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Gasoline refinery

Polymer Gasoline. Refinery trends tend to favor alkylation over polymerisation. Unlike the alkylation process, polymerisation does not require isobutane. The catalyst is usually phosphoric acid impregnated on kieselghur pellets. Polymerisation of butylenes is not an attractive alternative to alkylation unless isobutane is unavailable. The motor octane number of polymer gasoline is also low, and there is considerable shrinkage ia product volume. The only commercial unit to be built ia recent years is at Sasol ia South Africa. The commercial process was developed by UOP ia the 1940s (104). [Pg.371]

Another interesting trend which may develop as a consequence of lead free gasoline is increased interest in isobutane pyrolysis. Hydrocracking may well be used as an important tool in the lead free gasoline refinery. This process produces considerable yields of isobutane. It is... [Pg.190]

Derivation An important component of natural gasoline, refinery gases, wet natural gas also obtained by isomerization of butane. [Pg.705]

The CARB report indicated that hydrogen would be produced at large, central facilities similar to a gasoline refinery. But hydrogen could be made at neighborhood refueling stations or at renewable energy farms. [Pg.119]

A natural gasoline plant has available, as a by-product from the natural gasoline refinery, 60,000 ft of butane per day, based on standard gas conditions. This by-product is to be utilized by oxidizing in the vapor phase the butane under controlled conditions to produce partial-oxidation products, totaling 159 lb/1,000 ft of butane, the product consisting of aldehydes, alcohols, ketones, and acids, according to the following analysis ... [Pg.264]

Fig. 22-5. Graphical analysis of natural gasoline. Refinery Supply Co. TvUa, Okla.)... Fig. 22-5. Graphical analysis of natural gasoline. Refinery Supply Co. TvUa, Okla.)...
Along the same lines, a distillation can be simulated by gas phase chromatography. As in a refinery, distillation in the laboratory is very often the first step to be carried out, because it gives the yields in different cuts gasoline, kerosene, etc., and makes further characterization of the cuts possible. [Pg.18]

We believe to have shown here that the RVP of gasoline is a primary characteristic for quality resulting from a delicate compromise between the demands for vehicle performance, optimization of refinery operations and environmental protection. [Pg.190]

All modern refineries have conversion units, designed to transform black effluent streams into lighter products gas, gasoline, diesel fuel. Among these conversion units, coking processes take place by pyrolysis and push the cracking reaction so far that the residue from the operation is very heavy it is called coke . [Pg.292]

The flowscheme of the typical refinery during the period 1950-1970 was essentially focused on the production of gasoline, diesel oil, domestic heating oil and industrial fuel-oil. Except for heavy naphtha, the product streams underwent no deep conversion. [Pg.406]

We cite isomerization of Cs-Ce paraffinic cuts, aliphatic alkylation making isoparaffinic gasoline from C3-C5 olefins and isobutane, and etherification of C4-C5 olefins with the C1-C2 alcohols. This type of refinery can need more hydrogen than is available from naphtha reforming. Flexibility is greatly improved over the simple conventional refinery. Nonetheless some products are not eliminated, for example, the heavy fuel of marginal quality, and the conversion product qualities may not be adequate, even after severe treatment, to meet certain specifications such as the gasoline octane number, diesel cetane number, and allowable levels of certain components. [Pg.485]

The market value of natural gas Hquids is highly volatile and historically has been weakly related to the world price of cmde oil. During the 1980s, the market value of natural gas Hquids ranged from approximately 60% of the price of cmde to 73% (12). In this 10-year interval, several fluctuations occurred in the natural gas Hquid market. Because of the variabiHty of the natural gas Hquid market, the NGL recovery plants need to have flexibiHty. Natural gas Hquid products compete in the following markets ethane propane a Hquefted petroleum gas (LPG) a C-3/C-4 mix and / -butane all compete as petrochemical feedstocks. Propane and LPG are also used as industrial and domestic fuels, whereas 2-butane and natural gasoline, consisting of C-5 and heavier hydrocarbons, are used as refinery feedstocks. [Pg.171]


See other pages where Gasoline refinery is mentioned: [Pg.208]    [Pg.203]    [Pg.986]    [Pg.99]    [Pg.140]    [Pg.368]    [Pg.423]    [Pg.203]    [Pg.818]    [Pg.91]    [Pg.133]    [Pg.155]    [Pg.134]    [Pg.840]    [Pg.609]    [Pg.208]    [Pg.203]    [Pg.986]    [Pg.99]    [Pg.140]    [Pg.368]    [Pg.423]    [Pg.203]    [Pg.818]    [Pg.91]    [Pg.133]    [Pg.155]    [Pg.134]    [Pg.840]    [Pg.609]    [Pg.200]    [Pg.205]    [Pg.231]    [Pg.242]    [Pg.2789]    [Pg.129]    [Pg.226]    [Pg.30]    [Pg.421]    [Pg.171]    [Pg.171]    [Pg.175]    [Pg.175]    [Pg.175]    [Pg.85]    [Pg.179]    [Pg.182]    [Pg.183]    [Pg.183]    [Pg.184]    [Pg.184]    [Pg.185]   
See also in sourсe #XX -- [ Pg.152 ]




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Refineries

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