Page 35 - Chemical and process design handbook
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Speight_Part 1_H  11/7/01  3:03 PM  Page 1.21









                                   HALOGENATION













                    Halogenation is almost always chlorination, for the difference in cost
                    between chlorine and the other halogens, particularly on a molar basis, is
                    quite substantial. In some cases, the presence of bromine (Br), iodine (I),
                    or fluorine (F) confers additional properties to warrant manufacture.
                      Chlorination proceeds (1) by addition to an unsaturated bond, (2) by
                    substitution for hydrogen, or (3) by replacement of another group such as
                    hydroxyl (–OH) or sulfonic (–SO H). Light catalyzes some chlorination
                                                  3
                    reactions, temperature has a profound effect, and polychlorination almost
                    always occurs to some degree. All halogenation reactions are strongly
                    exothermic.
                      In the chlorination process (Fig.1), chlorine and methane (fresh and recy-
                    cled) are charged in the ratio 0.6/1.0 to a reactor in which the temperature
                                            o
                    is maintained at 340 to 370 C. The reaction product contains chlorinated
                    hydrocarbons with unreacted methane, hydrogen chloride, chlorine, and
                    heavier chlorinated products. Secondary chlorination reactions take place
                    at ambient temperature in a light-catalyzed reactor that converts methylene
                    chloride to chloroform, and in a reactor that converts chloroform to carbon
                    tetrachloride. By changing reagent ratios, temperatures, and recycling
                    ratio, it is possible to vary the product mix somewhat to satisfy market
                    demands. Ignition is avoided by using narrow channels and high velocities
                    in the reactor. The chlorine conversion is total, and the methane conversion
                    around 65 percent.
                      Equipment for the commercial chlorination reactions is more difficult to
                    select, since the combination of halogen, oxygen, halogen acid, water, and
                    heat is particularly corrosive. Alloys such as Hastelloy and Durichlor resist
                    well and are often used, and glass, glass-enameled steel, and tantalum are
                    totally resistant but not always available. Anhydrous conditions permit
                    operation with steel or nickel alloys. With nonaqueous media, apparatus
                    constructed of iron and lined with plastics and/or lead and glazed tile is the
                    most suitable, though chemical stoneware, fused quartz, glass, or glass-lined
                    equipment can be used for either the whole plant or specific apparatus.


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