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Chlorobenzenes design

Predict the products formed when each of the following isotopically substituted denvatives of chlorobenzene is treated with sodium amide in liquid ammonia Estimate as quantitatively as possible the composition of the product mixture The astensk ( ) in part (a) designates C and D in part (b) is... [Pg.988]

Prepare a sieve-plate column design for the chlorobenzene distillation and make dimensioned sketches showing details of the plate layout including the weir and the downcomer. [Pg.969]

Prepare a mechanical design of the chlorobenzene column, estimating the shell thickness, the positions and sizes of all nozzles, and the method of support for the plates and the column shell. Make a dimensioned sketch suitable for submission to a drawing office. [Pg.969]

We then designed model studies by adsorbing cinchonidine from CCU solution onto a polycrystalline platinum disk, and then rinsing the platinum surface with a solvent. The fate of the adsorbed cinchonidine was monitored by reflection-absorption infrared spectroscopy (RAIRS) that probes the adsorbed cinchonidine on the surface. By trying 54 different solvents, we are able to identify two broad trends (Figure 17) [66]. For the first trend, the cinchonidine initially adsorbed at the CCR-Pt interface is not easily removed by the second solvent such as cyclohexane, n-pentane, n-hexane, carbon tetrachloride, carbon disulfide, toluene, benzene, ethyl ether, chlorobenzene, and formamide. For the second trend, the initially established adsorption-desorption equilibrium at the CCR-Pt interface is obviously perturbed by flushing the system with another solvent such as dichloromethane, ethyl acetate, methanol, ethanol, and acetic acid. These trends can already explain the above-mentioned observations made by catalysis researchers, in the sense that the perturbation of initially established adsorption-desorption equilibrium is related to the nature of the solvent. [Pg.255]

The 2003 threshold limit valuetime-weighted average (TLV-TWA) for chlorobenzene is 10 ppm (46mg/m ) with an A3-confirmed animal carcinogen with unknown relevance to humans designation. [Pg.147]

In a number of important industrial processes, it is necessary to carry out a reaction between a gas and a liquid. Usually the object is to make a particular product, for example, a chlorinated hydrocarbon such as chlorobenzene by the re action of gaseous chlorine with liquid benzene. Sometimes the liquid is simply the reaction medium, perhaps containing a catalyst, and all the reactants and products are gaseous. In other cases the main aim is to separate a constituent such as C02 from a gas mixture although pure water could be used to remove CO2, a solution of caustic soda, potassium carbonate or ethanolamine has the advantages of increasing both the absorption capacity of the liquid and the rate of absorption. The subject of gas-liquid reactor design thus really includes absorption with chemical reaction which is discussed in Volume 2, Chapter 12. [Pg.196]

Section 104(i)(5) of CERCLA, directs the Administrator of ATSDR (in consultation with the Administrator of EPA and agencies and programs of the Public Health Service) to assess whether adequate information on the health effects of chlorobenzene is available. Where adequate information is not available, ATSDR, in conjunction with the National Toxicology Program (NTP), is required to assure the initiation of a program of research designed to determine the health effects (and techniques for developing methods to determine such health effects) of chlorobenzene. [Pg.46]

Fig. 19.9 Sketch of the flow undivided electrochemical reactor working in batch recycle mode designed for the hydroxylation of chlorobenzene and phenol (Hsiao et al. 1993)... Fig. 19.9 Sketch of the flow undivided electrochemical reactor working in batch recycle mode designed for the hydroxylation of chlorobenzene and phenol (Hsiao et al. 1993)...
Equation (37) forms the basis for the initial design analysis of this system. Equation (38) is not used for the kinetic analysis because the system is isothermal. Because there is no input or output flow of benzene or chlorobenzenes, the material balances, by Eq. (37), become... [Pg.718]

Information flow diagram of mathematical model for chlorobenzene reactor-design example... [Pg.721]

Printout of PASCAL program for solution of chlorobenzene reactor-design example (Continued)... [Pg.725]

Plot of dimensionless concentration vs. time for chlorobenzene reactor-design example showing... [Pg.726]

Chlorobenzenes are also toxic substances that must be handled with care. Both benzene and solutions containing benzene or chlorobenzenes must be disposed of properly in a designated waste container. [Pg.346]


See other pages where Chlorobenzenes design is mentioned: [Pg.139]    [Pg.49]    [Pg.110]    [Pg.578]    [Pg.65]    [Pg.265]    [Pg.246]    [Pg.227]    [Pg.205]    [Pg.2459]    [Pg.53]    [Pg.59]    [Pg.78]    [Pg.409]    [Pg.326]    [Pg.160]    [Pg.718]    [Pg.719]    [Pg.321]    [Pg.358]    [Pg.578]    [Pg.3592]    [Pg.719]   


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Chlorobenzene

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