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Comparative evaluation of some brown midrib sorghum mutants for the production of food grain and 2,3-butanediol
Pacific Rim Summit on Industrial Biotechnology and Bioenergy
December 9, 2014
Yadhu N Guragain1, K.S. Vinutha2, G.S. Anil Kumar2, Reggeany Barrios1, P.V. VaraPrasad3, P. Srinivasa Rao2, Praveen V. Vadlani1
1Bioprocessing and Renewable Energy Laboratory, Grain Science and Industry, Kansas State University, USA2International Crops Research Institute for the Semi-Arid Tropics (ICRISAT), India3Department of Agronomy, Kansas State University (KSU), USA
Bioprocessing and Renewable Energy Laboratory, KSU Dr. Praveen Vadlani: -Director Two Post-doc Four Ph D students One Master Student Undergraduate students Research Scientists Summer REU students
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Research Areas
Biofuels – cellulosic ethanol, biobutanol
Biochemicals – 2,3-butanediol, lactic acid, succinic acid
Co-product utilization – animal feed, bioproducts
Specialty chemicals – flavor, pre and probiotics, fragrances, neutraceuticals
HPLC
GC-MSUV-VIS
5 L
fermenterParr
Reactor
GC
Pretreatment
Hydrolysis Monomer
sugars
Fermentation
Product recovery
Fuels and
Chemicals
Lignin
(Enzymes)
High Value aromatic
compounds and
macromolecules
Cellulose and
Hemicellulose
(Holocellulose)
Bioprocessing of Lignocellulosic Biomass
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Source: - http://crf.sandia.gov/index.php/
A lot of challenges in each steps
Major Challenges for lignocellulosic biorefineries
1. Pretreatment of biomass
Cost Production of inhibitors
• Phenolics, furan compounds, aliphatic acids
Environmental issues
2. Cost of enzymes
3. Valorization of lignin
4. Handling and storage of bulky biomass
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Source: - http://crf.sandia.gov/index.php/
5
37
22
29
12
Douglas Fir (Softwood)
40
22
21
17
Poplar (Hardwood)
Glucan XylanLignin Others
35
29
17
20
Switchgrass (Grass)
31
1916
34
Corn stover (Grass)
35
21
20
23
Sorghum stalk (Grass)
In general, alkali pretreatment efficiency ∞ lignin content;
however, this is not always true.
• Among five biomass here, douglas fir the most difficult and corn stover is the easiest for delignification
• Switchgrass is little more difficult than sorghum, and poplar is much more difficult than sorghum
Each biomass must be separately evaluated !
Sorghum is a model energy crop because of its high photosynthetic efficiency,abiotic stress tolerance, and wide applications as food, feed, and fuels.
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bmr mutation of sorghum leads to change in composition of its stover
bmr sorghum as a potential feedstock for bioenergy and biochemicals production needs investigation
Brown midrib White midrib
Both bmr mutations had longer flowering time and lower yields than their background, except stover yield of Kansas Collier
8
0
10
20
30
40
50
60
70
80
90
0
1
2
3
4
5
6
7
Early Hegari(EH)
bmr6 (EH) bmr12 (EH) Atlas (AT) bmr6 (AT) bmr12 (AT) KansasCollier (KC)
bmr6 (KC) bmr12 (KC)
50
% F
low
erin
g ti
me
(day
s)
Yie
ld (
t/h
a)
Genotype
Agronomy dataStover yield
Grain yield
50% Flowering time
bmr mutation led to decrease in lignin (10 to 25%) and carbohydrate polymers (2 to 9%), and increase in extractives (6 to 43% )for Atlas and Kansas collier
This was not true for bmr 12 of Early Hegari.
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0
10
20
30
40
50
Cellulose + Hemicellulose Lignin Extractives
Co
mp
osi
tio
n (
%, d
ry w
eigh
t b
asis
)
Biomass Component
Composition of biomassEarly Hegari (EH) bmr 6 (EH) bmr 12 (EH)
Atlas (AT) bmr 6 (AT) bmr 12 (AT)
Kansas Collier (KC) bmr 6 (KC) bmr 12 (KC)
Significant proportion of extractives in soluble sugars (sucrose, glucose and fructose)
Sugar proportion significantly higher in bmr mutants in all wild types, except,bmr12 of Kansas Collier (consistent with composition data)
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0
10
20
30
40
50
60
70
Early Hegari(EH)
bmr 6 (EH) bmr 12 (EH) Atlas (AT) bmr 6 (AT) bmr 12 (AT( KansasCollier (KC)
bmr 6 (KC) bmr 12 (KC)
Am
ou
nt
(%, W
/W))
Genotype
Total extractives Vs sugarsTotal extractives
Sugars in water extraction
Sugar proportion
Both bmr mutats had higher sugar yield than wild type in all biomass, except bmr12 of Kansas Collier
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0
10
20
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40
50
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80
90
0 10 20 30 40 50
Suga
r yi
eld
(%
, g/g
pre
tre
ate
d b
iom
ass)
Hydrolysis time (h)
Hydrolysis yield for monomer sugars from pretreated biomass
Early Hegari (EH) bmr 6 (EH) bmr 12 (EH)
Atlas (AT) bmr 6 (AT) bmr 12 (AT)
Kansas Collier (KC) bmr 6 (KC) bmr 12 (KC)
2,3-butanediol yield was around 0.3 g/g sugars or lower (theoretical maximum 0.5)
Significant byproduct formation: glycerol, acetic acid, ethanol
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0.27 0.26 0.27 0.26 0.27 0.260.28
0.330.31
0.27
0.0
0.1
0.2
0.3
EarlyHageri (EH)
bmr6 (EH) bmr12 (EH) Atlas (AT) bmr6 (AT) bmr12 (AT) KansasCollier (KC)
bmr6 (KC) bmr12 (KC) Control2,3
-bu
tan
ed
iol y
ield
(g/
g su
gar
con
sum
ed
)
Axis Title
Shake flask fermentation using Bacillus licheniformis
Overall mass balance: Stover to fermentable sugars
Hydrolysis
Pretreatment
Pretreated biomass
Liquid stream
Released sugars
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Ground Biomass
100100100
100100100
100100100
KCATEH
172826
112121
15193
KCATEH
Wild→bmr 6→
bmr 12→
44394
454345
454555
KCATEH
293134
313035
343741
KCATEH
445959
415157
505542
KCATEH8
1716
71410
17153
KCATEH
Sugars
333
333
434
KCATEH
Phenolics
Sugar extraction (in water)
% increment in sugar yieldEH AT KC
bmr 6 10 25 33
bmr 12 -16 38 33
% increment in sugar yieldEH AT KC
bmr 6 6 -1 5
bmr 12 19 16 14
Grain and stover yield significantly vary among bmrsorghum mutants
1.25% (W/V) NaOH is optimum for pretreatment of bmrsorghum
bmr mutation alters the biomass composition, andimproves hydrolysis efficiency of stalk. However, theeffects significantly vary among sorghum varietiesindicating background effect.
bmr mutation leads to increase in non-structural sugarcontent in sorghum, which must be extracted beforepretreatment
Biomass derived sugar can be used for 2,3-butanediolproduction using Bacillus licheniformis.
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Conclusion:
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Acknowledgement:
ICRISAT-KSU bmr sorghum project from USAID-CGIAR-US varsity linkage program
The Small Business Innovation Research (SBIR),Navy, and Department of Defense, USA