Ceramic Membranes in Process Technology

Similar documents
Lecture 10. Membrane Separation Materials and Modules

Membrane processes selective hydromechanical diffusion-based porous nonporous

Ion exchange (ionex) Ion exchange. Advantages. Disadvantages

Materials development for inorganic membrane layers at ECN

Estimate the extent of concentration polarization in crossflow filtration Select filtration unit operations to meet product requirements, consistent

Basic Principles of Membrane Technolog

General Separation Techniques

Membrane operations in the green technology: Solvent recovery and process water treatment

VOLATILE ORGANIC COMPOUNDS (VOC) REMOVAL BY PERVAPORATION IN A TUBULAR TYPE MEMBRANE MATHEMATICAL MODELLING AND PRELIMINARY TESTS

Dansk Mejeriteknisk Selskab Billund, June 14th Challenges in the Dairy Industry: Perspective on extreme performance membranes

Development of Technologies for Recovery and Removal of Fluorinated Compounds Causing Global Warming Abstract of the Report

Technologies and Approaches of CO 2 Capture

Membrane Performance Forecast

Technical membranes processing, Materials, modification, applications

1 Introduction to membrane filtration of liquids

LATEST TECHNOLOGY IN Safe handling & Recovery OF Solvents in Pharma Industry

FRAUNHOFER INSTITUTE FOR INTERFACIAL ENGINEERING AND BIOTECHNOLOGY IGB TECHNICAL MEMBRANES MATERIALS, PROCESSING, APPLICATIONS

Feed. Figure 1. The above image depicts the construction of a typical spiral wound element.

Control of Physical Aging in Super Glassy Polymer Membranes Without Permeability Loss MOF Mixed Matrix Membranes

Pervaporation: An Overview

Membrane Filtration 111 CAMBRIDGE. A Problem Solving Approach with MATLAB GREG FOLEY UNIVERSITY PRESS. Dublin City University

D-MAVT Membrane Separation Processes

A Research Agenda for a New Era in Separations Science: Understanding Synthesis for Separations. Benny Freeman

Supplementary Information. Experimental Methods

WASTEWATER RECYCLE, REUSE, AND RECLAMATION Vol. I - Membrane Separation Technologies - Takeshi Matsuura

Aalborg Universitet. Transport phenomena in gas-selective silica membranes Boffa, Vittorio. Creative Commons License Unspecified

Physicochemical Processes

Adsorption Processes. Ali Ahmadpour Chemical Eng. Dept. Ferdowsi University of Mashhad

Equipment Design and Costs for Separating Homogeneous Mixtures

Two-dimensional mathematical modeling of oxidative coupling of methane in a membrane reactor

CNT STABILITY WITHIN POLYMER NANOCOMPOSITE MEMBRANE MATRICES

Some physico-chemical data can be found at the web page (E-Tables):

CHMA2000 EXPT 7: The Physical and Chemical Properties of Alcohols

Dehydrogenation of propane with selective hydrogen combustion: A mechanistic study by transient analysis of products

Chapter 3 Membrane Processes for Water Production

Hydrothermal stability of a new hybrid membrane in dehydration applications

Beneficial Effect of Particle Adsorption in UF/MF Outside-In Hollow Fiber Filters. Yuriy Polyakov USPolyResearch, New Jersey Institute of Technology

A User-Defined Pervaporation Unit Operation in AspenPlus on the Basis of Experimental Results from Three Different Organophilic Membranes

HybSi membranes:materials, processes, outlook

Membrane Clean In Place Recipe Optimization

Membrane separation and Ionexchange SRM University Internal circulation only

Membrane reactors for improved processes: How to integrate reaction and separation in one apparatus

Removal of suspended and dissolved organic solids

SEPARATION BY BARRIER

HYDRACoRe. CHLORINE TOLERANT SPIRAL WOUND Nanofiltration Color Removal Membrane Elements. February Lenntech

Investigating the effect of graphene oxide on scaling in thin-film composite polyamide reverse osmosis membranes

WP3 Membrane Based Technologies

Nano-Enabled Catalysts for the Commercially Viable Production of H 2 O 2

CHAPTER 9: MEMBRANE SEPARATION PROCESS

Controlling membrane pore blocking and filter cake build-up in side-stream MBR systems

C11.1 Organic Chemistry Quiz Questions & Answers. Parts 1 & 2; all sets Parts 3 & 4; Sets 1 & 2 only

Chemical Product and Process Modeling

Nanofiltration properties of PTMSP in binary organic solvents mixtures

TRITIUM RECOVERY FROM WASTE USING A PALLADIUM MEMBRANE REACTOR

/05/ MAIK Nauka /Interperiodica

INDUSTRIAL EXPERIENCE WITH HYBRID DISTILLATION PERVAPORATION OR VAPOR PERMEATION APPLICATIONS

Separation of CO 2 Using Ultra-Thin Multi-Layer Polymeric Membranes for Compartmentalized Fiber Optic Sensor Applications

Nonlinear Operability of a Membrane Reactor for Direct Methane Aromatization

Chapter 11 Properties of Solutions

Supplementary Figure 1. Crystal structure of MIL-100. a, Trimer of Fe-based

Hydrothermal Stability Analysis of Carbonised Template Molecular Sieve Silica Membranes

Hollow ceramic fiber supported ZIF-8 membrane with enhanced. gas separation performance prepared by hot dip-coating seeding

NANOCOMPOSITE CATION EXCHANGE MEMBRANE WITH FOULING RESISTANCE AND ENHANCED SALINITY GRADIENT POWER GENERATION FOR REVERSE ELECTRODIALYSIS

EQ121 - Membrane Processes and Technologies

CENG 5210 Advanced Separation Processes. Reverse osmosis

Distillation is a method of separating mixtures based

INPHAZE HiRes-EIS High Resolution Electrical Impedance Spectroscopy. HiRes-EIS for Characterization of Membranes & Membrane Fouling

THE FUTURE OF THE CHEMISTRY: CONTINUOUS FLOW REACTIONS BASEL 2016

Membrane for water reuse: effect of pre-coagulation on fouling and selectivity

Simulation of 1,3-butadiene extractive distillation process using N-methyl-2-pyrrolidone solvent

Membrane Technology. in the Chemical Industry. Edited by Suzana Pereira Nunes and Klaus-Viktor Peinemann. Second, Revised and Extended Edition

SOLUTIONS. Dissolution of sugar in water. General Chemistry I. General Chemistry I CHAPTER

2 THEORY OF TRANSPORT IN MEMBRANES

Report No. 46. by PARK L. MORSE. January A private report by the PROCESS ECONOMICS PROGRAM PARK, CALIFORNIA STANFORD RESEARCH INSTITUTE I

Solvent flux behaviour and rejection characteristics of hydrophilic and hydrophobic TiO2 and ZrO2 membranes

Membrane Process. Prof. Chung-Hak Lee. School of Chemical and Biological Engineering Seoul National University, Seoul, Korea

NOA DRIE

A systematic Design Methodology for Multicomponent Membrane Systems

Simulation study of membrane supported oxidation of methane with simultaneous steam reforming using O 2 - selective Perowskite hollow fibres

G-L Taylor Flow reactor system Oxidation of ethylbenzene R. Sumbharaju L.A. Correia D.F. Meyer Y.C. van Delft A. de Groot

Review Photocatalytic Membrane Reactors (PMRs) in Water Treatment: Configurations and Influencing Factors

John Falconer Richard Noble

Diffusion and Reaction in Fe-Based Catalyst for Fischer- Tropsch Synthesis Using Micro Kinetic Rate Expressions

Modeling and Simulation of Distillation + Pervaporation Hybrid Unit: Study of IPA - Water Separation

The Pennsylvania State University. The Graduate School. Department of Civil and Environmental Engineering

An important fuel is methane, natural gas. The equation for its combustion is as follows. CO 2 + 2H 2 O

Le Lycee Mauricien. Proposed Syllabus Chemistry (5070) - Form 5

CFD STUDY OF MASS TRANSFER IN SPACER FILLED MEMBRANE MODULE

What type of samples are common? Time spent on different operations during LC analyses. Number of samples? Aims. Sources of error. Sample preparation

Nanocomposite Polymeric Membranes for Thermally Driven Desalina8on Processes. Ming Li and Jonathan Brant, P.E., Ph.D. University of Wyoming

Review of temperature distribution in cathode of PEMFC

the study of things all around us, its properties, what makes it up and how things can change.

Molecular Dynamics Simulation on Permeation of Acetone/Nitrogen Mixed Gas

Case Study : An Energy efficient way to retrieve Ethyl acetate from a waste stream

Experimental and Simulation Study on the Reactive Distillation Process for the Production of Ethyl Acetate

Agilent J&W PoraBOND Q PT Analyzes Oxygenates in Mixed C4 Hydrocarbon Streams by GC/FID and GC/MSD

Catalytic Membrane Reactors

Membrane and Membrane Separation Process

Removal of Metal Iron from Groundwater Using Aceh Natural Zeolite and Membrane Filtration

UT-3 Hydrogen Separation Process Mass Flow Rate Characterization and. Selection of Zirconium Silica Hydrogen Separator Membrane

Transcription:

BASF SE Ludwigshafen Hartwig Voß, Jacek Malisz, Patrick Schmidt, Jörg Therre Ceramic Membranes in Process Technology Status, future Trends, Challenges Strategie WS Hochleistungskeramiken, Bonn 20.01.2015

outline introduction / membrane processes some current applications emerging future applications challenges / need for research & development Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 2

outline introduction / membrane processes some current applications emerging future applications challenges / need for research & development Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 3

introduction some basic definitions flux = J i =L ii X i + ΣL ij X j permeance = P i = J i / X i Permselectivity = P i / P j J i J j feed (F) c F i p F T F c P i p P T P permeate (P) membrane Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 4

introduction membrane processes driving force pressure partial pressure c, electr. potential reverse osmosis RO pervaporation PV dialysis D nanofiltration NF vapor separation VS electrodialysis ED ultrafiltration UF gas separation GS microfiltration MF membrane distillation MD membranes materials (porous/dense) geometries modules polymers flat sheet plate and frame ceramics hollow fibers spiral wound metals, carbon tube multi tube Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 5

outline introduction / membrane processes some current applications emerging future applications challenges / need for research & development Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 6

Some current applications concentration and cleaning of dispersions and suspensions recycling of catalysts separation of particles from product streams fractionation of dissolved compounds with different molecular weight separation of cells (bacteria, yeast, fungi) from fermentation broths water cleaning (waste/process water recycling, drinking water) water separation from organic solvents membrane type material examples porous membranes (MF,UF,NF) α-al 2 O 3, TiO 2, ZrO 2 micro-porous membranes (PV, VS) zeolite A, amorphous SiO 2 Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 7

Some current applications concentration and cleaning of a suspended catalyst (micro filtration) 1. catalyst, product, solvent 2. washing with solvent catalyst & solvent product & solvent Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 8

Some current applications water cleaning (drinking water, waste water recycling) advantages of ceramic membranes high flux and fouling resistance easy cleaning: resistance against acids, bases, Cl 2 (NaOCl) need for cheaper membrane & module concepts membrane channel plugged Filtrate slit retentate permeate feed monolitic elements with ca. 10 m² from NGK or Violia (Ceramem) Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 9

outline introduction / membrane processes some current applications emerging future applications challenges / need for research & development Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 10

emerging future applications gas or vapor separation H 2 (from CO 2 or hydrocarbons) CO 2 from CH 4 (natural gas) molecular organic-organic separations O 2 from air nanofiltration water cleaning, molecular sieving in organic solvents membrane type micro-porous membranes non-porous membranes examples zeolites, MOF s, ZIF s, carbon oxidic or non-oxidic amorphous ceramics ionic conductors like perowskites micro-porous membranes amorphous (Ti/Zr)O 2 Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 11

emerging future applications membrane reactors dehydrogenations / water gas shift [CO+H 2 O = CO 2 +H 2 ] (H 2 separation) partial oxidations (O 2 supply from air) membrane type micro-porous membranes non-porous membranes examples zeolites, MOF s, ZIF s, carbon oxidic or non-oxidic amorphous ceramics ionic conductors like perowskites Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 12

emerging future applications n- / iso-butene separation molecular separations The separation is not possible by distillation. The state of the art process utilizes the high reactivity of iso-butene: n-c 4 iso-c 4 + HO etherification ether cleavage O 1-butene iso-butene C 4 -mixture without butadiene iso-butene iso-butanol iso-butyl-tert-butylether IBTBE Only iso-butene reacts with alcohols to an ether. The ether can be separated from the mixture by distillation and cleaved back. Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 13

emerging future applications n- / iso-butene separation by a zeolithe membrane With increasing TMP (driving force) only the flux of iso-buten increases linearly, the permeance stays nearly constant. the n-butene flux increases to a limit, the permeance decreases. the permselectivity is nearly gone at the wanted process condition. no competitive process! Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 14

emerging future applications O 2 separation from air replacement of cryogenic air separation in oxy-fuel technology (coal fired power plants with CO 2 capture) material: perowskite O 2- and e - conductance at T > 700 C air side up to 10 bar oxygen side slight vacuum status: not commercial, pilot stage (air products) oxygen membrane side pure oxygen O 2- + e - conductor O 2-2 e - air side N 2 O 2 membrane and module design extremely ambitious! Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 15

emerging future applications OCM membrane reactor 2CH 4 + O 2 C 2 H 4 + 2H 2 O set-up BCFZ hollow fiber catalyst: NaMnWO 4 feed : 20 % CH 4 in He T = 800 C, P = 1 bar Caro et al ind. eng. chem. res. 49(2010)p10230 higher ethylen yield but but comparable conversion and C 2 selectivity! Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 16

outline introduction / membrane processes some current applications emerging future applications challenges / need for research & development Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 17

challenges / need for R&D challenges permeance permselectivity (membrane material, thickness of membrane layer) (membrane material, accuracy of membrane layer) operation temperature (membrane material, module) chemical stability mechanical stability module construction (membrane material, module) (membrane material, geometry of membrane) (module material, sealing, thermal elongation) membrane performance / costs of membranes and modules! Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 18

challenges / need for R&D membrane material process operation membrane technical technical type example condition performance membrane modul zeolithe LTA PV 140 C xxxx xxxx xxxx DDR PV, GS 200 C xxxx xxxx xxxx MOF's, ZIF's ZIF 8 GS < 150 C xxxx xxxx xxxx carbon turbostratic carbon GS 300 C xxxx xxxx xxxx amorphous oxide ceramic amorphous nonoxide ceramic xxxx xxxx modified SiO 2 PV, GS 140 C xxxx xxxx xxxx (Ti/Zr)O 2 NF 200 C xxxx xxxx xxxx SiC, SiCN GS 500 C xxxx xxxx xxxx performance in technical range / developed technical concept aviable performance not sufficent / not developed Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 19

challenges / need for R&D membrane material process operation membrane technical technical type example condition performance membrane modul perowskite (O 2- - permeable) dense (H + - permeable) Ba 0,5 Sr 0,5 Co 0,8 Fe 0,2 O 3 GS 900 C xxxx xxxx xxxx membrane reactor GS 900 C xxxx xxxx xxxx CO 2 stable types GS 900 C xxxx xxxx xxxx perowskite GS 1000 C xxxx xxxx xxxx cermet Zr(Y)O 2 /Pd GS 600 C xxxx xxxx xxxx xxxx xxxx performance in technical range performance not sufficent / developed technical concept aviable / not developed Dr. Hartwig Voß, GCP/TC Process Research and Chemical Engineering 20 th January 2015 20

R & D - demand fundamentals of transport new materials, material improvement membrane scale up technical modules