Active extract purification activity

A method for extraction, purification and preconcentration of dialkyldimethylammo-nium compounds and other detergents before determining their concentration in sewage water and activated sludge was described. It consists of a series of LLE and LC operations, the details of which are dependent of the original matrix, and end analysis was by HPLC-ELCD406. 

Intact antibodies with biologically active glycosylation profiles, crucial for the effector functions, require eukaryotic expression (in vitro or in vivo). These circumstances have inspired many scientists to find effective methods for production, as well as methods for the selection of the best extraction-purification methods. 

Antibodies are very diverse in molecular properties, chemical characteristics, and biological activity. Purification strategies are therefore also diverse, since they are based on a large variety of molecular interactions. Antibodies have several common properties that are frequently exploited from the initial feedstock. Knowledge about the nature and concentration of impurities is the key to success. Therefore, the initial composition of feedstock is important when designing the separation process. The expression system can be selected to simplify the extraction-purification procedures. 

In environmental chemical analytical procedures such as extraction, purification, and fractionation with basic aluminum oxide and activated carbon,... 

A crucial point when discussing economics of phase systems is the loading of the system. The more biological material that can be loaded, lesser is the cost of phase system per unit processed. Furthermore, extensive studies have been carried out concerning recirculation of the phase components. The latter efforts have mainly been focused on PEG/salt systems, and also on the polymer/polymer phase systems employing affinity ligands. Kula and coworkers reported the reuse of the salt phase when carrying out extractive purification (37). They showed that the phases could be recycled 4 times without any marked loss in performance of the phase separation and in specific activity of the purified protein. 

You Q,Yin X, Zhang S, Jiang Z. Extraction, purification, and antioxidant activities of polysaccharides from Tricholoma mongolicum Imai. Carbohydr Polym 2014 99 1-10. 

The extent of purification depends on the use requirements. Generally, either intense aqueous extractive distillation, or post-treatment by fixed-bed absorption (qv) using activated carbon, molecular sieves (qv), and certain metals on carriers, is employed to improve odor and to remove minor impurities. Essence grade is produced by final distillation in nonferrous, eg, copper, equipment (66). 

Many attempts have been made to reduce the ammoniacal and sulfurous odor of the standard thioglycolate formulations. As the cosmetics market is very sensitive to the presence of impurities, odor, and color, various treatments of purification have been claimed to improve the olfactory properties of thioglycolic acid and its salts, such as distillation (33), stabilization against the formation of H2S using active ingredients (34), extraction with solvents (35), active carbon (36), and chelate resin treatments (37). 

Pharmaceuticals. Pharmaceuticals account for 6% of the Hquid-phase activated carbon consumption (74). Many antibiotics, vitarnins, and steroids are isolated from fermentation broths by adsorption onto carbon foUowed by solvent extraction and distillation (82). Other uses in pharmaceutical production include process water purification and removal of impurities from intravenous solutions prior to packaging (83). 

Most purification procedures for a particular protein are developed in an empirical manner, the overriding principle being purification of the protein to a homogeneous state with acceptable yield. Table 5.5 presents a summary of a purification scheme for a selected protein. Note that the specific activity of the protein (the enzyme xanthine dehydrogenase) in the immuno-affinity purified fraction (fraction 5) has been increased 152/0.108, or 1407 times the specific activity in the crude extract (fraction 1). Thus, xanthine dehydrogenase in fraction 5 versus fraction 1 is enriched more than 1400-fold by the purification procedure. 

Two other factors are noteworthy the deleterious effects on chemical and mechanical properties of small amounts of impurities residual from extraction of the metal, and its toxicity. The first of these factors is obviated by vacuum melting the raw metal (for purification) as an essential prerequisite to further processing. The toxicity of beryllium is essentially a pulmonary problem and great care must be taken in handling the finely divided metal or its compounds. In practice, this type of activity is usually carried out under well-ventilated conditions. Certain tolerance levels for atmospheric beryllium are now internationally accepted and merit careful study before work on beryllium is embarked upon. 

B. 2-Methylcyclopenlane-l,3,5-trione hydrate. A mixture of 200 g. (0.89 mole) of the keto ester prepared above, 910 ml. of water, and 100 ml. of 85% phosphoric acid is healed under reflux for 4 hours and then cooled in an ice-salt bath to —5°. The trione mixed with oxalic acid separates and is collected by filtration and dried under reduced pressure. The dried material is extracted with boiling ether (250-300 ml.) under reflux, and the ethereal extract is separated from the undissolved oxalic acid. The original aqueous filtrate is also extracted with ether in a continuous extractor. The two extracts are combined, and ether is removed by distillation. The crude trione separates as a dark brown solid and is crystallized from ca. 250 ml. of hot water. The once-crystallized, faintly yellow product weighs 95-105 g. (74-82%), m.p. 70-74°. This product is used in the next step without further purification. A better specimen, m.p. 77-78°, which is almost colorless, can be obtained by recrystallization from hot water after treatment with Norit activated carbon. 

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