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              Acetylene                                                                                    67

              TABLE IX Acetylene from Natural Gas, Petroleum, and Coal Sources a
               Typical process       Principal feedstock          Technology              Typical companies
              Electric arc    Methane, gas oils            Arc or plasma           Huels, Du Pont
              Sachsse         Methane, natural gas mixtures  Partial combustion (one stage)  BASF, Dow, Monsanto
              SBA             Methane, natural gas mixtures (first stage);  Partial combustion  SBA, M. W. Kellogg
                               naphthas, heavier feedstocks  (one and two stage)
                               (second stage)
              Wulff           Natural gas, naphthas, heavier feedstocks  Regenerative furnace pyrolysis  Union Carbide, Wulff
                                                             (four cycles)
              Montecatini     Natural gas, naphthas        Partial combustion under pressure  Montecatini, Diamond Alkali
              By-product acetylene  Ethane, hydrocarbons, naphthas, oil  Steam cracking  Major oil and chemical companies
                                                                                     (EXXON, Shell, Dow, Union Carbide)
              Calcium carbide  Limestone (CaCO 3 ) and coke  CaC 2 from C + CaCO 3 ;C 2 H 2  AIRCO-BOC, Union Carbide
                                                             from CaC 2 + H 2 O
              AVCO            Coal and hydrogen            Hydrogen plasma         AVCO (pilot and demonstration plants)
                a  Reprinted from Tedeschi, R. J. (1982). “Acetylene-Based Chemicals from Coal and Other Natural Resources,” p. 11, courtesy of Dekker, New
              York.

              subjected to an intense energy source and thereby heated  stage) and an oxygen–steam off-gas mixture to provide a
              to 1200–1500 K. By the use of very short residence times  moist flame zone in the lower end of the burner to crack
              (0.01–0.001 sec) and quick quenching of the cracked gas  naphtha to acetylene. About two-thirds of the hydrocar-
              to 550 K, acetylene and the starting feedstock can be re-  bon feed is burned in the reactor to provide the thermal
              covered. The recovery and purification of petrochemical  energy needed to crack the remaining feed to acetylene.
              acetylene is a lengthy operation compared with the simple  The AVCO coal–hdrogen plasma process has not yet
              calcium carbide process, which readily yields high-purity  been scaled up to commercial production. However in
              acetylene.                                        a joint AVCO–DOE project (1980) at Wilmington, MA,
                The petrochemical acetylene processes most likely to  a coal-fed hydrogen–plasma reactor capable of produc-
              be practiced today are the partial oxidation types. Promi-  ing 2 million pounds/year of acetylene was successfully
              nent among these are Sachsse, SBA, and Montecatini pro-  demonstrated, The pilot unit gave an acetylene yield of
              cesses. The SBA and Montecatini processes utilize either  35%basedoncoalwithlowelectricalusage.AVCOclaims
              natural gas or naphtha feedstocks, while the Sachsse pro-
              cess is designed primarily for natural gas or methane, but
              can be modified for naphtha. However, Sachsse technol-
              ogy has been widely practiced both in the United States
              and in Europe, showing it to be reliable and trouble free.
                In contrast, the electric are process is more sensitive
              to process variables, which can lead to the formation of
              large amounts of by-product carbon. The Wulff process
              was once widely used in Europe, South America, Japan,
              and the United States. By controlling the feedstock and
              operating conditions, the four-cycle regenerative process
              could be made to deliver mainly acetylene or ethylene,
              making it more versatile than other petrochemical pro-
              cesses. The fact that the Wulff process is now seldom used
              may be due to the high efficiency of stream cracking of
              alkanes to form ethylene and propylene at lower energy
              usage, thereby making the Wulff mixed product stream
              less attractive.                                  FIGURE 2 BASF (Sachsse) burner. (1) Oxygen; (2) inert gas
                A process diagram of the BASF Sachsse (burner) reac-  (safety purge); (3) methane or naphtha feed; (4) neck and mix-
                                                                ing chamber; (5) auxiliary oxygen; (6) burner block; (7) reac-
              torisshowninFig.2.Normally,withnaturalgastheburner
                                                                tion chamber; (8) water quench. [Reprinted from Tedeschi, R. J.
              is a one-stage reactor. However, it can be modified to use  (1982). “Acetylene-Based Chemicals from Coal and Other Natural
              naphtha by extension of the combustion chamber (second  Resources,” p. 21, courtesy of Dekker, New York.]
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