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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.]