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              Acetylene                                                                                    69

























                     FIGURE 4 Butynediol–propargyl alcohol process. (1) Acetylene storage; (2) compressor; (3) recycle compressor;
                     (4) pressure reactor; (5) vent; (6) separator; (7) pumps; (8) stripping still; (8a) recycle formaldehyde; (9) formaldehyde
                     storage; (10) NaOH feed; (11) settling tank; (12) waste effluent; (13) butynediol storage; (14) recycle C 2 H 2 stream
                     for vinylpyrrolidone production. [Reprinted from Tedeschi, R. J. (1982). “Acetylene-Based Chemicals from Coal and
                     Other Natural Resources,” p. 105, courtesy of Dekker, New York.]



              at 90–130 C. The products resulting from this reaction,  in commercial practice. Below is shown the formation of
                      ◦
              butynediol and propargyl alcohol, are formed in approxi-  sodium acetylide in liquid ammonia and its reaction with
              mately 9:1 ratio, with butynediol the predominant product.  a vitamin E intermediate, geranylacetone (GA), to yield
              The reaction proceeds readily (exothermic) in total con-  the important terpene alkynol, dehydronerolidol (DHN):
              versions and selectivity of well over 90%.
                                                                                 Fe(NO 3 ) 3    1
                                  CuC 2 H                       1. Na + Liquid NH −−−→ NaNH 2 + H 2        (3)
                                                                                3
                    HCHO + C 2 H 2 −−−→ H C C CH 2 OH                             −33 C         2
                                                                                    ◦
                                         Propargyl alcohol
                                                                                NH 3
                                                                2. NaNH 2 + C 2 H 2 −→ NaC 2 H + NH 3
                      + HO CH 2 C C CH 2 OH
                                 Butynediol
                                                                                        CH 3
                Higher aldehydes or reactive methyl ketones fail to re-                 |
              act in the Reppe system. Even a reactive aldehyde such  3. (CH 3 ) 2 C CH (CH 2 ) 2  C CH (CH 2 ) 2
                                                                                       GA
              as acetaldehyde reacts very slowly and gives only an 18%
                                                                      COCH 3 + C 2 H(NH 3 )
                                   ◦
              conversion in 22 hr at 125 C. In contrast, formaldehyde
                                                                            
              reacts exothermically and is the basis for the continuous      1.NaC 2 H
                                                                              2.H 2 O−NH 4 Cl
              operation in current Reppe plants. Flow diagrams of the                                      (4)
              butynediol–propargyl alcohol process and the continuous
              process for the production of all Reppe products are shown             CH 3          CH 3
                                                                                      |             |
              in Figs. 4 and 5, respectively. The commercial importance  (CH 3 )  C CH (CH 2 )  C CH (CH 2 )  C C CH
                                                                     2             2             2
              of these acetylene-based products and their estimated pro-                            |
                                                                                                   OH
              duction volumes are discussed in Sections VI.A–VI.D.
                                                                                     DHN
                                                                                                           (5)
              C. Sodium and Lithium Acetylides
                                                                  This technology is used by Hoffmann–La Roche to pre-
                 in Liquid Ammonia
                                                                pare intermediates for the manufacture of vitamins A and
              Although alkali metal acetylides can be prepared in polar  E. The process has been in operation since the early 1950s.
              organic solvents by the reaction of acetylene with alkali  The use of lithium acetylide is preferred for more sensitive
              metal dispersions, the preparation and synthetic use of  or less reactive carbonyl compounds. Reactions (3)–(5)
              either sodium or lithium acetylides in liquid ammonia has  are run consecutively in liquid ammonia without isola-
              proved to be the preferred route both in the laboratory and  tion. The formation of the alkali metal acetylide (sodium,
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