2006
DOI: 10.1016/j.jchromb.2006.03.016
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Direct comparison between ion-exchange chromatography and aqueous two-phase processes for the partial purification of penicillin acylase produced by E. coli

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Cited by 66 publications
(31 citation statements)
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“…19 The system tie-line length (TLL), which represents the length of the line that connects the compositions of the top and bottom phases in a phase diagram for a defined system, was calculated as described previously. 24 Predetermined quantities of stock solutions of potassium phosphate and poly(ethylene glycol) (PEG; Sigma Chemicals, St Louis, MO, USA) of nominal molecular weights 600, 1000, 1450 and 3350 g mol −1 were mixed with 0.2 g of fractionated soybean extracts (7S or 11S; with a protein concentration of 32 and 9.0 mg cm −3 , respectively) or 0.2 g of purified β-glucuronidase solution with 30 059 U cm −3 (Sigma Chemicals) to give the desired PEG/salt composition (Table 1) with a final weight of 2.0 g (the amount of fractionated soybean extracts or the purified protein solution added to the ATPS represent 10% w/w of the total system). The amount of GUS in the stock solution (30 059 U cm −3 ) was defined to ensure enzyme activity detection in the ATPS.…”
Section: Aqueous Two-phase Experimentsmentioning
confidence: 99%
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“…19 The system tie-line length (TLL), which represents the length of the line that connects the compositions of the top and bottom phases in a phase diagram for a defined system, was calculated as described previously. 24 Predetermined quantities of stock solutions of potassium phosphate and poly(ethylene glycol) (PEG; Sigma Chemicals, St Louis, MO, USA) of nominal molecular weights 600, 1000, 1450 and 3350 g mol −1 were mixed with 0.2 g of fractionated soybean extracts (7S or 11S; with a protein concentration of 32 and 9.0 mg cm −3 , respectively) or 0.2 g of purified β-glucuronidase solution with 30 059 U cm −3 (Sigma Chemicals) to give the desired PEG/salt composition (Table 1) with a final weight of 2.0 g (the amount of fractionated soybean extracts or the purified protein solution added to the ATPS represent 10% w/w of the total system). The amount of GUS in the stock solution (30 059 U cm −3 ) was defined to ensure enzyme activity detection in the ATPS.…”
Section: Aqueous Two-phase Experimentsmentioning
confidence: 99%
“…The potential economic benefits of substitution of costly unit operations, such as chromatography, by ATPS without commitment of the yield, have previously been addressed and the same strategies can be applied to plant-made products. 7,24 Recently, the potential applicability of ATPS for integrated extractive partitioning applied to the recovery of a model recombinant protein expressed in maize and tobacco has been demonstrated. 7,25 However, the potential application of ATPS to process soybean extracts as a route to the recovery of recombinant proteins has yet to be addressed.…”
Section: Introductionmentioning
confidence: 99%
“…For example, very recently, ATPS composed of PEG and sodium citrate was successfully used for textile effluent dye removal [12]. It has been proven by many researchers that ATPS is an efficient and economical process when compared to other separation processes like precipitation, chromatography, and so forth [13][14][15].…”
Section: Introductionmentioning
confidence: 99%
“…One explanation for this observation is that high molecular weight of PEG has high hydrophobicity and thus increases the salting-out characters that drive the partition of recombinant bromelain to the upper phase [22]. Conversely, low molecular weight of polymer attracts the migration of contaminant proteins to the top phase and causes a decrease in remaining free volume available for the recombinant bromelain to occupy [23]. Thus, the K E , PF, and enzyme activity recovery values at the top phase were significantly reduced.…”
Section: Aqueous Two-phase Systemmentioning
confidence: 99%
“…In terms of reusability, the resin can be re-used up to 100 times only, with an additional cost of using sodium hydroxide, sodium chloride, nickel sulphate, and EDTA for stripping and regenerating the resin after each run. In the case of ATPS, the polymer and salt cannot be recycled as they were part of the final purified enzyme [23]. Such economic and operation analysis provides understanding for further research, and the ATPS process is proven to be a costeffective, time-saving, and a higher recovery method that may be scaled up for industrial purpose.…”
Section: Comparison Of Purification By Atps and Chromatographic Technmentioning
confidence: 99%