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Xylenes, separation

Complex Formation. AH four Cg aromatic isomers have a strong tendency to form several different types of complexes. Complexes with electrophilic agents ate utilized in xylene separation. The formation of the HE-BF —MX complex is the basis of the Mitsubishi Gas—Chemical Company (MGCC) commercial process for MX recovery, discussed herein. Equimolar complexes of MX and HBr (mp — 77°C) and EB and HBr (mp — 103°C) have been reported (32,33). Similatly, HCl complexes undergo rapid formation and decomposition at —80°C (34). [Pg.414]

Fig. 9. Xylenes separation via Mitsubishi Gas—Chemical Co. HF-BF extraction—isomerization process (107). A = extractor B = decomposer C = separator D = isomerization reactor E = heavy ends tower F = raffinate tower G = separator H = light ends fractionator ... Fig. 9. Xylenes separation via Mitsubishi Gas—Chemical Co. HF-BF extraction—isomerization process (107). A = extractor B = decomposer C = separator D = isomerization reactor E = heavy ends tower F = raffinate tower G = separator H = light ends fractionator ...
Another approach is the simulated moving-bed system, which has large-volume appHcations in normal-paraffin separation andpara- s.yXen.e separation. Since its introduction in 1970, the simulated moving-bed system has largely displaced crystallisation ia xylene separations. The unique feature of the system is that, although the bed is fixed, the feed point shifts to simulate a moving bed (see Adsorption,liquid separation). [Pg.86]

The distillate (overhead) from Unit H, containing mosdy ethylben2ene [100-41 -4] p-xy en.e and / -xylene, and some o-xylene becomes the feed for the -xylene separation process (UnitJ). [Pg.312]

Although MIL-47, and especially MIL-53(A1), had been found on many occasions to dynamically respond to adsorption of particular compounds, referred to as breathing [35] in the literature, in these liquid phase conditions, only minor changes of the lattice parameters have been observed. A study of xylene separations in vapor phase on MIL-5 3(A1) shows that breathing profoundly influences the shape of the obtained breakthrough profiles as a function of adsorbate concentration [97]. [Pg.87]

Solution Although the relative volatilities are recalculated for each column, Table 11.7 shows the relative volatilities of the feed mixture to the sequence at a pressure of 1 atm. This shows clearly that the ethyl benzene/xylenes separation is by far the most difficult with relative volatilities for the xylenes close to unity. The volatilities of the components are such that all separations can be carried out at atmospheric pressure and at the same time allow the use of cooling water in the condensers. Thus, column pressures are fixed to atmospheric pressure with the relative volatilities... [Pg.216]

Co-exposure to -hexane and xylene resulted in a loss of auditory sensitivity in male Sprague-Dawley rats (Nylen et al. 1994) as measured by the auditory brainstem response. Exposure to -hexane or xylene alone at 1,000 ppm for 61 days for 18 hours a day caused a slight loss of auditory sensitivity when measured 2 days after the end of exposure. Simultaneous exposure to w-hexane and xylene (1,000 ppm each) caused a greater and persistent loss of auditory sensitivity which was greater than the sum of effects of exposure to w-hexane and xylene separately. These effects were still observed 4 and 10 months after exposure ended. In contrast, combined exposure to -hexane and xylene partially reversed the decreased nerve conduction velocities and action potential amplitudes observed in the group treated with 77-hexane alone. These effects were persistent from 2 days to 10 months after cessation of exposure. [Pg.155]

TOLUENE/O-XYLENE SEPARATION AT 90 MM HC RIGOROUS VAPOR-HYDRAULIC MODEL (VAPOR RATES calculated from pressure drop through TRAYS) USING LSODE IMPLICIT STIFF INTEGRATOR PROGRAM ASSUMPTIONS ... [Pg.144]

Zinnen, H.A. (1990) Zeolitic para-xylene separation with diethyltoluene heavy desorbent. U.S. Patent 4,864,069. [Pg.197]

Until late 1990s, purified m-xylene was produced predominantly by the HF/BF3 process developed by Mitsubishi Gas Chemical Co. The separation is based on the complex formation between m-xylene and solvent HF/BF3. However, concerns about the process operation, environment, metallurgy and safety render the process commercially unattractive due to its use of HF/BF3. These concerns led to many developments in the adsorptive separation process for m-xylene separation [3-8]. The UOP MX Sorbex process, developed by UOP and commercialized in 1998, already accounts for more than 70% of the world s m-xylene capacity. A 95% m-xylene recovery with 99.5% purity can be achieved by the MX Sorbex process. [Pg.205]

The ultimate in xylene separation is claimed, however, by Hetzner (10), who first distills the mixture to remove o-xylene by taking m-p-xylene and ethylbenzene overhead in a column having about 35 to 60 theoretical plates. It is reported that concentrates containing up to 97% o-xylene have been produced by this process. The m-xylene, p-xylene, and ethylbenzene mixture is selectively sulfonated to remove m-xylene. In this operation, 2 moles of Sulfuric acid (96 to 98%) are added per mole of m-xylene in the mixture to be treated. After separation, the aqueous layer is hydrolyzed at 250° to 300° F. to recover a concentrate containing 90% or more m-xylene. The hydrocarbon layer is cooled to produce p-xylene crystals, which are separated by filtration or centrifugation. The 85 to 90% p-xylene concentrate is reprocessed to recover a final product containing 96% p-xylene. The mother liquor from the p-xylene crystallization contains impure ethylbenzene and is rejected from the system. [Pg.309]

At least one commercial installation for p-xylene separation is operating (3), and others are under consideration. m-Xylene, however, appears to sustain only a limited interest at the present time, and is available only in pilot unit quantities. [Pg.309]

In the manufacture of terephthalic acid by the oxidation of p-xylene, separation of the xylene from its isomeric mixture is necessary (see Section 2.5.2). An alternative process introduced in Japan uses the oxidation of p-tolualdehyde, which is obtained in good regioselectivity by the HF—BF3 catalyzed carbonylation of toluene without the necessity of separation of the isomers. [Pg.515]

Xylene Separation-U.O.P. s Parex Process. The continued rapid increase in the p-xylene demand as a raw material for polyester products in... [Pg.313]

Sr. Ba" Sr21 Ba22[( A102)86(Si02) io ] 12-ring 8.0 Xylene separation... [Pg.496]

Complex Formation. All four Cx aromatic isomers have a strong tendency to form several different types of complexes. Complexes with electrophilic agents are utilized in xylene separation. [Pg.1765]

Igarashi, Y. and T. Ueno A New Xylene Separation Process, ACS Meeting, Atlantic City, NJ. 1968. [Pg.1766]

Separation of xylenes separation of lower-molecular-weight aromatic hydrocarbon isomers, especially at the lower area of the nematic region. [Pg.59]


See other pages where Xylenes, separation is mentioned: [Pg.1078]    [Pg.1078]    [Pg.300]    [Pg.313]    [Pg.323]    [Pg.1029]    [Pg.247]    [Pg.242]    [Pg.313]    [Pg.314]    [Pg.496]    [Pg.496]    [Pg.496]    [Pg.992]    [Pg.32]    [Pg.32]    [Pg.96]    [Pg.81]    [Pg.83]    [Pg.84]   
See also in sourсe #XX -- [ Pg.56 , Pg.194 ]

See also in sourсe #XX -- [ Pg.202 ]

See also in sourсe #XX -- [ Pg.115 ]




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Hydrocarbon processing xylene isomer separation

Paraxylene xylenes separation

Petrochemical industry xylene isomer separation

Polymeric membranes, xylene isomers separation

Separation of Xylenes Isomers by Selective Adsorption on FAU Type Zeolite

Separation of xylenes

Separation p-xylene

Separation para-xylene

Solvent recovery xylene separation

Xylenes isomer separation

Xylenes separation by crystallization

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