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SCIENCE/TECHNOLOGY
Alternative Fuels to Petroleum Gain Increased Attention
Oxygenates are most promising of alternative fuel candidates, and Fischer-Tropsch process gaining new prominence
Joseph Haggin, C&EN Chicago
With the idea of alternative fuels development regaining currency, a substantial change in viewpoint about how and why fuels are produced may be taking place. Economics remains a principal consideration. But national security, the inexorable decline in petroleum reserves and rise of other hydrocarbon sources, and the issue of environmental protection have emerged as being of more than academic importance in the search for alternatives to petroleum. Problems of developing appropriate fuels for new kinds of vehicles and new fuels for old kinds also exist.
Oxygenates, either neat or as additives to fuels, appear to be the principal alternative fuel candidates beyond the petroleum refinery, d chemistry, on the back burner following the oil price drops of a few years ago, may be restored to some prominence as a means both for new fuels and for organic chemicals.
Promoting the idea of alternatives to petroleum, the U.S. Alternative Fuels Act of 1988 responded to the potential threats from more than 95% of U.S. fuel requirements being satisfied from petroleum and from nearly half of U.S. petroleum being imported. More recently, development of alternative fuels—methanol for powering automobiles—was advocated by President Bush. Further underscoring interest in this area is a Department of Energy study on
alternative fuels scheduled to be issued by the end of this year.
The panic that followed the Arab oil embargo of 1974 produced little in the way of alternative fuels, but it did highlight some of the problems of producing them. Probably the greatest impediment to launching a new era of alternative fuels is the complete dependence of the transport fuels industry on petroleum as a feedstock. The dominance of petroleum has skewed the economics of production in its favor.
Nevertheless, over the past few years, significant developments in catalytic chemistry have suggested that alternative fuels from sources other than petroleum are possible and practical. Some of them are even now competing with petroleum-based fuels in some markets.
The results of the forthcoming DOE study are already known, in large part, from preliminary status reports. One authoritative view of the study's conclusions is that of G. Alex Mills, senior scientist in the
Center for Catalytic Science & Technology at the University of Delaware. He suggests the report will likely show that methanol may become a serious contender as motor fuel and that a number of other alcohols and ethers will also enter the picture. These oxygenates can be produced with high-octane properties, can be produced from various hydrocarbon sources other than petroleum, and frequently can offer environmental advantages.
The oxygenates, says Mills, are the best alternative fuels so far. Contrary to some opinions, he believes that the problems of changeover from gasoline to oxygenates are foreseeable and soluble, although there would be problems, and any change would cost something and be irritating to many people. Methanol would probably be the alternative fuel most difficult to accommodate. Higher alcohols and ethers would be easier. Alcohol fuels would require higher engine compression ratios, and fuel tanks would need to
Current alternative fuels come from synthesis gas
fuels & chemicals
Ci-Ce alcohols *
CH4 «
Isoparaffins <4
[ Gasoline
Diesel fuel +
Chemicals
Gasoline Diesel fuel
Benzene/toluene/xylene
¥ Methyl te/f-butyl ether
Turbine fuel Auto fuel additives
Fuel cell feed • Ethanol * Basic auto fuel
: Near-commercial process
All the products are derived from the catalytic conversion of syngas (carbon monoxide and hydrogen), either directly or via hydrogen.
August 14, 1989 C&EN 25
Science/Technology
Metal-catalyzed F-T reactions generate many products
On the basis of the latest research from South Africa's SASOL operation, the following mechanism has been suggested for the classical Fischer-Tropsch chemistry:
CH3OH -*
RC-C=0 * \ x H
H H RC-C-OH
H H H
RC-COOH H
be larger to accommodate the lower energy density of alcohol fuels.
It is expected that oxygenates would assist in suppressing vehicle pollutants in air. The effects are somewhat seasonal, with higher values in some pollutants being experienced in cold weather. In a trial program, Colorado required that motor fuels containing 1.5% oxygen be used during the past winter. This was done by addition of ethanol and methyl-fert-butyl ether (MTBE). The level of carbon monoxide in the air dropped, and the program is being continued in the coming winter with required oxygen content being raised to 2%.
Combustion of methanol is claimed to produce undesirable quantities of aldehydes in vehicle engine exhausts. However, it has also been found that the aldehyde concentration can be diminished to acceptable levels by exhaust converters. Mills believes that the problem can be overcome without very much additional development. The benefits of reduced carbon monoxide and nitrogen oxide concentrations with alcohol fuels are well established.
Of all the oxygenates, MTBE is inherently attractive for technical reasons. It has a low vapor pressure, can be blended with other fuels without phase separation, and has desirable octane characteristics. Methyl tert-butyl ether has been used in motor fuels for about 15 years, beginning in Europe but growing rapidly in recent years in the U.S. Present U.S. production of MTBE exceeds 3 million gal per day.
If oxygenates achieve recognition as vehicle fuels, the biggest contributor will probably be methanol, production of which is mostly from synthesis gas derived from methane. The process is catalytic, and currenty a great deal of research is in progress to develop a catalyst and process for the direct conversion of methane to either methanol or to ethylene, which could subsequently be hydrated to methanol. The production economics of methanol are peculiar in that imported methanol prices have been dropping while domestic prices have risen. This is attributed to the very low natural gas prices that a num
ber of foreign manufacturers take advantage of in producing methanol.
The higher alcohols offer some potential as motor fuels, but their successful production awaits better catalysts. Development of such catalysts has mostly been discontinued because of the falling oil prices, but recently interest has been renewed, largely because of some significant developments in catalyst design.
Most of the catalytic development is focused on new active copper-containing catalysts, which can be promoted with rubidium, cesium, and potassium. Potassium is used because of its lower cost, and the catalysts can be made highly selective to methanol over higher alcohols. Higher alcohols can be produced at temperatures below 300 °C, using copper/zinc oxide/alumina catalysts promoted with potassium. Although it is currently cheaper to make isobutyl alcohol from by-product isobutylene, it can be synthesized from syngas with alkali-promoted zinc oxide catalysts at temperatures above 400 °C.
Isobutyl alcohol is of particular interest because of its high octane rating, which makes it desirable as a gasoline blending agent. It can also be catalytically reacted with methanol to produce MTBE. In any case, consumption of MTBE is growing steadily whatever its source. There seems to be little doubt that eventually syngas will be the principal source.
It is the potential value of syngas as a source of motor fuels and chemicals that is expected to make it the first major challenger of petroleum. Syngas can be made from any carbon source, but the current choice is methane. Discoveries of major natural gas resources offshore in New Zealand, Australia, South Africa, and the Gulf of Siam, as well as smaller finds offshore in China and the giant onshore gas reserves in Saudi Arabia, have considerably altered the perception of motor fuel feedstocks worldwide.
Any challenge to petroleum by syngas will be the result of successful exploitation of catalytic Q chemistry, with production of methanol using the active Cu/ZnO/alumina catalysts being the classic example. The structure of these catalysts has
recently been determined to involve copper crystallites dissolved in zinc oxide crystallites in solid solution. The solution forms the active phase suspended in amorphous alumina.
The mechanism is still under debate. Some favor initial union of carbon monoxide from the syngas with the catalyst by adsorption of either the carbon or the oxygen. A third possibility is that carbon dioxide is formed first, before the reaction can proceed.
Carbon monoxide hydrogénation is highly exothermic. This limits per-pass conversion and usually requires high recycle of the reactant feedgas. It also requires separation of un-
26 August 14, 1989 C&EN
reacted feed from some products or staging of the process with intermittent heat removal. For these reasons, methanol winds up as an energy consumer.
To minimize or eliminate some of these problems, a slurry catalytic process is under development to permit better temperature control and greater conversion per pass. The highly proprietary process is rumored to be nearly ready for commercialization. In the long term, the methanol process may involve syngas generation, methanol synthesis, and electricity generation in a combined cycle. Union Carbide has proposed such an integrated process in connection with its new methanol process.
Higher alcohols and ethers are formed in methanol synthesis with alkali promoters, with appreciable amounts of isobutyl alcohol being produced by the copper catalysts used for methanol. The effects of the usual promoter, potassium, are attributed to a basic character that favors formaldehyde condensation. Another octane enhancer is terf-amyl-methyl ether (TAME), which is made from methanol and isoamylene.
Other than with the zinc oxide-based catalysts, methanol can be synthesized using alkali alkoxide catalysts. However, the economics are currently unfavorable because of separation problems by this route. Of great theoretical interest are transition-metal complexes used in homogeneous systems. Metallic complex catalysts may also be used for the reduction of the carbon oxides in the manufacture of hydrocarbons.
Metal clusters have been of interest catalytically for a long time. The clusters contain more than one transition metal. An example of this type of chemistry is the production of ethylene glycol from syngas via rhodium catalysis. Though clusters have yet to be widely accepted as proficient industrial catalysts, they are being thoroughly investigated.
The Fischer-Tropsch (F-T) reactions and the water-gas shift reaction are the basis of today's Q chemistry. These reactions were developed many years ago, and, with a few exceptions, have been supplanted with chemical technology based on petroleum. However, a new era
for this kind of chemistry may be in the making for the manufacture of hydrocarbon fuels.
F-T reactions are catalyzed by iron, cobalt, nickel, and ruthenium. Iron is less active than cobalt in the hydrogénation of carbon monoxide and produces more olefins and alcohols. Ruthenium produces higher hydrocarbons but is very expensive. Only iron displays any activity in the water-gas shift reaction, where carbon monoxide and water react to form additional hydrogen. The water-gas shift reaction is essential in controlling the composition of syngas as well as for being a source of hydrogen.
Classical F-T reactions have not been selective ones, and much of the recent development in F-T chemistry has been aimed at improving catalyst selectivity. In addition to the above-mentioned catalysts, nitrides, carbides, and carbo-nitrides have been shown to be potential F-T catalysts. These are of particular interest because of their resistance to coking and oxidation. Raney iron-manganese is another active F-T catalyst. The problems of sulfur poisoning in F-T chemistry may be partially overcome by using deliberately sulfided bimetallic clusters and alloy catalysts, such as amorphous nickel/zirconium.
A modern classic chemistry for the production of hydrocarbon fuels is the Mobil MTG (methanol-to-gasoline) process. This process produces high-octane gasoline from methane via methanol intermediates. The hydrocarbons are formed from the methanol using ZSM-5 zeolites. The first commercial plant, built in New Zealand, utilized fixed beds, but Mobil and a West German partner also have successfully piloted a fluid-bed process. The original MTG process manufactured the methanol as a feedstock for the production of hydrocarbons in two steps, but there have been several attempts to integrate the syngas/ methanol/hydrocarbon production in a single process train.
The improvement of syngas conversion depends on the development of catalysts that are more selective, more active, and, for economic reasons, of less noble character. Methane conversion to syngas is effi
cient, and there has been considerable interest in syngas generation from such sources as coal and shales. Gasification of coal is still plagued by high syngas costs. Suitable gasification catalysts are under development, notably at Lawrence Berkeley Laboratory. However, a long-held desire has been the direct conversion of methane without the necessity of intermediate syngas.
Short of direct conversion of methane, there is a growing conviction among research chemists that the direct conversion of syngas to fuels, without the necessity of intermediate methanol, is a closer goal. In this regard, zeolites offer promise as support for conventional catalysts in F-T syntheses. Improvements in F-T chemistry at South Africa's SASOL coal conversion operation produced a slurry reactor that uses finely divided catalyst suspended in oil, which produces a higher conversion per pass than conventional reactors. Another variation in F-T chemistry is the upgrading of F-T hydrocarbons with ZSM-5 catalysts. Isoparaffins can be produced in a variation of the F-T synthesis, which operates under more severe conditions and uses a thoria catalyst. The best catalysts are rather expensive rare metals.
Economic studies at SASOL indicate that the cost of fuels from syngas via F-T chemistry is dominated by syngas production. Some 58% of the cost of production at SASOL is devoted to syngas from coal gasification. The F-T synthesis itself consumes 18%, product separation 12%, and further refining 10%. This is, obviously, the Achilles' heel of Ci chemistry from coal.
Educated speculation by Mills and others indicate that in the near term the R&D effort in alternative fuels should be channeled to several specific areas. Integration of the F-T/ MTG process, integration of the MTG process itself by developing a multifunctional catalyst to permit the use of a single reactor for both methanol production and conversion to hydrocarbons, and direct conversion of methane to Q chemicals are some of the projects of immediate concern. Longer term, the potential of metal complexes and clusters and biocatalysts should be exploited. D
August 14, 1989 C&EN 27