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Distillation components

Reagents such as water, ammonia, hydrochloric acid, nitric acid, perchloric acid, and sulfuric acid can be purified via distillation (preferably under reduced pressure and particularly with perchloric acid) using an allglass still. Isothermal distillation is convenient for ammonia a beaker containing concentrated ammonia is placed alongside a beaker of distilled water for several days in an empty desiccator so that some of the ammonia distils over into the water. The redistilled ammonia should be kept in polyethylene or parafrin-waxed bottles. Hydrochloric acid can be purified in the same way. To ensure the absence of metal contaminants from some salts (e.g. ammonium acetate), it may be more expedient to synthesise the salts using distilled components rather than to attempt to purify the salts themselves. [Pg.53]

In naphtha and light distillate components, oxygen-containing compounds appear as carboxylic acids and phenols. Most of these compounds concentrate in the kerosene, fuel oil, and lighter lubricant fractions. Straight-run gasoline, heavy distillates, and residual fuels usually contain few acids. [Pg.38]

Jet fuels are blended primarily from straight-run distillate components and contain virtually no olefins. Aromatics in jet fuel are also limited. High aromatic content can cause smoke to form during combustion and can lead to carbon deposition in engines. A total aromatic content >30% can cause deterioration of aircraft fuel system elastomers and lead to fuel leakage. [Pg.51]

The product structures available in this process are primarily determined by components in the paraffinic distillates used. The heterogeneity of virgin distillates has been illustrated by API sponsored work on distillate components 21). The preferred predominance of relatively straight-chain alkyl groups may be effected by combinations of selection of paraffin distillate source, and use of acid or solvent refining to effect enrichment of paraffinic components. With the advent of the urea precipitation technique of isolating the n-paraffins 26), particularly those in the decyl to hexadecyl range, it is now possible to produce products which are limited principally to the isomeric secondary phenyl alkanes a dodecyl benzene mixture prepared by this process from a 95+% n-dodecane would consist essentially of the 2-, 3-, 4-, 5-, and 6-phenyl-substituted dodec-anes. [Pg.330]

Operating the column at the minimum pressure minimizes the energy cost of separation. Towering this pressure increases the relative volatility of distillation components and thereby increases the capacity of the reboiler by reducing operating temperature, which also results in reduced fouling. Reducing pressure also affects other parameters, such as tray efficiencies and latent heats of vaporization. [Pg.244]

Data calculated from that for composite synthetic crude obtained after coking and Unifining of extracted bitumen, from Bachman and Stormont [2]. Before Unifining (hydrogenation) mean density of the composite stream would be somewhat higher, and sulfur content would be about 3%. Proportions of distillate components are approximate carbon content quoted is the coke residue on pyrolysis of bitumen. [Pg.594]

The distillate component flow rates may now be calculated from an overall col-... [Pg.442]

Jet fuels consist entirely of hydrocarbons except for trace quantities of sulfur compounds and approved additives. Jet fuels are produced, for example, by blending straight-run distillate components, and olefins are limited by specification (ASTM D-1319, IP 156) or by the bromine number (ASTM D-1159, ASTM D-2710, IP 130). [Pg.144]

Securing distillation components - do not use plastic joint clips on the hot end of a distillation apparatus since they may melt and the joints may separate. [Pg.107]

The light key, the heavy key, and all components having K values between those of the keys are called distributed components. Components heavier than the heavy key are called separated heavy components because they are separated in the rectifying section and do not appear in the distillate. Components lighter than the light key are called separated light components because they are separated in the stripping section and do not appear in the bottom product B. More precisely, a separated heavy component is any component for which... [Pg.372]

Component 2 in distillate Component 2 in bottoms Componertt 3 in bottoms Component 3 in distillate ... [Pg.377]

CompositionThe main components are limonene (50-60%) and y-terpinene (see p-menthadienes) (10-20%). In contrast to pressed L. the distilled oil contains many components that are formed during the production process by action of the acidic juice on the oil liberated from of the fruit skin. Thus, under the conditions of distillation components such as p-cymol (see cymenes), 1,4- and l,8- cineole, fenchol, bomeol, a- and 8-terpineol (seep-menthenols), etc. are formed. All these compounds are either not present or are present in much lower concentrations in pressed oil. [Pg.360]

As can be seen in Figs. 3.3 and 3.4, at R = 00, N = 00, and with the increase of the parameter D/F, the top product point shifts from the unstable node (vertex 1) to the feed point and the bottom product point shifts from the feed point to the stable node (to vertex 3 in Fig. 3.3 or vertex 4 in Fig. 3.4). For this, the number of distillate components increases and the number of the bottom product components decreases. [Pg.46]

Feasible sharp reversible distillation split of ideal mixtures can be presented as follows 1, 2,... (n - 1) 2,3... n. Therefore, at the reversible distillation, components 2, 3,... (n - 1) are distributed among the top and the bottom products. At nonsharp and semisharp reversible distillation, both products contain all the components or one of the products does not contain the lightest or the heaviest component. At nonsharp reversible distillation, product points lie in the same straight line as at sharp distillation but at some distance from the hyperfaces of the concentration simplex. [Pg.80]

Styrene was first discovered in 1839 as a distillation component of balsam oil by E. Simon (1), who recorded the name styrol for this substance. It was accompanied by a sticky, viscous material which we can now safely assume was the corresponding polystyrene. This discovery began a field of chemistry that has evoked Intense academic and industrial interest for over a century and whose fascinating early history is recorded in Boundy and Boyer s treatise on styrene (2). [Pg.223]


See other pages where Distillation components is mentioned: [Pg.86]    [Pg.70]    [Pg.337]    [Pg.91]    [Pg.115]    [Pg.52]    [Pg.180]    [Pg.258]    [Pg.692]    [Pg.276]    [Pg.180]    [Pg.183]    [Pg.91]    [Pg.82]    [Pg.2791]    [Pg.70]    [Pg.52]    [Pg.1112]    [Pg.35]    [Pg.353]    [Pg.71]    [Pg.443]    [Pg.75]    [Pg.102]    [Pg.195]    [Pg.681]   
See also in sourсe #XX -- [ Pg.166 ]

See also in sourсe #XX -- [ Pg.166 ]

See also in sourсe #XX -- [ Pg.166 ]




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Component Separation Conventional Distillation

Component vacuum distillation unit

Diagrams of Extractive Reversible Distillation for Three-Component Mixtures

Diagrams of Three-Component Mixture Reversible Distillation

Distillation columns component balance

Distillation multi component mixtures

Distillation sequence nonkey components

Distillation sequencing nonkey components

Distillation three-component

Four-component distillation

Four-component mixtures distillation regions

Four-component mixtures reversible distillation trajectories

Intermediate components, multicomponent distillation

Key components in multicomponent distillation

Multi component distillation

Multicomponent distillation components

Sharp Extractive Distillation of Three-Component Mixtures

Three-component mixtures distillation region

Three-component mixtures reversible distillation

Three-component mixtures reversible distillation trajectories

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