Page 64 - Chemical and process design handbook
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Speight_Part II_A  11/7/01  3:16 PM  Page 2.5







                                               ACETALDEHYDE                        2.5

                            Reactor   Reactor  Still    Gas separator  Still
                                                                            Waste gas
                                   Air
                                                                            Acetaldehyde







                    Ethylene
                                                                            Steam
                    Air
                    FIGURE 2  Acetaldehyde manufacture by the two-stage process.

                    slight pressure. The water evaporated during the reaction absorbs the heat
                    evolved, and makeup water is fed as necessary to maintain the desired cat-
                    alyst concentration. The gases are water scrubbed, and the resulting
                    acetaldehyde solution is fed to a distillation column. The tail gas from the
                    scrubber is recycled to the reactor. Inert materials are eliminated from
                    the recycle gas in a bleed stream that flows to an auxiliary reactor for
                    additional ethylene conversion.
                      In the two-stage process (Fig. 2), ethylene is almost completely oxi-
                    dized by air to acetaldehyde in one pass in a tubular plug-flow reactor
                                                                        o
                    made of titanium. The reaction is conducted at 125 to 130 C and 150 psi
                    (1.03 MPa) with the palladium and cupric chloride catalysts. Acetaldehyde
                    produced in the first reactor is removed from the reaction loop by adiabatic
                    flashing in a tower. The flash step also removes the heat of reaction. The
                    catalyst solution is recycled from the flash-tower base to the second stage
                    (or oxidation reactor), where the cuprous salt is oxidized to the cupric state
                    with air. The high-pressure off-gas from the oxidation reactor, mostly
                    nitrogen, is separated from the liquid catalyst solution and scrubbed to
                    remove acetaldehyde before venting. A small portion of the catalyst stream
                    is heated in the catalyst regenerator to destroy any undesirable copper
                    oxalate. The flasher overhead is fed to a distillation system where water is
                    removed for recycle to the reactor system and organic impurities, includ-
                    ing chlorinated aldehydes, are separated from the purified acetaldehyde
                    product. Synthesis techniques purported to reduce the quantity of chlori-
                    nated by-products generated have been patented.
                      Acetaldehyde was first used extensively during World War I as a start-
                    ing material for making acetone (CH COCH ) from acetic acid
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