Carbon Dioxide Emission Management in Power Generation. Prof. Lars O. NordЧитать онлайн 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.

Nomenclature

      Latin Symbols

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
	mass flow rate	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
Q	heat	kJ
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