This single entry covers a group of enzymes whose specificity is directed mainly towards the exohydrolysis of (1->4)-alpha-glucosidic linkages, and that hydrolyse oligosaccharides rapidly, relative to polysaccharide, which are hydrolysed relatively slowly, or not at all. The intestinal enzyme also hydrolyses polysaccharides, catalysing the reactions of EC 3.2.1.3 glucan 1,4-alpha-glucosidase and, more slowly, hydrolyses (1->6)-alpha-D-glucose links.
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REACTION
REACTION DIAGRAM
COMMENTARY
ORGANISM
UNIPROT
LITERATURE
Hydrolysis of terminal, non-reducing (1->4)-linked alpha-D-glucose residues with release of D-glucose
substrate recognition and catalytic mechanism, active site structure, residues R400, D87, W284, M321, F327 are involved in formation of the +1 subsite in the GH31 alpha-glucosidase substrate binding
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SYSTEMATIC NAME
IUBMB Comments
alpha-D-glucoside glucohydrolase
This single entry covers a group of enzymes whose specificity is directed mainly towards the exohydrolysis of (1->4)-alpha-glucosidic linkages, and that hydrolyse oligosaccharides rapidly, relative to polysaccharide, which are hydrolysed relatively slowly, or not at all. The intestinal enzyme also hydrolyses polysaccharides, catalysing the reactions of EC 3.2.1.3 glucan 1,4-alpha-glucosidase and, more slowly, hydrolyses (1->6)-alpha-D-glucose links.
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CRYSTALLIZATION (Commentary)
ORGANISM
UNIPROT
LITERATURE
purified recombinant wild-type and selenomethionine-labeled enzyme, hanging drop vapour diffusion method, hexameric crystal form, X-ray diffraction structure determination and analysis of the different crystal forms at 2.5 A resolution, structure modelling of domains, full-length enzyme, and active site
purified recombinant wild-type and selenomethionine-labeled enzyme, hanging drop vapour diffusion method, 2-5 mg/ml protein in 20 mM Tris-HCl, pH 7.5, and 20 mM NaCl, 0.002 ml protein solution is mixed with 0.003 ml reservoir solution and equilibrated against 1 ml reservoir solution, different compositions of the reservoir solution result in different crystal forms, overview, X-ray diffraction structure determination and analysis of the different crystal forms at 2.5-4.2 A resolution
protein production method optimization and evaluation of a microfiltration membrane bioreactor to improve the control of the concentration of key components in the growth of recombinant Escherichia coli strain BL21(DE3) cells expressing the enzyme, influence of medium composition and inducers, overview
treatment with trypsin or chymotrypsin at 30°C or proteinase K at 30°C or at 55°C for 20 min in 40 mM N-2-hydroxyethylpiperazine-N'-2-ethanesulfonic acid, pH 7.6, 8 mM magnesium acetate, 0.3 mM EDTA, 2 mM dithiothreitol, 10 mM sodium chloride and 20 mM potassium chloride has no effect
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PURIFICATION (Commentary)
ORGANISM
UNIPROT
LITERATURE
recombinant wild-type and selenomethionine-labeled enzyme from Escherichia coli strain NF1830 by ammonium sulfate fractionation, ion exchange chromatography, and gel filtration
recombinant wild-type and selenomethionine-labeled enzyme from Escherichia coli by ammonium sulfate fractionation, ion exchange chromatography, and gel filtration
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CLONED (Commentary)
ORGANISM
UNIPROT
LITERATURE
gene malA, DNA and amino acid sequence analysis, phylogenetic tree, overexpression of wild-type and selenomethionine-labeled enzyme in Escherichia coli strain NF1830
gene malA, library preparation, DNA and amino acid sequence determination and analysis, genetic structure and organization, sequences 3' to position -33, including a consensus archaeal TATA box, play an essential role in malA expression, detection of malA homologues, overview, phylogenetic analysis, expression of MalA in Escherichia coli revealing differences from the native enzyme in thermostability and electrophoretic behavior, overview
expression of the thermostable, cytosolic enzyme in Escherichia coli strain BL21(DE3) using a microfiltration membrane bioreactor to improve the control of the concentration of key components in the growth of the cells, overview
induction when cells which were maintained in sucrose minimal medium with yeast extract are down shifted to sucrose minimal medium without yeast extract addtion
glucose production from maltodextrins employing a thermophilic immobilized cell biocatalyst in a packed-bed reactor, biotransformation of a commercial dextrin mixture at industrial concentrations (3040%, w/v) into glucose at 75°C, achieving up to 98% conversion
Martino, A.; Schiraldi, C.; Fusco, S.; Di Lernia, I.; Costabile, T.; Pellicano, T.; Marotta, M.; Generoso, M.; van der Oost, J.; Sensen, C.W.; Charlebois, R.L.; Moracci, M.; Rossi, M.; De Rosa, M.
Properties of the recombinant alpha-glucosidase from Sulfolobus solfataricus in relation to starch processing