Download MC & UM Algae/Biodiesel Project

Survey
yes no Was this document useful for you?
   Thank you for your participation!

* Your assessment is very important for improving the work of artificial intelligence, which forms the content of this project

Document related concepts
no text concepts found
Transcript
MC & UM
Algae/Biodiesel Project
• Background Review
• Status as of May 12, 2009
MCES Interest in Algae
GHG
1.0 -> 0.3
Hypoxia
CO2 + P + N + light 
Concept
1) Extract oil from algal cell mass –
some species => 50% oil by weight
2) Use catalytic hydrothermal
gasification on wet material to
generate usable synthetic gas, heavy
oil, and char
Project Goal
Determine the technical and economic
feasibility of using algae to reduce nutrient
and carbon dioxide emissions and
subsequently recover oil and other energy
products from the algal cell mass.
MC Focus
• Phosphorus removal
– MPCA proposing substantial
reduction in effluent limits
– Any value from cell mass reduces net
cost of P removal
• CO2 removal and value of credits
• Nitrogen removal
Metro Plant Schematic
Scrn
Grit
Primary
Settling
Activated
Sludge
Aeration
Final
Settling
Sludge
Thickening
Dewatering
centrate
Disinfect
Sludge
Incineration
Application at Metro
Concentration
Mass
Total N
centrate
125 mg/l
1,040 lb/day
Soluble P
centrate
190 mg/l
1,580 lb/day
1.7 – lb/lb dry
sludge burned
430 ton/day
CO2
incineration
Oil Production Potential
centrate P - mg/l
200
measure
P removal - %
50
assume
centrate flow - mgd
1
known
algal cell mass - % P
1
literature
P removal - lb/day
833
calculate
algal cell mass produced - lb/day
83,300
calculate
algal cell oil content - %
20
assume
oil recovery efficiency - %
80
assume
oil production - lb/day
13,328
calculate
oil production – gal/day
1,780
calculate
UM Screening Algal Species
UM Bioreactor Design
UM/MC Harvesting Experiments
Metro Pilot Plant
Located in SMB
Door closed to
protect intellectual
property – reactor
design
Experimental Reactors
Reactor A
Reactor B
Tanks
4
4
Type
Plug Flow
Mixed
1.5 X
X
Light
intensity
Simplified Growth Model
CO2 + N + P + light
O2 +
Corganic + O2 + N + P
CO2 +
Pilot Plant Performance*
Reactor A
Reactor B
TSS Produced
497 gm/day
415 gm/day
STP removed
47 gm/day
43 gm/day
STP removed
67%
60%
* Varying wasting schedule during startup – not steady state operation
Project Funding
Phase 1
Phase 2
MC
$40k
$250k
UM – IREE
$40k
$250k
Xcel Energy
$150k
State of Minn ______
$500k__
Totals
$1,000k
$230k
Related documents