Carbon Dioxide Emission Management in Power Generation. Prof. Lars O. Nord

Чтение книги онлайн.

Читать онлайн книгу Carbon Dioxide Emission Management in Power Generation - Prof. Lars O. Nord страница 9

Carbon Dioxide Emission Management in Power Generation - Prof. Lars O. Nord

Скачать книгу

      We convey our thanks to many persons that in one way or another have been involved in the book.

      Thanks to Olav Kaarstad for inputs to CO2 storage, Kjell Erik Rian for gas compression and separation, Ivar Ertesvåg for efficiency definitions and separation work, and Tord Ursin for efficiency calculations and definitions.

      Multiple experts have provided inputs and feedback on the CO2 capture methods including Hallvard Svendsen for gas absorption, Konrad Eichhorn Colombo for inputs on membranes and the AZEP, May-Britt Hägg on membranes, Giorgia Mondino on adsorption, Ed Blekkan on gas reforming, Ola Maurstad on coal gasification, and Peter Koch on combustion. Thank you all!

      For proofreading, we thank Zeinab Amrollahi, Aldo Bischi, and Rahul Anantharaman.

      Many thanks to Konstantinos Kyprianidis and the SOFIA research group at Mälardalen University for hosting Lars Nord during his sabbatical under which the book was finalized.

      And of course, last but not the least, we thank our wives Synnøve (Olav) and Nataša (Lars) for the patience and having to hear more than you probably have liked to about this book.

      Latin Symbols

Скачать книгу

a effective interfacial area per unit volume of packing m2/m3
A cross-sectional area m2
A m membrane surface area m2
c p specific heat capacity at constant pressure kJ/(kg K)
c v specific heat capacity at constant volume kJ/(kg K)
d g abundance of gas component g kg
F Faraday constant
h specific enthalpy on mass basis kJ/kg
specific enthalpy on molar basis kJ/kmol
specific enthalpy of formation on molar basis kJ/kmol
H enthalpy kJ
H 0 enthalpy of formation kJ
He Henry's law constant Pa/kmol fraction gas in liquid
He Henry's law constant (Pa m3)/kmol gas in liquid
HHV higher heating value kJ/kg
HR heat rate kJ/kWh
J i flux through a membrane m/s
LHV lower heating value kJ/kg
m mass kg or t
kg/s
MW molecular weight kg/kmol
n polytropic coefficient
n i number of moles for specie i mol
Nu Nusselt number
p absolute pressure Pa, bar
p f partial pressure of the permeated gas at the feed side of a membrane Pa, bar
p i partial pressure of component i Pa, bar
p p partial pressure of the permeated gas at the permeate side of a membrane Pa, bar
P membrane permeability m3(STP)/(m h bar)
Pr Prandtl number
q i gas adsorbed per unit mass of adsorbent mol gas/kg adsorbent
q p,i volumetric flow rate through membrane m3(STP)/h