Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Solvent excessive

Carbowax 20M, polysiloxanes, and N-cyclo-3-azetidinol are the most widely used sutetances for the thermal degradation method [143,180,192-194]. In the case of the Carbowax treatment deactivation can be carried out in either of two ways. The column can be dynamically coated with a solution of Carbowax 20H in a volatile solvent, excess solvent evaporated with a stream of nitrogen, the column ends sealed and the column heated at about... [Pg.77]

Solvent displacement, and isotherms. 954. 955 Solvent excess entropy at the interface, 912 Solvent interactions, 923, 964 Soriaga, M., 1103, 1146 Specifically adsorbed ions, 886 Spectrometer, 797 Spikes, electrodeposition. 1336 Spillover electrons, of metal, 889 Spiral growth, electrodeposition, 1316, 1324, 1326, 1324,1328 s-polarized light, 802 Srinivasan, S 1439,1494 Standard electrode potential American convention, 1354 convention, 1351 rUPAC convention, 1355 prediction of reactions, 1359 the zinc-minus and copper-plus convention, 1352... [Pg.50]

Guidelli model of, 899 Habib and Bockris, 899 at the interface, importance of, 918 -ion interaction energy, 924 -metal interactions, 896 chemical forces, 897, 972 lateral forces, 897 monomers of, definition, 899 orientation of, 898 Parsons model of, 899 and potential of the electrode. 900. 924 preferential orientation of, 912 and solvent excess entropy, 912 the "three-state water model 898, 899 Wave nature of electrons, 788 Wavenumber, 799 Waves... [Pg.53]

Solvent Excess Entropy of the Interface A Key to Obtaining Structural Information on Interfacial Water Molecules... [Pg.195]

Caution Potassium and potassium-graphite laminate (C8K) are pyrophoric and react violently with water, low molecular weight alcohols, and chlorinated solvents. They must be handled with care and used in strictly anhydrous solvents. Excess K or C8K can be safely destroyed by suspending them in anhydrous THF and slowly adding an excess of isopropanol (technical grade). [Pg.299]

In order to take advantage of this purification effect and to optimise the water content of the iodine-rich phase, CEA has proposed to use a counter-current reactor to perform the Bunsen reaction. This idea arises from the consideration that, aside from S02, the chemical system includes two almost immiscible solvents (excess water and excess iodine) and two solutes (H2S04 and HI). Bunsen reactor... [Pg.168]

Pattern Development. The development of patterns exposed in thin films of PVTMSK was diflScult because of its high solubility in almost all organic solvents. Excessive thinning of the unexposed areas could be prevented by carrying out the development at low temperatures either by spray development with a 2-propanol mist while the wafer is spinning at 1000-2500 rpm or by dip development in 2-propanol at + 5 C. Spray development cooled the wafer to as low as 8-10 °C because of the fast evaporation of the solvent, but even at such low temperatures and short development times (5-15 s), a nonuniform thinning of the film occurred. [Pg.701]

Extractive Distillation Recovery of Isoprene. A typical flow-sketch and material balance of distillation and solvent recovery towers for extracting isoprene from a mixture of cracked products with aqueous acetonitrile appears in Figure 13.25. A description of the flowsheet of a complete plant is given in Example 2.9. In spite of the fact that several trays for washing by reflux are provided, some volatilization of solvent still occurs so that the complete plant also has water wash columns on both hydrocarbon product streams. A further complication is that acetonitrile and water form an azeotrope containing about 69 mol % solvent. Excess water enters the process in the form of a solution to control poly-... [Pg.444]

Oxaspiro(cyclopropane-l, 5 -bicyclo[4.3.0]nonane-3, 7, 9 -trione) (2-Trimethylsiloxy)allylidenecyclo-propane (870 mg, 5,2 mmol) and maleic anhydride (1.0 g, 10.2 mmol) in benzene (3 mL) were heated in a sealed glass tube under argon at 130 °C for 24 h. After evaporation of the solvent excess maleic anhydride was sublimed off, the residue dissolved in EtjO (30 mL) and the mixture left to crystallize at 0 °C. The precipitate was washed with cold EtjO, recrystallized (EtjO) and dried yield 685 mg (68%) mp 75°C. [Pg.1567]

When the Gibbs adsorption approach is applied to any monolayer in which the Gibbs dividing plane is located, where n = 0 for the solvent excess, then we have, from Equation (225)... [Pg.184]

There are times when excess starting material can serve as the solvent. Excess liquid chlorine has been used in the chlorination of natural rubber to eliminate the need for the usual carbon tetrachloride.42 It is difficult to remove the last traces of carbon tetrachloride from the chlorinated rubber. The dimethyl terephthalate and terephthalic acid used in the preparation of polyethylene terephthalate) (8.1) are made by the oxidation of xylene.43... [Pg.203]

The most explicit recognition of macromolecular energies as surface energies of solvent excess or deficit is in the work of Blank (28, 29), who showed the essential equivalence of Gibbs adsorption isotherms and the changes in the energy of alternate protein states. [Pg.187]

After every reaction step, the product can be extracted from the organic phase with fluorinated solvents. Excess reagents remain in the organic phase and can be easily removed. The strategy has also been successfully used in a Ugi multicomponent-type reaction condensing derivatised benzoic acid 31 with amines, aldehydes and isonitriles as shown in Scheme 3.3.2. The reaction was carried out in TFE and products 32 were isolated by liquid-liquid extraction. After cleavage of the fluorinated chain with TBAF followed by another extraction, the desired products 33 were isolated in good to excellent yields and with purities >80% (determined by GC). [Pg.223]

FIGURE 9.2. In the Gibbs approach to detming the surface excess concentration, the Gibbs dividing surface (GDS) is defined as the plane in which the solvent excess concentration becomes zero (the shaded area is equal on each side of the plane) as in (a). The surface excess of component i wiU then be the difference in the concentrations of that component on either side of that plane (the shaded area) (i>). [Pg.182]

Seal incompatibility with one or more of the solvents Excessive baseline noise, short column life time Mixers and damper Replace the seal with another seal compatible with the solvents used... [Pg.1957]


See other pages where Solvent excessive is mentioned: [Pg.279]    [Pg.141]    [Pg.90]    [Pg.878]    [Pg.196]    [Pg.639]    [Pg.232]    [Pg.420]    [Pg.281]    [Pg.82]    [Pg.168]    [Pg.668]    [Pg.127]    [Pg.279]    [Pg.7]    [Pg.294]    [Pg.5]    [Pg.420]    [Pg.420]    [Pg.420]    [Pg.90]    [Pg.377]    [Pg.90]    [Pg.539]    [Pg.279]    [Pg.842]    [Pg.167]    [Pg.667]    [Pg.242]    [Pg.292]    [Pg.118]    [Pg.121]    [Pg.123]    [Pg.245]    [Pg.20]   
See also in sourсe #XX -- [ Pg.59 , Pg.60 ]




SEARCH



Excess solvent

Excess solvent

Excessive Solvent Use

Solvent excess function

Solvent medium effects and excess polarizabilities

© 2024 chempedia.info