A new R2R capable process to produce platinum-poor fuel cells was presented in the lab scale. Platinum particles were deposited electrochemically on a mesoporous carbon carrier with various carbon carriers (Super P Li, Denka Black Li 400, Denka Black Li 435, Ketjenblack EC300). FESEM images showed particles in the range of 50 nm one the electrode surface. The catalyst containing electrodes were transferred via hot press from different metallic and polymeric decal materials on a polymer exchange membrane. First functional membrane electrode assemblies show the proof-of-principles of this new process. / Ein neuer R2R-fähiger Prozess für die Herstellung platinumarmer Brennstoffzellen wurde im Labormaßstab etabliert. Platinumpartikel wurde elektrochemisch auf einen mesoporösen Kohlenstoffträger mit verschieden Leitrußen (Super P Li, Denka Black Li 400, Denka Black Li 435, Ketjenblack EC300) abgeschieden. FESEM-Aufnahmen zeigen Partikel in der Größenordnung von 50 nm auf der Elektrodenoberfläche. Die katalysatorhaltige Elektrode wird mittels eines Heißpressverfahren auf eine Polymeraustauschmembran übertragen. Erste funktionsfähige Membran-Elektroden-Assemblierungen zeigen die Funktionsfähigkeit des Prozesses.

The yarn tension and balloon form are the most important physical process parameters to characterize the dynamic yarn path in ring spinning. The present research work focuses on the in situ measurement of yarn tension in different regions of the yarn path in a developed turbo ring spinning tester with a friction-free superconducting magnetic bearing (SMB) twisting system and at an angular spindle speed of up to 50,000 rpm. The influence of different parameters, such as angular spindle speeds (15,000–50,000 rpm), yarn counts (15–40 tex) and balloon control ring (one or multiple), were evaluated to identify the influence of acting forces, for example, centrifugal forces. The effects of these process parameters were analyzed statistically using an analysis of variance. The yarn tension between the delivery rollers and the yarn guide was measured using a modified one-roller tensile yarn tension sensor. The yarn tension between the yarn guide and the SMB system was determined with an already existing optical approach at a higher angular spindle speed. As the highest yarn tension theoretically occurs between the SMB system and the cop, it was estimated in this region by measuring the coefficient of friction between the yarn and the yarn guide using the friction module of the constant tension tester equipment. The maximum balloon diameter was determined from the recorded balloon form between the yarn guide and the SMB system with respect to different angular spindle speeds. The results provide valuable information about the highest possible spinnable speed and enable a better understanding of the dynamic yarn path in the SMB spinning system. Keywords

The change in morphology of a char particle affects both its trajectory and carbon consumption rate, hence the performance and efficiency of an entrained-flow gasifier. Among key processes taking place in the gasifier, the char conversion process is a limiting step for the overall carbon conversion. For that reason, the Ph.D. thesis presents the evolution of morphology of char particles during the carbon conversion process using particle-resolved transient CFD calculations. Analyses of numerical data obtained from the transient CFD calculations were carried out. As a result, new sub models related to the drag coefficient and the fundamental parameters of char conversion model were emerged. The new sub models were applied for modeling a pressured entrained-flow gasifier at laboratory scale. The numerical results of the gasifier show a good agreement with experimental data and an improvement of the sub models applied.

Textile structures made of biocompatible, osteoconductive and resorbable chitosan-filaments provide excellent preconditions as scaffolds for Bone Tissue Engineering applications. The novel Net Shape Nonwoven (NSN) technique that enables short fibers to be processed into three-dimensional net-shaped nonwoven structures with adjustable pore size distributions is described. NSN scaffolds made of pure chitosan fibers were fabricated. NSN hybrid scaffolds for improved initial cell adhesion were realized by combining the NSN technique with electrospinning and dip-coating with collagen, respectively. Scanning electron microscopy and liquid displacement porosimetry revealed an interconnecting open porous scaffold structure. The novel chitosan-hybrid scaffolds provide proper conditions for adhesion, proliferation and differentiation of the seeded human bone marrow stromal cells, proving that they are suitable for usage in hard-tissue regeneration.

The availability of a considerable amount of waste carbon fiber (CF) and the increased pressure to recycle/reuse materials at the end of their life cycle have put the utilization of recycled CF (rCF) under the spotlight. This article reports the successful manufacturing of hybrid yarns consisting of staple CF cut from virgin CF filament yarn and polyamide 6 fibers of defined lengths (40 and 60 mm). Carding and drawing are performed to prepare slivers with improved fiber orientation and mixing for the manufacturing of hybrid yarns. The slivers are then spun into hybrid yarns on a flyer machine. The investigations reveal the influence of fiber length and mixing ratio on the quality of the card web, slivers and on the strength of the hybrid yarns. The findings based on the results of this research work will help realize value-added products from rCF on an industrial scale in the near future.

In order to advance consistent lightweight construction principles in automotive and mechanical engineering, support frame construction made from high-performance materials is becoming more commonplace. These consist of complexly structured nodular connection elements. The required connection elements have not yet been produced satisfactorily. The developed node element structures in this paper are produced on a shuttle weaving loom by flattening and weaving them as multi-surface woven fabrics. The development of the woven concept for the realization of node element structures is based on the fragmentation of the individual sub-elements. The goal of this research is development of a flexible technology for weaving fabrics and intended for the integral realization of woven nodular semi-finished products with complex geometries and connections, which are to be used to connect Fiber-reinforced Plastic components in support frame structures.

Organic hybrid composites based on carboxylated nitrile rubber and nylon-12 reinforced with mercerized and diisocyanated lignocellulose residue (LCR) was prepared. The influence of the LCR on the viscoelastic properties of these organic hybrids was investigated by dynamic mechanical analysis and thermal analysis (differential scanning calorimetry (DSC)). It is found that either the position of the damping peak was shifted to higher values or the intensity of the damping peak was significantly increased with LCR. These results could imply that the LCR enhanced the damping properties of the composites. The thermal stability of the composites was evaluated with the mean values obtained using thermogravimetrical analysis. The decomposition rate was investigated using differential thermal gravimetry. The crystallization behavior of the prepared composites was checked by DSC.

Diese Arbeit stellt die nichtlineare Parameterschätzung als alternative Auswertemethode von Kuchenfiltrationsexperimenten vor. Anhand eines größeren Datensatzes werden die Vorteile dieser Methode gegenüber der verbreiteten Auswertung mittels einer linearisierten Form der Kuchenfiltrationsgleichung für den Fall konstanten Drucks gezeigt. Zur Bewertung der Anpassungsgüte werden Residuenplots erläutert und verwendet. Die Unterschiede der Ergebnisse bewegen sich im Bereich von 5 bis 15% bei der Bestimmung des spezifischen Kuchenfiltrationswiderstands, welcher der wichtigste Parameter bei der Auslegung von Filtrationsapparaten ist. Weitere Möglichkeiten der Auswertung werden aufgezeigt, die durch die nichtlineare Parameterschätzung möglich werden, darunter die Auswertung von Experimenten bei variablem Druck, die Bestimmung des Kuchenwiderstands kompressibler Feststoffsysteme sowie eine Bewertung der anfänglichen Verblockungsvorgänge am Filtermedium.:1 Introduction 2 Cake Filtration Theory 2.1 Historical Development 2.2 Derivation of the Cake Filtration Equation 2.3 Fit Procedures for Cake Filtration Data 2.4 Additional Methods for Finding the Time Offset 3 Materials and Methods 3.1 Materials 3.2 Filter Medium 3.3 Laboratory Pressure Filters 3.4 Example Dataset 3.5 Preparation of Example Dataset 3.6 Residual Plots and Chi-Squares 3.7 Bootstrapped Statistics 4 Proposed Fit Procedure 4.1 Nonlinear Regression 4.2 Region of Best Fit 5 Results and Discussion 5.1 Constant-Pressure Filtration 5.2 Hermans & Bredée Models 5.3 Residual Plots of Fit Results 5.4 Nonconstant Filtration 5.5 Compressibility Effects 5.6 Optimal Parameter Definition 5.7 The Role of the t/V-V-Diagram 6 Conclusions 7 Outlook 7.1 Constant-Flux Filtration 7.2 Inline Resistance Measurements 7.3 Parameter Estimation in Chemical Engineering A Appendix A.1 The Concentration Parameter A.2 Obsolete Fit Methods A.3 Residual Statistics A.4 Bootstrapped Statistics Data A.5 Fit Example in Microsoft Excel A.6 Experimental Data and Metadata B References / This thesis presents nonlinear parameter estimation as an alternative method for the evaluation of cake filtration experiments. A dataset of 225 constant-pressure filtration experiments is used to highlight the advantages of this method compared to the widely used evaluation method which uses a linear transformation of the cake filtration equation. The goodness-of-fit is tested through the means of residual plots, which are introduced and discussed. The difference in results for the two methods for the specific cake resistance parameter, which is the most important parameter in the dimensioning of filtration apparatused, lies between 5 and 15%. Further possibilities of evaluation are presented, which become possible through the use of nonlinear parameter estimation, such as: evaluation of filtration experiments with nonconstant pressure, the determination of cake resistances for compressible systems, and the investigation of the processes present in the beginning stages of cake filtration.:1 Introduction 2 Cake Filtration Theory 2.1 Historical Development 2.2 Derivation of the Cake Filtration Equation 2.3 Fit Procedures for Cake Filtration Data 2.4 Additional Methods for Finding the Time Offset 3 Materials and Methods 3.1 Materials 3.2 Filter Medium 3.3 Laboratory Pressure Filters 3.4 Example Dataset 3.5 Preparation of Example Dataset 3.6 Residual Plots and Chi-Squares 3.7 Bootstrapped Statistics 4 Proposed Fit Procedure 4.1 Nonlinear Regression 4.2 Region of Best Fit 5 Results and Discussion 5.1 Constant-Pressure Filtration 5.2 Hermans & Bredée Models 5.3 Residual Plots of Fit Results 5.4 Nonconstant Filtration 5.5 Compressibility Effects 5.6 Optimal Parameter Definition 5.7 The Role of the t/V-V-Diagram 6 Conclusions 7 Outlook 7.1 Constant-Flux Filtration 7.2 Inline Resistance Measurements 7.3 Parameter Estimation in Chemical Engineering A Appendix A.1 The Concentration Parameter A.2 Obsolete Fit Methods A.3 Residual Statistics A.4 Bootstrapped Statistics Data A.5 Fit Example in Microsoft Excel A.6 Experimental Data and Metadata B References

The need for innovative lightweight materials are rapidly increased in the recent years, owing to their cost-effective, high-strength, environmentally-sound use of materials and process technologies, in addition to that they reduce the weight of a product. The characteristics of 3D-spacer fabrics as one of the most important lightweight materials in future are multifaceted not only owing to its extremely light materials, but also because of exceptionally high stiffness to weight ratio compared to other constructions. It is also one possible method for improving the properties of fabric-reinforced composites. It can enhance the through-the-thickness properties, such as shear strength, dimensional stability, damage, tolerance, and fracture toughness that are critical for many structural applications. Spacer fabric has been employed in high-technology applications because of its critical mechanical properties related to high tensile strength, tear strength and stiffness. Furthermore, its multidirectional structures allow with more reinforcement along the thickness direction leading to an increase in stiffness and strength properties. The fundamental aim of this thesis exists in the development of a new kind of woven spacer fabrics for the light weight composites materials, in an effort to weave spacer fabrics that can not be realized with the old technology which are mentioned above. Therefore, the work in brief focuses on two main goals: 1. Development of a new kind of spacer fabrics for composites in the lightweight constructions. 2. Development of special devices of a narrow weaving machine for standing the process of the new kind of spacer fabrics production. The slippage strength test had to be carried out for the floated warp yarns through the ground fabrics by using different elements of woven fabric structures variables represented in different fabric constructions, different weft densities and different repeats of constructions by using different materials. The importance of this test related to the backward-movement of the floated warp yarns which is the crucial stage in the weaving process of spacer fabrics during the backward-movement. The results of this test determine the required forces for the backward-movement, on the other side it is the best method to observe the behavior of structure elements during the backward movement. The results of the slippage strength had been statistically analyzed, and the weaving process for the spacer fabrics had been achieved. It was concluded that the best properties for the woven spacer fabrics and the optimum case for the weaving process on the test weaving machine had been achieved when the following items are realized: Development of the narrow weaving machine is closed in assisting operations, let-off and take-up and enhancement for take-up processes. Extra let-off and take-up devices must be constructed at the weaving machine. Extra let-off device has to be used for controlling the floated warp yarns of ground fabrics. On the other side, extra take-up and the developed take-up devices have to be used for controlling the woven spacer fabrics. The experimental results give fundamental knowledges for the next steps in research and development of woven spacer fabrics made of high-performance yarns on the wide weaving machine. / Die Ziele der Arbeit bestanden in der Entwicklung der Geometrie der Spacer Fabrics und der notwendigen Falteneinrichtung an der Bandwebmaschine. Spacer Fabrics werden ausschließlich aus zwei Deckflächen, die durch eingewebte Stege verbunden sind, gefertigt. Zur Entwicklung der Spacer Fabrics muss eine Doppelnadel-Bandwebmaschine mit zwei Webfächern eingesetzt werden. Für die Faltenwebeinrichtung werden der entwickelte Extra-Kettablass und der Extra-Abzug benötigt. Der Antrieb und die Steuerung des Extra-Abzuges erfolgen durch einen Synchronantrieb und der Antrieb und die Steuerung des Extra-Ablasses durch Pneumatik.Eine frei programmierbare Steuerung der Faltenwebeinrichtung ermöglicht eine sichere und optimierte Synchronisation zwischen Webprozess und Faltenbildung. Im Ergebnis einer systematischen Strukturentwicklung von Spacer Fabrics und der Simulation ihrer günstigen Herstellung mittles eines speziell entwickelten Slippage Strength Tests werden die optimalen Strukturen ermittelt. Die experimentellen Untersuchungen bringen grundlegende Erkenntnisse für die folgenden Forschungsschritte zur Entwicklung von gewebten Spacer Fabrics mit Hochleistungsgarnen auf Doppelgreiferwebmaschinen.

Zementklinker ist der Hauptbestandteil von Zement und verbraucht zu dessen Herstellung signifikante Mengen von natürlichen Ressourcen und trägt gleichzeitig zu seiner sehr ungünstigen Treibhausgasbilanz bei. In dieser Arbeit wird gezeigt, dass Zementersatzstoffe mit spezifischen Eigenschaften aus Abfallstoffen wie Kieswaschschlämmen, Strassenwaschschlämmen und Gipskartonplatten ohne Leistungseinbußen auf Produktseite, bei geringeren Temperaturen und geringerer CO2 Emission hergestellt werden können. Entsprechend den angestrebten Eigenschaften solcher zum Teil anthropogener Zementbestandteile wurden lokal verfügbare geeignete Abfallstoffe ausgewählt und thermisch aktiviert. Eine industriell anwendbare Methode zur Aktivierung solcher Stoffe bei Temperaturen von 700 °C – 850 °C wurde entwickelt und patentiert. Es basiert auf einem neu entwickelten Trocknungsverfahren und der Kombination von zwei Produktionslinien, um durch die Verknüpfung der Gasströme beider Systeme eine energieeffiziente thermische Behandlung von Abfallstoffen zu ermöglichen sowie auf umweltfreundliche Weise einen Zementersatzstoff herzustellen.:Table of Contents List of Tables List of Figures List of Abbreviations Glossary Chapter 1: Introduction 1.1 Motivation 1.2 Research hypotheses and objectives 1.3 Research methodology 1.4 Thesis outline Chapter 2: State of the art in SCM production 2.1 Supplementary cementitious materials 2.2 Classification of SCMs 2.2.1 Classification according to origin 2.2.2 Classification according to reaction behaviour 2.3 Chemical composition of SCMs 2.4 Formation of hydraulic or pozzolanic minerals in thermal processes 2.4.1 Cement clinker 2.4.2 Burnt oil shale 2.4.3 Fly ash 2.4.4 Calcined clay 2.5 Performance of composite cements 2.6 Calcining technologies 2.6.1 Flash calciner 2.6.2 Rotary calciner 2.7 Comparison of process technologies 2.8 Summary of Chapter 2 Chapter 3: Alternative SCMs and a new method for activation 3.1 Introduction 3.2 Target of alternative SCM 3.3 Waste materials 3.3.1 Aggregate washing sludge 3.3.2 Road cleaning sludge 3.3.3 Deconstruction gypsum 3.4 Producing alternative SCMs 3.5 Thermal activation of alternative SCMs 3.6 Limitations in current calcining technology 3.6.1 Difficult emission control 3.6.1.1 Particulate emission 3.6.1.2 Gaseous emission 3.6.2 Challenging material preparation 3.6.3 Demand for noble fuels 3.6.4 Difficult colour control 3.6.5 Strict temperature control 3.6.6 CO2 footprint of calciners 3.7 Proposed new method of calcination 3.7.1 Feed material handling 3.7.2 Thermal heat-exchange system 3.7.3 Clay calciner design 3.7.4 Grinding 3.8 Summary Chapter 3 Chapter 4: Theoretical Considerations 4.1 Material considerations 4.1.1 Composition of alternative SCM 4.1.2 Anticipated products and characteristics 4.2 Process considerations 4.2.1 System capacity 4.2.2 Material characteristics 4.2.3 Material receiving, crushing and handling 4.2.4 Thermodynamic modelling 4.2.4.1 Mass balance 4.2.4.2 Drying and cooling heat balance 4.2.4.3 Calcination heat balance 4.2.4.4 Gas balance 4.2.4.5 Impact on clinker kiln line 4.2.4.6 Impact of calcite on the gas balance 4.2.5 Calciner design 4.2.6 Colour control 4.2.7 Emission prediction 4.2.7.1 Emission during drying 4.2.7.2 Emission during calcination 4.2.8 CO2 footprint of produced material 4.2.9 Grinding requirements 4.3 Summary of Chapter 4 Chapter 5: Experimental tests and proof of concept 5.1 Introduction 5.2 Sampling and characterization 5.2.1 Kaolinitic AWS from France 5.2.2 Non-kaolinitic AWS from Switzerland 5.2.3 Road cleaning sludges from Switzerland 5.2.4 Deconstruction gypsum from Switzerland 5.2.5 Sample preparation and shipping 5.3 Drying screw conveyor testing 5.4 Calcination testing 5.4.1 Mineralogy of activated products 5.4.1.1 Non-kaolinitic SCM 5.4.1.2 Kaolinitic AWS from France 5.4.2 Colour 5.5 Crushing tests 5.6 Grinding tests 5.7 Mortar compressive strength testing 5.8 Water demand testing 5.9 Summary of Chapter 5 Chapter 6: Experimental results 6.1 Characteristics of activated materials 6.2 Concrete performance and colour 6.2.1 Thermally activated kaolinitic AWS from France 6.2.2 Thermally activated non-kaolinitic alternative SCM from Switzerland 6.3 Equipment dimensioning 6.3.1 Process mass flow 6.3.2 Heat-exchanging screws and thermal oil system 6.3.3 Rotary calciner dimensioning 6.3.4 Ball mill dimensioning 6.4 CO2 reduction 6.5 Summary of Chapter 6 Chapter 7: Conclusion and outlook 7.1 Conclusions 7.2 Outlook. Literature