Synthese cyclischer Peptide und von Kohlenhydraten abgeleitete Katalysatoren zur enantioselektiven Darstellung von Cyanhydrinen

Der Suche nach neuen Wirkstoffen für den chemischen Pflanzenschutz kommt insbesondere vor dem Hintergrund der steigenden Weltbevölkerung und weniger zur Verfügung stehenden kulturfähigen Ackerflächen eine stetig wachsende Bedeutung zu. Ziel dieser Arbeit war die Synthese von cyclischen Peptiden und Depsipeptiden, die aufgrund ihrer biologischen Aktivität als potentielle Insektizide für den chemischen Pflanzenschutz in Frage kommen. Darüber hinaus sollten von Kohlenhydraten abgeleitete Katalysatoren zur enantioselektiven Cyanhydrinsynthese entwickelt werden, um einen leichten Zugang zu den Bausteinen der Depsipeptide zu ermöglichen. Als vielversprechender Naturstoff mit insektiziden Eigenschaften gilt das cyclische Pentapeptid Cycloaspeptid E, dessen Totalsynthese in 10 Stufen mit einer Gesamtausbeute von 25% erreicht wurde, sodass die Verbindung für biologische Tests bereitgestellt werden konnte. Zusätzlich gelang die Kristallisation der Verbindung, was eine Röntgenstrukturanalyse ermöglichte. Ein Derivat von Cycloaspeptid E sollte 2-Aminonicotinsäure anstelle von Anthranilsäure enthalten. Die Synthese dieser Verbindung wurde auf drei Wegen versucht. Dabei zeigte sich, dass es bei einer zur Totalsynthese des Naturstoffs analogen Strategie zur quantitativen Bildung eines Diketopiperazins kommt. Auf den anderen Routen ließ sich entweder ein Kupplungsschritt nicht realisieren, oder die Verbindung erwies sich unter den gewählten Bedingungen als instabil. Die Darstellung eines 2-Aminonicotinsäure-Derivats von Cycloaspeptid E bleibt daher weiterhin ein ungelöstes Problem, das weiterer Forschung bedarf. Verticilid A1 ist ein cyclisches Depsipeptid, das aufgrund seiner Bindungsfähigkeit an den Ryanodinrezeptor von Insekten, als Leitstruktur für die Suche nach neuen Insektiziden von Interesse ist. Um zu untersuchen, wie wichtig die Esterbindungen im Molekül für die biologische Aktivität sind, sollte das entsprechende Amid-Derivat und das Cyclodepsipeptid mit nur zwei statt vier Esterbindungen hergestellt werden. Hierbei zeigte sich, dass eine zur Darstellung von Verticilid A1 analoge Syntheseroute zu einer ausgeprägten Epimerisierung führt. Eine lineare Synthese der Derivate endet in der Bildung des Diketopiperazins. Weiterhin wurden zwei neue, zueinander pseudoenantiomere Vanadium(IV)-Katalysatoren auf Basis von D-Glucose einerseits und L-Xylose andererseits dargestellt. Diese lassen sich in fünf bzw. 14 Stufen synthetisieren und liefern in der enantioselektiven Katalyse von Mandelsäurenitril Enantiomerenüberschüsse von 89% bzw. 91% bei hohen Ausbeuten. Zusammenfassend lässt sich feststellen, dass im Rahmen dieser Arbeit die Totalsynthese von Cycloaspeptid E erfolgreich durchgeführt wurde, und die Syntheseversuche von weiteren cyclischen Peptiden wichtige Erkenntnisse für weitere Synthesen lieferten. Mit den beiden hergestellten Vanadium(IV)-Komplexen wurden zwei potente, auf Kohlenhydraten basierende Katalysatoren für die enantioselektive Synthese von Cyanhydrinen entwickelt.

Entwicklung eines Thermodruckhydrolyse-Verfahrens zur Vorbehandlung von Weizenstroh ohne vorherige mechanische Zerkleinerung für die Produktion von Polyhydroxybuttersäure

In der vorliegenden Arbeit wurde der nachwachsende Rohstoff Weizenstroh für die Produktion des Biopolymers Polyhydroxybuttersäure genutzt. Als Lignocellulose enthält Weizenstroh einen hohen Anteil an Glucose und Xylose in Form von Cellulose und Hemicellulose. Eine Gewinnung ist aufgrund der komplexen Struktur mit Lignin als dritte Hauptkomponente nur durch eine Vorbehandlung möglich. Hierzu wurde ein thermochemisches Vorbehandlungsverfahren im halbtechnischen (125 l Reaktor) und technisch (425 l Reaktor) Maßstab mit verdünnter Salpetersäure (bis 1 % v/v) etabliert und hinsichtlich verschiedener Versuchsparameter (Behandlungstemperatur, Säure-Konzentration, etc.) optimiert. Auf eine mechanische Vorbehandlung wurde verzichtet. Danach erfolgte eine enzymatische Hydrolyse der vorbehandelten Biomasse. Der PHB-Produzent Cupriavidus necator DSM 545 wurde eingesetzt, um aus den freigesetzten Zuckern PHB zu synthetisieren. rnDurch die Optimierung der Vorbehandlung konnten bis zu 90 % der Glucose und 82 % der Xylose nach der enzymatischen Hydrolyse aus dem Stroh als Monomere und Oligomere freigesetzt werden. Außerdem wurde eine erfolgreiche Überführung des Vorbehandlungsprozesses in den 425 l Reaktor demonstriert. In den gewonnenen Zucker-Hydrolysaten konnten hohe Zelldichten und PHB-Gehalte mit bis zu 38 % erreicht werden. Eine vorherige kostenintensive Reinigung der Hydrolysate war nicht nötig. Zusätzlich konnte gezeigt werden, dass die Reststoffe nach der enzymatischen Hydrolyse, Zellkultur und PHB-Extraktion ausreichendes Potential für eine Biogas-Produktion besitzen. rn

Mikrobielle Synthese von Biopolymeren aus der nachwachsenden Rohstoffquelle Weizenstroh

Weizenstroh als erneuerbare Ressource zur Produktion von Biopolymeren und wichtigen Grundchemikalien stellt eine ökologisch sinnvolle Alternative dar. Durch die vom PFI durchgeführte Thermodruckhydrolyse konnte das Weizenstroh und die darin enthaltenen Zucker fast vollständig mobilisiert werden. Ein umfangreiches Screening nach Organismen, welche die Zucker des Weizenstrohs verwerten konnten, ergab, dass einige wenige Stämme zur PHB-Bildung aus Xylose befähigt waren (10 %). Zur PHB-Synthese aus Glucose waren indes ca. doppelt so viele Organismen in der Lage (20 %). Zwei der insgesamt 118 untersuchten Organismen zeigten besonders gute PHB-Bildung sowohl mit Xylose als auch mit Glucose als Substrat. Dabei handelte es sich um die hauseigenen Stämme Bacillus licheniformis KHC 3 und Bacillus megaterium KNaC 2. Nach Enttoxifizierung der hemicellulosischen Fraktion konnte diese als C-Quelle im Mineral Medium eingesetzt werden. Burkholderia sacchari DSM 17165 und Hydrogenophaga pseudoflava DSM 1034, sowie die hauseigenen Isolate Bacillus licheniformis KHC 3 und Bacillus megaterium KNaC 2 wurden für die Synthese von PHB aus der hemicellulosischen Fraktion verwendet. Die Zucker der hemicellulosischen Fraktion (Xylose, Glucose, Arabinose) konnten durch diese Organismen zur PHB-Synthese genutzt werden. Hierbei stellte sich heraus, dass die beiden Bacillus-Stämme besser zur Produktion von PHB aus dem hemicellulosischen Hydrolysat geeignet waren als die Stämme der DSMZ. Die alternative Umsetzung der im hemicellulosischem Hydrolysat enthaltenen Zucker (Xylose, Glucose und Arabinose) in die wichtigen Grundchemikalien Lactat und Acetat konnte durch die Verwendung von heterofermentativen Milchsäurebakterien verwirklicht werden. Die Bildung dieser wichtigen Grundchemikalien stellt eine interessante Alternative zur PHB-Synthese dar. Die Menge an teuren Zusätzen wie Tomatensaft, welcher für das Wachstum der MSB essentiell war, konnte reduziert werden. Die Glucose der zweiten Fraktion des Weizenstrohs, der cellulosischen Fraktion, konnte ebenfalls durch den Einsatz von Mikroorganismen in PHB umgewandelt werden. Kommerzielle Cellulasen der Firma Novozymes konnten große Mengen an Glucose (≥10 g/l) aus der cellulosischen Fraktion freisetzen. Diese freie Glucose wurde mit Hilfe von Cupriavidus necator DSM 545, Cupriavidus necator NCIMB 11599, Bacillus licheniformis KHC 3 und Bacillus megaterium KNaC 2 zu PHB fermentiert. Wie auch beim hemicellulosischen Hydrolysat konnten hier die beiden Bacillus-Stämme die besten Ergebnisse erzielen. Bei ihnen machte die PHB mehr als die Hälfte der Trockenmasse aus. Die Abtrennung des Zielprodukts ohne die Verwendung von umweltschädlichen Lösungsmitteln wurde durch die Lyse der Zielzellen durch eigens isolierte Enzyme aus Streptomyceten verwirklicht. Die Zelllyse durch die Enzyme aus Streptomyces globisporus subsp. caucasius DSM 40814 und Streptomyces albidoflavus DSM 40233 war erfolgreich und zeigte vor allem bei den Bacillen hohe Wirkung (83 % und 99 % Zelllyse). Bei dem Gram-negativen Organismus Cupriavidus necator DSM 428 konnte die anfangs niedrige Zelllyse von 38 % durch Ultraschallbehandlung auf ca. 75 % erhöht werden.

Bedeutung von allelen Varianten des Hexose-Transporters Hxt3p und der Hexokinasen Hxk1p und Hxk2p für Aufnahme und Verwertung von Glucose und Fructose durch Weinhefen

In Hinsicht darauf, dass sich S. cerevisiae-Stämme im Laufe der Domestizierung und Anpassung an verschiedene Habitate genetisch verändert haben, wurde in dieser Arbeit eine repräsentative Auswahl von Labor-, kommerziellen und in der Natur vorkommenden Saccharomyces-Stämmen und ihren Interspezies-Hybriden auf die Verbreitung alleler Varianten der Hexokinase-Gene HXK1 und HXK2 getestet. Von den Hexose-Transportern stand Hxt3p im Mittelpunkt, da seine essentielle Rolle bei der Vergärung von Glucose und Fructose bereits belegt wurde.rnIn dieser Arbeit wurde gezeigt, dass es bedeutende Unterschiede in der Vergärung von Glucose und Fructose zwischen Weinhefen der Gattung Saccharomyces gibt, die z.T. mit Struktur-Varianten des Hexose-Transporter Hxt3p korrelieren. rnInsgesamt 51 Hefestämme wurden auf ihre allele Variante des HXT3-Gens untersucht. Dabei haben sich drei Hauptgruppen (die Fermichamp®-Typ Gruppe, Bierhefen und Hybrid-Stämme) mit unterschiedlichem HXT3-Allel ergeben. Im Zusammenhang mit der Weinherstellung wurden signifikante Nukleotid-Substitutionen innerhalb des HXT3-Gens der robusten S. cerevisiae-Stämme (wie z.B. Sekthefen, kommerzielle Starterkulturen) und Hybrid-Stämmen festgestellt. Diese Hefen zeichneten sich durch die Fähigkeit aus, den Most trotz stressigen Umwelt-Bedingungen (wie hohe Ethanol-Konzentration, reduzierter Ammonium-Gehalt, ungünstiges Glucose:Fructose-Verhältnis) zu vergären. rnDie Experimente deuten darauf hin, dass die HXT3-Allel-Variante des als Starterkultur verwendbaren Stammes Fermichamp®, für den verstärkten Fructose-Abbau verantwortlich ist. Ein gleiches Verhalten der Stämme mit dieser Allel-Variante wurde ebenfalls beobachtet. Getestet wurden die S. cerevisiae-Stämme Fermichamp® und 54.41, die bezüglich Hxt3p-Aminosäuresequenz gleich sind, gegenüber zwei S. cerevisiae-Stämmen mit dem HXT3-Standard-Alleltyp Fermivin® und 33. Der Unterschied in der Hexose-Verwertung zwischen Stämmen mit Fermichamp®- und Standard-Alleltyp war in der Mitte des Gärverlaufs am deutlichsten zu beobachten. Beide Gruppen, sowohl mit HXT3 Fermichamp®- als auch Fermivin®-Alleltyp vergoren die Glucose schneller als die Fructose. Der Unterschied aber zwischen diesen HXT3-Alleltypen bei der Zucker-Verwertung lag darin, dass der Fermichamp®-Typ eine kleinere Differenz in der Abbau-Geschwindigkeit der beiden Hexosen zeigte als der Fermivin®-Typ. Die Zuckeraufnahme-Messungen haben die relativ gute Fructose-Aufnahme dieser Stämme bestätigt.rnEbenfalls korrelierte der fructophile Charakter des Triple-Hybrides S. cerevisiae x S. kudriavzevii x S. bayanus-Stamm HL78 in Transportexperimenten mit verstärkter Aufnahme von Fructose im Vergleich zu Glucose. Insgesamt zeigte dieser Stamm ähnliches Verhalten wie die S. cerevisiae-Stämme Fermichamp® und 54.41. rnIn dieser Arbeit wurde ein Struktur-Modell des Hexose-Transporters Hxt3p erstellt. Als Basis diente die zu 30 % homologe Struktur des Proton/Xylose-Symporters XylE aus Escherichia coli. Anhand des Hxt3p-Modells konnten Sequenzbereiche mit hoher Variabilität (Hotspots) in drei Hxt3p-Isoformen der Hauptgruppen (die Fermichamp®-Typ Gruppe, Bierhefen und Hybrid-Stämme) detektiert werden. Diese signifikanten Aminosäure-Substitutionen, die eine mögliche Veränderung der physikalischen und chemischen Eigenschaften des Carriers mit sich bringen, konzentrieren sich auf drei Bereiche. Dazu gehören die Region zwischen den N- und C-terminalen Domänen, die cytosolische Domäne und der Outside-Loop zwischen Transmembranregion 9 und Transmembranregion 10. rnObwohl die Transportmessungen keinen Zusammenhang zwischen Stämmen mit unterschiedlichen HXT3-Allelen und ihrer Toleranz gegenüber Ethanol ergaben, wurde ein signifikanter Anstieg in der Zuckeraufnahme nach vorheriger 24-stündiger Inkubation mit 4 Vol% Ethanol bei den Teststämmen beobachtet. rnInsgesamt könnten allele Varianten von HXT3-Gen ein nützliches Kriterium bei der Suche nach robusten Hefen für die Weinherstellung oder für andere industrielle Anwendungen sein. Die Auswirkung dieser Modifikationen auf die Struktur und Effizienz des Hexose-Transporters, sowie der mögliche Zusammenhang mit Ethanol-Resistenz müssen weiter ausführlich untersucht werden. rnEin Zusammenhang zwischen den niedrig variablen Allel-Varianten der Hexokinase-Gene HXK1 und HXK2 und dem Zucker-Metabolismus wurde nicht gefunden. Die Hexokinasen der untersuchten Stämme wiesen allerdings generell eine signifikante geringere Affinität zu Fructose im Vergleich zu Glucose auf. Hier liegt sicherlich eine Hauptursache für den Anstieg des Fructose:Glucose-Verhältnisses im Laufe der Vergärung von Traubenmosten.rn

In vitro efficacy of dicationic compounds and mefloquine enantiomers against Echinococcus multilocularis metacestodes

The current chemotherapy of alveolar echinococcosis (AE) is based on benzimidazoles such as albendazole and has been shown to be parasitostatic rather than parasiticidal, requiring lifelong duration. Thus, new and more efficient treatment options are urgently needed. By employing a recently validated assay based on the release of functional phosphoglucose isomerase (PGI) from dying parasites, the activities of 26 dicationic compounds and of the (+)- and (-)-erythro-enantiomers of mefloquine were investigated. Initial screening of compounds was performed at 40 muM, and those compounds exhibiting considerable antiparasitic activities were also assessed at lower concentrations. Of the dicationic drugs, DB1127 (a diguanidino compound) with activities comparable to nitazoxanide was further studied. The activity of DB1127 was dose dependent and led to severe structural alterations, as visualized by electron microscopy. The (+)- and (-)-erythro-enantiomers of mefloquine showed similar dose-dependent effects, although higher concentrations of these compounds than of DB1127 were required for metacestode damage. In conclusion, of the drugs investigated here, the diguanidino compound DB1127 represents the most promising compound for further study in appropriate in vivo models for Echinococcus multilocularis infection.

Classification of organisms previously reported as the SP and Stewart-Letscher groups, with descriptions of Necropsobacter gen. nov. and of Necropsobacter rosorum sp. nov. for organisms of the SP group

To allow classification of bacteria previously reported as the SP group and the Stewart-Letscher group, 35 isolates from rodents (21), rabbits (eight), a dog and humans (five) were phenotypically and genotypically characterized. Comparison of partial rpoB sequences showed that 34 of the isolates were closely related, demonstrating at least 97.4 % similarity. 16S rRNA gene sequence comparison of 20 selected isolates confirmed the monophyly of the SP group and revealed 98.5 %-100 % similarity between isolates. A blast search using the 16S rRNA gene sequences showed that the highest similarity outside the SP group was 95.5 % to an unclassified rat isolate. The single strain, P625, representing the Stewart-Letscher group showed the highest 16S rRNA gene similarity (94.9-95.5 %) to members of the SP group. recN gene sequence analysis of 11 representative strains resulted in similarities of 97-100 % among the SP group strains, which showed 80 % sequence similarity to the Stewart-Letscher group strain. Sequence similarity values based on the recN gene, indicative for whole genome similarity, showed the SP group being clearly separated from established genera, whereas the Stewart-Letscher group strain was associated with the SP group. A new genus, Necropsobacter gen. nov., with only one species, Necropsobacter rosorum sp. nov., is proposed to include all members of the SP group. The new genus can be separated from existing genera of the family Pasteurellaceae by at least three phenotypic characters. The most characteristic properties of the new genus are that haemolysis is not observed on bovine blood agar, positive reactions are observed in the porphyrin test, acid is produced from (+)-L-arabinose, (+)-D-xylose, dulcitol, (+)-D-galactose, (+)-D-mannose, maltose and melibiose, and negative reactions are observed for symbiotic growth, urease, ornithine decarboxylase and indole. Previous publications have documented that both ubiquinones and demethylmenaquinone were produced by the proposed type strain of the new genus, Michel A/76(T), and that the major polyamine of representative strains (type strain not included) of the genus is 1,3-diaminopropane, spermidine is present in moderate amounts and putrescine and spermine are detectable only in minor amounts. The major fatty acids of strain Michel A/76(T) are C(14 : 0), C(16 : 0), C(16:1)omega7c and summed feature C(14 : 0) 3-OH/iso-C(16 : 1) I. This fatty acid profile is typical for members of the family Pasteurellaceae. The G+C content of DNA of strain Michel A/76(T) was estimated to be 52.5 mol% in a previous investigation. The type strain is P709(T) ( = Michel A/76(T) = CCUG 28028(T) = CIP 110147(T) = CCM 7802(T)).

Proteomic changes in the rat brain induced by homogenous irradiation and by the bystander effect resulting from high energy synchrotron X-ray microbeams

Abstract Purpose: To further evaluate the use of microbeam irradiation (MBI) as a potential means of non-invasive brain tumor treatment by investigating the induction of a bystander effect in non-irradiated tissue. Methods: Adult rats were irradiated with 35 or 350 Gy at the European Synchotron Research Facility (ESRF), using homogenous (broad beam) irradiation (HI) or a high energy microbeam delivered to the right brain hemisphere only. The proteome of the frontal lobes were then analyzed using two-dimensional electrophoresis (2-DE) and mass spectrometry. Results: HI resulted in proteomic responses indicative of tumourigenesis; increased albumin, aconitase and triosphosphate isomerase (TPI), and decreased dihydrolipoyldehydrogenase (DLD). The MBI bystander effect proteomic changes were indicative of reactive oxygen species mediated apoptosis; reduced TPI, prohibitin and tubulin and increased glial fibrillary acidic protein (GFAP). These potentially anti-tumourigenic apoptotic proteomic changes are also associated with neurodegeneration. However the bystander effect also increased heat shock protein (HSP) 71 turnover. HSP 71 is known to protect against all of the neurological disorders characterized by the bystander effect proteome changes. Conclusions: These results indicate that the collective interaction of these MBI-induced bystander effect proteins and their mediation by HSP 71, may confer a protective effect which now warrants additional experimental attention.

Proteome and radioimmunoassay analyses of pituitary hormones and proteins in response to feed restriction of dairy cows

The hypothalamic-pituitary system controls homeostasis during feed energy reduction. In order to examine which pituitary proteins and hormone variants are potentially associated with metabolic adaptation, pituitary glands from ad libitum and energy restrictively fed dairy cows were characterized using RIA and 2-DE followed by MALDI-TOF-MS. We found 64 different spots of regulatory hormones: growth hormone (44), preprolactin (16), luteinizing hormone (LH) (1), thyrotropin (1), proopiomelanocortin (1) and its cleavage product lipotropin (1), but none of these did significantly differ between feeding groups. Quantification of total pituitary LH and prolactin concentrations by RIA confirmed the results obtained by proteome analysis. Also, feed energy restriction provoked increasing non-esterified fatty acid, decreasing prolactin, but unaltered glucose, LH and growth hormone plasma concentrations. Energy restriction decreased the expression of glial fibrillary acidic protein, triosephosphate isomerase, purine-rich element-binding protein A and elongation factor Tu, whereas it increased expression of proline synthetase co-transcribed homolog, peroxiredoxin III, beta-tubulin and annexin A5 which is involved in the hormone secretion process. Our results indicate that in response to feed energy restriction the pituitary reservoir of all posttranslationally modified hormone forms remains constant. Changing plasma hormone concentrations are likely attributed to a regulated releasing process from the gland into the blood.

Evaluation of gastrointestinal permeability and mucosal absorptive capacity in dogs with chronic enteropathy

OBJECTIVE: To assess intestinal mucosal function by measuring permeability and absorptive capacity in dogs with chronic enteropathy (CE) before and after treatment and to determine whether those variables were correlated with clinical disease activity or histologic scoring of intestinal biopsy specimens. ANIMALS: 29 dogs with CE. PROCEDURE: Dogs were designated as having dietresponsive CE or CE requiring glucorticoid treatment. Severity of clinical signs was assessed by calculating the canine inflammatory bowel disease activity index (CIBDAI). Histologic severity of intestinal infiltration was assessed before and after 4 weeks of treatment in the diet-responsive group and before and after 10 weeks of treatment in the glucocorticoid group. Gastrointestinal permeability and mucosal absorptive capacity were assessed by use of intragastric administration of a solution containing lactulose, rhamnose, xylose, 3-O-methylglucose, and sucrose. Urine was collected 6 hours after administration of the sugar solution to determine urinary lactulose-to-rhamnose (L:R), xylose-to-methylglucose (X:M), and sucrose-to-methylglucose (S:M) ratios. RESULTS: Median CIBDAI scores decreased significantly in both groups of dogs after treatment. However, the median histologic grade of intestinal biopsy specimens did not change with treatment in either group. There were no significant differences in L:R, X:M, or S:M ratios after treatment in either group and no significant correlations between L:R, X:M, or S:M ratios and CIBDAI or histologic scores. CONCLUSIONS AND CLINICAL RELEVANCE: Results of tests for intestinal permeability and mucosal absorptive capacity were not useful indicators of clinical disease activity as assessed by the CIBDAI or the sever ity of infiltration as indicated by histologic evaluation.

Screening, optimization and extraction of polyhydroxyalkanoates and peptidoglycan from Bacillus megaterium

Bioplastics are polymers (such as polyesters) produced from bacterial fermentations that are biodegradable and nonhazardous. They are produced by a wide variety of bacteria and are made only when stress conditions allow, such as when nutrient levels are low, more specifically levels of nitrogen and oxygen. These stress conditions cause certain bacteria to build up excess carbon deposits as energy reserves in the form of polyhydroxyalkanoates (PHAs). PHAs can be extracted and formed into actual plastic with the same strength of conventional, synthetic-based plastics without the need to rely on foreign petroleum. The overall goal of this project was to select for a bacteria that could grow on sugars found in the lignocellulosic biomass, and get the bacteria to produce PHAs and peptidoglycan. Once this was accomplished the goal was to extract PHAs and peptidoglycan in order to make a stronger more rigid plastic, by combing them into a co-polymer. The individual goals of this project were to: (1) Select and screen bacteria that are capable of producing PHAs by utilizing the carbon/energy sources found in lignocellulosic biomass; (2) Maximize the utilization of those sugars present in woody biomass in order to produce optimal levels of PHAs. (3) Use room temperature ionic liquids (RTILs) in order to separate the cell membrane and peptidoglycan, allowing for better extraction of PHAs and more intact peptidoglycan. B. megaterium a Gram-positive PHA-producing bacterium was selected for study in this project. It was grown on a variety of different substrates in order to maximize both its growth and production of PHAs. The optimal conditions were found to be 30°C, pH 6.0 and sugar concentration of either 30g/L glucose or xylose. After optimal growth was obtained, both RTILs and enzymatic treatments were used to break the cell wall, in order to extract the PHAs, and peptidoglycan. PHAs and peptidoglycan were successfully extracted from the cell, and will be used in the future to create a new stronger co-polymer. Peptidoglycan recovery yield was 16% of the cells’ dry weight.

Optimization of ethanol production by yeasts from lignocellulosic feedstocks

Ethanol from lignocellulosic feedstocks is not currently competitive with corn-based ethanol in terms of yields and commercial feasibility. Through optimization of the pretreatment and fermentation steps this could change. The overall goal of this study was to evaluate, characterize, and optimize ethanol production from lignocellulosic feedstocks by the yeasts Saccharomyces cerevisiae (strain Ethanol Red, ER) and Pichia stipitis CBS 6054. Through a series of fermentations and growth studies, P. stipitis CBS 6054 and S. cerevisiae (ER) were evaluated on their ability to produce ethanol from both single substrate (xylose and glucose) and mixed substrate (five sugars present in hemicellulose) fermentations. The yeasts were also evaluated on their ability to produce ethanol from dilute acid pretreated hydrolysate and enzymatic hydrolysate. Hardwood (aspen), softwood (balsam), and herbaceous (switchgrass) hydrolysates were also tested to determine the effect of the source of the feedstock. P. stipitis produced ethanol from 66-98% of the theoretical yield throughout the fermentation studies completed over the course of this work. S. cerevisiae (ER) was determined to not be ideal for dilute acid pretreated lignocellulose because it was not able to utilize all the sugars found in hemicellulose. S. cerevisiae (ER) was instead used to optimize enzymatic pretreated lignocellulose that contained only glucose monomers. It was able to produce ethanol from enzymatically pretreated hydrolysate but the sugar level was so low (>3 g/L) that it would not be commercially feasible. Two lignocellulosic degradation products, furfural and acetic acid, were evaluated for whether or not they had an inhibitory effect on biomass production, substrate utilization, and ethanol production by P. stipitis and S. cerevisiae (ER). It was determined that inhibition is directly related to the concentration of the inhibitor and the organism. The final phase for this thesis focused on adapting P. stipitis CBS 6054 to toxic compounds present in dilute acid pretreated hydrolysate through directed evolution. Cultures were transferred to increasing concentrations of dilute acid pretreated hydrolysate in the fermentation media. The adapted strains’ fermentation capabilities were tested against the unadapted parent strain at each hydrolysate concentration. The fermentation capabilities of the adapted strain were significantly improved over the unadapted parentstrain. On media containing 60% hydrolysate the adapted strain yielded 0.30 g_ethanol/g_sugar ± 0.033 (g/g) and the unadapted parent strain yielded 0.11 g/g ±0.028. The culture has been successfully adapted to growth on media containing 65%, 70%, 75%, and 80% hydrolysate but with below optimal ethanol yields (0.14-0.19 g/g). Cell recycle could be a viable option for improving ethanol yields in these cases. A study was conducted to determine the optimal media for production of ethanol from xylose and mixed substrate fermentations by P. stipitis. Growth, substrate utilization, and ethanol production were the three factors used to evaluate the media. The three media tested were Yeast Peptone (YP), Yeast Nitrogen Base (YNB), and Corn Steep Liquor (CSL). The ethanol yields (g/g) for each medium are as follows: YP - 0.40-0.42, YNB -0.28-.030, and CSL - 0.44-.051. The results show that media containing CSL result in slightly higher ethanol yields then other fermentation media. P. stipitis was successfully adapted to dilute acid pretreated aspen hydrolysate in increasing concentrations in order to produce higher ethanol yields compared to the unadapted parent strain. S. cerevisiae (ER) produced ethanol from enzymatic pretreated cellulose containing low concentrations of glucose (1-3g/L). These results show that fermentations of lignocellulosic feedstocks can be optimized based on the substrate and organism for increased ethanol yields.

Kinetic characterization for pretreatment of timber varieties and switchgrass using diluted acid hydrolysis

In recent years, growing attention has been devoted to the use of lignocellulosic biomass as a feedstock to produce renewable carbohydrates as a source of energy products, including liquid alternatives to fossil fuels. The benefits of developing woody biomass to ethanol technology are to increase the long-term national energy security, reduce fossil energy consumption, lower greenhouse gas emissions, use renewable rather than depletable resources, and create local jobs. Currently, research is driven by the need to reduce the cost of biomass-ethanol production. One of the preferred methods is to thermochemically pretreat the biomass material and subsequently, enzymatically hydrolyze the pretreated material to fermentable sugars that can then be converted to ethanol using specialized microorganisms. The goals of pretreatment are to remove the hemicellulose fraction from other biomass components, reduce bioconversion time, enhance enzymatic conversion of the cellulose fraction, and, hopefully, obtain a higher ethanol yield. The primary goal of this research is to obtain kinetic detailed data for dilute acid hydrolysis for several timber species from the Upper Peninsula of Michigan and switchgrass. These results will be used to identify optimum reaction conditions to maximize production of fermentable sugars and minimize production of non-fermentable byproducts. The structural carbohydrate analysis of the biomass species used in this project was performed using the procedure proposed by National Renewable Energy Laboratory (NREL). Subsequently, dilute acid-catalyzed hydrolysis of biomass, including aspen, basswood, balsam, red maple, and switchgrass, was studied at various temperatures, acid concentrations, and particle sizes in a 1-L well-mixed batch reactor (Parr Instruments, ii Model 4571). 25 g of biomass and 500 mL of diluted acid solution were added into a 1-L glass liner, and then put into the reactor. During the experiment, 5 mL samples were taken starting at 100°C at 3 min intervals until reaching the targeted temperature (160, 175, or 190°C), followed by 4 samples after achieving the desired temperature. The collected samples were then cooled in an ice bath immediately to stop the reaction. The cooled samples were filtered using 0.2 μm MILLIPORE membrane filter to remove suspended solids. The filtered samples were then analyzed using High Performance Liquid Chromatography (HPLC) with a Bio-Rad Aminex HPX-87P column, and refractive index detection to measure monomeric and polymeric sugars plus degradation byproducts. A first order reaction model was assumed and the kinetic parameters such as activation energy and pre-exponential factor from Arrhenius equation were obtained from a match between the model and experimental data. The reaction temperature increases linearly after 40 minutes during experiments. Xylose and other sugars were formed from hemicellulose hydrolysis over this heat up period until a maximum concentration was reached at the time near when the targeted temperature was reached. However, negligible amount of xylose byproducts and small concentrations of other soluble sugars, such as mannose, arabinose, and galactose were detected during this initial heat up period. Very little cellulose hydrolysis yielding glucose was observed during the initial heat up period. On the other hand, later in the reaction during the constant temperature period xylose was degraded to furfural. Glucose production from cellulose was increased during this constant temperature period at later time points in the reaction. The kinetic coefficient governing the generation of xylose from hemicellulose and the generation of furfural from xylose presented a coherent dependence on both temperature and acid concentration. However, no effect was observed in the particle size. There were three types of biomass used in this project; hardwood (aspen, basswood, and red maple), softwood (balsam), and a herbaceous crop (switchgrass). The activation energies and the pre-exponential factors of the timber species and switchgrass were in a range of 49 - 180 kJ/mol and from 7.5x104 - 2.6x1020 min-1, respectively, for the xylose formation model. In addition, for xylose degradation, the activation energies and the preexponential factors ranged from 130 - 170 kJ/mol and from 6.8x1013 - 3.7x1017 min-1, respectively. The results compare favorably with the literature values given by Ranganathan et al, 1985. Overall, up to 92 % of the xylose was able to generate from the dilute acid hydrolysis in this project.

Ethanol Production from Hardboard Manufacturing Process Wastewater: Methods for Improving Product Yields from Hemicellulose Hydrolysates

Waste effluents from the forest products industry are sources of lignocellulosic biomass that can be converted to ethanol by yeast after pretreatment. However, the challenge of improving ethanol yields from a mixed pentose and hexose fermentation of a potentially inhibitory hydrolysate still remains. Hardboard manufacturing process wastewater (HPW) was evaluated at a potential feedstream for lignocellulosic ethanol production by native xylose-fermenting yeast. After screening of xylose-fermenting yeasts, Scheffersomyces stipitis CBS 6054 was selected as the ideal organism for conversion of the HPW hydrolysate material. The individual and synergistic effects of inhibitory compounds present in the hydrolysate were evaluated using response surface methodology. It was concluded that organic acids have an additive negative effect on fermentations. Fermentation conditions were also optimized in terms of aeration and pH. Methods for improving productivity and achieving higher ethanol yields were investigated. Adaptation to the conditions present in the hydrolysate through repeated cell sub-culturing was used. The objectives of this present study were to adapt S. stipitis CBS6054 to a dilute-acid pretreated lignocellulosic containing waste stream; compare the physiological, metabolic, and proteomic profiles of the adapted strain to its parent; quantify changes in protein expression/regulation, metabolite abundance, and enzyme activity; and determine the biochemical and molecular mechanism of adaptation. The adapted culture showed improvement in both substrate utilization and ethanol yields compared to the unadapted parent strain. The adapted strain also represented a growth phenotype compared to its unadapted parent based on its physiological and proteomic profiles. Several potential targets that could be responsible for strain improvement were identified. These targets could have implications for metabolic engineering of strains for improved ethanol production from lignocellulosic feedstocks. Although this work focuses specifically on the conversion of HPW to ethanol, the methods developed can be used for any feedstock/product systems that employ a microbial conversion step. The benefit of this research is that the organisms will the optimized for a company's specific system.

THE POTENTIAL OF INDUSTRIAL WASTE AND AGRICULTURAL FEEDSTOCK TOWARDS SUSTAINABLE BIOFUELS PRODUCTION: TECHNO-ECONOMIC AND ENVIRONMENTAL IMPACT PERSPECTIVES

This Ph.D. research is comprised of three major components; (i) Characterization study to analyze the composition of defatted corn syrup (DCS) from a dry corn mill facility (ii) Hydrolysis experiments to optimize the production of fermentable sugars and amino acid platform using DCS and (iii) Sustainability analyses. Analyses of DCS included total solids, ash content, total protein, amino acids, inorganic elements, starch, total carbohydrates, lignin, organic acids, glycerol, and presence of functional groups. Total solids content was 37.4% (± 0.4%) by weight, and the mass balance closure was 101%. Total carbohydrates [27% (± 5%) wt.] comprised of starch (5.6%), soluble monomer carbohydrates (12%) and non-starch carbohydrates (10%). Hemicellulose components (structural and non-structural) were; xylan (6%), xylose (1%), mannan (1%), mannose (0.4%), arabinan (1%), arabinose (0.4%), galatactan (3%) and galactose (0.4%). Based on the measured physical and chemical components, bio-chemical conversion route and subsequent fermentation to value added products was identified as promising. DCS has potential to serve as an important fermentation feedstock for bio-based chemicals production. In the sugar hydrolysis experiments, reaction parameters such as acid concentration and retention time were analyzed to determine the optimal conditions to maximize monomer sugar yields while keeping the inhibitors at minimum. Total fermentable sugars produced can reach approximately 86% of theoretical yield when subjected to dilute acid pretreatment (DAP). DAP followed by subsequent enzymatic hydrolysis was most effective for 0 wt% acid hydrolysate samples and least efficient towards 1 and 2 wt% acid hydrolysate samples. The best hydrolysis scheme DCS from an industry's point of view is standalone 60 minutes dilute acid hydrolysis at 2 wt% acid concentration. The combined effect of hydrolysis reaction time, temperature and ratio of enzyme to substrate ratio to develop hydrolysis process that optimizes the production of amino acids in DCS were studied. Four key hydrolysis pathways were investigated for the production of amino acids using DCS. The first hydrolysis pathway is the amino acid analysis using DAP. The second pathway is DAP of DCS followed by protein hydrolysis using proteases [Trypsin, Pronase E (Streptomyces griseus) and Protex 6L]. The third hydrolysis pathway investigated a standalone experiment using proteases (Trypsin, Pronase E, Protex 6L, and Alcalase) on the DCS without any pretreatment. The final pathway investigated the use of Accellerase 1500® and Protex 6L to simultaneously produce fermentable sugars and amino acids over a 24 hour hydrolysis reaction time. The 3 key objectives of the techno-economic analysis component of this PhD research included; (i) Development of a process design for the production of both the sugar and amino acid platforms with DAP using DCS (ii) A preliminary cost analysis to estimate the initial capital cost and operating cost of this facility (iii) A greenhouse gas analysis to understand the environmental impact of this facility. Using Aspen Plus®, a conceptual process design has been constructed. Finally, both Aspen Plus Economic Analyzer® and Simapro® sofware were employed to conduct the cost analysis as well as the carbon footprint emissions of this process facility respectively. Another section of my PhD research work focused on the life cycle assessment (LCA) of commonly used dairy feeds in the U.S. Greenhouse gas (GHG) emissions analysis was conducted for cultivation, harvesting, and production of common dairy feeds used for the production of dairy milk in the U.S. The goal was to determine the carbon footprint [grams CO2 equivalents (gCO2e)/kg of dry feed] in the U.S. on a regional basis, identify key inputs, and make recommendations for emissions reduction. The final section of my Ph.D. research work was an LCA of a single dairy feed mill located in Michigan, USA. The primary goal was to conduct a preliminary assessment of dairy feed mill operations and ultimately determine the GHG emissions for 1 kilogram of milled dairy feed.

Biochemical Conversions of Lignocellulosic Biomass for Sustainable Fuel-Ethanol Production in the Upper Midwest

Biofuels are an increasingly important component of worldwide energy supply. This research aims to understand the pathways and impacts of biofuels production, and to improve these processes to make them more efficient. In Chapter 2, a life cycle assessment (LCA) is presented for cellulosic ethanol production from five potential feedstocks of regional importance to the upper Midwest - hybrid poplar, hybrid willow, switchgrass, diverse prairie grasses, and logging residues - according to the requirements of Renewable Fuel Standard (RFS). Direct land use change emissions are included for the conversion of abandoned agricultural land to feedstock production, and computer models of the conversion process are used in order to determine the effect of varying biomass composition on overall life cycle impacts. All scenarios analyzed here result in greater than 60% reduction in greenhouse gas emissions relative to petroleum gasoline. Land use change effects were found to contribute significantly to the overall emissions for the first 20 years after plantation establishment. Chapter 3 is an investigation of the effects of biomass mixtures on overall sugar recovery from the combined processes of dilute acid pretreatment and enzymatic hydrolysis. Biomass mixtures studied were aspen, a hardwood species well suited to biochemical processing; balsam, a high-lignin softwood species, and switchgrass, an herbaceous energy crop with high ash content. A matrix of three different dilute acid pretreatment severities and three different enzyme loading levels was used to characterize interactions between pretreatment and enzymatic hydrolysis. Maximum glucose yield for any species was 70% oftheoretical for switchgrass, and maximum xylose yield was 99.7% of theoretical for aspen. Supplemental β-glucosidase increased glucose yield from enzymatic hydrolysis by an average of 15%, and total sugar recoveries for mixtures could be predicted to within 4% by linear interpolation of the pure species results. Chapter 4 is an evaluation of the potential for producing Trichoderma reesei cellulose hydrolases in the Kluyveromyces lactis yeast expression system. The exoglucanases Cel6A and Cel7A, and the endoglucanase Cel7B were inserted separately into the K. lactis and the enzymes were analyzed for activity on various substrates. Recombinant Cel7B was found to be active on carboxymethyl cellulose and Avicel powdered cellulose substrates. Recombinant Cel6A was also found to be active on Avicel. Recombinant Cel7A was produced, but no enzymatic activity was detected on any substrate. Chapter 5 presents a new method for enzyme improvement studies using enzyme co-expression and yeast growth rate measurements as a potential high-throughput expression and screening system in K. lactis yeast. Two different K. lactis strains were evaluated for their usefulness in growth screening studies, one wild-type strain and one strain which has had the main galactose metabolic pathway disabled. Sequential transformation and co-expression of the exoglucanase Cel6A and endoglucanase Cel7B was performed, and improved hydrolysis rates on Avicel were detectable in the cell culture supernatant. Future work should focus on hydrolysis of natural substrates, developing the growth screening method, and utilizing the K. lactis expression system for directed evolution of enzymes.