CFD Study of the Numbering up of Membrane Microreactors for CO2 Capture

Carbon dioxide (CO2) is one of the major atmospheric greenhouse gases (GHG). The continuous increase of CO2 concentration and its long atmospheric lifetime may cause long-term negative effects on the climate. It is important to develop technologies to capture and minimize those emissions into the atmosphere. The objective of this work is to design and study theoretically and experimentally a numbering-up/scale-out membrane microreactor in order to be used as a capture system. The main aim of the work is to obtain an even flow distribution at each plate of the reactor. Nearly uniform flow distribution was achieved at each layer of the numbering-up microreactor according to the carried-out CFD models. The maximum difference between the average velocities was less than 6% for both gas and liquid flows. To obtain better flow distribution into the microreactor, the radius of the inlet/outlet tube was optimized. Results from CFD and experimental simulations do not match, and slightly maldistribution in achieved in the experimental system due to phase breakthrough and imperfections on the fabrication of the plates. Moreover, comparing the single channel microreactor to the scale-out microreactor, the latter showed poorer performance on CO2 removal while expecting the reactors to have similar performance. By installing inserts with different channel widths, the experimental results were identical to the original case.

CO2 capture using membrane contactors: a systematic literature review

With fossil fuel being the major source of energy, CO2 emission levels need to be reduced to a minimal amount namely from anthropogenic sources. Energy consumption is expected to rise by 48% in the next 30 years, and global warming is becoming an alarming issue which needs to be addressed on a thorough technical basis. Nonetheless, exploring CO2 capture using membrane contactor technology has shown great potential to be applied and utilised by industry to deal with post- and pre-combustion of CO2. A systematic review of the literature has been conducted to analyse and assess CO2 removal using membrane contactors for capturing techniques in industrial processes. The review began with a total of 2650 papers, which were obtained from three major databases, and then were excluded down to a final number of 525 papers following a defined set of criteria. The results showed that the use of hollow fibre membranes have demonstrated popularity, as well as the use of amine solvents for CO2 removal. This current systematic review in CO2 removal and capture is an important milestone in the synthesis of up to date research with the potential to serve as a benchmark databank for further research in similar areas of work. This study provides the first systematic enquiry in the evidence to research further sustainable methods to capture and separate CO2.

Computational fluid dynamics (CFD) and reaction modelling study of bio-oil catalytic hydrodeoxygenation in microreactors

A computational fluid dynamics (CFD) model was derived and validated in order to investigate the hydrodeoxygenation reaction of 4-propylguaiacol, which is a lignin-derived compound present in bio-oil.

Liquid fuel synthesis in microreactors

This review paper provides an in-depth review of microreactors for the intensification of the liquid fuel production processes.

Strategies for regeneration of nicotinamide coenzymes emphasizing self-sufficient closed-loop recycling systems

Biocatalytic reduction reactions depending on nicotinamide coenzymes require an additional reaction to regenerate the consumed cofactor. For preparative application the preferred method is the simultaneous coupling of an in situ regeneration reaction. There are different strategically advantageous routes to achieve this goal. The standard method uses a second enzyme and a second co-substrate, for example formate and formate dehydrogenase or glucose and glucose dehydrogenase. Alternatively, a second substrate is employed which is converted by the same enzyme used for the primary reaction. For example, alcohol dehydrogenase catalyzed reactions are often coupled with excess 2-propanol which is oxidized to acetone during the regeneration of NAD(P)H. A third method utilizes a reaction-internal sequence by the direct coupling of an oxidizing and a reducing enzyme reaction. Neither an additional substrate nor a further regenerating enzyme are required for the recycling reaction. This kind of "closed-loop" or "self-sufficient" redox process for cofactor regeneration has been used rarely so far. Its most intriguing advantage is that even redox reactions with unstable precursors can be realized provided that this compound is produced in situ by an opposite redox reaction. This elegant method is applicable in special cases only but increasing numbers of examples have been published during the last years.