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Trans-exchange

If the disposition of hydroxyl groups is such that either an ethylene oxide or a hydrofuranol ring could be formed, then it is the threemembered anhydro ring that is preferentially established. Thus, if 6-tosyl-isopropylidene-D-glucofuranose (XII), in which there are present free hydroxyls at C3 and C5, is submitted to alkaline hydrolysis, it is the 5,6-anhydride VI alone that is formed the 3,6-anhydride appears only if the hydroxyl at C5 is protected by substitution as in X. [Pg.44]


It is interesting that for R = Me, carbamoyl-type complexes are obtained with the composition [NEt4][M MeNC(H)NMeCO (CO)4] with one CO group inserted between M and N as indicated by the CO stretching frequency of about 1642-1649cm 1 (M = Cr, Mo, W).87 The complexes are fluxional with cis/trans exchange of the terminal CO groups via a transition state of Q, or symmetry. [Pg.203]

The complexes Mo(CO)4(R-DAB) are not conformationally stable, as indicated by 13C NMR spectroscopy which shows cis-trans exchange of the carbonyl ligands, probably via a transition state with pseudo C4, symmetry.133... [Pg.209]

An interesting variation of this experiment involves using the same technique of NMR line-width measurements to study the cis-trans exchange rate in N,N-dimethylacetamide. By determining this rate as a function of temperature over the range 300 to 500 K, one can evaluate the rotational barrier for this cis-trans isomerization. ... [Pg.270]

Exdhange s. Interchange, Replacement, Trans... Exchangers s. Ion exchailgers Extraction s. Alkylation, extractive. Ion pair extraction... [Pg.266]

Table 8.2 EXSY experiments to explore the ds-trans exchange of alkyl-substituted metalla-cydes derived from terminal alkenes at -87°C (186K). Table 8.2 EXSY experiments to explore the ds-trans exchange of alkyl-substituted metalla-cydes derived from terminal alkenes at -87°C (186K).
Proton n.m.r. has been used to measure the exchange rate of methanol from cis and trans co-ordination sites of [Co(NCS)(MeOH)5]+. It is concluded that the exchange occurs from both types of co-ordination site without internal rearrangement of the complex, and that the cis and trans exchange rates are equal in addition, the exchange occurs exclusively between the bulk and bound environments. These results are markedly different from those reported previously for similar systems e.g. [Co(OH2)(MeOH)6] + and [CoCl(MeOH)5]+ in which the mean lifetime of a methanol molecule in the trans site is 0.59 times that for the cis). The reason for the difference is unclear. [Pg.295]

Hgura 7.10 A large overall temperature cross requires shells in series to reduce the cross in individual exchangers. (From Ahmad, Linnhoff, and Smith, Trans. ASME, J. Heat Transfer, 110 304, 1988 reproduced by permission of the American Society of Mechanical Engineers.)... [Pg.226]

Polley, G. T., Panjeh Shahi, M. H., and Jegede, F. O., Pressure Drop Considerations in the Retrofit of Heat Exchanger Networks, Trans. IChemE, part A, 68 211, 1990. [Pg.236]

Synthesis and Detailed Heat Exchanger Design, Trans. IChemE, part A, 69 445, 1991. [Pg.237]

In the physical separation process, a molecular sieve adsorbent is used as in the Union Carbide Olefins Siv process (88—90). Linear butenes are selectively adsorbed, and the isobutylene effluent is distilled to obtain a polymer-grade product. The adsorbent is a synthetic 2eohte, Type 5A in the calcium cation exchanged form (91). UOP also offers an adsorption process, the Sorbutene process (92). The UOP process utilizes ahquid B—B stream, and uses a proprietary rotary valve containing multiple ports, which direct the flow of Hquid to various sections of the adsorber (93,94). The cis- and trans-isomers are alkylated and used in the gasoline blending pool. [Pg.369]

F. Kamenetski, Diffusion and Heat Exchange in Chemical Kinetics, Princeton University Press, Princeton, N.J., 1955 trans. from Russian by Thanel. [Pg.531]

There are at least two mechanisms available for aziridine cis-trans isomerism. The first is base-catalyzed and proceeds via an intermediate carbanion (235). The second mechanism can be either thermally or photochemically initiated and proceeds by way of an intermediate azomethine ylide. The absence of a catalytic effect and interception of the 1,3-dipole intermediate provide support for this route. A variety of aziridinyl ketones have been found to undergo equilibration when subjected to base-catalyzed conditions (65JA1050). In most of these cases the cis isomer is more stable than the trans. Base-catalyzed isotope exchange has also been observed in at least one molecule which lacks a stabilizing carbonyl group (72TL3591). [Pg.72]

If the gas volume is not isothermal and is zoned, an additional magnitude, the gas-to-gas total-exchange area QGj, arises (see Hottel and Sarofim. Radiative Tran.sfer, McGraw-Hill, New York, 1967, chap. 11). Space does not permit derivations of special cases only the single-gas-zone system is treated here. [Pg.583]

For extended surfaces, which include fins mounted perpendicularly to the tubes or spiral-wound fins, pin fins, plate fins, and so on, friction data for the specific surface involved should be used. For details, see Kays and London (Compact Heat Exchangers, 2d ed., McGraw-HiU, New York, 1964). If specific data are unavailable, the correlation by Gunter and Shaw (Trans. ASME, 67, 643-660 [1945]) may be used as an approximation. [Pg.663]

Calculate the. shell-side heat-tran.sfer coefficient for the exchanger h, from... [Pg.1039]

Shell and Tube Heat Exchangers for General Piefineiy Seivices, API Standard 660, 4th ed., 1982, is published by the American Petroleum Institute to supplement both the TEMA Standards and the ASME Code. Many companies in the chemical and petroleum processing fields have their own standards to supplement these various requirements. The Jnterrelation.ships between Codes, Standards, and Customer Specifications for Proce.ss Heat Tran.sfer Equipment is a symposium volume which was edited by F. L. Rubin and pubhshed by ASME in December 1979. (See discussion of pressure-vessel codes in Sec. 6.)... [Pg.1065]


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Fluid Flow and Trans-membrane Exchange in a Hemodialyzer Module

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