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