Chlorine — Cl2
Copyright © 2014 CIEC at the University of York, York, UK
Chlorine, along with its important by-product, sodium hydroxide, is produced from the readily available starting material, rock salt (sodium chloride). It is well known for its use in sterilizing drinking water and in particular swimming pool water.
However, most chlorine is used in the chemical industry in the manufacture of other products. Sometimes chlorine is in the product molecule but on other occasions it is used to produce intermediates in the manufacture of products that do not contain chlorine and the element is recycled.
Uses of chlorine
The largest use is in the manufacture of poly(chloroethene), PVC. Other major polymers produced using chlorine include the polyurethanes . Although chlorine does not appear in the polyurethane molecule, chlorine is used to make the intermediates, the isocyanates. The oxygenates (Figure 1) are principally epoxypropane and propane-1,3-diol, which are used to make polyols. These, like the isocyanates, are used in turn to make polyurethanes.
1-Chloro-2,3-epoxypropane has many industrial uses, the most important being in the manufacture of the epoxy resins. Among the uses of the chloromethanes are the manufacture of silicones and poly(tetrafluoroethene), PTFE.
The solvents (including trichloroethene) are used in dry cleaning.
Chlorine is also used in the manufacture of many inorganic compounds, notably titanium dioxide and hydrogen chloride.
Most chlorine is produced on the site on which it is going to be used, for example, to make hydrochloric acid and the other compounds described above.
However, some chlorine needs to be transported for example, when it is to be used to purify water. For this, the chlorine is dried by passing it through concentrated sulfuric acid and then compressed and liquefied into cylinders, ready for transportation.
Annual production of chlorine
|World||56 million tonnes|
|Europe||16 million tonnes|
|North America||11 million tonnes|
Manufacture of chlorine
Most chlorine is manufactured by the electrolysis of sodium chloride solutions. The other main commercial product is sodium hydroxide. The primary raw material for this process is rock salt (sodium chloride), available worldwide usually in the form of underground deposits of high purity. It is pumped to the surface with high pressure water as a concentrated solution. This solution is often called brine.
A solution of sodium chloride contains Na+(aq) and Cl-(aq) ions and, from the dissociation of water, very low concentrations of H+(aq) and OH-(aq) ions. During the electrolysis of the solution, chlorine and hydrogen gases are produced
As the hydrogen ions are discharged, more water dissociates forming more hydrogen and hydroxide ions. This results in a gradual build-up of the concentrations of hydroxide ions around the cathode, thus producing a solution of sodium hydroxide. The essential requirement is to maintain an effective and economic means of separating the anode and cathode reactions so that the products, chlorine and caustic soda, will not react to form sodium hypochlorite. This separation has been achieved historically by the mercury amalgam and diaphragm processes. However, these are being phased out and most new plants use ion exchange membranes, which are the most environmentally and economically sound means of chlorine production
|(a) Cation exchange membrane cell|
|The cation exchange membrane does not allow any gas or negative ions to flow through it but it allows Na+ ions to move between the brine and caustic compartments.|
|(b) Mercury amalgam cell|
|In the flowing mercury cathode process sodium ions are discharged in the form of a mercury sodium amalgam and chloride ions are converted to chlorine. The amalgam flows to a totally separate compartment, the decomposer (denuder) in which it reacts with water to yield sodium hydroxide solution and hydrogen gas.|
|(c) Percolating diaphragm cell|
|A percolating diaphragm, usually of asbestos, allows a through flow of brine from anode to cathode. It separates the chlorine and hydrogen gas spaces. The migration of OH- ions from the cathode to the anode is prevented by the velocity of liquid flow against them.|
Table 1 The key features of the three electrolytic processes.
(a) Cation exchange membrane cell
The anodes are made of titanium coated with ruthenium dioxide. The cathodes are nickel, often with a coating to reduce energy consumption. The anode and cathode compartments are completely separated by an ion-permeable membrane (Figure 3). The membrane is permeable to cations, but not anions; it allows the passage of sodium ions but not chloride or hydroxide ions . Sodium ions pass through in hydrated form (Na.xH2O)+ so some water is transferred, but the membrane is impermeable to free water molecules.
The sodium hydroxide solution leaving the cell is at ca 30% (w/w) concentration. It is concentrated by evaporation using steam, under pressure, until the solution is ca 50% (w/w), the usual concentration needed for ease of transportation and storage.
The membrane (0.15-0.3 mm thick) is a co-polymer of tetrafluoroethene ((Unit 66) and a similar fluorinated monomer with anionic (carboxylate and sulfonate) groups.
(b) The mercury cell
Typical modern gas-tight, rubber-lined or PVC-lined steel cells (Figure 4) are used, which measure about 2 m x 15 m. They have a slightly sloping base over which flows a thin layer of mercury, acting as a cathode. The anodes are a series of titanium plates coated with a precious metal oxide layer, and positioned about 2 mm from the cathode. The cells typically operate in series of approximately 100.
Purified, saturated brine (25% (w/w) sodium chloride solution) at typically 333 K flows through the cell in the same direction as the mercury. This high salt concentration and the anode coating ensures the oxidation of chloride ions rather than that of water which would yield oxygen at the titanium anodes.
The chlorine is led off as shown in Figure 4.
At the mercury cathode, sodium ions are discharged in preference to hydrogen ions due to the high overvoltage of hydrogen. The sodium forms an amalgam with the mercury.
The amalgam contains approximately 0.3% (w/w)
sodium. It moves on to a decomposer cell situated alongside the mercury cell.
The exit brine, containing typically 15-20% (w/w) sodium chloride, is freed of chlorine by blowing air through it, or subjecting the solution to a vacuum. The solution is resaturated with sodium chloride and returned to the cell.
The decomposer cell (Figure 4) is made of steel and contains graphite blocks fixed in the flow of amalgam. Alternatively, the decomposer is a tower packed with graphite spheres. The decomposer acts as a short circuited cell. At the anode sites, sodium is oxidized and the ions pass into solution. At the cathode sites, hydrogen is discharged.
The mercury is returned to the electrolysis cell and the hydrogen passes out of the decomposer. A 50% (w/w) solution of sodium hydroxide is produced in the decomposer and most of it is sold in this form. Some is concentrated by evaporation to 75% (w/w) and then heat ed to 750-850 K to obtain solid sodium hydroxide.
(c) The percolating diaphragm cell
In the diaphragm cell (Figure 6), the anodes are titanium coated with a precious metal oxide and the cathodes are steel. There is a porous asbestos diaphragm to separate chlorine and hydrogen that are liberated during electrolysis.
The hydroxide ions formed in the cathode compartment, together with the sodium ions, produce a solution of sodium hydroxide.
The electrolyte level is maintained higher in the anode compartment so that the brine percolates through the diaphragm into the cathode section from where it flows out of the cell with the sodium hydroxide solution.
The chlorine formed on the anodes rises and is led away.
The cathode solution contains about 10-12% (w/w) sodium hydroxide and 15% (w/w) sodium chloride. This is evaporated to one-fifth of its original volume when the much less soluble sodium chloride crystallizes to leave a solution containing 50% (w/w) sodium hydroxide and less than 1% (w/w) sodium chloride.
Comparison of mercury, diaphragm and membrane cells
Factors such as capital and energy costs and environmental concerns all favour the membrane process (Table 2) but its development was not possible until work by Du Pont in the US in the early 1960s, and more recently in Japan, resulted in the production of the membrane material discussed above.
|construction costs||expensive||relatively cheap||cheaper than mercury cell|
|operation||toxic mercury must be removed from effluent||frequent asbestos diaphragm replacement||low maintenance costs|
|NaOH product concentration||high purity 50% – as required||less pure 12% -needs concentration||high purity 30% – needs concentration|
|typical cell energy consumption (kw hours per tonne of chlorine)||3 360||2 720||2 500|
|steam consumption per caustic evaporation||nil||high||medium|
|purity of brine||important||important||very important|
Table 2 Comparison of the three cells.
The chlorine-alkali balance
For every tonne of chlorine, 2.25 tonnes of 50% sodium hydroxide and 340 m3 of hydrogen (under normal conditions) are also produced. It is necessary, therefore, to ensure that all these products can be sold.
A large research programme in Germany, led by Bayer, is looking at ways of reducing the amount of electrical power used which, at present, contributes half the cost of chlorine production and also produces large amounts of carbon dioxide from the power stations. when hydrogen ions migrate to the cathode, hydrogen is liberated. However, if oxygen is pumped into this part of the cell, the hydrogen reacts to form water and the voltage needed for the electrolysis process is reduced by a third. This, in turn, reduces the power costs and thus the amount of carbon dioxide formed in the power station by a third. A disadvantage is that the hydrogen is no longer available as an important and valuable by-product (Unit 32), together with oxygen being consumed as an additional raw material.
There are technical difficulties in applying this process (known as an oxygen-depolarised cathode, ODC) to the electrolysis of brine. However it is easier to apply to the electrolysis of aqueous hydrochloric acid in order to generate chlorine. A large commercial plant has been constructed in China, using ODC technology.