Innovative Temperature Swing Adsorption Simulation Model for Biogas Upgrading

被引：4

作者：

Vogtenhuber, Hannes ^{[1
]}

Sonnleitner, Elisabeth ^{[2
]}

Helminger, Franz ^{[3
]}

Hofmann, Rene ^{[1
]}

Schoeny, Gerhard ^{[2
]}

Wilk, Veronika ^{[3
]}

Lauermann, Michael ^{[3
]}

Werner, Andreas ^{[1
]}

Hofbauer, Hermann ^{[2
]}

机构：

[1] TU Wien, Inst Energy Syst & Thermodynam, Getreidemarkt 9-302, A-1060 Vienna, Austria

[2] TU Wien, Inst Chem Engn, Getreidemarkt 9-166, A-1060 Vienna, Austria

[3] AIT, Ctr Energy, Giefinggasse 2, A-1210 Vienna, Austria

来源：

28TH EUROPEAN SYMPOSIUM ON COMPUTER AIDED PROCESS ENGINEERING | 2018年 / 43卷

关键词：

modeling and simulation; fluidized bed; TSA; CO2; capture; biogas upgrading; FLUIDIZED-BED SYSTEM; CO2; CAPTURE; SORBENTS;

D O I：

10.1016/B978-0-444-64235-6.50241-2

中图分类号：

X [环境科学、安全科学];

学科分类号：

08 ; 0830 ;

摘要：

A multi-stage fluidized bed system for temperature swing adsorption (TSA), which uses solid amine sorbents for CO2 capture and a heat pump for further optimization of the energy consumption, is studied in detail. The present work introduces detailed models for the most important aspects of the process, in order to study interactions in a simulation model. The overall efficiency depends on three different aspects: adsorption efficiency, heat transfer and heat recovery with a heat displacement system. These three modeling aspects have been combined to gain information about different limiting factors of the proposed TSA process for biogas upgrading. With the new TSA process model, a tool has been created which enables the design and dimensioning of a biogas upgrading plant, as well as the comparison to other biogas upgrading processes.

引用

页码：1377 / 1382

页数：6

共 14 条

[1] Simultaneous Adsorption of H2S and CO2 on Triamine-Grafted Pore-Expanded Mesoporous MCM-41 Silica [J].

Belmabkhout, Youssef ;

Heymans, Nicolas ;

De Weireld, Guy ;

Sayari, Abdelhamid .

ENERGY & FUELS, 2011, 25 (03) :1310-1315

[2]

Do D. D., 1998, ADSORPTION ANALYSISE

[3] Investigating wall-to-bed heat transfer in view of a continuous temperature swing adsorption process [J].

Hofer, G. ;

Schoeny, G. ;

Fuchs, J. ;

Proell, T. .

FUEL PROCESSING TECHNOLOGY, 2018, 169 :157-169

[4]

Martin H., 2010, WARMEUBERGANG WIRBEL

[5] PARTICLE MIGRATION AT SOLID-SURFACES AND HEAT-TRANSFER IN BUBBLING FLUIDIZED-BEDS .2. PREDICTION OF HEAT-TRANSFER IN BUBBLING FLUIDIZED-BEDS [J].

MOLERUS, O ;

BURSCHKA, A ;

DIETZ, S .

CHEMICAL ENGINEERING SCIENCE, 1995, 50 (05) :879-885

[6]

Nikolaidis GN, 2015, COMPUT-AIDED CHEM EN, V37, P287

[7]

NIST, 2017, NIST REF FLUID THERM

[8] Introduction and evaluation of a double loop staged fluidized bed system for post-combustion CO2 capture using solid sorbents in a continuous temperature swing adsorption process [J].

Proell, Tobias ;

Schoeny, Gerhard ;

Sprachmann, Gerald ;

Hofbauer, Hermann .

CHEMICAL ENGINEERING SCIENCE, 2016, 141 :166-174

[9] Techniques for transformation of biogas to biomethane [J].

Ryckebosch, E. ;

Drouillon, M. ;

Veruaeren, H. .

BIOMASS & BIOENERGY, 2011, 35 (05) :1633-1645

[10] A multi-stage fluidized bed system for continuous CO2 capture by means of temperature swing adsorption - First results from bench scale experiments [J].

Schoeny, Gerhard ;

Dietrich, Florian ;

Fuchs, Johannes ;

Proell, Tobias ;

Hofbauer, Hermann .

POWDER TECHNOLOGY, 2017, 316 :519-527

← 1 2 →