
Process Intensification for Sustainable Energy Conversion
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Content
Preface xi
List of Contributors xiii
1. Introduction 1
Fausto Gallucci and Martin van Sint Annaland
2. Cryogenic CO2 Capture 7
M. van Sint Annaland, M. J. Tuinier and F. Gallucci
2.1 Introduction - CCS and Cryogenic Systems 7
2.1.1 Carbon Capture and Storage 8
2.1.2 Cryogenic separation 10
2.2 Cryogenic Packed Bed Process Concept 11
2.2.1 Capture Step 11
2.2.2 CO2 Recovery Step 12
2.2.3 H2O Recovery and Cooling Step 13
2.3 Detailed Numerical Model 13
2.3.1 Model Description 13
2.3.2 Simulation Results 15
2.3.3 Simplified Model: Sharp Front Approach 16
2.3.4 Model Description 16
2.3.5 Process Analysis 22
2.3.6 Initial Bed Temperature 24
2.3.7 CO2 Inlet Concentration 24
2.3.8 Inlet Temperature 25
2.3.9 Bed Properties 25
2.4 Small-Scale Demonstration (Proof of Principle) 25
2.4.1 Results of the Proof of Principle 26
2.5 Experimental Demonstration of the Novel Process Concept in a Pilot-Scale Set-Up 31
2.5.1 Experimental Procedure 32
2.5.2 Experimental Results 33
2.5.3 Simulations for the Proof of Concept 36
2.5.4 Radial Temperature Profiles 36
2.5.5 Influence of the Wall 38
2.6 Techno-Economic Evaluation 39
2.6.1 Process Evaluation 40
2.6.2 Parametric Study 41
2.6.3 Comparison with Absorption and Membrane Technology 45
2.7 Conclusions 49
2.8 Note for the Reader 49
List of symbols 50
Greek letters 50
Subscripts 51
3. Novel Pre-Combustion Power Production: Membrane Reactors 53
F. Gallucci and M. van Sint Annaland
3.1 Introduction 53
3.2 The Membrane Reactor Concept 55
3.3 Types of Reactors 57
3.3.1 Packed Bed Membrane Reactors 58
3.3.2 Fluidized Bed Membrane Reactors 65
3.3.3 Membrane Micro-Reactors 72
3.4 Conclusions 74
3.5 Note for the reader 75
4. Oxy Fuel Combustion Power Production Using High Temperature O2 Membranes 81
Vesna Middelkoop and Bart Michielsen
4.1 Introduction 81
4.2 MIEC Perovskites as Oxygen Separation Membrane Materials for the Oxy-fuel Combustion Power Production 83
4.3 MIEC Membrane Fabrication 85
4.4 High-temperature ceramic oxygen separation membrane system on laboratory scale 87
4.4.1 Oxygen permeation measurements and sealing dense MIEC ceramic membranes 87
4.4.2 BaxSr1-xCo1-xFeyO3-d and LaxSr1-xCo1-yFeyO3-d Membranes 89
4.4.3 Chemical Stability of Perovskite Membranes Under Flue-Gas Conditions 96
4.4.4 CO2-Tolerant MIEC Membranes 99
4.5 Integration of High-Temperature O2 Transport Membranes into Oxy-Fuel Process: Real World and Economic Feasibility 103
4.5.1 Four-End and Three-End Integration Modes 103
4.5.2 Pilot-Scale Membrane Systems 104
4.5.3 Further Scale-Up of O2 Production Systems 106
5. Chemical Looping Combustion for Power Production 117
V. Spallina H. P. Hamers, F. Gallucci and M. van Sint Annaland
5.1 Introduction 117
5.2 Oxygen carriers 120
5.2.1 Nickel-based OCs 122
5.2.2 Iron-based OCs 122
5.2.3 Copper-based OCs 122
5.2.4 Manganese-based OCs 123
5.2.5 Other Oxygen Carriers 123
5.2.6 Sulfur Tolerance 123
5.3 Reactor Concepts 124
5.3.1 Interconnected Fluidized Bed Reactors 124
5.3.2 Packed Bed Reactors 132
5.3.3 Rotating Reactor 143
5.4 The Integration of CLC Reactor in Power Plant 144
5.4.1 Natural Gas Power Plant with CLC 144
5.4.2 Coal-Based Power Plant with CLC 148
5.4.3 Comparison between CLC in packed beds and circulated fluidized beds 162
5.5 Conclusions 164
Nomenclature 167
Subscripts 168
6. Sorption-Enhanced Fuel Conversion 175
G. Manzolini, D. Jansen and A. D. Wright
6.1 Introduction 175
6.2 Development in Sorption-Enhanced Processes 176
6.2.1 Enhanced Steam Methane Reformer 177
6.2.2 SEWGS 177
6.3 Sorbent Development 180
6.3.1 Sorbent for Sorption-Enhanced Reforming 180
6.3.2 Sorbent for Enhanced Water-Gas Shift 182
6.4 Process Descriptions 188
6.4.1 Fluidised Beds 189
6.4.2 Fixed Beds 190
6.4.3 Design Optimisation of Fixed Bed Processes 195
6.5 Sorption-Enhanced Reaction Processes in Power Plant for CO2 Capture 196
6.5.1 SER 196
6.5.2 SEWGS case 199
6.6 Conclusions 203
Nomenclature 204
7. Pd-Based Membranes in Hydrogen Production for Fuel cells 209
Rune Bredesen, Thijs A. Peters, Tim Boeltken and Roland Dittmeyer
7.1 Introduction 209
7.2 Characteristics of Fuel Cells and Applications 211
7.3 Centralized and Distributed Hydrogen Production for Energy Applications 213
7.4 Pd-Based Membranes 216
7.5 Hydrogen Production Using Pd-Based Membranes 216
7.5.1 Hydrogen from Natural Gas and Coal 217
7.5.2 Hydrogen from Ethanol 219
7.5.3 Hydrogen from Methanol 220
7.5.4 Hydrogen from Other Hydrocarbon Sources 221
7.5.5 Hydrogen from Ammonia 221
7.6 Process Intensification by Microstructured Membrane Reactors 221
7.7 Integration of Pd-Based Membranes and Fuel Cells 229
7.8 Final Remarks 231
8. From Biomass to SNG 243
Luca Di Felice and Francesca Micheli
8.1 Introduction 243
8.2 Current Status of Bio-SNG Production and Facilities in Europe 244
8.3 Bio-SNG Process Configuration 245
8.3.1 The Gasification Step 247
8.3.2 Gas Cleaning 248
8.3.3 The Synthesis Step 250
8.4 Catalytic Systems 251
8.5 The Case Study 253
8.5.1 The Feeding Composition 254
8.5.2 Heat Exchangers 256
8.5.3 Scrubber Tar Removal 257
8.5.4 Ammonia Absorber 258
8.5.5 HCl and H2S Removal 259
8.5.6 Compression Section 259
8.5.7 Separation Section: H2O and CO2 Removal 259
8.5.8 Methanation Section Case 1: Adiabatic Fixed Bed with Intermediate Cooling 260
8.5.9 Methanation Section Case 2: Isothermal Fluidized Bed 262
8.6 Chemical Efficiency 263
8.7 Conclusions 263
9. Blue Energy: Salinity Gradient for Energy Conversion 267
Paolo Chiesa, Marco Astolfi and Antonio Giuffrida
9.1 Introduction 267
9.2 Fundamentals of Salinity Gradient Exploitation 268
9.3 Pressure Retarded Osmosis Technology 270
9.3.1 Operating Principles 271
9.3.2 Plant Layout and Components 272
9.3.3 Design Criteria and Optimization 276
9.3.4 Technology Review 277
9.3.5 Pilot Testing 278
9.4 The Reverse Electrodialysis Technology 279
9.4.1 Operating Principles and Plant Layout 279
9.4.2 RED Technology Review 282
9.5 Other Salinity Gradient Technologies 284
9.5.1 Reverse Vapor Compression 284
9.5.2 Hydrocratic Generator 288
9.6 Osmotic Power Plants Potential 290
9.6.1 Site Criteria for Osmotic Power Plants 292
9.7 Conclusions 294
10. Solar Process Heat and Process Intensification 299
Bettina Muster and Christoph Brunner
10.1 Solar Process Heat - A Short Technology Review 299
10.1.1 Examples of solar process heat system concepts 301
10.1.2 Solar process heat collector development 302
10.2 Potential of Solar Process Heat in Industry 305
10.3 Bottlenecks for Integration of Solar Process Heat in Industry 305
10.3.1 Introduction 305
10.3.2 Bottlenecks of the Industrial Process to Integrate Solar Heat Supply 306
10.3.3 Bottlenecks of the Solar Process Heat System 308
10.3.4 Engineering Intensified Process Systems for Renewable Energy Integration 308
10.4 PI - A Promising Approach to Increase the Solar Process Heat Potential? 309
10.4.1 Intensifying the Industrial Process and Possible Effects on Solar Process Heat 311
10.5 Conclusion 328
11. Bioenergy - Intensified Biomass Utilization 331
Katia Gallucci and Pier Ugo Foscolo
11.1 Introduction 331
11.2 Biomass Gasification: State-of-the-Art Overview 332
11.2.1 Cold Gas Cleaning and Conditioning: Current Systems 335
11.3 Hot Gas Cleaning 343
11.3.1 Contaminant Problems Addressed 343
11.3.2 Dust Filtration 349
11.3.3 Catalytic Conditioning 352
11.3.4 The UNIQUE Concept for Gasification and Hot Gas Cleaning and Conditioning 363
11.4 Conclusions 376
Index 387
Chapter 1
Introduction
Fausto Gallucci and Martin van Sint Annaland
Eindhoven University of Technology, Chemical Process Intensification, Department of Chemical Engineering and Chemistry, Eindhoven, The Netherlands
It is expected that in the current century, the theme "energy" will become increasingly more important and will pose some serious challenges to our society and our way of living, but it may also create opportunities.
On the one hand, the combination of a rapidly growing world population and increasing energy consumption per capita requires large investments to secure sufficient energy supply at affordable prices. On the other hand, fossil fuel reserves are shrinking, while the transition toward a world economy based on energy supply via sustainable or renewable resources is still in its infancy. According to the World Energy Outlook 2013 of the International Energy Agency (IEA), the world energy demand will increase by more than 30% by 2035 (compared with 2011) and the demand for oil alone will still be more than 57% in 2035. Oil and gas reserves are increasingly concentrated in a few countries that control them through monopoly companies. The dependence of Europe on imported oil and gas is growing: we import 50% of our energy, and it will be 55% by 2035 (Bp Outlook 2035), if we do not act.
The relevance of this issue is even higher when one relates the increase in anthropogenic CO2 emissions by the use of fossil fuels to the evident changes in the Earth's climate. The International Panel on Climate Change (IPCC) has collected results of substantial research efforts to obtain a comprehensive scientific framework describing the evolution of the climate over very long time periods, the observed deviations from this behavior in recent times, the interpretation of both natural and anthropogenic causes and their effect on the increase of the greenhouse effect, the consequences of global warming in the past, present and future and possible solutions to combat further climate changes. In its 2013 Assessment Report, IPCC conclude that (Climate Change 2013: The Physical Science Basis), see Figure 1.1:
Figure 1.1 Detection and attribution signals in some elements of the climate system, at regional scales (top panels) and global scales (bottom four panels). Brown panels are land surface-temperature-time series, green panels are precipitation-time series, blue panels are ocean heat content-time series and white panels are sea ice-time series. Observations are shown on each panel in black or black and shades of grey. Blue shading is the model time series for natural forcing simulations and pink shading is the combined natural and anthropogenic forcings. The dark blue and dark red lines are the ensemble means from the model simulations. All panels show the 5-95% intervals of the natural forcing simulations and the natural and anthropogenic forcing simulations.
(Source: Extracted from the IPCC report 2013)
"From up in the stratosphere, down through the troposphere to the surface of the Earth and into the depths of the oceans there are detectable signals of change such that the assessed likelihood of a detectable, and often quantifiable, human contribution ranges from likely to extremely likely for many climate variables."
According to IPCC, the effect of human activities on changes in the climate is very likely to have been dominating natural variations (due to, e.g., variations in solar irradiance) especially in the past 50 years. Since the beginning of the industrial revolution, the concentrations of the relevant greenhouse gases (especially carbon dioxide, methane, nitrous oxide, and halocarbons) have increased substantially and now by far exceed natural ranges encountered in the past 650,000 years [1].
On the short term, significant reductions of carbon dioxide emissions may be attained from energy savings, for example, via efficiency improvements both in power production and consumer products and as a consequence of increased public awareness. However, strong economic growth anticipated in especially the developing countries is expected to impede a net decrease in anthropogenic emissions. On the longer term, the use of fossil fuels for energy supply will need to be phased out not only to stabilize greenhouse gas concentrations but also to avoid shortages in raw materials for the production of, for example, bulk chemicals.
The transition towards a world economy based on energy supply via sustainable sources such as wind-, hydro- and solar energy, or nuclear power (of which fission still suffers from a bad public image caused by concerns over nuclear waste and proliferation, whereas fusion has so far failed to live up to its potential) is therefore expected to be a lengthy process that cannot be expected to be solely responsible for the stabilization of atmospheric greenhouse gas concentrations in this century. Rather, a combination of many of the mitigation alternatives will need to be adopted to significantly curb CO2 emissions.
In this respect, novel concepts based on process intensification can help to reduce CO2 emissions and can lead the transition towards a more sustainable energy scenario. Indeed, according to Ramshaw [2], process intensification is a strategy for making dramatic reductions in the size of a chemical plant so as to reach a given production objective. As such, applying process intensification to the energy sector can result in a dramatic decrease in the production of wastes including greenhouse gas emissions.
According to Stankiewicz and Moulijn [3], the whole field of process intensification can be classified into two main categories:
- Process-intensifying equipment:
These include novel reactors and intensive mixing, heat-transfer and mass-transfer devices, and so on.
- Process-intensifying methods:
These include new or hybrid separations, integration of reaction and separation, heat exchange, or phase transition (in multifunctional reactors), techniques using alternative energy sources (light, ultrasound, etc.) and new process-control methods (like intentional unsteady-state operation).
Clearly, as also indicated by Stankiewicz and Moulijn, there is a big overlap between the two areas. For instance, membrane reactors are an example of process-intensifying equipment (novel reactor) making use of process-intensifying methods (integration of reaction and separation).
Since the "invention" of the term process intensification, many articles and books appeared on the same topic. An interested reader is referred to the book of Reay et al. [4] for an overview of the various process intensification methods. In the present book, a selection of different, novel process intensification methods and reactors are presented and discussed with the focus on sustainable energy conversion.
In particular, in Chapter 2 the development of a new cryogenic separation technology based on dynamic operation of packed bed columns is described. When it is possible to exploit the cold available at, for example, LNG regasification stations, this new technology could be used as an efficient post-combustion CO2 capture technology. In the chapter, the technology is described to freeze-out CO2 from flue gases at atmospheric pressures. The dynamic operation and the effects of the operating conditions have been analyzed in detail using modelling and an experimental proof of principle at laboratory scale and small pilot scale is provided. Finally, a techno-economic analysis shows the great potential of the technology over other post-combustion capture processes such as amine scrubbing and membrane separation, when cold duty is available at low prices or when high CO2 capture efficiencies are required. This makes the cryogenic technology also particularly interesting as an auxiliary unit downstream of other post-combustion technologies.
Chapter 3 describes the application of membrane reactors in pre-combustion CO2 capture technologies. Different membrane reactor configurations are described, among which the fluidized bed membrane reactor configuration seems to have the most potential. In this concept, hydrogen perm-selective membranes are submerged in a fluidized suspension. Thus, mass and heat transfer coefficients are much improved compared to packed bed membrane reactor configurations (decreasing problems in heat management and concentration polarization), while maintaining a relatively large amount of catalyst combined with a relatively low pressure drop in comparison with micro-membrane reactors. The chapter also describes a hybrid concept integrating both membrane reactors and chemical looping combustion for autothermal operation with integrated CO2 capture. With this new concept, high hydrogen efficiency can be obtained at lower temperatures compared with other concepts, while the amount of membrane area required is kept to a minimum.
Chapter 4 focuses on the possibility to apply high-temperature oxygen-selective membranes in oxy-fuel power production systems. These perovskite-like or mixed ionic electronic conducting materials present an infinite perm-selectivity for oxygen compared with other gases and can thus be used to separate oxygen from air at high temperatures. The chapter describes the main features of oxygen selective membranes, their production methods and their integration in membrane (reactor) modules. The chapter also reports on the progress of research projects on oxygen selective membranes.
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