continuous process using two tanks with recycling to build upparticle size for natural flocculation. The recycling ratio is about 7:1. The particles are separated under gravity in a thickening stage in a vessel called a clarifier. The clear juice is then gassed further in another tank and filtered. The concentrated mud from the clarifier is filtered and/or pressed to recover more liquid. The Dorr process is low in maintenance and man-power but susceptible to filtration problems when frost damaged beets are processed. It is favoured in the UK and the USA.
DDS -- multistage process involving pre-liming where the pH of the juice is gradually increased to start precipitation of proteins, followed by addition of further lime and CO2 gas. The particles are removed at each stage by filtration.
RT - another multistage process with a pre-liming stage. Particles also removed by filtration.
Both DDS and RT processes are favoured by European factories. The carbonatation system is generally matched to the diffusion scheme; juice from RT diffusers being processed by the RT carbonatation. The clear juice from carbonatation is generally known as "thin juice". it may undergo pH adjustment with soda ash and addition of sulfur prior to the next stage which is concentration by multiple effect evaporation.
