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Fischer-Tropsch synthesi

A number of chemical products are derived from Sasol s synthetic fuel operations based on the Fischer-Tropsch synthesis including paraffin waxes from the Arge process and several polar and nonpolar hydrocarbon mixtures from the Synthol process. Products suitable for use as hot melt adhesives, PVC lubricants, cormgated cardboard coating emulsions, and poHshes have been developed from Arge waxes. Wax blends containing medium and hard wax fractions are useful for making candles, and over 20,000 t/yr of wax are sold for this appHcation. [Pg.168]

The second reaction is called the Fischer-Tropsch synthesis of hydrocarbons. Depending on the conditions and catalysts, a wide range of hydrocarbons from very light materials up to heavy waxes can be produced. Catalysts for the Fischer-Tropsch reaction iaclude iron, cobalt, nickel, and mthenium. Reaction temperatures range from about 150 to 350°C reaction pressures range from 0.1 to tens of MPa (1 to several hundred atm) (77). The Fischer-Tropsch process was developed iadustriaHy under the designation of the Synthol process by the M. W. Kellogg Co. from 1940 to 1960 (83). [Pg.416]

Heat Release and Reactor Stability. Highly exothermic reactions, such as with phthaHc anhydride manufacture or Fischer-Tropsch synthesis, compounded with the low thermal conductivity of catalyst peUets, make fixed-bed reactors vulnerable to temperature excursions and mnaways. The larger fixed-bed reactors are more difficult to control and thus may limit the reactions to jacketed bundles of tubes with diameters under - 5 cm. The concerns may even be sufficiently large to favor the more complex but back-mixed slurry reactors. [Pg.519]

Fischer-Tropsch Waxes. Polymethylene wax [8002-74-2] production is based on the Fischer-Tropsch synthesis, which is basicaHy the polymerisation of carbon monoxide under high pressure and over special catalysts to produce hydrocarbons (see Fuels, synthetic-liquid fuels). [Pg.317]

The first demonstration of catalytic conversion of synthesis gas to hydrocarbons was accompHshed ia 1902 usiag a nickel catalyst (42). The fundamental research and process development on the catalytic reduction of carbon monoxide was carried out by Fischer, Tropsch, and Pichler (43). Whereas the chemistry of the Fischer-Tropsch synthesis is complex, generalized stoichiometric relationships are often used to represent the fundamental aspects ... [Pg.289]

Fig. 11. Optimum pressure/temperature ranges for Fischer-Tropsch synthesis processes showiag the various catalysts ia parentheses. To convert MPa to... Fig. 11. Optimum pressure/temperature ranges for Fischer-Tropsch synthesis processes showiag the various catalysts ia parentheses. To convert MPa to...
General References Dry, The Fischer-Tropsch Synthesis, Catalysis Sci-... [Pg.2375]

Fischer-Tropsch Synthesis The best-known technology for producing hydrocarbons from synthesis gas is the Fischer-Tropsch synthesis. This technology was first demonstrated in Germany in 1902 by Sabatier and Senderens when they hydrogenated carbon monoxide (CO) to methane, using a nickel catalyst. In 1926 Fischer and Tropsch were awarded a patent for the discovery of a catalytic technique to convert synthesis gas to liquid hydrocarbons similar to petroleum. [Pg.2376]

Other reactions may also occur during the Fischer-Tropsch synthesis, depending on the catalyst employed and the conditions used Water-gas shift ... [Pg.2376]

The indirect liquefaction basehne design is for a plant of similar size. Unhke the direct hquefaction basehne, the design focuses on producing refined transportation fuels by use of Sheh gasification technology. Table 27-17 shows that the crude oil equivalent price is approximately 216/m ( 34/bbl). Additional technological advances in the production of synthesis gas, the Fischer-Tropsch synthesis, and product refining have the potential to reduce the cost to 171/m ( 27/bbl) (1993 US dollars), as shown in the second column of Table 27-17. [Pg.2378]

As an example of the chemical signihcance of the process technology, the products of die Fischer-Tropsch synthesis, in which a signihcant amount of gas phase polymerization occurs vary markedly from hxed bed operation to the fluidized bed. The hxed bed product contains a higher proportion of straight chain hydrocarbons, and the huidized bed produces a larger proportion of branched chain compounds. [Pg.145]

J.R. Anderson and M. Boudait (eds), Catalysis, Science and Technology, Several volumes. Springer Verlag, Berlin TP156 C35 C375 Volume 1 M.E. Diy, The Fischer-Tropsch synthesis, pp. 160-255. [Pg.145]

Hot (230-240°F) potassium carbonate treating was patented in Germany in 1904 and perfected into modem commercial requirements by the U.S. Bureau of Mines. The U.S. Bureau of Mines was working on Fischer-Tropsch synthesis gas at the time. Potassium carbonate treating requires high partial pressures of CO2. It therefore cannot successfully treat gas containing only H2S. ... [Pg.192]

Masters, Adv. Organometallic Chem. 17, 61-103 (1979). R. B. Anderson, The Fischer-Tropsch Synthesis, Academic Press, London, 1984, 320 pp. [Pg.309]

Diy, M. E. (1990). Fischer-Tropsch Synthesis over Iron Catalysts, Spring 1990 A.I.Ch.E. Meeting, Orlando, Florida. March 18-22, 1990. [Pg.834]

During the late seventies and early eighties, when oil prices rose after the 1973 war, extensive research was done to change coal to liquid hydrocarbons. However, coal-derived hydrocarbons were more expensive than crude oils. Another way to use coal is through gasification to a fuel gas mixture of CO and H2 (medium Btu gas). This gas mixture could be used as a fuel or as a synthesis gas mixture for the production of fuels and chemicals via a Fischer Tropsch synthesis route. This process is... [Pg.23]

Synthesis gas consists of a nonhydrocarhon mixture (H2,CO) ohtain-ahle from more than one source. It is included in this chapter and is further noted in Chapter 5 in relation to methane as a major feedstock for this mixture. This chapter discusses the use of synthesis gas obtained from coal gasification and from different petroleum sources for producing gaseous as well as liquid hydrocarbons (Fischer Tropsch synthesis). [Pg.111]

Hydrocarbons from Synthesis Gas (Fischer Tropsch Synthesis, FTS)... [Pg.123]

Fischer Tropsch synthesis is catalyzed by a variety of transition metals such as iron, nickel, and cobalt. Iron is the preferred catalyst due to its higher activity and lower cost. Nickel produces large amounts of methane, while cobalt has a lower reaction rate and lower selectivity than iron. By comparing cobalt and iron catalysts, it was found that cobalt promotes more middle-distillate products. In FTS, cobalt produces... [Pg.124]

Dry, M. E., The Fischer Tropsch Synthesis, in Catalysis Science and Technology, edited hy J. R. Anderson and M. Boudart, Springer Verlag, 1981. [Pg.134]

Rober, M. Fischer-Tropsch Synthesis in Catalysis in Cj Chemistry, edited by W. Keim, D. Reidel Publishing Company, Dordrecht, The Netherlands, 1983, pp. 41-87. [Pg.134]

Many chemicals are produced from synthesis gas. This is a consequence of the high reactivity associated with hydrogen and carhon monoxide gases, the two constituents of synthesis gas. The reactivity of this mixture was demonstrated during World War II, when it was used to produce alternative hydrocarbon fuels using Fischer Tropsch technology. The synthesis gas mixture was produced then hy gasifying coal. Fischer Tropsch synthesis of hydrocarbons is discussed in Chapter 4. [Pg.143]


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See also in sourсe #XX -- [ Pg.3 , Pg.3 , Pg.4 , Pg.6 , Pg.6 , Pg.6 , Pg.6 , Pg.6 , Pg.6 , Pg.6 , Pg.9 , Pg.14 , Pg.14 , Pg.14 , Pg.14 ]




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Amorphous catalyst Fischer-Tropsch synthesis

Biomass Fischer-Tropsch synthesis

Carbidic intermediates Fischer-Tropsch synthesis

Carbon Fischer-Tropsch synthesis

Carbon monoxide Fischer-Tropsch synthesis

Chain growth, Fischer-Tropsch synthesis

Cobalt catalysts Fischer-Tropsch synthesis rates, metal

Cobalt-based Fischer-Tropsch synthesis

Cobalt-based Fischer-Tropsch synthesis carbon

Cobalt-based Fischer-Tropsch synthesis hydrogenation

Cobalt-based catalyst, fischer-Tropsch synthesis

FTS (See Fischer Tropsch synthesis

Fischer Tropsch synthesis catalysts

Fischer Tropsch synthesis mechanism

Fischer Tropsch synthesis product analysis

Fischer Tropsch synthesis reactions

Fischer-Tropsch Synthesis of Hydrocarbons

Fischer-Tropsch Synthesis via Carbidic Intermediates

Fischer-Tropsch Synthesis, Methanation and Steam Reforming

Fischer-Tropsch biofuel synthesis

Fischer-Tropsch medium pressure synthesis

Fischer-Tropsch normal pressure synthesis

Fischer-Tropsch synthesis

Fischer-Tropsch synthesis

Fischer-Tropsch synthesis Schulz-Flory distribution

Fischer-Tropsch synthesis acetylene

Fischer-Tropsch synthesis activity, catalyst

Fischer-Tropsch synthesis added olefin reactions

Fischer-Tropsch synthesis carbon monoxide effects

Fischer-Tropsch synthesis carbon monoxide-hydrogen distribution

Fischer-Tropsch synthesis catalysis

Fischer-Tropsch synthesis catalyst design

Fischer-Tropsch synthesis catalytic activity

Fischer-Tropsch synthesis catalytic measurements

Fischer-Tropsch synthesis chain growth probability

Fischer-Tropsch synthesis chain growth reaction

Fischer-Tropsch synthesis concentration

Fischer-Tropsch synthesis conductivity

Fischer-Tropsch synthesis coverage

Fischer-Tropsch synthesis dissociation

Fischer-Tropsch synthesis effect

Fischer-Tropsch synthesis functionality

Fischer-Tropsch synthesis high temperature operation

Fischer-Tropsch synthesis insertion

Fischer-Tropsch synthesis insertion mechanism

Fischer-Tropsch synthesis iron catalyzed

Fischer-Tropsch synthesis kinetics

Fischer-Tropsch synthesis labeled

Fischer-Tropsch synthesis membrane reactors

Fischer-Tropsch synthesis metathesis reaction

Fischer-Tropsch synthesis methanation reaction

Fischer-Tropsch synthesis model

Fischer-Tropsch synthesis modified

Fischer-Tropsch synthesis nitrides

Fischer-Tropsch synthesis olefin selectivity

Fischer-Tropsch synthesis operating temperature

Fischer-Tropsch synthesis oxygenates

Fischer-Tropsch synthesis parameters

Fischer-Tropsch synthesis primary product secondary reactions

Fischer-Tropsch synthesis production distribution

Fischer-Tropsch synthesis products

Fischer-Tropsch synthesis rate constants

Fischer-Tropsch synthesis rate equations

Fischer-Tropsch synthesis reaction rate

Fischer-Tropsch synthesis reaction scheme

Fischer-Tropsch synthesis reactor modeling

Fischer-Tropsch synthesis removal, reaction mixture

Fischer-Tropsch synthesis selectivity

Fischer-Tropsch synthesis selectivity control

Fischer-Tropsch synthesis slurry process

Fischer-Tropsch synthesis spectroscopy

Fischer-Tropsch synthesis steady-state

Fischer-Tropsch synthesis steady-state production

Fischer-Tropsch synthesis surface carbon

Fischer-Tropsch synthesis termination reaction

Fischer-Tropsch synthesis three-phase bubble column

Fischer-Tropsch synthesis transient kinetics

Fischer-Tropsch synthesis turnover frequency

Fischer-Tropsch type synthesis

Fischer—Tropsch synthesis catalyst particle size effects

Fischer—Tropsch synthesis catalyst pore size effects

Fischer—Tropsch synthesis development

Fischer—Tropsch synthesis diffusivity effects

Fischer—Tropsch synthesis history

Fischer—Tropsch synthesis kinetic model

Fischer—Tropsch synthesis product distribution

Fischer—Tropsch synthesis surface carbide mechanism

Fluid Fischer-Tropsch synthesis

Fuel Fischer-Tropsch synthesis

Heterogeneous Fischer Tropsch synthesis

Heterogeneous catalysis Fischer-Tropsch synthesis

High-temperature Fischer-Tropsch synthesis

History, Current Status, and Perspectives of Fischer-Tropsch Synthesis

Hydroformylation, Fischer-Tropsch synthesis

Hydroformylation, Fischer-Tropsch synthesis cobalt catalysts

Hydrogenation Fischer-Tropsch synthesis

In Fischer-Tropsch synthesis

Industrial processes Fischer-Tropsch synthesis

Kinetic study, modeling, Fischer-Tropsch synthesis

Low-temperature Fischer-Tropsch synthesis

Methanation Fischer-Tropsch synthesis

Molecular weight distributions Fischer-Tropsch synthesis

Olefins Fischer-Tropsch synthesis product

Pore diffusion modeling in Fischer-Tropsch synthesis

Processes Related to the Fischer-Tropsch Synthesis

Product functionality, Fischer-Tropsch synthesis

Reactions and Mechanisms of Fischer-Tropsch Synthesis

Reactor approaches for Fischer-Tropsch synthesis

Reactor for Fischer-Tropsch synthesis

Ruthenium-Catalyzed Fischer-Tropsch Synthesis Methane and Polymethylenes

Selectivity of Fischer-Tropsch synthesis

Slurry-phase reactor, Fischer-Tropsch synthesis

Supercritical fluids Fischer-Tropsch synthesis

Syngas to Synthetic Fuels The Fischer-Tropsch Synthesis

Synthetic Fischer-Tropsch synthesis

Synthol reactors Fischer-Tropsch synthesis

The Fischer-Tropsch Synthesis

Zeolite Fischer-Tropsch synthesis

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