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Carbon ratio

Figure C2.13.7. Change between polymerizing and etching conditions in a fluorocarbon plasma as detennined by tire fluorine-to-carbon ratio of chemically reactive species and tire bias voltage applied to tire substrate surface [36]. Figure C2.13.7. Change between polymerizing and etching conditions in a fluorocarbon plasma as detennined by tire fluorine-to-carbon ratio of chemically reactive species and tire bias voltage applied to tire substrate surface [36].
Hydrocarbon resources can be classified as organic materials which are either mobile such as cmde oil or natural gas, or immobile materials including coal, lignite, oil shales, and tar sands. Most hydrocarbon resources occur as immobile organic materials which have a low hydrogen-to-carbon ratio. However, most hydrocarbon products in demand have a H C higher than 1.0. [Pg.364]

Naphtha desulfurization is conducted in the vapor phase as described for natural gas. Raw naphtha is preheated and vaporized in a separate furnace. If the sulfur content of the naphtha is very high, after Co—Mo hydrotreating, the naphtha is condensed, H2S is stripped out, and the residual H2S is adsorbed on ZnO. The primary reformer operates at conditions similar to those used with natural gas feed. The nickel catalyst, however, requires a promoter such as potassium in order to avoid carbon deposition at the practical levels of steam-to-carbon ratios of 3.5—5.0. Deposition of carbon from hydrocarbons cracking on the particles of the catalyst reduces the activity of the catalyst for the reforming and results in local uneven heating of the reformer tubes because the firing heat is not removed by the reforming reaction. [Pg.420]

This reaction is affected by the steam-to-carbon ratio, temperature, and pressure, as well as catalyst activity. [Pg.454]

Carbon produced by these latter reactions is formed in the catalyst pores, making it much more difficult to remove, and potentially causing physical breakage. Operating steam to carbon ratios are chosen above the minimum required in order to make carbon formation by these reactions thermodynamically impossible (3). Steam is another potential source of contaminants. Chemicals from the boiler feedwater or the cooling system are poisons to the reformer catalyst, so steam quality must be carefully monitored. [Pg.346]

HTS catalyst consists mainly of magnetite crystals stabilized using chromium oxide. Phosphoms, arsenic, and sulfur are poisons to the catalyst. Low reformer steam to carbon ratios give rise to conditions favoring the formation of iron carbides which catalyze the synthesis of hydrocarbons by the Fisher-Tropsch reaction. Modified iron and iron-free HTS catalysts have been developed to avoid these problems (49,50) and allow operation at steam to carbon ratios as low as 2.7. Kinetic and equiUbrium data for the water gas shift reaction are available in reference 51. [Pg.348]

D. Kitchen, A. Pinto, and H. Van-Praag, "ICI s Operating Experience with Shift Catalyst at Low Steam to Carbon Ratios," AIChE Ammonia Safety Symposium, Denver, Colo., Aug. 22—24, 1988, American Institute of Chemical Engineers, New York, 1989. [Pg.360]

Other hydrocarbons can be used. Stoichiometricahy, ethane [74-84-0] is preferable to methane since its lower hydrogen/carbon ratio results in a smaller yield of coproduct hydrogen sulfide ... [Pg.29]

The carbon monoxide concentration of gas streams is a function of many parameters. In general, increased carbon monoxide concentration is found with an increase in the carbon-to-hydrogen ratio in the feed hydrocarbon a decrease in the steam-to-feed-carbon ratio increase in the synthesis gas exit temperature and avoidance of reequiUbration of the gas stream at a temperature lower than the synthesis temperature. Specific improvement in carbon monoxide production by steam reformers is made by recycling by-product carbon dioxide to the process feed inlet of the reformer (83,84). This increases the relative carbon-to-hydrogen ratio of the feed and raises the equiUbrium carbon monoxide concentration of the effluent. [Pg.54]

Coal Hquefaction iavolves raising the atomic hydrogen-to-carbon ratio from approximately 0.8/1.0 for a typical bituminous coal, to 2/1 for Hquid transportation fuels or 4/1 for methane (4). In this process, molecular weight reduction and removal of mineral matter and heteroatoms such as sulfur, oxygen, and nitrogen may need to be effected. [Pg.280]

Fig. 3. Theoretical mole percent of the principal combustion products of hydrocarbon fuels for fuel hydrogen carbon ratios from 1, eg, to 4, eg, CH, ... Fig. 3. Theoretical mole percent of the principal combustion products of hydrocarbon fuels for fuel hydrogen carbon ratios from 1, eg, to 4, eg, CH, ...
By tire coiTect choice of the metal oxide/carbon ratio in the ingoing burden for the furnace, the alloy which is produced can have a controlled content of carbon, which does not lead to the separation of solid carbides during the reduction reaction. The combination of the carbon electrode, tire gaseous oxides and the foamed slag probably causes tire formation of a plasma region between the electrode aird the slag, and this is responsible for the reduction of elecU ical and audible noise which is found in this operation, in comparison with tire arc melting of scrap iron which is extremely noisy, and which injects unwanted electrical noise into the local electrical distribution network. [Pg.336]

The higher the hydrogen to carbon ratio in the polymer the greater is the tendency to burning (other factors being equal). [Pg.105]

Cracking and isomerization reactions occur readily in acidic chloroaluminate(III) ionic liquids. A remarkable example of this is the reaction of poly(ethene), which is converted into a mixture of gaseous alkanes of formula (C Ff2n+2, where n = 3-5) and cyclic alkanes with a hydrogen to carbon ratio of less than two (Figure 5.1-4, Scheme 5.1-68) [99]. [Pg.208]

The major chemical difference between natural gas, crude oil, and coal is their hydrogen-to-carbon ratios. Coal is carbon-rich and hydrogen-poor, so to produce a synthetic liquid or gas from coal requires an increase in the hydrogen-to-carbon ratio. Coal s ratio of about 0.8 has to be raised to 1.4 to 1.8 for a... [Pg.1114]

A promoted nickel type catalyst contained in the reactor tubes is used at temperature and pressure ranges of 700-800°C and 30-50 atmospheres, respectively. The reforming reaction is equilibrium limited. It is favored at high temperatures, low pressures, and a high steam to carbon ratio. These conditions minimize methane slip at the reformer outlet and yield an equilibrium mixture that is rich in hydrogen. ... [Pg.140]

The high hydrogen/carbon ratio of gas means that the quantity of water vapor in the products of combustion is greater than most other fossil fuels. The latent heat of this cannot be released in conventional appliances leading to a low net/gross ratio of calorific value of 90 per cent. (It is normal practice to quote gross CV in Europe net CV is often used. If net CV is quoted, efficiencies of over 190 per cent are possible.)... [Pg.264]

The ratio of net/gross CV is about 90 per cent, reflecting the high hydrocarbon/carbon ratio for gas. The range of... [Pg.275]

OCR dating Abbreviation for oxidizable carbon ratio dating. [Pg.526]


See other pages where Carbon ratio is mentioned: [Pg.502]    [Pg.503]    [Pg.2808]    [Pg.211]    [Pg.54]    [Pg.78]    [Pg.88]    [Pg.195]    [Pg.419]    [Pg.420]    [Pg.13]    [Pg.153]    [Pg.276]    [Pg.277]    [Pg.401]    [Pg.341]    [Pg.346]    [Pg.352]    [Pg.352]    [Pg.408]    [Pg.5]    [Pg.482]    [Pg.2372]    [Pg.14]    [Pg.271]    [Pg.251]    [Pg.13]    [Pg.359]    [Pg.301]    [Pg.205]    [Pg.500]    [Pg.528]   
See also in sourсe #XX -- [ Pg.252 ]




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Atomic hydrogen to carbon ratio

Bacteria carbon:nitrogen ratio

Calcium carbonate oxygen isotopic ratio determination

Carbon bone collagen isotope ratios

Carbon content ratio

Carbon dioxide heat capacity ratio

Carbon dioxide mixing ratio

Carbon dioxide ratios

Carbon fiber aspect ratio

Carbon heat capacity ratio

Carbon isotope ratios

Carbon isotope ratios for

Carbon isotopic ratio

Carbon mixing ratio

Carbon monoxide heat capacity ratio

Carbon monoxide mixing ratios

Carbon monoxide ratios

Carbon monoxide, tropospheric mixing ratio

Carbon monoxide/methanol molar ratio

Carbon nanotubes aspect ratio

Carbon nanotubes ratio

Carbon stable isotope ratio analysis

Carbon stable isotope ratio test

Carbon steels ratio

Carbon-nitrogen ratio

Carbon-nitrogen ratio size-distribution

Carbon-nitrogen ratios elemental analyses

Carbon-nitrogen ratios marine organic matter

Carbon-nitrogen ratios pyrolysis

Carbon-nitrogen ratios sample preparation

Carbon-oxygen ratio, organometallic

Carbon-sulfur ratio

Carbon-to-nitrogen ratios

Carbon-to-phosphorus ratio

Coke deposition steam-carbon ratio

Composts carbon-nitrogen ratios

Critical steam-to-carbon ratio

Dating techniques organic carbon ratio

Dolomites carbon isotope ratios

Elemental ratios carbon

Fluorine-to-carbon ratio

Fluorine/carbon elemental ratios

Graphitized carbon capacity ratios

Hydrogen to Carbon Monoxide Ratio

Hydrogen-carbon monoxide ratio

Hydrogen-carbon monoxide ratio liquid reaction products

Hydrogen-carbon monoxide ratio, effect

Hydrogen-carbon ratios

Hydrogen-carbon ratios estimates

Hydrogen-carbon ratios sample preparation

Hydrogen-to-carbon ratio

Hydrogen/carbon ratios, variation with

Isotope ratio mass spectrometry carbon

Isotope ratios Carbon isotopes

Isotopic ratios of carbon

Natural organic carbon-water distribution ratio

Nitrogen-carbon ratios, marine organic

Organic carbon ratio

Organic carbon-nitrogen ratio, effect

Oxygen to carbon ratio

Oxygen-.carbon ratio

Oxygen-carbon ratios, marine organic

Oxygen/carbon elemental ratios

Oxygen/carbon ratios, variation with

Reactions hydroxide/carbon ratio effects

Stable carbon isotope ratios animals

Stable carbon isotope ratios collagen

Stable carbon isotope ratios diets

Stable isotope ratios carbon

Steam-to-carbon ratios

Steam/carbon ratio

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