| 1 | FN Thomson Reuters Web of Knowledge |
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| 2 | VR 1.0 |
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| 3 | PT J |
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| 4 | AU Zelle, Rintze M. |
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| 5 | Harrison, Jacob C. |
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| 6 | Pronk, Jack T. |
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| 7 | van Maris, Antonius J. A. |
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| 8 | TI Anaplerotic Role for Cytosolic Malic Enzyme in Engineered Saccharomyces |
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| 9 | cerevisiae Strains |
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| 10 | SO APPLIED AND ENVIRONMENTAL MICROBIOLOGY |
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| 11 | VL 77 |
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| 12 | IS 3 |
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| 13 | BP 732 |
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| 14 | EP 738 |
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| 15 | DI 10.1128/AEM.02132-10 |
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| 16 | PD FEB 2011 |
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| 17 | PY 2011 |
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| 18 | AB Malic enzyme catalyzes the reversible oxidative decarboxylation of |
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| 19 | malate to pyruvate and CO(2). The Saccharomyces cerevisiae MAE1 gene |
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| 20 | encodes a mitochondrial malic enzyme whose proposed physiological roles |
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| 21 | are related to the oxidative, malate-decarboxylating reaction. Hitherto, |
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| 22 | the inability of pyruvate carboxylase-negative (Pyc(-)) S. cerevisiae |
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| 23 | strains to grow on glucose suggested that Mae1p cannot act as a |
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| 24 | pyruvate-carboxylating, anaplerotic enzyme. In this study, relocation of |
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| 25 | malic enzyme to the cytosol and creation of thermodynamically favorable |
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| 26 | conditions for pyruvate carboxylation by metabolic engineering, process |
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| 27 | design, and adaptive evolution, enabled malic enzyme to act as the sole |
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| 28 | anaplerotic enzyme in S. cerevisiae. The Escherichia coli NADH-dependent |
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| 29 | sfcA malic enzyme was expressed in a Pyc(-) S. cerevisiae background. |
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| 30 | When PDC2, a transcriptional regulator of pyruvate decarboxylase genes, |
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| 31 | was deleted to increase intracellular pyruvate levels and cells were |
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| 32 | grown under a CO(2) atmosphere to favor carboxylation, adaptive |
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| 33 | evolution yielded a strain that grew on glucose (specific growth rate, |
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| 34 | 0.06 +/- 0.01 h(-1)). Growth of the evolved strain was enabled by a |
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| 35 | single point mutation (Asp336Gly) that switched the cofactor preference |
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| 36 | of E. coli malic enzyme from NADH to NADPH. Consistently, cytosolic |
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| 37 | relocalization of the native Mae1p, which can use both NADH and NADPH, |
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| 38 | in a pyc1,2 Delta pdc2 Delta strain grown under a CO(2) atmosphere, also |
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| 39 | enabled slow-growth on glucose. Although growth rates of these strains |
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| 40 | are still low, the higher ATP efficiency of carboxylation via malic |
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| 41 | enzyme, compared to the pyruvate carboxylase pathway, may contribute to |
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| 42 | metabolic engineering of S. cerevisiae for anaerobic, high-yield |
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| 43 | C(4)-dicarboxylic acid production. |
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| 44 | TC 0 |
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| 45 | Z9 0 |
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| 46 | SN 0099-2240 |
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| 47 | UT WOS:000286597100004 |
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| 48 | ER |
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| 49 | |
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| 50 | PT J |
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| 51 | AU Zelle, Rintze M. |
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| 52 | Trueheart, Josh |
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| 53 | Harrison, Jacob C. |
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| 54 | Pronk, Jack T. |
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| 55 | van Maris, Antonius J. A. |
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| 56 | TI Phosphoenolpyruvate Carboxykinase as the Sole Anaplerotic Enzyme in |
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| 57 | Saccharomyces cerevisiae |
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| 58 | SO APPLIED AND ENVIRONMENTAL MICROBIOLOGY |
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| 59 | VL 76 |
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| 60 | IS 16 |
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| 61 | BP 5383 |
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| 62 | EP 5389 |
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| 63 | DI 10.1128/AEM.01077-10 |
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| 64 | PD AUG 2010 |
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| 65 | PY 2010 |
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| 66 | AB Pyruvate carboxylase is the sole anaplerotic enzyme in glucose-grown |
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| 67 | cultures of wild-type Saccharomyces cerevisiae. Pyruvate |
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| 68 | carboxylase-negative (Pyc(-)) S. cerevisiae strains cannot grow on |
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| 69 | glucose unless media are supplemented with C(4) compounds, such as |
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| 70 | aspartic acid. In several succinate-producing prokaryotes, |
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| 71 | phosphoenolpyruvate carboxykinase (PEPCK) fulfills this anaplerotic |
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| 72 | role. However, the S. cerevisiae PEPCK encoded by PCK1 is repressed by |
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| 73 | glucose and is considered to have a purely decarboxylating and |
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| 74 | gluconeogenic function. This study investigates whether and under which |
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| 75 | conditions PEPCK can replace the anaplerotic function of pyruvate |
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| 76 | carboxylase in S. cerevisiae. Pyc(-) S. cerevisiae strains |
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| 77 | constitutively overexpressing the PEPCK either from S. cerevisiae or |
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| 78 | from Actinobacillus succinogenes did not grow on glucose as the sole |
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| 79 | carbon source. However, evolutionary engineering yielded mutants able to |
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| 80 | grow on glucose as the sole carbon source at a maximum specific growth |
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| 81 | rate of ca. 0.14 h(-1), one-half that of the (pyruvate |
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| 82 | carboxylase-positive) reference strain grown under the same conditions. |
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| 83 | Growth was dependent on high carbon dioxide concentrations, indicating |
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| 84 | that the reaction catalyzed by PEPCK operates near thermodynamic |
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| 85 | equilibrium. Analysis and reverse engineering of two independently |
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| 86 | evolved strains showed that single point mutations in pyruvate kinase, |
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| 87 | which competes with PEPCK for phosphoenolpyruvate, were sufficient to |
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| 88 | enable the use of PEPCK as the sole anaplerotic enzyme. The PEPCK |
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| 89 | reaction produces one ATP per carboxylation event, whereas the original |
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| 90 | route through pyruvate kinase and pyruvate carboxylase is ATP neutral. |
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| 91 | This increased ATP yield may prove crucial for engineering of efficient |
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| 92 | and low-cost anaerobic production of C(4) dicarboxylic acids in S. |
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| 93 | cerevisiae. |
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| 94 | TC 1 |
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| 95 | Z9 1 |
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| 96 | SN 0099-2240 |
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| 97 | UT WOS:000280633400006 |
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| 98 | ER |
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| 99 | |
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| 100 | PT J |
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| 101 | AU Zelle, Rintze M. |
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| 102 | De Hulster, Erik |
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| 103 | Kloezen, Wendy |
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| 104 | Pronk, Jack T. |
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| 105 | van Maris, Antonius J. A. |
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| 106 | TI Key Process Conditions for Production of C(4) Dicarboxylic Acids in |
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| 107 | Bioreactor Batch Cultures of an Engineered Saccharomyces cerevisiae |
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| 108 | Strain |
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| 109 | SO APPLIED AND ENVIRONMENTAL MICROBIOLOGY |
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| 110 | VL 76 |
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| 111 | IS 3 |
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| 112 | BP 744 |
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| 113 | EP 750 |
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| 114 | DI 10.1128/AEM.02396-09 |
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| 115 | PD FEB 2010 |
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| 116 | PY 2010 |
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| 117 | AB A recent effort to improve malic acid production by Saccharomyces |
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| 118 | cerevisiae by means of metabolic engineering resulted in a strain that |
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| 119 | produced up to 59 g liter(-1) of malate at a yield of 0.42 mol (mol |
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| 120 | glucose)(-1) in calcium carbonate-buffered shake flask cultures. With |
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| 121 | shake flasks, process parameters that are important for scaling up this |
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| 122 | process cannot be controlled independently. In this study, growth and |
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| 123 | product formation by the engineered strain were studied in bioreactors |
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| 124 | in order to separately analyze the effects of pH, calcium, and carbon |
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| 125 | dioxide and oxygen availability. A near-neutral pH, which in shake |
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| 126 | flasks was achieved by adding CaCO(3), was required for efficient C(4) |
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| 127 | dicarboxylic acid production. Increased calcium concentrations, a side |
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| 128 | effect of CaCO(3) dissolution, had a small positive effect on malate |
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| 129 | formation. Carbon dioxide enrichment of the sparging gas (up to 15% |
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| 130 | [vol/vol]) improved production of both malate and succinate. At higher |
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| 131 | concentrations, succinate titers further increased, reaching 0.29 mol |
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| 132 | (mol glucose)(-1), whereas malate formation strongly decreased. Although |
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| 133 | fully aerobic conditions could be achieved, it was found that moderate |
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| 134 | oxygen limitation benefitted malate production. In conclusion, malic |
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| 135 | acid production with the engineered S. cerevisiae strain could be |
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| 136 | successfully transferred from shake flasks to 1-liter batch bioreactors |
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| 137 | by simultaneous optimization of four process parameters (pH and |
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| 138 | concentrations of CO(2), calcium, and O(2)). Under optimized conditions, |
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| 139 | a malate yield of 0.48 +/- 0.01 mol (mol glucose)(-1) was obtained in |
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| 140 | bioreactors, a 19% increase over yields in shake flask experiments. |
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| 141 | TC 2 |
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| 142 | Z9 2 |
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| 143 | SN 0099-2240 |
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| 144 | UT WOS:000274017400015 |
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| 145 | ER |
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| 146 | |
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| 147 | PT J |
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| 148 | AU Abbott, Derek A. |
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| 149 | Zelle, Rintze M. |
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| 150 | Pronk, Jack T. |
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| 151 | van Maris, Antonius J. A. |
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| 152 | TI Metabolic engineering of Saccharomyces cerevisiae for production of |
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| 153 | carboxylic acids: current status and challenges |
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| 154 | SO FEMS YEAST RESEARCH |
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| 155 | VL 9 |
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| 156 | IS 8 |
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| 157 | BP 1123 |
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| 158 | EP 1136 |
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| 159 | DI 10.1111/j.1567-1364.2009.00537.x |
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| 160 | PD DEC 2009 |
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| 161 | PY 2009 |
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| 162 | AB To meet the demands of future generations for chemicals and energy and |
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| 163 | to reduce the environmental footprint of the chemical industry, |
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| 164 | alternatives for petrochemistry are required. Microbial conversion of |
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| 165 | renewable feedstocks has a huge potential for cleaner, sustainable |
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| 166 | industrial production of fuels and chemicals. Microbial production of |
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| 167 | organic acids is a promising approach for production of chemical |
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| 168 | building blocks that can replace their petrochemically derived |
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| 169 | equivalents. Although Saccharomyces cerevisiae does not naturally |
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| 170 | produce organic acids in large quantities, its robustness, pH tolerance, |
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| 171 | simple nutrient requirements and long history as an industrial workhorse |
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| 172 | make it an excellent candidate biocatalyst for such processes. Genetic |
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| 173 | engineering, along with evolution and selection, has been successfully |
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| 174 | used to divert carbon from ethanol, the natural endproduct of S. |
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| 175 | cerevisiae, to pyruvate. Further engineering, which included expression |
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| 176 | of heterologous enzymes and transporters, yielded strains capable of |
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| 177 | producing lactate and malate from pyruvate. Besides these metabolic |
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| 178 | engineering strategies, this review discusses the impact of transport |
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| 179 | and energetics as well as the tolerance towards these organic acids. In |
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| 180 | addition to recent progress in engineering S. cerevisiae for organic |
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| 181 | acid production, the key limitations and challenges are discussed in the |
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| 182 | context of sustainable industrial production of organic acids from |
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| 183 | renewable feedstocks. |
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| 184 | TC 11 |
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| 185 | Z9 11 |
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| 186 | SN 1567-1356 |
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| 187 | UT WOS:000271264400001 |
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| 188 | ER |
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| 189 | |
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| 190 | PT J |
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| 191 | AU Zelle, Rintze M. |
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| 192 | de Hulster, Erik |
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| 193 | van Winden, WoUter A. |
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| 194 | de Waard, Pieter |
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| 195 | Dijkema, Cor |
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| 196 | Winkler, Aaron A. |
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| 197 | Geertman, Jan-Maarten A. |
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| 198 | van Dijken, Johannes P. |
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| 199 | Pronk, Jack T. |
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| 200 | van Maris, Antonius J. A. |
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| 201 | TI Malic acid production by Saccharomyces cerevisiae: Engineering of |
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| 202 | pyruvate carboxylation, oxaloacetate reduction, and malate export |
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| 203 | SO APPLIED AND ENVIRONMENTAL MICROBIOLOGY |
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| 204 | VL 74 |
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| 205 | IS 9 |
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| 206 | BP 2766 |
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| 207 | EP 2777 |
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| 208 | DI 10.1128/AEM.02591-07 |
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| 209 | PD MAY 2008 |
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| 210 | PY 2008 |
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| 211 | AB Malic acid is a potential biomass-derivable "building block" for |
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| 212 | chemical synthesis. Since wild-type Saccharomyces cerevisiae strains |
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| 213 | produce only low levels of malate, metabolic engineering is required to |
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| 214 | achieve efficient malate production with this yeast. A promising pathway |
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| 215 | for malate production from glucose proceeds via carboxylation of |
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| 216 | pyruvate, followed by reduction of oxaloacetate to malate. This redox- |
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| 217 | and ATP-neutral, CO2-fixing pathway has a theoretical maximum yield of 2 |
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| 218 | mol malate (mol glucose)(-1). A previously engineered glucose-tolerant, |
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| 219 | C-2-independent pyruvate decarboxylase-negative S. cerevisiae strain was |
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| 220 | used as the platform to evaluate the impact of individual and combined |
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| 221 | introduction of three genetic modifications: (i) overexpression of the |
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| 222 | native pyruvate carboxylase encoded by PYC2, (ii) high-level expression |
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| 223 | of an allele of the MDH3 gene, of which the encoded malate dehydrogenase |
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| 224 | was retargeted to the cytosol by deletion of the C-terminal peroxisomal |
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| 225 | targeting sequence, and (iii) functional expression of the |
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| 226 | Schizosaccharomyces pombe malate transporter gene SpMAE1. While single |
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| 227 | or double modifications improved malate production, the highest malate |
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| 228 | yields and titers were obtained with the simultaneous introduction of |
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| 229 | all three modifications. In glucose-grown batch cultures, the resulting |
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| 230 | engineered strain produced malate at titers of up to 59 g liter(-1) at a |
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| 231 | malate yield of 0.42 mol (mol glucose)(-1). Metabolic flux analysis |
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| 232 | showed that metabolite labeling patterns observed upon nuclear magnetic |
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| 233 | resonance analyses of cultures grown on C-13-labeled glucose were |
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| 234 | consistent with the envisaged nonoxidative, fermentative pathway for |
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| 235 | malate production. The engineered strains still produced substantial |
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| 236 | amounts of pyruvate, indicating that the pathway efficiency can be |
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| 237 | further improved. |
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| 238 | TC 15 |
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| 239 | Z9 17 |
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| 240 | SN 0099-2240 |
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| 241 | UT WOS:000255567900024 |
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| 242 | ER |
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| 243 | |
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| 244 | EF |
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