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Exact(5)

Methanol and chloroform fractions resulted in the highest amount of total extractable compounds, whereas the extraction yield with ethyl acetate and n-hexane was significantly less (P < 0.01) as compared to methanol and chloroform fraction.

SPE-HA showed higher sorption capacity because of its larger specific surface area, whereas the extraction yield of DBE-HA was twice that of SPE-HA.

The amount of extracted K from rice straw charcoal was found to be higher at lower pH (pH <3) whereas the extraction was almost constant at 60 70 % at pH between 3 and 13.

The results showed that manufacture is the most contaminant stage for chitosan and agar films, whereas the extraction of raw materials is the stage with the highest environmental burden for soy protein films.

With the TCM-CTAB method, the DNA concentrations of samples QD and SG were 589.0 ± 61.2 and 691.0 ± 54.2 ng/μL, respectively, whereas the extraction rates were 70.7 ± 7.3 and 82.9 ± 6.3 μg/g, respectively.

Similar(55)

Increasing the temperature and the buffer-to-protein ratio during extraction significantly increased protein recovery, whereas increasing the extraction time had no significant impact.

The results showed that both increasing the temperature from 25to5555 °C and increasing the nozzle diameter from 0.15 to 0.24 mm caused an increasing effect on the average particle size, whereas increasing the extraction pressure (100 250 bar) led a decrease in the average particle size.

The chemical extraction generally used in jatropha oil extraction (extraction by solvents) produces wastes similar to adsorbent E, whereas the mechanical extraction of oil from the jatropha seeds (pressing) produces a residue similar to that used for the adsorbent E + T (FACT 2010).

Different kinds of pectins can be obtained with good yields at pH 1. Galacturonic acid amounts of the extracted pectins were nearly constant whatever the extraction conditions, whereas the degrees of methylation and acetylation showed large variations.

Governments spent more time fixing lucrative extraction contracts than investing in refineries. Louis Brown Ogbeifun, a former head of an oil managers' union, says a refinery manager could spend only $35,000 without having to ask permission from the central government, whereas his counterpart on the extraction side could spend up to $2 million off his own bat on a single project.

The results demonstrated that the significant factors studied were the drug load in extractor, the ethanol/water ratio and the stirring speed whereas the temperature and the extraction time were not significant.

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