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Bio-Diesel plant Wind Blade
1.Biodiesel Technology | 2. Biodiesel Process (Catalyst type) | 3. DCB Process
  4. DCB Process Cost account | 5.Oil content of vegetables  
  6. Standard for Biodiesel | 7. Specification for Biodiesel Plant  
 
Division
Unit price
UNIT
Monthly
UNIT
Annual
UNIT
A. Material cost
417.6
USD/Ton
835,145
USD
10,021,744
USD
B. Personnel expenses
12.1
USD/Ton
24,200
USD
290,400
USD
C. Utility
21.8
USD/Ton
43,680
USD
524,160
USD
D. Other
2.0
USD/Ton
4,000
USD
48,000
USD
         
 
Grand total
454
USD/Ton
907,025
USD
10,884,304
USD
* Case a. Price of jatrophajatrophaseed : US$100/Tonseed Tonb. b.    BiodieselBiodieselProduction capacity : 100 Ton/day
Kinds
Oil content (%)
Remarks
Bean
18 ~ 22
 
Corn
36 ~ 42
 
Rape flowers
35 ~ 45
 
Safflower
32 ~ 40
 
Sunflower
30 ~ 40
 
Castor bean
45 ~ 70
 
Jatrophacurcas
30 ~ 37
 
Palm
45 ~ 50
 
Olive
18 ~ 35
 
Rice bran
18 ~ 20
 
Coconut
45 ~ 50
 
Cottonseed
15 ~ 25
 
Property
Unit
Minimum
Maximum
Test Method
Ester Content
% (m/m)
96.5
pr EN 14103
Density @ 15℃
kg/m3
860
900
EN ISO 3675 , N ISO 12185
Viscosity @ 40℃
mm2/s
3.5
5.0
EN ISO 310
Flash Point
Above 101
ISO / CD 3679
Sulfur Content
mg/Kg
?
10
 
Carbon Residue (10% Bottoms)
% (m/m)
?
0.3
EN ISO 10370
CetaneNumber
51.0
EN ISO 5165
SulphatedAsh Content
% (m/m)
?
0.02
ISO 3987
Water Content
mg/Kg
?
500
EN ISO 12937
Total Contamination
mg/Kg
?
24
EN 12662
Copper Strip Corrosion (3hr @ 50℃)
rating
Class 1
Class 1
EN ISO 2160
Thermal Stability
?
?
?
?
Oxidation Stability, 110℃
hours
6
?
pr EN 14112
Acid Value
mg KOH/g
0.5
pr EN 14104
Iodine Value
?
120
pr EN 14111
Linolenic acid methyl ester
% (m/m)
12
pr EN 14103
Polyunsaturated (>= 4 double bonds) methyl esters
% (m/m)
1
?
Methanol Content
% (m/m)
0.2
pr EN 14110
MonoglycerideContent
% (m/m)
0.8
pr EN 14105
DiglycerideContent
% (m/m)
0.2
pr EN 14105
Triglyceride Content
% (m/m)
0.2
pr EN 14105
Free Gylcerol
% (m/m)
0.02
pr EN 14105 / pr EN 14106
Total Gylcerol
% (m/m)
0.25
pr EN 14105
Alkaline Metals (Na + K)
mg/Kg
5
pr EN 14108 , pr EN 14109
Phosphorus Content
mg/Kg
10
pr EN 14107
Property
Requirements
Flash point (closed cup) 130 ℃min. (150℃average)
Water and sediment 0.050% by vol. max.
Kinematic viscosity at 40℃ 1.9-6.0 mm2/s
Ramsbottom carbon residue, % mass 0.10
Sulfated ash 0.020% by mass, max.
Sulfur 0.05% by mass, max.
Copper strip corrosion No. 3 max
Cetane 47 min.
Carbon residue 0.050% by mass, max.
Acid number - mg KOH/g 0.80 max.
Free glycerin 0.020 % mass
Total glycerine (free glycerineand unconverted glyceridecombined) 0.240% by mass, max.
Phosphorus content 0.001 max. % mass
Distillation 90% @ 360℃
Classification
Model
Capacity
Batch Type
(Intermittent type)
DB-05-B
500 Kg/Cha
DB-10-B
1,000 Kg/Cha
DB-20-B
2,000 Kg/Cha
DB-50-B
5,000 Kg/Cha
DB-80-B
8,000 Kg/Cha
DCB Process
(Continuous type)
DB-10-C
1,000 Kg/h (25 TPD)
DB-20-C
2,100 Kg/h (50 TPD)
DB-30-C
3,100 Kg/h (75 TPD)
DB-50-C
5,000 Kg/h (100 TPD)
DB-60-C
6,200 Kg/h (150 TPD)
DB-80-C
8,300 Kg/h (200 TPD)
DB-120-C
12,500 Kg/h (300 TPD)