Title: Experiences from the PDU Mats Galbe Department of Chemical Engineering Lund University
1Experiences from the PDUMats GalbeDepartment of
Chemical EngineeringLund University
2Process 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
3Purpose of a Process Development Unit
4Process 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
5Pretreatment unit (small)
- 4-litre capacity
- Jacket for less heat losses
- Improved control of temperature
- Surface-coated flash-off vessel
Implemented in large reactor
6Steam 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
7Dilute-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
8Acid hydrolysis of spruce One-step at two
temperatures
9By-products in one-step acid hydrolysis using a
temperature profile
10Steam 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)
11Different 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
12PDU 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
13High-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!
14Higher dry-matter concentrations
- Terrafors (originally for solid-state
fermentations) - Difficult to control pH
- Mixing less efficient with increased liquefaction
15High-WIS hydrolysis quick tests
Rotating with steel balls for mixing
16High-WIS (SHF or SSF)Test of equipment
17First test of enzymatichydrolysis of spruce