Chemical Reaction Engineering

Hydrogenation of aqueous solutions of sugars from renewable resources

Nowadays, the majority of chemicals are produced from fossil resources like crude oil or natural gas. Considering the high related emissions of carbon dioxide, alternative sustainable processes based on renewable resources such as sugars, sugar alcohols, oils and lignocellulose become more and more attractive. An example for such sustainable syntheses is the production of polyols from sugar. These polyols are applied in the polymer industry and as source material for different plastics. Moreover, some small chain polyols are being used as deicer in the aviation industry. Due to good emulsifying properties of some polyols, they can be used as supporting material for colorants, antioxidants and enzymes in chemical, pharmaceutical, cosmetic and food applications.
The aim of this project is to develop a process for the hydrogenation of aqueous solution of sugars to produce polyols. Besides the selection of a suitable catalyst and reaction conditions, an adequate analysis method for the complex product mixture has to be developed and phase equilibria in the reactor have to be considered. For the determination of the reaction kinetics, systematic experiments at pressures of up to 120 bar are performed in a stirred tank reactor.

Contact: Carina Kirstein, M. Sc.

Unsteady-State Methanation of Carbon Oxides

One of the most intensively discussed processes for the chemical storage of renewable energy is the methanation of carbon oxides (CO, CO2). In this process renewable electrical energy is transferred into hydrogen by electrolysis of water, which is used for the hydrogenation of carbon oxides into synthetic natural gas (SNG). The concept, known as “Power-to-Gas”, is complicated by the unsteady state availability of hydrogen, due to the fluctuation in renewable energy supply. However, the unsteady state behaviour of the methanation reaction is still not completely understood. Consequently, the project aims at understanding the unsteady state processing during this reaction in order to contribute to the industrial implementation of the methanation in renewable energy storage.

Contact: Bjarne Kreitz, M. Sc.

Micro- and milli-structured fixed bed reactors

 Supported by:

Heterogeneously catalyzed gas-phase reactions such as the synthesis of maleic anhydride, phthalic anhydride or acrolein exhibit highly exothermic behavior. On industrial scale, these reactions are conducted in multi-tubular reactors with up to 30.000 single tubes including the catalytic fixed bed. Due to the limited heat removal in the radial direction of the fixed bed axial temperature profiles with hot spots occur, thus reducing the reactor performance. A significant increase in heat removal can be achieved by reducing the reactor dimensions down to the micro- and milli-structured scale. Thereby the specific surface area for the heat removal is enhanced while the characteristic length of the radial heat conduction through the fixed bed is reduced.
The aim of this project is to investigate this type of process intensification for the selective oxidation of n-butane to maleic anhydride. The main focus of the investigations is to determine the optimal geometric configuration of catalyst and reaction channels with regard to high product yields and low pressure drops. Therefore experiments with different catalyst fractions and channel geometries are conducted with variable concentration of n-butane and volume flow rates of the reactants, which are evaluated with a suitable mathematical reactor model.

Contact: Mauritio Müller, M. Sc.

Experimental studies of high-temperature reactions in a downer reactor

When gas-solid reactions are carried out in a circulating fluidized bed (CFB), the commonly used riser is strongly affected by backmixing of phases because of solid downflow near the wall resulting in a broad residence time distribution (RTD). In a downer reactor, however, backmixing is minimized due to the same direction of gravity and gas flow. Therefore plug-flow behavior can be approximated. In a laboratory scale downer reactor ceramic powders will be studied during different high-temperature chemical reactions. For this purpose, different temperatures, gases, gas velocities and mass flows of solids and gas are going to be used. Furthermore, a mathematical model will be developed which allows for both analysis of the experiments and scale-up of the reactor.

Contact: Prof. Dr.-Ing. Thomas Turek

Heterogeneously catalyzed reactive extraction for the hydration of olefins

Within this project the concept of a reactive extraction for process intensification will be investigated using the example of the hydration of propene to isopropyl alcohol with an acid ion exchange resin as catalyst. At high pressure the reaction mixture forms two phases: The reaction takes place in the aqueous phase surrounding the solid catalyst and the product is simultaneously extracted to the organic phase. Using a lab-scale reactive extraction column equipped with a structured packing containing the catalyst the influence of the flow directions, the residence times and the hold-ups of both phases as well as the wettability and flow characteristics of the structured packing will be determined. Furthermore, a formerly developed mathematical model for this process shall be verified experimentally.

Contact: Prof. Dr.-Ing. Ulrich Kunz

Catalysts and reactors for Fischer-Tropsch synthesis

 Supported by:

The Fischer-Tropsch synthesis (FTS) is a well-known reaction for the production of liquid hydrocarbon products from synthesis gas, which is currently undergoing a renaissance through the construction of large-scale plants for the conversion of natural gas ("Gas-to-Liquid"). The ICVT is working in the field of FTS since 2005, particularly on topics related to catalysts and reactors for low temperature synthesis. One of these topics is the development of structured catalysts and reactors, especially honeycomb structures and micro-structured fixed-bed reactors. Current research focusses on structuring catalysts on length scales below 1 µm. One project deals with the effect of pore diameter and structure on the activity and product composition. For that purpose a hierarchical pore structure is created and studied under synthesis conditions. Furthermore, bi-functional catalysts with activity in FTS and product upgrading are synthesized and evaluated. For performing the experimental investigations two experimental setups and the required analysis methods are available.

Contact: Dipl.-Chem. Nadine Kruse, Matthias Klee, M. Sc.

Electrochemical Engineering

The bio-electrical fuel cell as a component of an energy producing wastewater treatment equipment

 Supported by: ERWAS Joint Project

Goals of the subproject at the Institute of Chemical and Electrochemical Process Engineering (ICVT):

  • Selection of materials and material combinations for the electrode production
    Mainly carbon-polymer compounds of the cooperation partner Eisenhuth GmbH shall be examined referring to their performance as components for bio-electrical fuel cells. Those compounds are, by methods of polymer processing, producable in large quantities.
  • Selection and processing of catalysts and their precursors to obtain catalytically active layers
    The laminating methods available at the institute, especially a wet spraying process, shall come into operation. The potentials of laminating carbon-polymer compounds with materials on which biofilms can grow, shall be examined.
  • Operation of test fuel cells in a fuel cell testing equipment
    These procedures will be useful to identify appropriate materials, material combinations and operating procedures for test cell prototypes, as basic know-how for a future pilot plant designing and operation, concerted with the project partners.

Contact: MSc Bolong Jiang

Wastewater Treatment by Radicals - RADAR

 Supported by:

Numerous organic trace compounds as well as drug residues are found in municipal wastewater, which is insufficient purified by the biology of sewage treatment plants. Moreover, many process waters of the chemical industry are contaminated with organic compounds, too.
In order to remove the trace elements, an electrochemical wastewater treatment concept is developed for the first time within RADAR project (RADAR: german abbreviation for „Radikalische Abwasserreinigung; English: wastewater treatment by radicals). The developed concept will be realized up to demonstration scale. The basis of the new concept is a combination of a boron-doped diamond electrode and a gas diffusion electrode for generating highly oxidative species simultaneously. Furthermore, auxiliary electrodes are examined to avoid scaling on cathode side.
In the subproject of the Institute of Chemical and Electrochemical Process Engineering, the electrochemical evaluation of electrodes and the identification of best operating points will be done.

Gas diffusion electrodes of the project partner Covestro AG, diamond electrodes of the company Condias GmbH as well as auxiliary electrodes of Eisenhuth GmbH are evaluated. For the systematic exploration laboratory-scale reactors are used to identify degradation rates and the decalcification potential.

Aim of research is the identification of the most promising electrode material combination and an appropriate process engineering design, which is suitable for the technical realization of a novel electrochemical pollutant elimination.

Contact: Thorben Muddemann, M. Sc.

Alkaline water electrolysis - Analysis of cell and electrode geometries

Due to the strong expansion of renewable energies and the intermitting and fluctuating availability of wind- and solar energy large storage capabilities for electric energy need to be found. Currently the "Power to Gas" - concept is discussed to serve the long-term storage of huge amounts of energy. The idea is to save the electric energy from renewable sources in chemical compounds. A promising technology is the alkaline water electrolysis for the production of hydrogen, which in turn can be used for the synthesis of methane. In industry this form of water electrolysis has already been used for several decades, however no further scientific research was carried out.
Within the scope of this project, cell- and electrode geometries are examined, which promise a reduction in specific hydrogen production costs. Furthermore a mathematical model for the analysis of laboratory experiments is being developed.

Contact: M.Sc. Philipp Haug, M.Sc. Matthias Koj

DFG Research Unit „Multiscale analysis of complex three-phase systems: oxygen-reduction at gas-diffusion electrodes in aqueous electrolyte” (FOR 2397)

 Supported by:

Gas-diffusion electrodes (GDE) are key components for different electrochemical processes. This includes the transformation of chemically stored energy into electrical energy in fuel cells and metal-air batteries as well as the reversal of these energy conversion processes in the chlor-alkali electrolysis. However, in many technologies, gas diffusion electrodes are the limiting components and thus the main cost factor.

To improve the efficiency of GDE, it is necessary to have an overall comprehension of the complex interaction of transport and reaction processes inside the electrodes. In order to investigate these processes, subprojects of seven research facilities in Germany are combined in the DFG Research Unit.

At the ICVT working GDE are produced from silver powders and characterized by different methods. The measurements involve physico-chemical characterization of the pore systems and electrochemical measurements in half-cells. Based on these measurements it is possible to determine quantatively the effect of process conditions and electrode properties on the overpotential of the oxygen reduction reaction. Results of all subprojects will be also used to improve a mathematical model, which describes the stationary overpotential of the GDE.

Further information is given on the website of the DFG Research Unit.

Ansprechpartner: David Franzen, M. Sc., Barbara Ellendorff

Development of large-scale vanadium redox-flow batteries

Due to the turnaround in energy policy towards sustainability, renewable energies are playing an increasingly important role as power sources. Since both, the electricity supply and demand, fluctuate with the time of day and the time of year, efficient and cost-effective storage technologies are needed on an industrial scale. The goal of this project is to create the fundamentals for designing a vanadium redox-flow battery. This includes the material characterisation of porous carbon felts, bipolar plates and membranes as well as the development of a mathematical model which describes the processes within the battery. Furthermore, this results in an optimisation of the cell construction and the technical operations procedures of the overall system. The investigation is completed by an automated cell test bench. With this test bench single cell measurements can be performed at different operational conditions with an integrated inline and online analysis which allows an evaluation of the mathematical model. This project is carried out in cooperation with ThyssenKrupp Industrial Solutions AG.

Contact: Katharina Schafner, M. Sc.

Application of porous glass membranes in redox flow batteries - analysis of the influences of membrane thickness, pore structure and surface modification

 Supported by:

Two promising fields of research come together in the analysis of possible applications of porous glass membranes in redox flow batteries in this joint project of the institute for technical chemistry at Leipzig university and the institute for chemical and electrochemical process engineering at Clausthal university of technology. Redox flow batteries (RFB) count as promising candidates in the search for an efficient and reliable energy storage while porous glasses offer outstanding properties as a material for membranes in electrochemical applications.

In this project native as well as surface modified or charged porous glass membranes based on phase separated alkaliborosilicate glasses with varying pore structures are evaluated considering their usability in vanadium redox flow batteries (VRFBs). These membranes surfaces shall be modified in several ways or are to be charged with sulfuric acid or vanadium salts containing electrolytes.

The influence of the parameters pore size, pore structure, membrane thickness and surface functionalisation or charge concerning the usability of porous glass membranes as a separator in VRFBs are characterized and evaluated for the first time.

Contact: Dipl.-Ing. Horst Mögelin

New large size bipolar plates for redox-flow batteries produced with the extrusion process

 Gefördert durch:

Redox-flow batteries are suitable for storing electricity from fluctuating renewable energy. At present, commercial systems have a stack performance in the kilowatt range due to the limited size of the bipolar plates. This is significantly lower than required during the future development of the German “Energiewende”. Due to the modular design of redox-flow batteries it is possible to build energy storage devices with higher capacity and power by a numbering up of the existing cells. However, this results in too high specific investment costs. An alternative for providing storage capacities of at least 10 megawatts is a real scale up of the active cell area to 2 m² to 3 m². However, the production of those large bipolar plates with conventional processes such as pressing and injection molding is a challenge as the quality requirements are not yet fulfilled. Therefore this research project examines the production of new large and stable bipolar plates with the extrusion process. The characteristics of the developed bipolar plate are analyzed, and cell designs are proposed with the aid of a mathematical model.

For further information look here.

Ansprechpartner: Eva Prumbohm M. Sc.


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