Abstract
Membrane reactors are attracting increasing attention for ultrapure hydrogen production from fossil fuel, integrating catalytic reaction and separation processes into one single unit thus can realize the removal of hydrogen or introduction of reactant in situ, which removes the thermodynamic bottleneck and improves hydrogen yield and selectivity. In this review, the state-of-the-art concepts for hydrogen production through membrane reactors are introduced, mainly including fixed bed membrane reactors, fluidized bed membrane reactors, and micro-channel membrane reactors, referring higher hydrocarbons as feedstock, such as ethanol, propane, or heptane; novel heating methods, like solar energy realized through molten salt; new modular designs, including panel and tubular configurations; ultra-compact micro-channel designs; carbon dioxide capture with chemical looping; multifuel processors for liquid and/or solid hydrocarbons; etc. Recent developments and commercialization hurdles for each type of membrane reactor are summarized. Modeling the reactor is fundamental to explore complex hydrodynamics in reactor systems, meaningful to investigate the effects of some important operating factors on reactor performances. Researches for reactor modeling are also discussed. Reaction kinetics for hydrocarbons reforming and reactor hydrodynamics are summarized respectively. Cold model is introduced to investigate physical phenomena in reactors.
Funding statement: Funding: Specialized Research Fund for the Doctoral Program of Higher Education of China (Grant/Award Number: “20130172110011”); China Scholarship Council (Grant/Award Number: “201406150038”); Guangdong Scientific Development Program (Grant/Award Number: “2013B010405001”).
Acknowledgements
Financial supports from the Guangdong Scientific Development Program (project # 2013B010405001), Specialized Research Fund for the Doctoral Program of Higher Education of China (project # 20130172110011), and China Scholarship Council are gratefully acknowledged.
Nomenclature
Latin symbols
- Ar
Archimedes number, –
- Ai
Arrhenius pre-exponential factor, units depend on the reactions
- Cep
Membrane permeation capacity (ratio of membrane surface area to thickness), [km]
- C0
Initial concentration of CH4, [mol m–3]
- Ceq
Equilibrium concentration, [mol m–3]
- Csj
Concentration of active sites on the surface for jth reaction, [mol m−2]
- Deff
Effectivity diffusion coefficient of hydrogen, [m2 s−1]
- dp
Average particle diameter, [m]
- Eact,Pv
Activation energy for the perovskite membrane, [J mol–1]
- Eact,I
Activation energy for ith reaction, [J mol–1]
- Ep
Activation energy for permeation, [J mol–1]
- g
Gravity acceleration rate, [m s–2]
- Gp core
Solids circulation flux in the core area of reactor [kg m–2 s–1]
- k
Pre-exponential factor, [mol km–1 h–1 Pa–0.5]
- ki
Reaction rate for ith reaction, [mol s–1]
- Kia(b)
Equilibrium constants for reversible reactions, –
- L0
Reactor length, [m]
- L
Reactor bed length, [m]
- n
Pressure order for membrane permeation, –
- nmol
moles in a conventional flow reactor, –
- NRep
Particle Reynolds number, –
- O/C
Oxygen to carbon ratio, –
- P
Reactor pressure, [Pa]
- Pe
Pecklet number, –
- Pm,Pv0
Permeability of the perovskite membrane, [mol cm–1 s–1 K–1]
- PMH2
Hydrogen partial pressures in membrane permeate side, [Pa]
- PO2,f
Partial pressure of O2 in the feed side, [Pa]
- PO2,p
Partial pressure of O2 in the permeate side, [Pa]
- PRH2
Hydrogen partial pressures in reactor side, [Pa]
- QH2
Hydrogen permeation rate, [mol h–1]
- QO2
Oxygen flux through a membrane, [mol cm–2 s–1]
- r
Reaction rate in Table 2, [mol s–1]
- rr
Reaction rate in membrane reactor for IE 2, [mol g−1 s−1]
- R
Gas constant, [J mol−1 K−1]
- R1
Inner radius of the reactor, [m]
- R2
Inner radius of the membrane tube, [m]
- Re
Reynolds number, –
- Sg
Surface area of catalyst, [m2 kg−1]
- S/C
Steam to carbon ratio, –
- T
Temperature, [K]
- tm,Pv
Perovskite membrane thickness, [m]
- u
Reactant velocity, [m s−1]
- U
Superficial gas velocity, [m s−1]
- Ucore
Superficial gas velocity in core area of the reactor, [m s−1]
- Umf
Minimum fluidization velocity, [m s−1]
- x
Distance in axial direction of reactor bed, [m]
- X
Molar fraction of each component, –
Greek letters
- μ
Fluid viscosity, [Pa s]
- ρ
Fluid density, [kg m−3]
- ρf
Gas density, [kg m−3]
- ρp
Particle density, [kg m−3]
- θ
Tapered bed angle, [°]
- ΔC
Concentration difference of H2, [mol m−3]
- Δρ
Density difference between fluid and solid, [kg m−3]
- ΔHo298
Enthalpy change, [kJ mol−1]
- ΔGi
Gibbs free energy for ith reaction, [mol s–1]
Abbreviations
- ATR
Autothermal reforming
- CLC
Chemical looping combustion
- CLR
Chemical looping reforming
- CSTR
Continuously ideally stirred tank reactor
- DIA
Digital image analysis
- FBMR
Fluidized bed membrane reactor
- ICFBMR
Internally circulating fluidized bed membrane reactor
- MA-CLR
Membrane-assisted chemical looping reforming
- MFBMR
Micro-structured fluidized bed membrane reactor
- PSA
Pressure swing adsorption
- PIV
Particle image velocimetry
- SMR
Steam methane reforming
- TCD
Thermal conductivity detector
- TCTMR
Thermally coupled two-membrane reactor
- TMAFBR
Tapered membrane-assisted fluidized bed reactor
- WGS
Water gas shift
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©2016 by De Gruyter
Artikel in diesem Heft
- Frontmatter
- Review
- Novel Membrane Reactor Concepts for Hydrogen Production from Hydrocarbons: A Review
- Research Articles
- Modeling and Simulation Study of an Industrial Radial Moving Bed Reactor for Propane Dehydrogenation Process
- Oxidative Degradation of Methylene Blue in Aqueous Medium Catalyzed by Lab Prepared Nickel Hydroxide
- CFD Modelling of a Hollow Fibre Membrane for CO2 Removal by Aqueous Amine Solutions of MEA, DEA and MDEA
- Performance Study of a Thermally Double Coupled Multi-Tubular Reactor by Considering the Effect of Flow Type Patterns
- Radiative Three-Dimensional Flow with Chemical Reaction
- Three-Phase Model of a Fluidized-Bed Catalytic Reactor for Polyethylene Synthesis
- Study on the Effect of Nickel Doping on Mo-Bi Based Catalyst for Selective Oxidation of Isobutene to Methacrolein
- DM Water Plant Sedimentation as a Cheap and Waste Source of Catalyst for Biodiesel Production
- Recovery of Biogas from Meat Industry Wastewater Using Continuously Stirred Tank Reactor (CSTR): Modeling and Optimization
- Comparison of CFD Simulation and Simplified Modeling of a Fluidized Bed CO2 Capture Reactor
- Kinetic Study for Platinum Extraction from Spent Catalyst in Cyanide Solution at High Temperatures
- Hydroisomerization of Biomass Derived n-Hexadecane Towards Diesel Pool: Effect of Selective Removal External Surface Sites from Pt/ZSM-22
- Heat Flux and Variable Thermal Conductivity Effects on Casson Flow and Heat Transfer due to an Exponentially Stretching Sheet with Viscous Dissipation and Heat Generation
- Optimization of Nickel Chemical Extraction from Hazardous Residue
- Green Approach for Biodiesel Production from Jojoba Oil Supported by Process Modeling and Simulation
- Differentiating Process Performance of Various Coagulants in Removal of Congo red and Orange G Dyes
- CFD Simulation of Hydrodynamic of a Bubble Column Reactor Operating in Churn-Turbulent Regime and Effect of Gas Inlet Distribution on System Characteristics
- Transformation of Phenolic Compounds by Fe(III) in the Aqueous Solution in Dark and Under Irradiation
- Transient Predictive Model for Dynamic Analysis, Kinetic Study, and Reactor Design of Triglycerides Transesterification to Biodiesel
- Screening of Alternative Carbon Sources for Recombinant Protein Production in Pichia pastoris
- Optimization of a Large Scale Industrial Reactor Towards Tailor Made Polymers Using Genetic Algorithm
- Model of Reactive Transport within a Light Photocatalytic Textile
- Preparation of Chitosan based Nanofibers: Optimization and Modeling
- Adsorption of As (III) on Iron Coated Quartz Sand: Influence of Temperature on the Equilibrium Isotherm, Thermodynamics and Isosteric Heat of Adsorption Analysis
- Resistance Characteristics of Coal Slime in Pipe Flow at High Pressure
- Activity Comparison of Acidic Resins in the Production of Valuable Glycerol Acetates
- Bulk Polymerization of Styrene using Multifunctional Initiators in a Batch Reactor: A Comprehensive Mathematical Model
- An Effective Reaction Rate Model for Gas-Solid Reactions with High Intra-Particle Diffusion Resistance
- Heart-Like Micro-Flow Mixer
- Hydrogen Production by Hydrolysis of NaBH4 with Cr-Ni-W-B Catalyst: Effects of Cold Plasma and Chromium Content
- Prediction of Reactivity Ratios in Free Radical Copolymerization from Monomer Resonance–Polarity (Q–e) Parameters: Genetic Programming-Based Models
- Steady-State Modeling of Pt-Catalyzed H2 Combustion in a Monolithic Reactor: From Micro- to Macro-kinetics
- Premixed Methanol–Air Combustion Characteristics in a Mini-scale Catalytic Combustor
- Kinetic Modeling of VOC Photocatalytic Degradation Using a Process at Different Reactor Configurations and Scales
- Improvement of Activated Sludge Process Using a Nonlinear PI Controller Design via Adaptive Gain
- Modeling and Simulation of a Pilot-Scale Bubbling Fluidized Bed Gasifier for the Gasification of High Ash Indian Coal Using Eulerian Granular Approach
- Performance of a Catalytic Gas–Solid Fluidized Bed Reactor in the Presence of Interparticle Forces
- Mathematical Modeling of Biodiesel Production under Intense Agitation
- Extended Aeration Activated Sludge Reactor (EAASR) for Removal of Nitrobenzene: Air Stripped or Biologically Removed?
- CFD Modeling of Algae Flash Pyrolysis in the Batch Fluidized Bed Reactor Including Heat Carrier Particles
- A Robust Extended State Observer for the Estimation of Concentration and Kinetics in a CSTR
- Dynamic Modeling of CATOFIN® Fixed-Bed Iso-Butane Dehydrogenation Reactor for Operational Optimization
- Effect of Biomass Compositions on Combustion Kinetic Parameters using Response Surface Methodology
- Short Communications
- Discussions on Particle Flux Measurement in Gas-Solids Risers
- Use of New Regeneration Processes for Thermolabile Amines
- Oxidative-Extractive Desulfurization of Liquid Fuel by Dimethyl Sulfoxide and ZnCl2 Based Ionic Liquid
- Corrigendum
- Corrigendum to: Performance Analysis of Immobilized Enzyme Semifluidised Bed Bioreactors
Artikel in diesem Heft
- Frontmatter
- Review
- Novel Membrane Reactor Concepts for Hydrogen Production from Hydrocarbons: A Review
- Research Articles
- Modeling and Simulation Study of an Industrial Radial Moving Bed Reactor for Propane Dehydrogenation Process
- Oxidative Degradation of Methylene Blue in Aqueous Medium Catalyzed by Lab Prepared Nickel Hydroxide
- CFD Modelling of a Hollow Fibre Membrane for CO2 Removal by Aqueous Amine Solutions of MEA, DEA and MDEA
- Performance Study of a Thermally Double Coupled Multi-Tubular Reactor by Considering the Effect of Flow Type Patterns
- Radiative Three-Dimensional Flow with Chemical Reaction
- Three-Phase Model of a Fluidized-Bed Catalytic Reactor for Polyethylene Synthesis
- Study on the Effect of Nickel Doping on Mo-Bi Based Catalyst for Selective Oxidation of Isobutene to Methacrolein
- DM Water Plant Sedimentation as a Cheap and Waste Source of Catalyst for Biodiesel Production
- Recovery of Biogas from Meat Industry Wastewater Using Continuously Stirred Tank Reactor (CSTR): Modeling and Optimization
- Comparison of CFD Simulation and Simplified Modeling of a Fluidized Bed CO2 Capture Reactor
- Kinetic Study for Platinum Extraction from Spent Catalyst in Cyanide Solution at High Temperatures
- Hydroisomerization of Biomass Derived n-Hexadecane Towards Diesel Pool: Effect of Selective Removal External Surface Sites from Pt/ZSM-22
- Heat Flux and Variable Thermal Conductivity Effects on Casson Flow and Heat Transfer due to an Exponentially Stretching Sheet with Viscous Dissipation and Heat Generation
- Optimization of Nickel Chemical Extraction from Hazardous Residue
- Green Approach for Biodiesel Production from Jojoba Oil Supported by Process Modeling and Simulation
- Differentiating Process Performance of Various Coagulants in Removal of Congo red and Orange G Dyes
- CFD Simulation of Hydrodynamic of a Bubble Column Reactor Operating in Churn-Turbulent Regime and Effect of Gas Inlet Distribution on System Characteristics
- Transformation of Phenolic Compounds by Fe(III) in the Aqueous Solution in Dark and Under Irradiation
- Transient Predictive Model for Dynamic Analysis, Kinetic Study, and Reactor Design of Triglycerides Transesterification to Biodiesel
- Screening of Alternative Carbon Sources for Recombinant Protein Production in Pichia pastoris
- Optimization of a Large Scale Industrial Reactor Towards Tailor Made Polymers Using Genetic Algorithm
- Model of Reactive Transport within a Light Photocatalytic Textile
- Preparation of Chitosan based Nanofibers: Optimization and Modeling
- Adsorption of As (III) on Iron Coated Quartz Sand: Influence of Temperature on the Equilibrium Isotherm, Thermodynamics and Isosteric Heat of Adsorption Analysis
- Resistance Characteristics of Coal Slime in Pipe Flow at High Pressure
- Activity Comparison of Acidic Resins in the Production of Valuable Glycerol Acetates
- Bulk Polymerization of Styrene using Multifunctional Initiators in a Batch Reactor: A Comprehensive Mathematical Model
- An Effective Reaction Rate Model for Gas-Solid Reactions with High Intra-Particle Diffusion Resistance
- Heart-Like Micro-Flow Mixer
- Hydrogen Production by Hydrolysis of NaBH4 with Cr-Ni-W-B Catalyst: Effects of Cold Plasma and Chromium Content
- Prediction of Reactivity Ratios in Free Radical Copolymerization from Monomer Resonance–Polarity (Q–e) Parameters: Genetic Programming-Based Models
- Steady-State Modeling of Pt-Catalyzed H2 Combustion in a Monolithic Reactor: From Micro- to Macro-kinetics
- Premixed Methanol–Air Combustion Characteristics in a Mini-scale Catalytic Combustor
- Kinetic Modeling of VOC Photocatalytic Degradation Using a Process at Different Reactor Configurations and Scales
- Improvement of Activated Sludge Process Using a Nonlinear PI Controller Design via Adaptive Gain
- Modeling and Simulation of a Pilot-Scale Bubbling Fluidized Bed Gasifier for the Gasification of High Ash Indian Coal Using Eulerian Granular Approach
- Performance of a Catalytic Gas–Solid Fluidized Bed Reactor in the Presence of Interparticle Forces
- Mathematical Modeling of Biodiesel Production under Intense Agitation
- Extended Aeration Activated Sludge Reactor (EAASR) for Removal of Nitrobenzene: Air Stripped or Biologically Removed?
- CFD Modeling of Algae Flash Pyrolysis in the Batch Fluidized Bed Reactor Including Heat Carrier Particles
- A Robust Extended State Observer for the Estimation of Concentration and Kinetics in a CSTR
- Dynamic Modeling of CATOFIN® Fixed-Bed Iso-Butane Dehydrogenation Reactor for Operational Optimization
- Effect of Biomass Compositions on Combustion Kinetic Parameters using Response Surface Methodology
- Short Communications
- Discussions on Particle Flux Measurement in Gas-Solids Risers
- Use of New Regeneration Processes for Thermolabile Amines
- Oxidative-Extractive Desulfurization of Liquid Fuel by Dimethyl Sulfoxide and ZnCl2 Based Ionic Liquid
- Corrigendum
- Corrigendum to: Performance Analysis of Immobilized Enzyme Semifluidised Bed Bioreactors