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Toluene from benzene

Figure 1.7 An initial structure for the manufacture of benzene from toluene and hydrogen incorporating some redundant features. Figure 1.7 An initial structure for the manufacture of benzene from toluene and hydrogen incorporating some redundant features.
Reactor yield of benzene from toluene = ( luene fed to the reactor)... [Pg.24]

An example of where recycling can be effective in improving selectivity is in the production of benzene from toluene. The series reaction is reversible. Hence recycling diphenyl to the reactor can be used to suppress its formation at the source. [Pg.39]

Example 4.6 Calculate the process jueld of benzene from toluene and benzene from hydrogen for the approximate phase split in Example 4.2. [Pg.125]

Toluene. Toluene, e from sulphur compounds, may be purchased. If required dry, it is treated with anhydrous calcium chloride, followed by sodium wire (see under Benzene, 15). [Pg.173]

Estimate the chain transfer constants for styrene to isopropylbenzene, ethylbenzene, toluene, and benzene from the data presented in Fig. 6.8. Comment... [Pg.391]

The Tatoray process, which was developed by Toray Industries, Inc., and is available for Hcense through UOP, can be appHed to the production of xylenes and benzene from feedstock that consists typically of toluene [108-88-3] either alone or blended with aromatics (particularly trimethylbenzenes and ethyl-toluenes). The main reactions are transalkylation (or disproportionation) of toluene to xylene and benzene or of toluene and trimethylbenzenes to xylenes in the vapor phase over a highly selective fixed-bed catalyst in a hydrogen atmosphere at 350—500°C and 1—5 MPa (10—50 atm). Ethyl groups are... [Pg.52]

Toluene, Benzene, and BTX Reeoveiy. The composition of aromatics centers on the C - and Cg-fraction, depending somewhat on the boihng range of the feedstock used. Most catalytic reformate is used directiy in gasoline. That part which is converted to benzene, toluene, and xylenes for commercial sale is separated from the unreacted paraffins and cycloparaffins or naphthenes by hquid—hquid extraction or by extractive distillation. It is impossible to separate commercial purity aromatic products from reformates by distillation only because of the presence of azeotropes, although comphcated further by the closeness in boihng points of the aromatics, t/o-paraffin, and unreacted C -, C -, and Cg-paraffins. [Pg.179]

Tables 14 and 15 show historical U.S. prices for nitration- and commercial-grade toluene, respectively, from 1976 to 1995. The minimum price for the toluene used in chemicals is set by its value in unleaded gasoline, which is the principal use. The ceiling price is set by the relative values of benzene and toluene. When the value of benzene is such that the differential between benzene and toluene exceeds the cost of converting toluene to ben2ene, then the price of toluene is set by its value for the conversion to benzene. A differential of 91.00/t (ca 0.30/gal) is generally needed to make conversion of toluene to benzene economically attractive. Tables 14 and 15 show historical U.S. prices for nitration- and commercial-grade toluene, respectively, from 1976 to 1995. The minimum price for the toluene used in chemicals is set by its value in unleaded gasoline, which is the principal use. The ceiling price is set by the relative values of benzene and toluene. When the value of benzene is such that the differential between benzene and toluene exceeds the cost of converting toluene to ben2ene, then the price of toluene is set by its value for the conversion to benzene. A differential of 91.00/t (ca 0.30/gal) is generally needed to make conversion of toluene to benzene economically attractive.
Rapid, simple, quaUtative methods suitable for determining the presence of benzene in the workplace or surroundings have been utilized since the 1930s. Many early tests offered methods for detection of aromatics but were not specific for benzene. A straightforward test allowing selective detection of benzene involves nitration of a sample to y -dinitrobenzene and reaction of the resultant ether extract with an ethanoHc solution of sodium hydroxide and methyl ethyl ketone (2-butanone), followed by the addition of acetic acid to eliminate interferences from toluene and xylenes. Benzene imparts a persistent red color to the solution (87). The method is claimed to be sensitive to concentrations as low as 0.27 ppm benzene from 10 mL air samples. [Pg.46]

Extractive distillation, using similar solvents to those used in extraction, may be employed to recover aromatics from reformates which have been prefractionated to a narrow boiling range. Extractive distillation is also used to recover a mixed ben2ene—toluene stream from which high quaUty benzene can be produced by postfractionation in this case, the toluene product is less pure, but is stiU acceptable as a feedstock for dealkylation or gasoline blending. Extractive distillation processes for aromatics recovery include those Hsted in Table 4. [Pg.312]

Under tlicse conditions, one could expect 1.38 additional cases of cancer per 10,000, or 138 additional cases of cancer per 1,000,000 people exposed to toluene and benzene from tliis source. [Pg.419]

In the early days of organic chemistry, the word aromatic was used to describe such fragrant substances as benzaldehyde (from cherries, peaches, and almonds), toluene (from Tolu balsam), and benzene (from coal distillate). It was soon realized, however, that substances grouped as aromatic differed from most other organic compounds in their chemical behavior. [Pg.516]

Tyramine is an alkaloid found, among other places, in mistletoe and ripe cheese. How would you synthesize tyramine from benzene From toluene ... [Pg.968]

Low substrate selectivity accompanying high positional selectivity was also found in isopropylation of a range of alkyl and halogenobenzenes by /-propyl bromide or propene in nitromethane, tetramethylene sulphone, sulphur dioxide, or carbon disulphide, as indicated by the relative rates in Table 86. The toluene benzene reactivity ratio was measured under a wide range of conditions, and varied with /-propyl bromide (at 25 °C) from 1.41 (aluminium chloride-sulphur... [Pg.150]

Nesmeyanov et a/.546 have also measured the effects of substituents in deuteration of ferrocene by deuterated trifluoroacetic acid in dichloromethane at 25 °C. Rate coefficients were measured for ferrocene and its derivative in a range of such acid mixtures, the composition of which was omitted, and in some cases the rate of exchange for ferrocene was calculated on the basis of a linear relationship between log and —H0. Results including the calculated knl values are given in Table 161. It should be noted that, in discussing those results, the authors quoted the incorrect partial rate factors for dedeuteration of toluene arising from the use of the incorrect data for benzene (see p. 199). This should be taken into account... [Pg.249]

To confirm the production of benzene from the decomposition reaction of methyl(triphenylmethyl)dichlorosilane, the decomposition reaction of methyKdi-phenylmethyl)dichlorosilane in the presence of aluminum chloride was carried out in toluene solvent at 80 C. In this reaction, the exchange reaction between phenyl groups on the methyl group of (diphenylmethyl)(inethyl)dichlorosilane and toluene occurred to give [phenyl(tolyl)methylJ(methyl)dichlorosilane and (di-tolylmethyl)(methyl)dichlorosiIane (Scheme 1). " ... [Pg.175]

Grob K, Frauenfelder C, Artho A. 1990. Uptake by foods of tetrachloroethylene, trichloroethylene, toluene, and benzene from air. Z Lebensm Unters Forsch 191 435-441. [Pg.269]

Johnson GR, RH Olsen (1995) Nucleotide sequence analysis of genes encoding a toluene/benzene-2-mono-oxygenase from Pseudomonas sp. strain JS150. Appl Environ Microbiol 61 3336-3346. [Pg.140]

If the primary function of the column is to separate the benzene from the other components, the maximum toluene and xylene in the overheads would be specified say, at 5 kg/h and 3 kg/h, and the loss of benzene in the bottoms also specified say, at not greater than 5 kg/h. Three flows are specified, so the other flows can be calculated. [Pg.44]

Figure 1.9 A superstructure for the manufacture of benzene from toluene and hydrogen incorporating some redundant features. (From Kocis GR and Grossman IE, 1988, Comp Chem Eng, 13 797, reproduced by permission.). Figure 1.9 A superstructure for the manufacture of benzene from toluene and hydrogen incorporating some redundant features. (From Kocis GR and Grossman IE, 1988, Comp Chem Eng, 13 797, reproduced by permission.).

See other pages where Toluene from benzene is mentioned: [Pg.180]    [Pg.180]    [Pg.9]    [Pg.209]    [Pg.2419]    [Pg.94]    [Pg.47]    [Pg.47]    [Pg.478]    [Pg.175]    [Pg.179]    [Pg.185]    [Pg.191]    [Pg.2099]    [Pg.585]    [Pg.434]    [Pg.269]    [Pg.269]    [Pg.166]    [Pg.150]    [Pg.151]    [Pg.183]    [Pg.586]    [Pg.330]    [Pg.94]    [Pg.398]    [Pg.11]    [Pg.82]   
See also in sourсe #XX -- [ Pg.284 ]




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Benzene from toluene disproportionation

Benzene production from toluene

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Toluene separation from benzene

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