Enzyme engineering of aminotransferases for improved activity and thermostability

The production by biosynthesis of optically active amino acids and amines satisfies the pharmaceutical industry in its demand for chiral building blocks for the synthesis of various pharmaceuticals. Among several enzymatic methods that allow the synthesis of optically active aminoacids and amines, the use of minotransferase is a promising one due to its broad substrate specificity and no requirement for external cofactor regeneration. The synthesis of chiral compounds by aminotransferases can be done either by asymmetric synthesis starting from keto acids or ketones, and by kinetic resolution starting from racemic aminoacids or amines. The asymmetric synthesis of substituted (S)-aminotetralin, an active pharmaceutical ingredient (API), has shown to have two major factors that contribute to increasing the cost of production. These factors are the raw material cost of biocatalyst used to produce it and product loss during biocatalyst separation. To minimize the cost contribution of biocatalyst and to minimize the loss of product, two routes have been chosen in this research: 1. To engineer the aminotransferase biocatalyst to have greater specific activity, and 2. Improve the engineering of the process by immobilization of biocatalyst in calcium alginate and addition of cosolvents. An (S)-aminotransferase (Mutant CNB03-03) was immobilized, not as purified enzyme but as enzyme within spray dried cells, in calcium alginate beads and used to produce substituted (S)-aminotetralin at 50 °C and pH 7 in experiments where the immobilized biocatalyst was recycled. Initial rate of reaction for cycle 1 (6 hr duration) was determined to be 0.258 mM/min, for cycle 2 (20 hr duration) it decreased by ~50% compared to cycle 1, and for cycle 3 (20 hr duration) it decreased by ~90% compared to cycle 1 (immobilized preparation consisted of 50 mg of spray dried cells per gram of calcium alginate). Conversion to product for each cycle decreased as well, from 100% in cycle 1 (About 50 mM), 80% in cycle 2, and 30% after cycle 3. This mutant was determined to be deactivated at elevated temperatures during the reaction cycle and was not stable enough to allow multiple cycles in its immobilized form. A new mutant aminotransferase was isolated by applying error-prone polymerase chain reaction (PCR) on the gene coding for this enzyme and screening/selection: CNB04-01. This mutant showed a significant improvement in thermostability in comparison to CNB03-03. The new mutant was immobilized and tested under similar reaction conditions. Initial rate remained fairly constant (0.2 mM/min) over four cycles (each cycle with a duration of about 20 hours) with the mutant retaining almost 80% of initial rate in the fourth cycle. The final product concentrations after each cycle did not decrease during recycle experiments. Thermostability of CNB04-01 was much improved compared to CNB03-03. Under the same reaction conditions as stated above, the addition of co-solvents was studied in order to increase substituted tetralone solubility. Toluene and sodium dodecylsulfate (SDS) were used. SDS at 0.01% (w/v) allowed four recycles of the immobilized spray dried cells of CNB04-01, always reaching higher product concentration (80-85 mM) than the system with toluene at 3% (v/v) -70 mM-. The long term activity of immobilized CNB04-01 in a system with SDS 0.01% (w/v) at 50 °C, pH 7 was retained for three cycles (20 to 24 hours each one), reaching always final product concentration between 80-85 mM, but dropping precipitously in the fourth cycle to a final product concentration of 50 mM. Although significant improvement of immobilization on productivity and stability were observed using CNB04-01, another observation demonstrated the limitations of an immobilization strategy on reducing process costs. After analyzing the results of this experiment it was seen that a sudden drop occurred on final product concentration after the third recycle. This was due to product accumulation inside the immobilized preparation. In order to improve the economics of the process, research was focused on developing a free enzyme with an even higher activity, thus reducing raw material cost as well as improving biomass separation. A new enzyme was obtained (CNB05-01) using error-prone PCR and screening using as a template the gene derived from the previous improved enzyme. This mutant was determined to have 1.6 times the initial rate of CNB04-01 and had a higher temperature optimum (55°). This new enzyme would allow reducing enzyme loading in the reaction by five-fold compared to CNB03-03, when using it at concentration of one gram of spray dried cells per liter (completing the reaction after 20-24 hours). Also this mutant would allow reducing process time to 7-8 hours when used at a concentration of 5 grams of spray dried cells per liter compared to 24 hours for CNB03-03, assuming that the observations shown before are scalable. It could be possible to improve the economics of the process by either reducing enzyme concentration or reducing process time, since the production cost of the desired product is primarily a function of both enzyme concentration and process time.

SURFACTANT-OIL INTERACTIONS: FOAMING & TOXICITY

Surfactants find large applications in detergents, paints, coatings, food and pharmaceutical industries. Other than that, much focused work has been carried out in oil recovery in petroleum industries and raw material extraction in mining industries. This is because of their unique structure and ability to simultaneously adhere to materials which are both structurally and physically different. The current thesis focuses on interactions of oil with different commercially available and laboratory synthesized surfactants in terms of characteristics such as foaming, ultrasound exposure and toxicity. Foaming is one important characteristic of surfactants that is widely utilized for oil recovery purposes. Researchers utilize surfactants' special ability to provide foam stability to for more efficient oil herding capability. The foam stability and foam volumes are calculated using static foam height tests. Further dispersion or oil in water emulsion formation is observed using ultrasound sources. As described earlier surfactants are not only used as foams for oil displacement, but they are also used for dispersion purposes where they are key components of dispersant formulations. During such operations, especially in sea conditions where adverse effects on aquatic life are a concern, toxicity of chemicals used becomes an important factor. Our toxicity testing experiments involves different surfactants, solvents and crude oil combinations through exposure to special light luminescent bacteria. The decrease in light intensity of the exposed bacteria is related to toxic effects of the samples.

DYNAMICS AND CONTROL OF REACTIVE DISTILLATION PROCESS FOR MONOMER SYNTHESIS OF POLYCARBONATE PLANTS

Polycarbonate (PC) is an important engineering thermoplastic that is currently produced in large industrial scale using bisphenol A and monomers such as phosgene. Since phosgene is highly toxic, a non-phosgene approach using diphenyl carbonate (DPC) as an alternative monomer, as developed by Asahi Corporation of Japan, is a significantly more environmentally friendly alternative. Other advantages include the use of CO2 instead of CO as raw material and the elimination of major waste water production. However, for the production of DPC to be economically viable, reactive-distillation units are needed to obtain the necessary yields by shifting the reaction-equilibrium to the desired products and separating the products at the point where the equilibrium reaction occurs. In the field of chemical reaction engineering, there are many reactions that are suffering from the low equilibrium constant. The main goal of this research is to determine the optimal process needed to shift the reactions by using appropriate control strategies of the reactive distillation system. An extensive dynamic mathematical model has been developed to help us investigate different control and processing strategies of the reactive distillation units to increase the production of DPC. The high-fidelity dynamic models include extensive thermodynamic and reaction-kinetics models while incorporating the necessary mass and energy balance of the various stages of the reactive distillation units. The study presented in this document shows the possibility of producing DPC via one reactive distillation instead of the conventional two-column, with a production rate of 16.75 tons/h corresponding to start reactants materials of 74.69 tons/h of Phenol and 35.75 tons/h of Dimethyl Carbonate. This represents a threefold increase over the projected production rate given in the literature based on a two-column configuration. In addition, the purity of the DPC produced could reach levels as high as 99.5% with the effective use of controls. These studies are based on simulation done using high-fidelity dynamic models.

3D-Druck von Kunststoff-Medizinprodukten

Das Additive Manufacturing gewinnt im Bereich der Medizintechnik zur Herstellung von Prototypen bis hin zu Endprodukten zunehmend an Bedeutung. Ein großes Hemmnis stellen allerdings die relativ hohen Fertigungskosten dar. Hier bietet der verstärkte Einsatz der 3D-Drucktechnologie (3D Printing) ein erhebliches Potential zur Reduktion der Kosten. Aus dieser Motivation heraus wurde ein 3D-Druckverfahren zur Herstellung biokompatibler, sterilisierbarer Kunststoffmodelle entwickelt. Beim 3D-Druck-Verfahren handelt es sich um einen pulverbasierten Prozess zur schichtweisen Herstellung von Modellen direkt aus Computerdaten. Dabei werden dünne Schichten eines Pulvers auf eine Grundplatte aufgebracht, die dann durch gezielte Binderzugabe entsprechend des aktuellen Bauteilquerschnitts verfestigt werden. Ausgangsmaterial für diesen Prozess ist ein Granulatgemisch auf Basis von PMMA (Polymethylmethacrylat). Als Binderflüssigkeit wird ein Lösungsmittel eingesetzt. Die 3D gedruckten Modelle werden nach einer entsprechenden Trocknungszeit im Pulverbett entpackt und warmgelagert, um das Abdampfen des Lösungsmittels zu beschleunigen. Der Nachweis der Biokompatibilität der hergestellten Modelle erfolgte durch einen Test nach DIN EN ISO 10993-5. In Kooperation mit Anwendern wurden verschiedene Anwendungsbeispiele wie Bohrschablonen, Otoplastiken, Gebissmodelle und Modelle für die präoperative Planung realisiert und charakterisiert.

Experimentelle Analyse von Last- und Treibketten zur Optimierung der Lebensdauer

Zusammen mit einem namhaften Kettenhersteller hat das Institut für Fördertechnik und Logistik (IFT) im Rahmen eines AIF-geförderten Forschungsprojektes einen Kettenverschleißprüfstand für Last- und Treibketten entwickelt und gebaut, um neuentwickelte Ketten in kurzen Testphasen unter normierter Umgebung auf ihre Lebensdauer bzw. Verschleißfestigkeit zu prüfen. Durch steigende Rohstoffkosten und den immer größer werdenden Konkurrenzdruck im Bereich der Ketten entsteht ein hoher Bedarf an der Entwicklung neuer leistungsfähigerer Produkte. Die Neuheit dieser Projektidee liegt in dem erstmaligen Einsatz alternativer Werkstoffe und Konstruktionen in Kombination mit neuen verschleißarmen Beschichtungsverfahren für Kettenbauteile um Schmierstoffe langfristig einzulagern und bedarfsgerecht abzugeben

Complications with computer-aided designed/computer-assisted manufactured titanium and soldered gold bars for mandibular implant-overdentures: short-term observations

BACKGROUND Implant-overdentures supported by rigid bars provide stability in the edentulous atrophic mandible. However, fractures of solder joints and matrices, and loosening of screws and matrices were observed with soldered gold bars (G-bars). Computer-aided designed/computer-assisted manufactured (CAD/CAM) titanium bars (Ti-bars) may reduce technical complications due to enhanced material quality. PURPOSE To compare prosthetic-technical maintenance service of mandibular implant-overdentures supported by CAD/CAM Ti-bar and soldered G-bar. MATERIALS AND METHODS Edentulous patients were consecutively admitted for implant-prosthodontic treatment with a maxillary complete denture and a mandibular implant-overdenture connected to a rigid G-bar or Ti-bar. Maintenance service and problems with the implant-retention device complex and the prosthesis were recorded during minimally 3-4 years. Annual peri-implant crestal bone level changes (ΔBIC) were radiographically assessed. RESULTS Data of 213 edentulous patients (mean age 68 ± 10 years), who had received a total of 477 tapered implants, were available. Ti-bar and G-bar comprised 101 and 112 patients with 231 and 246 implants, respectively. Ti-bar mostly exhibited distal bar extensions (96%) compared to 34% of G-bar (p < .001). Fracture rate of bars extensions (4.7% vs 14.8%, p < .001) and matrices (1% vs 13%, p < .001) was lower for Ti-bar. Matrices activation was required 2.4× less often in Ti-bar. ΔBIC remained stable for both groups. CONCLUSIONS Implant overdentures supported by soldered gold bars or milled CAD/CAM Ti-bars are a successful treatment modality but require regular maintenance service. These short-term observations support the hypothesis that CAD/CAM Ti-bars reduce technical complications. Fracture location indicated that the titanium thickness around the screw-access hole should be increased.

Production of Ethanol from Hardwood

Diminishing crude oil and natural gas supplies, along with concern about greenhouse gas are major driving forces in the search for efficient renewable energy sources. The conversion of lignocellulosic biomass to energy and useful chemicals is a component of the solution. Ethanol is most commonly produced by enzymatic hydrolysis of complex carbohydrates to simple sugars followed by fermentation using yeast. C6Hl0O5 + H2O −Enxymes→ C6H12O6 −Yeast→ 2CH3CH2OH + 2C02 In the U.S. corn is the primary starting raw material for commercial ethanol production. However, there is insufficient corn available to meet the future demand for ethanol as a gasoline additive. Consequently a variety of processes are being developed for producing ethanol from biomass; among which is the NREL process for the production of ethanol from white hardwood. The objective of the thesis reported here was to perform a technical economic analysis of the hardwood to ethanol process. In this analysis a Greenfield plant was compared to co-locating the ethanol plant adjacent to a Kraft pulp mill. The advantage of the latter case is that facilities can be shared jointly for ethanol production and for the production of pulp. Preliminary process designs were performed for three cases; a base case size of 2205 dry tons/day of hardwood (52 million gallons of ethanol per year) as well as the two cases of half and double this size. The thermal efficiency of the NREL process was estimated to be approximately 36%; that is about 36% of the thermal energy in the wood is retained in the product ethanol and by-product electrical energy. The discounted cash flow rate of return on investment and the net present value methods of evaluating process alternatives were used to evaluate the economic feasibility of the NREL process. The minimum acceptable discounted cash flow rate of return after taxes was assumed to be 10%. In all of the process alternatives investigated, the dominant cost factors are the capital recovery charges and the cost of wood. The Greenfield NREL process is not economically viable with the cost of producing ethanol varying from $2.58 to $2.08/gallon for the half capacity and double capacity cases respectively. The co-location cases appear more promising due to reductions in capital costs. The most profitable co-location case resulted in a discounted cash flow rate of return improving from 8.5% for the half capacity case to 20.3% for the double capacity case. Due to economy of scale, the investments become more and more profitable as the size of the plant increases. This concept is limited by the amount of wood that can be delivered to the plant on a sustainable basis as well as the demand for ethanol within a reasonable distance of the plant.

Caracterización de germoplasma de topinambur (Helianthus tuberosus L.) por aptitud agronómica e industrial

El topinambur pertenece a la familia de las Asteráceas, es una especie originaria de América del Norte, de la que fundamentalmente se aprovechan sus tubérculos; tiene gran potencial como alimento, materia prima para productos industriales y producción de biocombustibles. En Argentina no hay cultivares de topinambur registrados. Sin embargo hay documentación y testimonios del ingreso de distintas variedades al país a principios del siglo XX. El objetivo de esta tesis fue caracterizar el germoplasma de topinambur que se cultiva, a pequeña escala, en distintas regiones de la Argentina. Se formó una colección de trabajo con introducciones provenientes de 5 provincias del país (Río Negro, Chubut, Buenos Aires, Mendoza y Córdoba), y se condujeron ensayos experimentales en dos ambientes de la provincia de Mendoza. Se evaluaron caracteres morfológicos (altura de plantas, dimensiones y ángulo de inserción de hojas, tamaño de tubérculos), fenológicos (emergencia, inicio, fin y duración de floración, senescencia del cultivo) y rendimiento. Se detectaron diferencias morfológicas que permitieron agrupar a las introducciones en dos grupos, correspondiendo uno a introducciones de tubérculos rojos y el otro a introducciones de tubérculos blancos. Se valoró la aptitud hortícola de las introducciones mediante evaluación sensorial; se realizó una prueba de preferencia y percepción de distintos aspectos de la hortaliza (color, olor, sabor y textura), consumida cruda. El nivel de aceptación general de la hortaliza fue bueno. Se evaluó el potencial industrial (obtención de inulina y producción de etanol). Se determinó por HPLC el contenido de inulina de cada introducción, que varió de 18.07 a 22.95 % y se estimó el potencial para producir etanol a partir de los hidratos de carbono fermentables de los tubérculos, que llegó a 4.934 litros por ha, aunque sin diferencias entre introducciones.

Tecnología cerámica : estudios experimentales sobre la cerámica del sitio arqueológico San Ignacio (Noroeste de Mendoza)

El propósito de este trabajo es explorar la disponibilidad de materias primas que pudieron ser utilizadas en el proceso de manufactura de la cerámica gris del sitio arqueológico San Ignacio, en el Valle de Potrerillos, ubicado al Norte de la provincia de Mendoza (640 dC). Se pretende, además, reproducir las técnicas de producción y cocción cerámica, a fin de obtener un producto de características análogas a las de la colección estudiada. La metodología utilizada presentó las siguientes etapas: recolección de materiales arcillosos; caracterización de las propiedades físicas en estado crudo; análisis químicos; desarrollo experimental de cocción y ensayos post-cocción de los mismos. Los productos obtenidos muestran una buena estructura y sinterización, aunque no se logró una atmósfera completamente reductora con este tipo de combustible.

Uso de aguas residuales urbanas en el riego de colza (Brassica napus L.) con destino a biocombustible

El aceite de colza es comestible pero también puede utilizarse en la producción de biodiesel. Cuando el destino es el energético, el cultivo puede regarse con aguas residuales urbanas o cloacales. La mayor proporción del uso de éstas en el mundo ocurre en regiones áridas donde otras fuentes de agua son escasas, situación que se plantea en los oasis irrigados de Mendoza. En este trabajo se comparó el rendimiento de un cultivar invernal de colza regado con agua cloacal (AC) y agua subterránea (AS), y su potencial para producir biodiesel. La experiencia se llevó a cabo en una planta de tratamiento de agua cloacal de Obras Sanitarias en el departamento Tunuyán (33° 32’ 89’’ S; 69° 00’ 80’’ O; 859 m snm). El rendimiento de semilla de AC fue significativamente mayor que el de AS (7690 y 3886 kg/ha, respectivamente). La cantidad de biodiesel factible de producir por cada hectárea de cultivo asciende a 2800 kg en el tratamiento AC y a 1400 kg en AS. El uso de aguas residuales urbanas genera un nicho interesante para la producción de biocombustibles, utilizando un recurso hídrico con limitaciones para producir alimentos.

Uso de agua en industrias de elaboración de conservas de tomate y de durazno de Mendoza, Argentina

El objetivo de este trabajo es conocer, a nivel de cuenca, el volumen de agua utilizado por las industrias de elaboración de conservas de tomate y de durazno de Mendoza. Para ello se estima la materia prima utilizada en la elaboración de estas conservas a partir de datos de superficie cultivada para tal destino y de rendimientos por superficie obtenidos en el Registro Permanente de Uso de la Tierra de Mendoza y el Instituto Nacional de Tecnología Agropecuaria. Se emplearon coeficientes de volumen de agua utilizada por unidad de materia prima procesada, que varían entre 5 y 25 L kg-1 de producto procesado, sin incluir el uso de agua para riego en fincas. Los resultados se analizaron para diferentes valores de coeficientes asociados a la eficiencia del uso del agua, en escenarios optimista y pesimista. Se concluye que las industrias elaboradoras de conservas de tomate y de durazno de Mendoza utilizan entre 0,66 y 6,15 hm3/año. El mayor consumo de agua de las conserveras de tomate ocurre en la cuenca Norte, alcanzando el 64,9% del total demandado por tales industrias. Para las conserveras de durazno, el mayor consumo se produce en la cuenca Sur con un 46% de total demandado.