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Mixtures, 65-66 heterogeneous separating

A very important part of such an undertaking is to be clear about what stages of a chemical process generate the most waste. Often this is found to be the separation stage, after the transformation of reactants to products, where all the various components of the final mixture are separated and purified. Approaches to chemical reactions which help to simplify this step are particularly powerful. Such an approach is exemplified by heterogeneous catalysis. This is an area of chemistry where the catalysts used are typically solids, and the reactants are all in the hquid or gas phase. The catalyst can speed up the reaction, increase the selectivity of the reaction, and then be easily recovered by filtration from the liquid, and reused. [Pg.60]

On the other hand, when cornstarch and water are stirred together and allowed to stand, the resulting mixture soon separates into its components. Because cornstarch is insoluble in water, a combination of cornstarch and water forms a heterogeneous mixture. That is, one microscopic portion of this mixture has a different composition than another microscopic portion does. An insoluble granule of cornstarch has an entirely different composition than a microscopic portion of water. [Pg.868]

The homogeneous palladium-catalyzed process for acetoxylation was never commercialized because of low selectivity and the difficulty in separating the catalyst from the reaction mixture. Heterogeneous palladium catalysts applied in the gas phase, in turn, quickly lose activity caused by buildup of polybutadiene. The Mitsubishi process uses a Pd-Te-on-active-carbon catalyst in the liquid phase. Tellurium apparently prevents palladium elution to acetic acid. [Pg.510]

Matter can be either a pure substance or a mixture. Pure substances cannot be further broken down into simpler components through physical processes and can be either elements (one type of atom) or compounds (more than one type of atom). Mixtures can be homogeneous (aka. solutions) or heterogeneous. Heterogeneous mixtures exhibit phase boundaries, or sharp demarcations where the chemical and/or physical properties of the sample change. Mixtures are separable into pure substances through physical processes. [Pg.388]

Heterogeneous Mixtures Heterogeneous mixtures do not have a uniform distribution of particles throughout the mixture. The different components of the mixture can easily be identified and separated. [Pg.50]

Because of their sizes, neither K+ nor Si + can enter into solid solution with the magnetite and so if some silica is present in the iron oxide used, small occlusions of alkali silicates are present as separate phases in the fused catalyst. Microscopic investigations of the milled catalyst showed that whereas the larger particles still contain alkali silicate occlusions, the finer particles consist of a mixture of separate alkali silicate and magnetite particles (20). Hence, the distribution of alkali in the milled, fused catalyst is heterogeneous. During reduction and FT synthesis, however, the alkali does to some extent spread over the catalyst surface ((7), chapter 3). [Pg.981]

A heterogeneous mixture is one with physically separate parts that have different properties. An easy example is salt and pepper. A heterogeneous mixture has separate phases. A phase represents the number of different... [Pg.45]

A homogeneous mixture is called a solution. Air is a solution consisting of a mixture of gases. Wine is a complex liquid solution. Brass is a solid solution of copper and zinc. Sand in water and iced tea with ice cubes are examples of heterogeneous mixtures. Heterogeneous mixtures usually can be separated into two or more homogeneous mixtures or pure substances (for example, the ice cubes can be separated from the tea). [Pg.28]

An example of heterogeneous azeotropic distillation is the system ethanol and water with benzene as entrainer (Figure 3.3.20). In a first column (without entrainer, column I in Figure 3.3.20b), the binary ethanol-water mixture is separated by normal distillation. An azeotrope with about 90 mol.% ethanol (96wt%) leaves the column on top (A) while water forms the bottom product. The azeotrope is fed to a second column where benzene (recycle of a phase rich in benzene from the separator of the top products of column II and III) is added as entrainer. A new low-boiling heterogeneous azeotrope (B) leaves column II as distillate, and pure ethanol remains as bottom product. After condensation, the heterogeneous azeotrope separates into two phases rich in either benzene (C) or water (D). The phase rich in benzene is recycled back into column II while the phase rich in water is reconditioned in a third column by distillation. The small amount of benzene is separated as top product (azeotrope B), and a mixture of ethanol and water (E) is recycled into column I. [Pg.107]

Various parameters of speed determine whether a mixture may separate or continue to flow. In fact, the designer of a thickener or a mixer is often more interested in the sinking velocity of particles. On the other hand, the designer of a pipeline has to pay attention to the critical velocity of flow, setding speed, and whether the flow is vertical or horizontal, particularly in the case of heterogeneous flows. [Pg.32]

Another approach to the determination of sequence heterogeneity of the bound 80 S and free cytoplasmic rRNA involved the fractionation of pancreatic RNase digests of rRNA by two-dimensional column chromatography. In a double-label experiment, free 26 S rRNA labeled with [ C]uracil and bound 26 S rRNA labeled with PH]uracil were mixed, digested with pancreatic RNase, and the oligonucleotide mixture was separated according to chain length on a column of DEAE-cellulose in... [Pg.178]

Separation of the different phases of a heterogeneous mixture should be carried out before homogeneous separation, taking advantage of what already exists. Phase separation tends to be easier and... [Pg.67]

The four principal methods for the separation of heterogeneous mixtures are... [Pg.68]

Let us briefly review the primary treatment methods used. Pretreatment usually starts with phase separation if the effluent is a heterogeneous mixture. [Pg.310]

Benzoylpropionitrile. To a mixture of 21 4 g. of p dimethylamino propiophenone hydrochloride, 13 0 g. of potassium cyanide in a 500 ml. flask, add 260 ml. of boiling water heat the heterogeneous mixture under reflux for 30 minutes. Part of the dimethylamine, which is eliminated in the reaction, distils collect this in dilute hydrochloric acid. Cool the reaction mixture in ice the oil sohdifies and crystals form from the aqueous layer. Collect the solid (crude p benzoylpropiouitrile, 10-5 g.) by suction filtration and recrystallise it from benzene - light petroleum (b.p. 40-60°) it separates as almost colourless blades, m.p. 76°. [Pg.912]

The ohmic drop across the electrolyte and the separator can also be calculated from Ohm s law usiag a modified expression for the resistance. When gas bubbles evolve at the electrodes they get dispersed ia and impart a heterogeneous character to the electrolyte. The resulting conductivity characteristics of the medium are different from those of a pure electrolyte. Although there is no exact description of this system, some approximate treatments are available, notably the treatment of Rousar (9), according to which the resistance of the gas—electrolyte mixture, R, is related to the resistance of the pure electrolyte, R ... [Pg.485]

The principal commercial source of 1-butanol is -butyraldehyde [123-72-8] obtained from the Oxo reaction of propylene. A mixture of n- and isobutyraldehyde [78-84-2] is obtained in this process this mixture is either separated initially and the individual aldehyde isomers hydrogenated, or the mixture of isomeric aldehydes is hydrogenated direcdy and the n- and isobutyl alcohol product mix separated by distillation. Typically, the hydrogenation is carried out in the vapor phase over a heterogeneous catalyst. For example, passing a mixture of n- and isobutyraldehyde with 60 40 H2 N2 over a CuO—ZnO—NiO catalyst at 25—196°C and 0.7 MPa proceeds in 99.95% efficiency to the corresponding alcohols at 98.6% conversion (7,8) (see Butyraldehydes Oxo process). [Pg.357]


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