2016
DOI: 10.1016/j.molcatb.2015.12.004
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One-pot enzymatic reaction sequence for the syntheses of d-glyceraldehyde 3-phosphate and l-glycerol 3-phosphate

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Cited by 10 publications
(10 citation statements)
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“…Triosephosphate metabolites such as dihydroxyacetone phosphate (DHAP) and DL‐GAP are unstable at neutral and alkaline pH conditions . The instability of L‐GAP at nearly neutral pH conditions is a critical factor for a biocatalytic process development using glycerol kinase from Cellulomonas sp., because the enzyme shows no activity at pH below 4, while L‐GAP is stable at pH below 4.…”
Section: Resultsmentioning
confidence: 99%
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“…Triosephosphate metabolites such as dihydroxyacetone phosphate (DHAP) and DL‐GAP are unstable at neutral and alkaline pH conditions . The instability of L‐GAP at nearly neutral pH conditions is a critical factor for a biocatalytic process development using glycerol kinase from Cellulomonas sp., because the enzyme shows no activity at pH below 4, while L‐GAP is stable at pH below 4.…”
Section: Resultsmentioning
confidence: 99%
“…Triosephosphate metabolites such as dihydroxyacetone phosphate (DHAP) and DL-GAP are unstable at neutral and alkaline pH conditions [8,15,[18][19][20][21]. The instability of L-GAP at nearly neutral pH conditions is a critical factor for a biocatalytic process development using glycerol…”
Section: Product Instabilitymentioning
confidence: 99%
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“…The intensification of a biocatalytic process for a selected route and the level of integration depends on the limiting step in the process design and needs to consider its debottlenecking (Figure ) with the development of the optimum reaction conditions with high substrate concentrations and low enzyme concentrations, the scaling concept, the type of reactor and subsequent operations for the optimum performance of a robust and stable overall process with high space‐time yield . Analysing the reaction kinetics, enzyme inhibition, instable products and other process bottlenecks has been useful for selecting the most suitable reaction conditions and reactor type, as shown in the case of the synthesis of glyceraldehyde‐3‐phosphates . The common inhibition of enzymatic reactions by substrates, products or byproducts can be overcome by a number of different approaches, such as using solid adsorbents for substrate and product inhibition, protecting reactive aldehyde groups as dimethylacetals or utilizing an enzymatic reaction for removing an inhibiting byproduct .…”
Section: Process and Reaction Engineeringmentioning
confidence: 99%
“…In cases of stability mismatches between substrate or product stabilities and enzyme activities and stabilities, rapid progress can be obtained by optimizing process windows 58 . Further optimization of reaction engineering parameters, such as the degree of conversion, selectivity, and specific productivity, require more work, but can lead to highly efficient synthetic procedures [59][60] . In addition to high space-time yield, reaction engineering and process intensification aim at complete conversion to the final product in order to avoid laborious product isolation operations [61][62][63] .…”
Section: Reaction Engineeringmentioning
confidence: 99%