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Requirements for Separation

The voltage used for electro dialysis is about 1 V per membrane pair, and the current flux is of the order of 100 A/m of membrane surface. The total power requirement increases with the feedwater salt concentration, amounting to about 10 MW per m product water per 1000 ppm reduction in salinity. About half this power is required for separation and half for pumping. Many plant flow arrangements exist, and their description can be found, along with other details about the process, in References 68 and 69. Many ED plants, as large as 15,000 vsf jd, are in operation, reducing brackish water concentration typically by a factor of 3—4. [Pg.253]

The macrocyclic antibiotic-based CSPs have not been used extensively in SFC. Two macrocyclic antibiotic CSPs, Chirobiotic T and Chirobiotic V, were included in a study of various CSPs in SFC. At least partial resolution of approximately half of the 44 test compounds could be obtained on these two CSPs in SFC [63]. A high concentration of modifier was necessary to elute some of the analytes. Enantioreso-lution of derivatized amino acids was also demonstrated in the same study. Flowever, a complex modifier comprised of methanol, water, and glycerol was required for separations performed on the Chirobiotic T CSP. The separation of coumachlor enantiomers on a vancomycin-based CSP (Chirobiotic V) in SFC is illustrated in Fig. 12-5 [32]. [Pg.310]

The manufacturer requires complete solids and/or liquids data, feed size analysis, and requirements for separation. In some instances, it may be best to have a sample tested by the manufacturer in their laboratory. [Pg.266]

In order to classify this diversity from the viewpoint of the separator, the basic requirements for separators in alkaline cells are discussed below and an attempt at structuring them accordingly is made. [Pg.282]

Figure 1 shows the results obtained by Qian et al. [1 ] in a process when AFM probe approaches and then separates from a SiQ2 substrate. The normal force required for separating the probe-substrate contact reads 33 nN. From a thermodynamic point of view, adhesion is in fact a state of the system at the energy minimum when the contact pairs interact with each other through interface, and additional work has to be applied to change the state of the system. [Pg.167]

Once equilibrium in the reagent mixture is attained, centrifugation in a common laboratory centrifuge, followed by decantation of the supernatant is all that is required for separation of bound and free label. [Pg.60]

The most widely used approach for the separation of enantiomers by TLC is based on a ligand exchange mechanism using commercially available reversed-phase plates impregnated with a solution of copper acetate and (2S,4R,2 RS)-4-hydroxy-l-(2-hydroxydodecyl)proline in optimized amounts. Figure 7.9 (10,97,98,107-109). Enantiomers are separated based on the differences in the stability of the diastereomeric complexes formed between the sample, copper, and the proline selector. As a consequence, a prime requirement for separation is that the seumple must be able to form complexes with copper. Such compounds include... [Pg.858]

For microbore HPLC, with a flow of less than lOOpLmin-1, off-line LC-FT1R has been developed using matrix isolation techniques. The solutes are deposited on a moving IR salt window [504] or on a rotating plated disc [486], and are measured afterwards with the aid of a FITR microscope or a reflectance accessory. FTIR detection was first applied to the analysis of microbore HPLC eluent by Teramae and Tanaka [505]. In microbore HPLC-FTIR the amount of mobile phase required for separation is much less than for conventional scale HPLC. This simplifies both flow-cell and mobile-phase elimination interfaces. Flow-cell... [Pg.492]

Apotex wove these facts into a prima facie case of obviousness as follows It would be obvious to separate an enantiomer from a known racemate using generally known techniques. Furthermore, there was motivation [19] to do so because enantiomers can have different properties from those displayed by the racemate, and because of a possible future FDA regulatory requirement for separation of enantiomers. Additionally, there was a reasonable expectation of success [20] in achieving the separation because techniques for separating enantiomers from racemates are known. And finally, it would be obvious to form an addition salt of the enantiomer to optimize selected physical properties. Thus, concluded Apotex, dextrorotatory clopidogrel bisulfate was obvious, it is therefore unpatentable, and this renders the 265 patent invalid. [Pg.456]

Electrophoresis can be carried out using paper or a gel as the supporting medium. Typically, it can only be carried out in media compatible with water because buffers or salt solutions are required to carry the electric current required for separation. CE is carried out in a fused-silica capillary filled with buffer. [Pg.285]

Based on the previous analysis of the different transport phenomena, which determine the overall mass transport rate, the structure of the solid phase matrix is of extreme importance. In the case of any chromatographic process, the different diffusion restrictions increase the time required for separation, since any increase of the flow rate of the mobile phase leads to an increase of the peak broadening [12]. Thus, the improvement of the existing chromatographic separation media (column packing of porous particles) and hence the speed of the separation should enable the following tasks ... [Pg.171]

Maleimide-functionalized peptides react quantitatively with thiols and thus with di-fatty acid substituted thioglycerol, a fact which facilitates purification of the amphiphilic lipopeptide derivatives by simple precipitation as required for separation of the excess lipid building block (Scheme 16).t163 164 167l... [Pg.365]

The Fairbrother separator A simple device was required for separating the contents of the anode and cathode chambers after an... [Pg.47]

Thin films (qv) of vitreous silica have been used extensively in semiconductor technology. These serve as insulating layers between conductor stripes and a semiconductor surface in integrated circuits, and as a surface passivation material in planar diodes, transistors, and injection lasers. They are also used for diffusion masking, as etchant surfaces, and for encapsulation and protection of completed electronic devices. Thin films serve an important function in multilayer conductor insulation technology where a variety of conducting paths are deposited in overlay patterns and insulating layers are required for separation. [Pg.512]

Figure 6.4 Mass resolution required for separation of atomic ions a) from oxide ions and b) from diatomic argon ions. Figure 6.4 Mass resolution required for separation of atomic ions a) from oxide ions and b) from diatomic argon ions.
The scale-up of chromatography separation means increasing the recovered amount of a target that satisfies the required purity per unit time. This can be achieved by simply increasing the column diameter, and also by shortening the time required for separation, and/or by increasing the sample volume applied to a column [9]. [Pg.245]

In the first, droplets separate from the earner vapor when the gravity force overcomes the Ruid drag force. The minimum requirement for separation occurs when the gravitv force balances the drag force, at which point the droplets fall at a constant terminal velocity. U,. [Pg.103]

Analysis time, t The minimum time required for separation. [Pg.21]

An alternative workup procedure takes advantage of the solubility of the lactone in MeOH. Upon completion of the reaction, the residual oil was dissolved in EtOAc and washed with 5% aq citric acid (50 mL), H20 (2 x 50 mL), 5% NaHC03 (50 mL), and H20 (2 x 50 mL). The organic phase was dried and concentrated, and the oil triturated with MeOH to afford the crystalline product yield 4.9 g (55%). The latter workup procedure, while very simple and economic, cannot be applied to other N-protected lactones, e.g. to the TV-Boc-4-hydroxy proline lactone, where careful flash chromatography was required for separation of other polar byproducts including Ph3PO. [Pg.66]


See other pages where Requirements for Separation is mentioned: [Pg.342]    [Pg.179]    [Pg.276]    [Pg.252]    [Pg.416]    [Pg.213]    [Pg.125]    [Pg.545]    [Pg.165]    [Pg.122]    [Pg.39]    [Pg.584]    [Pg.299]    [Pg.343]    [Pg.53]    [Pg.438]    [Pg.123]    [Pg.458]    [Pg.484]    [Pg.32]    [Pg.169]    [Pg.183]    [Pg.64]    [Pg.330]    [Pg.350]    [Pg.147]    [Pg.429]    [Pg.206]   


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Aspects of Mechanisms, Processes, and Requirements for Zeolite Separation

Energy required for separation

Energy requirement for separation

Minimum energy required for separation

Reducing energy required for separation

Separation requirements

Solvent requirements for different TLC separation chambers

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