Page 55 - Chemical and process design handbook
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Speight_Part 1_P  11/7/01  3:02 PM  Page 1.41










                                 POLYMERIZATION












                    Polymerization is a process in which similar molecules (usually olefins)
                    are linked to form a high-molecular-weight product; such as the formation
                    of polyethylene from ethylene

                                      nCH CH → H–( CH CH ) –H
                                          2   2           2   2 n
                    The molecular weight of the polyethylene can range from a few thousand
                    to several hundred thousand.
                      Polymerization of the monomer in bulk may be carried out in the liquid
                    or vapor state. The monomers and activator are mixed in a reactor and heated
                    or cooled as needed. As most polymerization reactions are exothermic, pro-
                    vision must be made to remove the excess heat. In some cases, the polymers
                    are soluble in their liquid monomers, causing the viscosity of the solution to
                    increase greatly. In other cases, the polymer is not soluble in the monomer
                    and it precipitates out after a small amount of polymerization occurs.
                      In the petroleum industry, the term polymerization takes on a different
                    meaning since the polymerization processes convert by-product hydrocar-
                    bon gases produced in cracking into liquid hydrocarbons suitable (of lim-
                    ited or specific molecular weight) for use as high-octane motor and
                    aviation fuels and for petrochemicals.
                      To combine olefinic gases by polymerization to form heavier fractions,
                    the combining fractions must be unsaturated. Hydrocarbon gases, particu-
                    larly olefins, from cracking reactors are the major feedstock of polymer-
                    ization.

                                 (CH ) C=CH → (CH ) CH C(CH )=CH
                                     3 2     2        3 3  2     3     2
                                     (CH ) CH C(CH )=CH → C H
                                        3 3   2     3    2      12  24
                      Vapor-phase cracking produces considerable quantities of unsaturated
                    gases suitable as feedstocks for polymerization units.
                      Catalytic polymerization is practical on both large and small scales and
                    is adaptable to combination with reforming to increase the quality of the



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