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| |
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 |
 |
 |
 |
 |
|
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)
|
|
| |
|
