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008			171102s2017 sz a ob 001 0 eng d
020			_a3319516884 _q(electronic bk.)
020			_a9783319516882 _q(electronic bk.)
020			_z3319516876
020			_z9783319516875
040			_aN$T _beng _erda _epn _cN$T _dN$T _dEBLCP _dYDX _dGW5XE _dNOC _dAZU _dUPM _dCOO _dOCLCQ _dIOG _dUAB _dES-MaUEC _bspa
050		4	_aTP159.D5 _b2017 EB
100			_aNitsche, Michael. _eautor _999465
245	1	0	_aPractical column design guide _cM. Nitsche, R. Gbadamosi.
264		1	_aCham, Switzerland _bSpringer International Publishing _c2017
300			_a1 recurso en línea _bilustraciones
336			_aTexto _btxt _2rdacontent
337			_aelectrónico _bc _2rdamedia
338			_arecurso electrónico _bcr _2rdacarrier
347			_atext file _bPDF
500			_a
504			_aIncluye referencias bibliográficas
505	0		_aPreface; Contents; Recommendation for Further Reading: Literature; 1 Planning of Distillation and Absorption Columns; 1.1 Planning Information; 1.2 Mass Balance for the Separation Task; 1.3 Separation Conditions; 1.4 Vapour-Liquid Equilibrium [4]; 1.4.1 The Ideal Equilibrium According to Raoult-Dalton; 1.4.2 Equations of State; 1.4.3 Equilibrium Models for Non-polar Materials Considering the Non-ideal Behaviour in the Liquid Phase Based on Pure Component Data.
505	8		_a1.12.1 Cooling Water Circulation Systems1.12.2 Comparison Between a Cooling Tower and an Air Cooler; 1.12.3 Cooling Water by Evaporating a Refrigerant or Adiabatic Evaporation; 1.12.4 Direct Condensation in Columns [6]; References; 2 Equilibria, Bubble Points, Dewpoints, Flash Calculations, and Activity Coefficients; 2.1 Vapour Pressure Calculations; 2.2 Phase Equilibrium of Ideal Binary Mixtures; 2.3 Bubble Point Calculation; 2.4 Dew Point Calculation; 2.5 Dew Point Calculation of Vapour Containing Inert Gases.
505	8		_a1.4.4 Equilibrium Models for Polar Components with High Non-ideal Behaviour in the Liquid Phase1.5 Energy and Mass Balance in the Column; 1.5.1 Mass Balance (Fig. 1.4); 1.5.2 Energy Balance (Fig. 1.5); 1.5.3 Required Column Diameter; 1.6 Selection of Column Internals; 1.7 Condensers [2]; 1.8 Reboiler [2]; 1.9 Vacuum Pumps [3]; 1.10 Control Facilities [5]; 1.11 Heating Systems with Steam or Hot Oil [3]; 1.11.1 Heat Transfer Coefficients; 1.11.2 Steam Heating [3]; 1.11.3 Heating with Hot Oil [3]; 1.12 Cooling Systems [3].
505	8		_a2.12.2 Calculation According to NRTL for Partially Miscible Components with Two Liquid Phases [9]2.12.3 Calculation According to Uniquac for Components with a Miscibility Gap; 2.12.4 Critical Comparison of the Activity Coefficients Calculated Using Different Models; 2.13 Bubble Point, Dew Point, and Flash Separation for Non-ideal Binary Mixtures; 2.14 Non-ideal Multi-component Mixtures; References; 3 Fractionation of Binary Mixtures; 3.1 Material Balance; 3.2 Vapoura-Liquid Equilibria; 3.2.1 Equilibria of Ideal Mixtures.
505	8		_a2.6 Dew and Bubble Point Lines of Ideal Binary Mixtures2.7 The Bubble Point and Dew Point of Immiscible Mixtures; 2.8 Flash Calculations for Ideal Binary Mixtures [1]; 2.9 Calculation of the Equilibrium and the Bubble and Dew Point Temperatures of Ideal Multi-component Mixtures; 2.10 Flash Calculations for Ideal Multi-component Mixtures [2]; 2.11 Phase Equilibrium of Non-ideal Binary Mixtures; 2.12 Calculation of the Activity Coefficients; 2.12.1 Calculation According to Wilson for Miscible Components [8].
520	3		_aThis book highlights the aspects that need to be considered when designing distillation columns in practice. It discusses the influencing parameters as well as the equations governing them, and presents several numerical examples. The book is intended both for experienced designers and for those who are new to the subject.
588	0		_aOnline resource; title from PDF title page (EBSCO, viewed November 03, 2017).
988			_aEBOOK, EBSPRINGER_2017
650		7	_2embne _aArquitectura _xDetalles _9330683
700	1		_aGbadamosi, Rasheed _eautor _9677386
856	4	0	_uhttps://go.openathens.net/redirector/universidadeuropea.es?url=http://link.springer.com/10.1007/978-3-319-51688-2 _zAcceso a este recurso digital (usuarios Universidad Europea de Madrid)
942			_2lcc _cLE
998			_b02/2018 _dz _e- _zSI