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High Performance Technologies for Ethanol Production from Sweet Potato
Chengdu Institute of Biology, Chinese Academy of Sciences, Chengdu 610041,China
EmailEmail::[email protected]@cib.ac.cn
Zhao Hai
3E PrincipleEnergyEnvironmentEconomy
Mode of Fuel Ethanol in ExistenceCorn Fuel Ethanol (American Mode) Sugarcane Fuel Ethanol (Brazil Mode)Cassava Fuel Ethanol (Thailand Mode)
Chinese Mode of Fuel Ethanol :3E+ Food Supplies Security
Mode of Chinese Fuel Ethanol Production
Feedstocks for bio-ethanol production
Cellulosic materialsCellulosic materials
Woody fiber grasses
Canna edulis Ker sweet potatosweet potato cassava
Sugar cropsSugar crops
Sugar beets sugar cane sweet sorghum
No grain No grain starch cropsstarch crops
Corn wheat
GrainsGrains
Why we use sweet potato to produce bio- ethanol?
High quantity of energy outputHigh quantity of energy output
Hall and Smittle. 1993. Industrial-type sweet potatoes: A renewable energy resource for Georgia. UGA Res. Rpt. 429.
Feedstock Gal/AcreWheat 340Corn 400
Sweet Sorghum 600Sweetpotato 640Sugarcane 650
Sugar Beets 700Switchgrass 1000Miscanthus 1250
Potential Ethanol Yields
Difficult to be utilized
Growth period
(month)
Root yield (kg/mu)
Starch content
(%)
Starch yield (kg/mu)
Ethanol yield (kg/mu)
Yearly ethanol yield(kg/Year/mu )
Sweet potato 5
Average 1500 20% 300 150 360
High 3000 25% 750 375 900
Cassava 10Average 1500 22% 330 165 198
High 3000 28% 740 370 444
Corn(CK) 3
Average 328 64% 210 105 420
High 500 64% 320 160 640
High speed of energy outputHigh speed of energy output
• China is the biggest sweet potato
producer in the world with the output
exceeded 100 M Ton (>80% world total)
in 2007(FAO, 2007).
• Sichuan province accounts for 16% of
total yield of sweet potato in China,
which is the biggest producer in China.
Abundant resourceAbundant resource
Plantation area of sweet potato
The issue of fuel ethanol production from sweet potato
Sweet potato is a kind of small farmer corpsSweet potato is a kind of small farmer corps------ItIt
is difficult to be used as industrial feedstockis difficult to be used as industrial feedstock
Main usageMain usage
Feedstuff(50Feedstuff(50%%))
Decomposition(30Decomposition(30%%))
Seed (10%)Seed (10%)
Commercial usage(10%)Commercial usage(10%) 10% Seed
10%commercial usage
50%feedstuff
30%Decomposition
High viscosity of sweet potatoHigh viscosity of sweet potato
• Low efficiency of heat exchangers
• Low efficiency of enzyme kinetics
• Impact on the escape of CO2
• Inhibit the activity of strain
Low ethanol content, high energy consumption Low ethanol content, high energy consumption in existing production technologiesin existing production technologies
Ratio Between Material and Water 1:1
Ethanol concentration
(% v/v)Fermentation
(h)
Fermentation efficiency
(%)
Corn (American) 15 50 >90
Sugar Cane (Brazil) 8-9 10 >90
Sweet Potato 5-6 >60 ≈88
More energy and water consumption
Our work
Sweet potato Microorganisms
Energy-saving Reactor
Fermentation technology
Very high gravity
fermentation
Rapid Fermentation
Ethanol tolerance
Temperature tolerance
Pressure tolerance
Mechanisms of Tolerance
Demonstration project
+
Viscosity ReductionTechnology
Breeding of Stress Tolerance Yeast Strain
Objective: To carry out the very high gravity fermentation
Ethanol tolerance yeast
Very High Gravity Fermentation(VHG)
Reduce water consumption
Reduce energy consumption
Reduce wastewater
Improve productivity of equipments
Avoid pollutionby other bacteria
8 ethanol tolerant strains of yeast were obtained . With Y1 or Y5,more than 18% of ethanol was produced within 60h,and the fermentation efficiency was 92%.
The characteristic hydrolysis enzymes map of the strains
Ethanol tolerance strain
Ordinary strain
02
46
810
1214
1618
20
0 20 40 60 80
发酵时间 Fermentation time (h)
糖浓
度 R
GC
% (w
/v)
乙醇
浓度
Eth
anol
con
cent
ratio
n %
(v/v
)
残糖浓度变化曲线 Changes of RGC
乙醇浓度变化曲线 Changes of ethanol concentration
Differential gene expression Differential gene expression ((PartialPartial))
Gene expression of the yeast in the
course of very high gravity fermentation
PathwayName Total PathwayName Total
Glycolysis / Gluconeogenesis 19 One carbon pool by folate 9
Purine metabolism 40 Terpenoid biosynthesis 4
Peptidoglycan biosynthesis 1 Ubiquinone biosynthesis 3
Pantothenate and CoA biosynthesis 5 Glycan structures - biosynthesis 2 7
Two-component system - Organism-specific 1 Valine, leucine and isoleucine degradation 8
Pyrimidine metabolism 26 Limonene and pinene degradation 6
Thiamine metabolism 1 Valine, leucine and isoleucine biosynthesis 10
Alanine and aspartate metabolism 11 Phosphatidylinositol signaling system 13
Glutamate metabolism 11 Bile acid biosynthesis 9
Aminoacyl-tRNA biosynthesis 23 Lysine biosynthesis 9
Ribosome 61 DNA polymerase 10
Main pathway involved in very high gravity of ethanol fermentation of Saccharomyces cerevisiae
Gene folder change in glycolysis
Gene Folder change
ADH2 0.16
ADH4 0.19
ALD3 0.50
ALD4 0.29
ALD5 0.40
ALD6 0.14
FBP1 0.10
PYK2 0.17
PDA1 0.41
PDB1 0.43
PDC5 0.34
PDC6 0.23
LAT1 0.43
HXK1 0.49
HXK2 0.50
ACS2 0.09
GAL10 6.25
GPM2 2.45
PGM1 3.59
Gene Folder change
IDI1 0.32
ERG8 0.28
ERG1 0.22
ERG9 0.49
ERG7 0.09
MVD1 0.20
HMG1 0.44
HMG2 0.29
ERG20 0.20
ERG12 0.38
Gene folder change in steriod synthesis
Genes folder change involved in heat shock proteinof Saccharomyces cerevisiae
-10
0
10
20
30
40
50
60
70
80
90
HSP26 FES1 SSA2 SSA4 HSP78 SSA3 HCH1 AHA1 HSC82 HSP82 SIS1 HSP10 SSE1 STI1 HSP42 YDJ1 ZIM17 SSZ1 SSB1 SSB2
基因
与对
照相
比的
变化
倍数
基因表达量变化倍数
Gene
Folder change
Objective:• To reduce water consumption in cooling• To maintain sustaining production in summer • To reduce pollution by other microorganisms which could not be tolerant to temperature• To relieve the inconsistency between the fermentation temperature of the yeast and process temperature of cellulase or amyloglucosidase in the Simultaneous saccharification and fermentation (SSF)
Temperature tolerance yeast
There were some similar mechanisms for yeast to tolerance high concentration of ethanol and high temperature
High concentration of
ethanol
High temperature
Increase of hsp protein + +
Increase of H+-ATPase protein in the membrane + +
Decrease of unsaturated fatty acid + +
Increase of trehalose + +
Increase of steriod + +
Partial references:Z.H.Liu. Appl Microbiol Biotechnol.(2007)77:901-908Agustín Aranda. Arch Microbiol (2002) 177 :304–312
Peter W.FEMS Microbiology Letters . ( 1995) 134 :121 – 127
Research strategic
Temperature tolerance strains were screened from ethanol tolerance strains after heat shock treatment. Taking into account of ethanol concentration, fermentation time and fermentation efficiency, a strain of yeast could ferment at 40 ℃ normally. 13% of ethanol could be produced within 33h, and the fermentation efficiency was 92%。
Sugar concentration(%,w/v)
Fermentation time(h)
Fermentation time(h)
Ethanol concentration(%,w/v)
Fermentation time(h)
OD value
Activity of key endoenzymes of the
yeast in the course of ethanol fermentation
at 40℃
0
0.2
0.4
0.6
0.8
1
1.2
1.4
1.6
1.8
0 10 20 30 40 发酵时间(h)
6-磷
酸葡
萄糖
脱氢
酶酶
活(U/g)
30
40
42
G-6-P
D (U
/g)
Fermentation time(h)
0
0. 5
1
1. 5
2
2. 5
3
0 10 20 30 40 发酵时间(h)
ATP酶
酶活
(U/g
)
30
40
42
ATPase(U
/g)
Fermentation time(h)
0
10
20
30
40
50
0 10 20 30 40发酵时间(h)
乙醇
脱氢
酶酶
活(U/g) 30
40
42
AD
H(U
/g)
Fermentation time(h)
PathwayName Total
Cell cycle 37
Purine metabolism 35
Pyrimidine metabolism 23
Ribosome 20
MAPK signaling pathway 19
Glycine, serine and threonine metabolism 18
Pyruvate metabolism 17
Glycerophospholipid metabolism 16
Phosphatidylinositol signaling system 15
Butanoate metabolism 14
Benzoate degradation via CoA ligation 14
Glycolysis / Gluconeogenesis 14
Citrate cycle (TCA cycle) 13
Starch and sucrose metabolism 13
Arginine and proline metabolism 13
Inositol phosphate metabolism 13
Glycerolipid metabolism 13
Tryptophan metabolism 12
Aminoacyl-tRNA biosynthesis 12
Alanine and aspartate metabolism 12
Gene expression of the yeast in the
course of ethanol fermentation at 40℃
Main pathway involved in ethanol fermentation at 40℃
Gene expression of the yeast in ethanol fermentation at 40℃
Gene Folder change
PGM1 18.27
ENO2 7.62
GAL10 6.28
GPM2 4.91
ALD5 3.73
PDC1 0.41
PDB1 0.40
ADH4 0.40
ALD4 0.34
PDC5 0.33
ALD6 0.25
ACS2 0.19
FBP1 0.15
PYK2 0.10
Gene Folder change
HSP26 21.90
SSA3 10.35
SSA4 8.38
SSA2 4.61
HSP104 3.00
HSP42 2.83
Genes folder change involved in heat shock protein
of Saccharomyces cerevisiae
Gene folder change in glycolysis
Pressure tolerance strain
• The more bigger fermentation scale, the less manufacture cost
• High pressure coursed by high fermentation mash could do damage to the strains
• High co2 pressure may result in lower fermentation parameters in scale-up compared with lab scale
FermentorHeight:15m
Volume:5000 Cubic metere
The strain we screened could
produce 9% of ethanol within
24h under the co2 pressure of
0.3Mpa,and the fermentation
efficiency was above 90%
Reactor for ethanol fermentation under high pressure
Ethanol(%,w
/w)
Sugar(%
,w/w
)
Fermentation time(h)
Fermentation time(h)
Activity of key endoenzymes of the yeast
01
234
56
10 15 20 25 30 发酵时间(h)
己糖
激酶
活力
(U/g
) 对照
0.1 Mpa
0.2 Mpa
0.3 Mpa
0.4 Mpa
密闭0
5
10
15
20
25
30
6 12 18 24 30 发酵时间(h)
ADH酶
活(U
/g)
对照
0. 1 Mpa
0. 2 Mpa
0. 3 Mpa
0. 4 Mpa
封闭
00.20.40.60.8
11.21.41.61.8
6 12 18 24 30发酵时间(h)
6-磷
酸葡
萄糖
脱氢
酶酶
活(U
/g)
对照
0.1 Mpa
0.2 Mpa
0.3 Mpa
0.4 Mpa
封闭0
0.51
1.52
2.53
3.5
0 10 20 30 40 发酵时间(h)
ATP酶
活(U
/g)
对照
0. 1 Mpa
0. 2 Mpa
0. 3 Mpa
0. 4 Mpa
密闭
G-6P
D(U
/g)
AD
H(U
/g)A
TPase(U
/g)
Hexokinase (U
/g)
Time(h) Time(h)
Time(h)Time(h)
Gene expression of the yeast in the
course of ethanol fermentation at
0.2mPa
Main pathway involved in ethanol fermentation at 0.2mPa
Pathway Name Total
Ribosome 98
Cell cycle 32
Purine metabolism 26
Pyrimidine metabolism 18
Glycine, serine and threonine metabolism 17
Glutamate metabolism 15
MAPK signaling pathway 14
Starch and sucrose metabolism 14
Oxidative phosphorylation 13
Selenoamino acid metabolism 12
Glycolysis / Gluconeogenesis 11
Glycerophospholipid metabolism 11
DNA polymerase 11
Pyruvate metabolism 10
Lysine degradation 10
Sulfur metabolism 10
Gene Folder change
HSP26 33.76
SSA2 3.38
HSP32 4.40
HSP30 3.07
HSP78 2.94
SSA4 2.87
HCH1 2.32
HSP82 2.20
HSP42 2.22
SIS1 2.03
Genes folder change involved in heat shock protein
of Saccharomyces cerevisiae
Gene folder change in glycolysis
基因名
ALD5 3.27
PGM1 1.83
ALD3 0.40
CDC19 0.39
PDC5 0.33
PGK1 0.30
PDC6 0.29
FBP1 0.13
ADH4 0.13
ENO2 0.09
ACS2 0.08
Viscosity reduction technology
Sweet potato and canna edulis ker are non-Newtonian fluid, the viscosity of which are more than 10×104 mPa.S, while the viscosity of ordinary fermentation culture are below 100 mPa.S
The excessive addition of water can be useful to reduce mash viscosity, however, the concentration of fermentable sugars in fermentor is also decreased by the dilution, and more energy is required for water evaporation.
Changes of polysaccharide and glucosidic bond in sweet potato under the function of
viscosity reduction technology
To understand the high viscosity mechanism of sweet potato by solid-phase moncolonic antibody for carbonhydrate
Viscosity reduction enzymes were developed according to polysaccharide and glucosidic bond which related to viscosity.
Under the function of optimal enzyme system, viscosity of fresh sweet potato mash reduced from 41154 mPa.S to 1384 mPa.S
After being processed with the enzyme system for viscosity reduction, the COD in the fermentation wastewater was partially removed and reduced from 64200mg/L to 41200 mg/L. Effect of enzymes on separation of liquid and solid in the
sweet potato mash
Effect of enzymes on viscosity reduction
Fermentation technologies
To enhance ethanol concentration, reduce energy consumption, decrease fermentation time and then reduce the production cost of ethanol
Objective:
Rapid ethanol fermentation technology from fresh sweet potato
Objective:•To use the feedstock in
harvest season as soon as
possible
•To avoid rot because of
overstocking of sweet potato
•To improve the productivity
of unit equipment
Overstocked sweet potato
0
20
40
60
80
100
120
140
160
180
200
0 3 6 9 12 15 18 21 24 27 30
时间 Time (h)
残糖浓度
Red
ucin
g su
gras
conc
entra
tion
(g/k
g)
0
20
40
60
80
100
酒精浓度
Eth
anol
con
cent
ratio
n(g
/kg)
18% 20% 22% 24%
18% 20% 22% 24%
0
20
40
60
80
100
120
140
160
180
200
0 3 6 9 12 15 18 21 24 27 30 33
Time (h)
Red
ucin
g su
gar (
g/kg
)
0
20
40
60
80
100
120
Eth
anol
(g/k
g)
1:1 sugar 2:1 sugar 3:1 sugar 5:1 sugar
1:1 ethanol 2:1 ethanol 3:1 ethanol 5:1 ethanol
With the screened yeast and
developed fermentation
technique,12.35% of ethanol
was produced within 24h, the
fermentation efficiency was
92%,and the ethanol
productivity was 4.06 g/kg/h
With the screened z.mobilis and
developed fermentation
technique,12.06% of ethanol
was produced within 21h,the
fermentation efficiency was
94%,and the ethanol
productivity was 4.53 g/kg/h
Rapid ethanol fermentation of yeast
Rapid ethanol fermentation of z.mobilis
Very high gravity ethanol fermentation technology for fresh sweet potato
Initial sugar concentration(w/g kg-1) 270 300 330
Fermentation time (h) 28 39 48
Ethanol concentration(w/g kg-1) 132.86 146.30 151.19
Fermentation efficiency(t) 91.44 90.42 84.15
Ethanol productivity(g kg-1 h-1) 4.75 3.75 3.15
Reducing sugars(w/g kg-
1) 5.64 6.82 20.68
Total reducing sugars(w/g kg-1) 15.19 18.38 31.53
Viscosity(mPa s) 1074.75 1798.25 3033.15
0
50
100
150
200
0 3 6 9 12 15 18 21 24 27 28时间Time( /h)
浓度
Con
cent
ratio
n(w
/g k
g-1)
0
1
2
3
4
5
6
pH值
pH
Val
ue
残还原糖 乙醇 pH
10L scale fermentation
A fermentation stimulant was developed to improve the activity of the strain. Under optimal condition,16.84% of ethanol was produced within 30h,ethanol fermentation efficiency was 91.44%,and the ethanol productivity was4.74 g kg-1 h-1
Demonstration project was carried out in 10 thousand ton scale production line of ethanol production factory at Sichuan province.
Compared with existed fermentation technique, fermentation time reduced from more than 60 hours to less than 30 hours, ethanol concentration increased from 5%-6%(v/v) to 12.41%(v/v), and fermentation efficiency enhanced from 88% to more than 90% in average.
Technique integration and demonstration project
Batch 1 2 3 4 5 6 7 8
Ratio of sweet potato to water 1:1.1 3:1 3.68:1 4:1 4.5:1 3:1 3:1 4:1
Viscosity of sweet potato with water
15676 21231 29876 33164 41154 11206 21929 30758
Viscosity of processed
sweet potato(mPa.S)
1108 1868 1654 1213 1384 1804 1453 1856
Ethanol concentration
(%,v/v)4.48 8.99 9.9 12.41 11.87 11.15 10.58 9.91
Time(h) 60 20 20 29 27 21 23 22
Final viscosity(mPa.S) 40 914 406 340 473 1138 603 635
Reducing sugars(%) 0.23 0.52 0.23 0.67 0.45 0.53 0.5 0.65
第三批试验发酵参数
02468
10121416
0 2 4 6 8 10 12 14 16 18 20
时间(h)
浓度
(%)
0
200
400
600
800
1000
1200
粘度
(mPa
.S)
还原糖
酒精
粘度
第四批试验发酵参数
0
3
6
9
12
15
0 2 4 6 8 10 12 14 16 18 20 22 24 26 28 29
时间(h)
浓度
(%)
0
200
400
600
800
1000
1200
1400
粘度
(m
Pa.S)
还原糖
酒精
粘度
第五批试验发酵参数
02468
1012141618
0 2 4 6 8 10 12 14 16 18 20 22 24 26 27
时间(h)
浓度
(%)
02004006008001000120014001600
粘度(
mPa
.S)
还原糖
酒精
粘度
第六批试验发酵参数
0
5
10
15
20
0 2 4 6 8 10 12 14 16 18 20 21
时间(h)
浓度(
%)
0
500
1000
1500
2000
粘度(
mPa
.S)
还原糖(%)酒精(%)粘度(mPa.S)
Sugars
Ethanol
viscosity
第三批试验发酵参数
02468
10121416
0 2 4 6 8 10 12 14 16 18 20
时间(h)
浓度
(%)
0
200
400
600
800
1000
1200
粘度
(mPa
.S)
还原糖
酒精
粘度
Sugars
Ethanol
viscosity
Sugars
Ethanol
viscosity
Sugars
Ethanol
viscosity
Sugars
Ethanol
viscosity
Time(h) Time(h)
Time(h)Time(h)
The third batch The fourth batch
The fifth batch The sixth batch
Concentration(%
)C
oncentration(%)
Concentration(%
)C
oncentration(%)
Viscosity(m
Pa.s)
Viscosity(m
Pa.s)
Viscosity(m
Pa.s)
Viscosity(m
Pa.s)
Viscosity(m
Pa.s)
第七批试验发酵参数
02468
101214
0 2 4 6 8 1012141618202223
时间(h)
浓度(
%)
0200400600800100012001400
粘度(
mPa
.S)
还原糖(%)酒精(%)粘度(mPa.S)
第八批试验发酵参数
02468
10121416
0 2 4 6 8 10 12 14 16 18 20 22
时间(h)
浓度(
%)
0
500
1000
1500
2000
粘度(
mPa
.S)
还原糖(%)酒精(%)粘度(mPa.S)
Sugars
Ethanol
viscosity
Sugars
Ethanol
viscosity
Concentration(%
)
Concentration(%
)
Viscosity(m
Pa.s)
Viscosity(m
Pa.s)
The seventh batch The eighth batch
Ratio of Ratio of sweet sweet potato potato
to waterto water
Viscosity Viscosity reductionreduction
FermentatFermentat ion timeion time
Ethanol Ethanol concentraconcentra
tiontion
FermeFerme ntation ntation efficienefficien
cycy
Present Present technologtechnolog
iesies11::11
By adding By adding excessive excessive
waterwater>60h>60h 55--6%(v/v)6%(v/v) <88%<88%
Our Our technologtechnolog
iesies4.54.5::11
>10000mPa.s >10000mPa.s to to
<1000mPa.s<1000mPa.s<30h<30h >12%(v/v)>12%(v/v) >90%>90%
Comparison between present technologies and these Comparison between present technologies and these technologiestechnologies
The advantage of our technologies
•less water was needed to be
added to the sweet potato mash,
and 70% of water could be
saved.
•ethanol concentration was
increased from 5-6% to
12%.Thus 40% of energy for
water evaporation was saved,
and wastewater could be
reduced from 16t to 9t.
•the COD in the wastewater was
partially removed and reduced
from 64200mg/L to 41200 mg/L.
Four technological breakthrough of non-grain ethanol production
HighHigh--efficient strains of efficient strains of ethanol fermentationethanol fermentationSelective breeding out high- concentration fermentation strains of withstand pressure and temperature resistance, which have industrialization value.
HighHigh--efficient fermentation efficient fermentation of high viscosity materialsof high viscosity materialsReducing viscosity of fermented mash , raising material-water ratio, which can cut down 70% water consumption.
HighHigh--concentration ethanol concentration ethanol fermentation of fresh sweet fermentation of fresh sweet potatopotatoImproving ethanol concentration, (from 5 to 12%)reducing energy cost, steam consume of ethanol distillation can cut down and discharge of waste water can cut down 40% at least.
Rapid ethanol fermentation Rapid ethanol fermentation of of fresh sweet potatofresh sweet potatoFermentation time will be shorten from 60h to 30h . It can enhance ethanol production capacity of unit equipment at least 1 times higher.
Joint Research Project of Chinese Academy of Sciences “Ethanol production
from Canna edulis Ker ”
Knowledge Innovation Program of The Chinese Academy of Sciences”Hot-
tolerance strain for ethanol production ”
Key Technologies R & D of Sichuan Province “Key technology of ethanol
production from sweet potato”
Key Technologies R & D of Sichuan Province“Key biotechnology of ethanol
production”
Program of Development and Reform Commission of Sichuan Province
“Establishment of the exclusive evaluation system of sweet potato for ethanol
production”
Our work was mainly supported by the following projects
Acknowledgements
National Key Technologies R & D“Energy-saving preservation technology
for sweet potato and ethanol production ”
National Key Technologies R & D“Ethanol production from Canna edulis
Ker and sweet potato at the scale of 5000ton of ethanol per year”
National High Technology Research and Development Program of China
(863 Program) “High efficiency transformation techniques of Lignocellulose”
International Cooperative Program of Sichuan Province“Relative
Characteristics of Sweet Potato for Bio-ethanol Production”
National Key Technologies R & D“Key technology of ethanol production
from sweet potato”
National Key Technologies R & D“Breeding of sweet potato for ethanol
production“
National Key Technologies R & D“Sustaining supply of sweet potato for
ethanol prodcution ”
National High Technology Research and Development Program of China (863
Program) “Rapid ethanol production from sweet potato with high viscosity”
The earmarked fund for Modern
Agro-industry Technology Research
System “Energy utilization of sweet
potato”