1953
DOI: 10.1021/ie50518a031
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Products of the Hydrogenation of Carbon Monoxide over an Iron Catalyst - Aliphatic and Alicyclic Hydrocarbons

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Cited by 54 publications
(16 citation statements)
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“…To reiterate, these include: multiple chain growth probabilities due to different types of active sites; [32][33][34][35][36][37][38] diffusion enhanced alpha olefin reincorporation; [39][40][41] greater solubility or physisorption strength; [42][43][44] vaporliquid equilibrium; 45,46 chain-length dependent product accumulation; [47][48][49] gradients in process conditions at the scale of the particle or reactor; 50 and dependent olefin desorption or greater olefin adsorptivity. [51][52][53] During FTS at realistic conditions using either a fixed bed or slurry phase reactor, catalyst pores are filled with hydrocarbon products. With a CSTR, Shi and Davis 48 demonstrated that product accumulation within the reactor significantly alters the apparent product distribution away from the ideal distribution.…”
Section: Catalysis Science and Technology Papermentioning
confidence: 99%
“…To reiterate, these include: multiple chain growth probabilities due to different types of active sites; [32][33][34][35][36][37][38] diffusion enhanced alpha olefin reincorporation; [39][40][41] greater solubility or physisorption strength; [42][43][44] vaporliquid equilibrium; 45,46 chain-length dependent product accumulation; [47][48][49] gradients in process conditions at the scale of the particle or reactor; 50 and dependent olefin desorption or greater olefin adsorptivity. [51][52][53] During FTS at realistic conditions using either a fixed bed or slurry phase reactor, catalyst pores are filled with hydrocarbon products. With a CSTR, Shi and Davis 48 demonstrated that product accumulation within the reactor significantly alters the apparent product distribution away from the ideal distribution.…”
Section: Catalysis Science and Technology Papermentioning
confidence: 99%
“…In all runs herein reported a 1:1 E2:CO synthesis gas was used. 6 Space velocity is here defined as volume of entering gas per volume of catalyst space per hour; the catalyst volume was 100 cc. in the radioactive methanol addition experiment and 50 cc.…”
Section: 1mentioning
confidence: 99%
“…Thus, any development to reduce our dependence on foreign suppliers of petroleum, e.g., an economic coal-based process, should have high priority (2). Hence, there has been a renewal of interest in Fischer-Tropsch processes (3)(4)(5)(6)(7)(8)(9)(10)(11)(12)(13)(14), the catalytic synthesis of primarily C5-C11 hydrocarbons from CO-H2 mixtures. Unfortunately, economic considerations indicate that a synthetic naphtha as cracker feedstock for American Chemical 0-8412-04^^j^3jlfm.â4^$05.00/0…”
mentioning
confidence: 99%