Lignite gasification ? Mathematical modeling of syngas equilibrium composition

Kód výsledku v IS VaVaI

<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F26722445%3A_____%2F15%3A%230001103" target="_blank" >RIV/26722445:_____/15:#0001103 - isvavai.cz</a>

Výsledek na webu

—

DOI - Digital Object Identifier

—

Jazyk výsledku

angličtina

Název v původním jazyce

Lignite gasification ? Mathematical modeling of syngas equilibrium composition

Popis výsledku v původním jazyce

The aim of this work was to develop a mathematical model of gasification unit for purposes of SYNKOPE project. The objective of SYNKOPE project is to efficiently couple high-temperature reactor (HTR - generation IV nuclear reactor with high outlet temperature) with refining process, namely lignite gasification. Water vapor produced by HTR will be used as a gasification media in the gasification unit for lignite gasification. The mathematical model was developed in MATLAB environment and is based on thecalculation of chemical equilibrium, which plays an important role in a composition of syngas generated during gasification process. For the calculation of chemical equilibrium, non-stoichiometric approach was applied. It is based on minimization of Gibbs energy of the whole reacting system simultaneously with calculation of balance equations without considering stoichiometry of particular chemical reactions. The developed mathematical model was used for the calculation of equilibrium co

Název v anglickém jazyce

Lignite gasification ? Mathematical modeling of syngas equilibrium composition

Popis výsledku anglicky

The aim of this work was to develop a mathematical model of gasification unit for purposes of SYNKOPE project. The objective of SYNKOPE project is to efficiently couple high-temperature reactor (HTR - generation IV nuclear reactor with high outlet temperature) with refining process, namely lignite gasification. Water vapor produced by HTR will be used as a gasification media in the gasification unit for lignite gasification. The mathematical model was developed in MATLAB environment and is based on thecalculation of chemical equilibrium, which plays an important role in a composition of syngas generated during gasification process. For the calculation of chemical equilibrium, non-stoichiometric approach was applied. It is based on minimization of Gibbs energy of the whole reacting system simultaneously with calculation of balance equations without considering stoichiometry of particular chemical reactions. The developed mathematical model was used for the calculation of equilibrium co

Druh

D - Stať ve sborníku

CEP obor

CH - Jaderná a kvantová chemie, fotochemie

OECD FORD obor

—

Projekt

<a href="/cs/project/ED2.1.00%2F03.0108" target="_blank" >ED2.1.00/03.0108: Udržitelná energetika</a><br>

Návaznosti

P - Projekt vyzkumu a vyvoje financovany z verejnych zdroju (s odkazem do CEP)

Rok uplatnění

2015

Kód důvěrnosti údajů

S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů

Název statě ve sborníku

Proceedings of the 3rd International Conference on Chemical Technology

ISBN

978-80-86238-79-1

ISSN

—

e-ISSN

—

Počet stran výsledku

4

Strana od-do

113-116

Název nakladatele

Czech Society of Industrial Chemistry

Místo vydání

Praha

Místo konání akce

Mikulov

Datum konání akce

1. 1. 2015

Typ akce podle státní příslušnosti

WRD - Celosvětová akce

Kód UT WoS článku

—