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Purification table

Synthesis gas preparation consists of three steps ( /) feedstock conversion, (2) carbon monoxide conversion, and (2) gas purification. Table 4 gives the main processes for each of the feedstocks (qv) used. In each case, except for water electrolysis, concommitant to the reactions shown, the water-gas shift reaction occurs. [Pg.340]

Advantage was taken of these solubility differences in refining mixtures of the chlorinated dibenzodioxins. Digestion with boiling chloroform was effective in removing trichlorodibenzodioxin while recrystallization from anisole reduced the penta-substituted isomer content. In a typical purification (Table II) these two procedures were alternated through four cycles. The assays were made by mass spectroscopy using the batch injection method to introduce the sample into the spectrometer. X-ray studies 14) confirmed the structure. [Pg.4]

Table 2. Purification Table of AMDase from A. bronchisepticus... Table 2. Purification Table of AMDase from A. bronchisepticus...
Table II. Purification Table for the Manganese Peroxidase (Ligninase) Isolated from Lentinula edodes Cultures Grown on a Commercial Wood Medium ... Table II. Purification Table for the Manganese Peroxidase (Ligninase) Isolated from Lentinula edodes Cultures Grown on a Commercial Wood Medium ...
After each purification step, the activity of the preparation (in units of enzyme activity) is assayed, the total amount of protein is determined independently, and the ratio of the two gives the specific activity. Activity and total protein generally decrease with each step. Activity decreases because some loss always occurs due to inactivation or nonideal interactions with chromatographic materials or other molecules in the solution. Total protein decreases because the objective is to remove as much unwanted or nonspecific protein as possible. In a successful step, the loss of nonspecific protein is much greater than the loss of activity therefore, specific activity increases even as total activity falls. The data are then assembled in a purification table similar to Table 3-5. A protein is generally considered pure... [Pg.95]

Purification of an Enzyme A biochemist discovers and purifies a new enzyme, generating the purification table below. [Pg.114]

The yield from any purification step may be reported as total protein, percentage of total activity, or change in specific activity. The yield information from progressive purification steps is used to construct a purification table (e.g., see Table B4.2.1). [Pg.279]

Purification protocols should always aim for brevity, to minimize complexity and cost. The goal of the protein purification procedure, besides a pure protein, is a purification table listing all the operations undertaken, with results on overall yield, specific activity, and purification factor. An assay for both protein function and protein concentration is required at every step. [Pg.210]

The purification table (Table 8.4) can be regarded as typical for a novel biocatalyst with unknown properties. [Pg.237]

The second example describes another redox enzyme, L-amino acid oxidase, which oxidizes L-amino acids to a-keto acids. Table 8.5 lists the results in a purification table, and Figure 8.9 describes the SDS-PAGE results. [Pg.238]

The purification table reveals that the first operation, anionic chromatography over a Macro Q column, either activates the enzyme or binds and removes inhibitors to yield 131% yields in excess of 100% are not uncommon in initial purifications steps. The purification factor of 144 after the third step indicates that the enzyme was not purified from an overexpressed gene but rather obtained from a non-recombinant strain. The SDS-PAGE diagram (Figure 8.9) reveals. The specific activity after the final step (4.6 U mg-1) is rather low. [Pg.238]

Examples of Biocatalyst Purification P 239 Table 8.5 Purification table for L-amino acid oxidase from Rhodococcus opacus. [Pg.239]

Table 8.6 Purification table for xylose isomerase from Thermoanaerobium strain JW/SL-YS 489. Table 8.6 Purification table for xylose isomerase from Thermoanaerobium strain JW/SL-YS 489.
Both the purification table and the electropherograms make it clear that ... [Pg.240]

For split generation we make use of heuristics, as given in Table 3.1. The removal of troublesome impurities is suggested in the first place, here H2S, benzene and chloro-ethane. Then the split is placed in an appropriate selector, in this case of type purification . Table 3.3 indicates that six separation methods could be applied to perform this task chemical absorption, molecular-sieve adsorption, physical adsorption, catalytic oxidation, catalytic hydrogenation and chemical treatment. [Pg.68]

The forthcoming description of catalysts and catalytic processes should only serve as a primer towards understanding the basic principles with some examples of applications in the field of petroleum processing, chemical production, and environmental air purification. Table 7.1 gives a list of some of the many commercial catalytic applications. [Pg.272]

SA in Table II - nmoles/hr/mg protein and N.D - not detectable. Tobacco, soy cultures and barley seedlings were the best source of ALS, both in terms of specific activity and total units. The enzyme preparations from all sources were unstable in buffer solutions in spite of protective thiol agents. The inactivation of ALS in the crude extract of tobacco showed a distinct biphasic kinetics, implying the presence of at least two isozymes (unpublished observations). The presence of two ALS genes in tobacco (29) and at least three in microorganisms (18) has also been noted by other workers. ALS from barley was most amenable to purification. Table III gives a profile for the rapid purification of this enzyme with high recovery. [Pg.275]

As has been shown there are a number of pollutants that have undergone gaseous photocatalytic oxidation and the research within this field is continually progressing. Unlike water photocatalytic oxidation which has found application on both a scientific and industrial basis gaseous PCO development has currently been limited to terrestrial indoor air purification (Table 2). The vast majority of industrial development and application is confined to Japan and the USA. [Pg.410]

Three other purification methods have been described in the literature—for cucumber 16) and for the enzyme from green squash 17,18). Table I summarizes the salient molecular properties of ascorbate oxidase purified according to the different procedures mentioned above. A detailed purification table is presented in References 15 and 18, and includes the enzyme yield calculated on the basis of total protein present in the crude juice. The yield is 14% for the method of Lee and Dawson... [Pg.226]

Methocell E4M, E50LV, and E4M (food grade) from The Dow Chemical Company were kindly supplied by Colorcon-Argentina and used without purification. Table 29.1 shows some characteristic properties, namely, the methyl/hydrox)/propyl ratio and the viscosity (25°C) of 1% wt solutions. [Pg.456]

Uninteresting proteins are in principle just as difficult to purify as interesting ones. Hence, the protein purifier without long-term employment searches for a protein whose purification catches the attention of wider circles. This is often possible. The first purification of a protein makes an impression, above all when you can present the purification briefly and clearly, with a purification table and a band pattern on the SDS gel. [Pg.109]

PV technology can be used for product separation or purification (Table 9.1). Membrane PV process was also used for the enhanced separation of fuel oils (Kujawski et al. 2002). For this process, a commercial hydrophilic membrane was used. PV technology is being developed for the treatment of brackish groundwater... [Pg.266]

Copol5miers prepared by grafting of monomers after ozonization always show some amounts of homopolymers due to the thermal or hydroperoxide initiation. Authors have tested the compatibUizing effect of copolymer, after or before purification. Table 3 summarizes our results for PEl/PVC blends to which 5 wt% of P(EgMMA) copolymer, grafted with 50% PMMA, was added. [Pg.148]

Table 2. Purification table of KAS II from oil palm mesocarp. Table 2. Purification table of KAS II from oil palm mesocarp.
A series of reactions was next conducted, systematically lowering the equivalence of the boronic ester 84 used. It was found that lowering the ratio of 84 94 increased the isolated yield of 43, by increasing the ease of chromatographic purification (Table 2.1, Entries 3-6). 2 equivalents of 84 gave an excellent 95 % yield... [Pg.48]


See other pages where Purification table is mentioned: [Pg.92]    [Pg.281]    [Pg.212]    [Pg.237]    [Pg.359]    [Pg.142]    [Pg.146]    [Pg.399]    [Pg.403]    [Pg.376]    [Pg.289]    [Pg.279]    [Pg.128]    [Pg.404]    [Pg.193]    [Pg.342]    [Pg.205]    [Pg.147]    [Pg.5058]   
See also in sourсe #XX -- [ Pg.212 , Pg.237 ]

See also in sourсe #XX -- [ Pg.404 ]




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