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Experiences from the PDU Mats Galbe Department of Chemical Engineering Lund University

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Title: Experiences from the PDU Mats Galbe Department of Chemical Engineering Lund University


1
Experiences from the PDUMats GalbeDepartment of
Chemical EngineeringLund University
2
Process Development Unit (PDU)
  • PDU lab and process equipment
  • Research in bench-scale, i.e., max size 100 litre
    fermentor vessel
  • National facility placed at Lund
    University,mainly financed by the Swedish Energy
    Agency
  • Commissioned work for companies and universities
  • Internal research

3
Purpose of a Process Development Unit
  • Lab scale
  • PDU
  • Pilot scale
  • Industrial scale

4
Process Development Unit (PDU) Steam pretreatment
unit
10 litre reactor 160 - 230 C Impregnation
with H2SO4 or SO2 or other catalysts
Main purposes Hydrolysis of hemicellulose Improve
the enzymatic hydrolysis of cellulose
Success A number of units constructed sold
5
Pretreatment unit (small)
  • 4-litre capacity
  • Jacket for less heat losses
  • Improved control of temperature
  • Surface-coated flash-off vessel

Implemented in large reactor
6
Steam pretreatment or acid hydrolysis?
  • What do we actually mean?
  • Steam pretreatment renders a material suitable
    for further processing (e.g, by enzymatic
    hydrolysis)
  • With or without catalyst (acid or base)
  • Acid hydrolysis (strong or dilute) ideally
    produces monomers that can be used without
    further treatment

7
Dilute-acid hydrolysis
  • Dilute-acid hydrolysis
  • Concentrations typically less than 2
  • Temperatures 180-220C
  • Residence time usually lt 15 min
  • One- or two-step hydrolysis
  • Advantage rather fast and simple
  • Drawback results in degradation products -gt may
    be difficult to ferment
  • Pentose sugars -gt furfural
  • Hexose sugars -gt HMF, formic and levulinic acid

8
Acid hydrolysis of spruce One-step at two
temperatures
9
By-products in one-step acid hydrolysis using a
temperature profile
10
Steam pretreatment
  • Addition of a catalyst during pretreatment
  • Milder conditions than in acid hydrolysis
  • Acid results in hydrolysis of the hemicellulose
  • H2SO4, H3PO4, SO2
  • Alkali mainly oligo- and polymers
  • NaOH, NH3
  • Enzymatic hydrolysis (SHF) or simultaneous
    saccharification and fermentation (SSF)

11
Different materials behavedifferently
  • Agricultural materials
  • Wheat straw
  • Corn stover
  • Sugar cane bagasse
  • Sorghum (sweet/fibre)
  • Arundo donax
  • Rice straw
  • Hemp
  • Barley straw
  • Paja Brava
  • Forest materials
  • Spruce
  • Pine
  • Poplar
  • Cypress
  • Salix

12
PDU International partner
  • Borregaard, Norway Steam pretratment
  • Chemtex, Italy SSF, steam pretreatment
  • Cargill, Germany Steam pretreatment
  • Mitsui Engineering Shipbuilding, Japan SSF
  • Nagurjana Hills, India SSF
  • NBE Sweden Hydrolysis, analysis, fermentation
  • SGCC (State grid of China) Project and
    cooperation
  • SEKAB SSF, analysis
  • Taurus Pretreatment and fermentation
  • CTH
  • KTH
  • Brazil-EU Partner in Cane Biofuel
  • NILE (EU) SSF, pretreatment (Partner)
  • University of Florida
  • University of Georgia
  • National Renewable Energy Labs (NREL), USA

Currently building full-scale plant in Italy
13
High-WIS applications(WIS Water-Insoluble
Solids)
  • High WIS is good
  • Potentially higher sugar concentrations-gt Higher
    ethanol concentrations-gt Less energy
    requirements
  • (or is it?)
  • Increased viscosity
  • Higher inhibitor concentrations
  • Less available liquid-gt unfriendly environment
  • Heat transport affected!
  • pH control initially difficult
  • OPTIMISATION!

14
Higher dry-matter concentrations
  • Terrafors (originally for solid-state
    fermentations)
  • Difficult to control pH
  • Mixing less efficient with increased liquefaction

15
High-WIS hydrolysis quick tests
Rotating with steel balls for mixing
16
High-WIS (SHF or SSF)Test of equipment
17
First test of enzymatichydrolysis of spruce
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