Zobrazeno 1 - 10
of 45
pro vyhledávání: '"Stan T. Kolaczkowski"'
Publikováno v:
Chemical Engineering Transactions, Vol 105 (2023)
There is much interest in the production of energy from waste via gasification to produce a Syngas/Producer gas stream, containing CO, H2, CO2, CH4, H2O, and N2. From such a stream, H2 could be separated creating a clean fuel to act as an energy vect
Externí odkaz:
https://doaj.org/article/df7238a28d6545f2b9d0668387a36471
Publikováno v:
Chemical Engineering Journal. 373:709-719
Open-cell metal foams are a promising alternative to conventional solid pellets for the application as structured catalyst support. Pellets made from metal foams can be used in fixed-bed reactors instead of ceramic pellets. In this contribution, a co
Autor:
Runtong Zhang, Stan T. Kolaczkowski
Publikováno v:
Chemical Engineering Research and Design. 123:248-258
It is shown how the chromatographic experimental technique may be applied, in combination with the use of convolution theorem, to determine the effective diffusivity of a binary pair of non-reacting gases, in spherical γ-alumina pellets (1.0 mm diam
Publikováno v:
Catalysis Today. 273:221-233
Experiments were performed in which the benefits of flow through the large interconnecting cavities in structured metal foams (acting as catalyst supports) could be better understood. For example, using tablet shaped (8 mm × 8 mm × 3 mm) metal foam
Autor:
Stan T. Kolaczkowski, C D Le
Publikováno v:
Le, C D & Kolaczkowski, S T 2015, ' Steam gasification of a refuse derived char : reactivity and kinetics ', Chemical Engineering Research & Design, vol. 102, pp. 389-398 . https://doi.org/10.1016/j.cherd.2015.07.004
A char was obtained from a commercial pilot-scale gasifier, which had been operating with a refuse derived fuel (RDF). Using this char, steam gasification experiments were then performed in a 15.6 mm i.d. packed bed tubular reactor. The effect of rea
Publikováno v:
Catalysis Today. 216:229-239
A novel design of pilot-scale continuous flow pharmaceutical fixed-bed catalytic reactor has been developed. This incorporates in a structured manner the use of multiple catalytic monoliths (o.d. = 20 mm; L = 50 mm). O2 was used as the oxidant (O2/N2
Publikováno v:
Chemical Engineering Research and Design. 91:1292-1306
An experimental technique is demonstrated, in which the spatial variations of temperature inside a diesel oxidation catalyst (DOC) can be measured during an NEDC drive cycle. This leads to the development of a methodology which enables more scientifi
Publikováno v:
Catalysis Today. 188:53-61
A methodology was developed, which enables transient experiments to be performed on a DOC connected to a live diesel engine, while the temperature of the DOC substrate is monitored at various locations. This was demonstrated on a full-scale Pt/γ-alu
Publikováno v:
The Canadian Journal of Chemical Engineering. 81:1192-1199
This paper describes a method for evaluating the kinetic constants in a rate expression for catalytic combustion applications using experimental light-off curves. The method uses a transient one-dimensional single channel monolith finite element reac
Publikováno v:
Chemical Engineering Research and Design. 85:1539-1552
A method is described by which a CFD code known as FLUENT, may be adapted to model the reactions that take place inside catalyst structures. To test the CFD code, simulations of gas flow in a circular tube are performed and compared with analytical s