SPECIFICATION EQUIPMENTS Preliminary Design Of Butyl Oleate Plantfromoleic Acid And Butanolcapacity 15,000 Tons/Year.
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
CHAPTER III
SPECIFICATION EQUIPMENTS
1.1 Oleic Acid Storage Tank
Code
: T-01
Duties
: Store raw materials oleic acid as 1,575.31
kg/hour
Type
: Vertical cylindrical tank with torispherical dished
head
Quantity
: 1 Piece
Volume
: 1,415.43 m3
Material
: Carbon steel SA 212 Grade B
Storage conditions
:
Pressure
: 1 atm
Temperature
: 35oC
Dimensions :
The diameter of the tank : 12.17 m
Height tank
Thick tank
: 12.17 m
: Coarse 1
: 0.4375 in
Coarse 2
: 0.375 in
Coarse 3
: 0.3125 in
Coarse 4
: 0.25 in
Coarse 5
: 0.25 in
Coarse 6
: 0.1875 in
Thick Head
: 0.5 in
Total high
: 14.3864 m
Price
: US $ 340,548.30
1.2 Storage Tank Butanol
Code
: T-02
Duties
: store raw materials butanol as 450.11 kg/hour.
29
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Type
: Vertical cylindrical tank with torispherical dished
head
Quantity
: 1 piece
Volume
: 446.14 m3
Material
: Carbon steel SA 212 Grade B
Storage conditions
:
Pressure
: 1 atm
Temperature : 35oC
Dimensions :
The diameter of the tank
: 8.28 m
Height tank
: 8.28 m
Thick tank :
Coarse 1
: 0.25 in
Coarse 2
: 0.25 in
Coarse 3
: 0.1875 in
Coarse 4
: 0.1875 in
Coarse 5
: 0.1875 in
Thick-Head
: 0.3125 in
Overall high
:9.79 m
Price
: US $ 215,985.33
1.3 Tank of Butyl Oleate
Code
: T-05
Duties
: store the product butyl oleate as 1,893.94 kg/hour
Type
: Vertical cylinder with torispherical dished head
Quantity
: 1 piece
Volume
: 826.27 m3
Material
: Carbon steel SA 212 Grade B
Storage conditions :
Pressure
: 1 atm
Temperature
: 35oC
Dimensions :
The diameter of the tank
: 10.17 m
High-tank
: 10.17 m
30
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Thick tank
: Coarse 1
: 0.25 in
Coarse 2
: 0.25 in
Coarse 3
: 0.25 in
Coarse 4
: 0.25 in
Coarse 5
: 0.1875 in
Coarse 6
: 0.1875 in
Thick-Head
: 0.4375 in
Overall high
: 12.02 m
Price
: US $ 270,838.75
1.4 Sulfuric Acid Tank
Code
: T-03
Duties
: To save as much sulfuric acid 47.46 kg/hour
Type
: Vertical cylindrical tank with torispherical dished head
Quantity
: 1 piece
Volume
: 20.69 m3
Material
: Carbon steel SA 212 Grade B
Storage conditions
: Pressure
: 1 atm
Temperature : 35oC
Dimensions :
The diameter of the tank
: 2.98 m
High-tank
: 2.98 m
Thick tank :
Coarse 1
: 0.1875 in
Coarse 2
: 0.1875 in
Thick Head
: 0.1875 in
Overall height
: 3.51 m
Price
: US $ 6,856.68
1.5 Tank Sodium Hydroxide
Code
: T-04
31
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Duties
: To save sodium Hydroxide as much as 96.22 kg/hour
Type
: Upright cylindrical tank covered with the top
torispherical dished head
Quantity
: 1 piece
Volume
: 55.47 m3
Material
: Carbon steel SA 212 Grade B
Storage conditions :
Pressure
: 1 atm
Temperature : 35oC
Dimensions :
The diameter of the tank
: 4.13 m
High-Tank
: 4.13 m
Thick Tank
: Coarse 1
: 0.1875 in
Coarse 2
: 0.1875 in
Thick Head
: 0.1875 in
Overall height
: 4.88 m
Price
: US $ 20,627.17
1.6
Reactor
Code
:R
Duties
: Reacting oleic acid and butanol to produce butyl oleate
with the help of Sulfuric Acid
Type
: Continueous Stirred Tank Reactor (CSTR)
Quantity
: 1 piece
Volume
: 23.39 m3
Material
: Carbon Steel SA 212 Grade B
Condition :
Pressure
: 1 atm
Temperature : 100oC
Dimensions :
The diameter of the tank
: 2.82 m
High-tank
: 3.46 m
Shell thickness
: 0.1875 in
32
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Dimensions head :
Shape
: Elliptical
Thick head
: 0.1875 in
High head
: 0.46 m
Mixer :
Type
: Turbine with 6 blades with 4 baffles
Quantity
: 1 piece
Diameter
: 0.94 m
Speed
: 67.68 rpm
Power
: 7.5 hp
Cooling jacket :
Ingredients
: Water
Diameter
: 3.06 m
Inlet temperature
: 30oC
Outlet temperature
: 40oC
High-jacket
: 2.59 m
Price
: US $ 253,697.05
1.7 Netralizer
Code
:N
Duties
: Neutralize sulfuric acid catalyst with sodium hydroxide
Quantity
: 1 piece
Temperature
: 47.28oC
Pressure
: 1 atm
Diameter
: 1.70 m
Height
: 1.70 m
Volume
: 4.95 m3
Type
: Continueous Stirred Tank Reactor (CSTR)
Type of head
: Torispherical dished head
Construction Materials
: Steel SA-283 Grade C
Mixer
33
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Type
: Blade disk turbine with 6 standard
Speed
: 106.19 rpm
Diameter
: 0.57 m
Power of motor
: 3 hp
Price
: US $ 21,255.70
3.8. Decanter
Code
:D
Function
: Separating butyl oleate and H2O
Operation
: Continuous
Quantity
: 1 piece
Temperature
: 47.28°C
Pressure
: 1 atm
Diameter
: 1.16 m
Lenght
: 3.47 m
Volume
: 3.03 m3
Type
: Horizontal Cylinders
Construction Material : Stainless steel SA-167 (type of 304)
Price
: US $ 5,713.90
3.9 . Mixer Tank 01
Code
Function
: MT-01
: Mixing oleic acid from the recycle of Flash drums and
fresh bait
Operation
: Continuous
Quantity
: 1 piece
Temperature
: 35°C
Pressure
: 1 atm
Diameter
: 0.75 m
Height
: 0.75 m
Volume
: 0.42 m3
34
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Type
: Vertical cylindrical tank stirred
Type of head
: Torispherical dished head
Material of construction
: Steel SA-283 Grade C
Mixer :
Type
: Turbine blade with 6 and 4 baffles
Speed
: 270.05rpm
Diameter
: 0.75 m
Power of motor
: 0.75 hp
Price
: US $ 11,542.07
3.10.Mixer Tank 02
Code
: MT-02
Function
: Butanol from the recycle of Distillation Tower and fresh
bait.
Operation
: Continuous
Quantity
: 1 piece
Temperature
: 35°C
Pressure
: 1 atm
Diameter
: 0.93 m
Height
: 0.93 m
Volume
: 0.84 m3
Type
: Vertical cylindrical tank stirred
Type of head
: Torispherical dished head
Material of construction
: Steel SA-283 Grade C
Mixer
Type
: Turbine blade with 6 and 4 baffles
Speed
: 176.67 rpm
Diameter
: 0.32 m
Power of motor
: 0.75 hp
Cooling Jacket :
35
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Ingredients
: Water
Diameter
: 0.93 m
Inlet temperature
: 25oC
Outlet temperature
: 50oC
High-jacket
: 0.82 m
Price
: US $ 11,542.07
3. 11. Distillation Tower
Code
: DT
Duties
: Separating butanol from the mixture after exit
decanter
Type
: Tower sieve tray
Number plate
: 36 plate
Material
: Low Alloy Steel SA 203 Grade C 2 1/2 Ni
Dimensions :
Diameter Top
: 0.78 m
Diameter Bottom
: 1.26
Height
: 17.121 m
Shell Thickness
: 0.1875 in
Dimensions Head
Type
: Torispherical Dished Head
Thick Head
: 0.1875 in
High Head
: 0.28 m
Operating Conditions:
Top
: Temperature : 118.33oC
Bottom
: Temperature : 146.0937oC Pressure : 1 atm
Price
: US $ 103,421.55
36
Pressure : 1 atm
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
3. 12. Flash Drum
Code
: FD
Duties
: Purify Butyl Oleate as the product of oleic acid
Type
: Vessel Vertical
Quantity
: 1 piece
Volume
: 2.27 m3
Material
: Steel SA-212 Grade B
Condition
: Pressure : 1 atm
Temperature : 196.78oC
Dimensions :
Tank Diameter
: 1.95 m
High-tank
: 7.8 m
Shell thickness
: 0.1875 in
Dimensi Head :
Type
: Elliptical
Thick Head
: 0.1875 m
Price
: US $ 68,566.77
3.13. Heat Exchanger
Code
: HE-01
Function
: Increasing the flow temperature of 10 to MD of
temperature 47.28°C to 121.82°C
Type
: Double pipe heat exchanger
Heating Load
: 1,045,682.80 kJ/hour
Heat transfer area
: 7.19 m2
Pipe Length
: 3.6 m
specifications
:
Anulus,
OD pipe
: 4.55 in
ID
: 4.026 in
37
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Pressure drop : 0,0015 psi
Inner pipe,
OD pipe
: 3.5 in
ID
: 3,068 in
Pressure drop : 0,0119 psi
UC
: 14.26 Btu/hour.ft2.oF
UD
: 13.67 Btu/hour.ft2.oF
Rd
: 0,003 Hour.ft2.oF /Btu
Construction Material : Inner (SS), Anulus (CS)
Total
:1
Price
: US $ 31,997.83
3.14. Heat Exchanger 02
Code
: HE-02
Function
: Increasing the temperature from the bottom of the
distillation tower to flash drums of temperature 146.09oC
to 196.7oC .
Type
: Double pipe heat exchanger
Heating Load
: 319,927.91 kJ/hour
Heat transfer area
: 3.97 m2
Lenght of pipe
: 3.6 m
Specification
:
Anulus,
OD pipe
: 2.38 in
ID
: 2.067 in
Pressure drop : 0,0014 psi
Inner pipe,
38
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
OD pipe
: 1.66 in
ID
: 1.38 in
Pressure drop : 0,1043 psi
UC
: 85.18 Btu/hour.ft2.oF
UD
: 67.84 Btu/hour.ft2.oF
Rd
: 0.003 hour.ft2.oF /Btu
Construction Material : Inner (SS), Anulus (CS)
Total
:1
Price
: US $ 23,998.37
3.15. Heat Exchanger 03
Code
: HE-03
Function
: Raising the temperature of mixing in the mixer 1 (flow 1
+ recycle at flow 14) to the reactor temperature 69.20oC to
100oC.
Type
: Double pipe heat exchanger
Heating Load
: 115,872.63 kJ/hour
Heat transfer area
: 0.78 m2
Pipe Lenght
: 36 m
Specification
:
Anulus,
OD pipa
: 4.5 in
ID
: 4.026 in
Pressure drop : 0.0000489 psi
Inner pipe,
OD pipa
: 3.5 in
ID
: 3.068 in
39
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Pressure drop : 0.0029 psi
UC
: 18.95 Btu/hour.ft2.oF
UD
: 17.93 Btu/hour.ft2.oF
Rd
: 0.003 Hour.ft2.oF /Btu
Construction Material : Inner (SS), Anulus (CS)
Total
:1
Price
: US $ 8,570.85
3.16 Cooler 01
Code
: Co-01
: Decreasing reactor outlet temperature before entering the
Duties
neutralizer of the temperature of 100oC to 40oC as much
as 5,237.06 kg/hour with water cooling medium.
Type
: Double Pipe Heat Exchanger
Cooling Load
: 1,013,420.48 kJ/hour
Heat transfer area
: 6.66 m2
Pipe Lenght
: 3.6 m
Specification
:
Anulus,
OD pipe
: 4.5 in
ID
: 4.026 in
Pressure drop : 0.21 psi
Inner pipe,
OD pipe
: 3.5 in
ID
: 3.068 in
Pressure drop : 0.11 psi
UC
: 74.76 Btu/hour.ft2.oF
UD
: 61.06 Btu/hour.ft2.oF
Rd
: 0.003 Hour.ft2.oF /Btu
Construction Material : Inner (SS), Anulus (CS)
40
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Total
:1
Price
: US $ 34,283.39
3.17. Cooler 02
Code
: Co-02
:.Decreasing flash drum outlet temperature as the product
Duties
of temperature 196,80oC to 35oC as much as 1,893.93
kg/hour with water cooling medium.
Type
: Double Pipe Heat Exchanger
Cooling Load
: 746,495.33 kJ/hour
Heat transfer area
: 4.41 m2
Pipe Lenght
: 3.6 m
Specification
:
Anulus,
OD pipe
: 2.38 in
ID
: 2.067 in
Pressure drop : 0.22 psi
Inner pipe,
OD pipe
: 1.66 in
ID
: 1.38 in
Pressure drop : 6.69 psi
UC
: 136.91 Btu/hour.ft2.oF
UD
: 97.05 Btu/hour.ft2.oF
Rd
: 0.003 Hour.ft2.oF /Btu
Construction Material : Inner (SS), Anulus (CS)
Total
:1
Price
: US $ 23,998.37
1.18. Reboiler
Code
: RB
41
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Function
:.Vaporize
bottom
liquid
distillation
tower
as
2,165.39 kg/h
Type
: Double Pipe
Heating Load
: 2,174,811.45 kJ/hour
Heat transfer area
: 3.31 m2
Pipe Lenght
: 3.6 m
Specification
:
Anulus,
OD pipe
: 4.5 in
ID
: 4.026 in
Pressure drop
: 0.0057 psi
OD pipe
: 3.5 in
ID
: 3.068 in
Pressure drop
: 0.0025 psi
Inner pipe,
UC
: 62.01 Btu/hour.ft2.oF
UD
: 52.28 Btu/hour.ft2.oF
Rd
: 0.003 hour.ft2.oF/Btu
Construction Material : Inner (SS), Anulus (CS)
Total
:1
Price
: US $ 19,427.25
3.19.Condensor 1
Code
Function
: Cd-01
:.For condensing distillation tower top products as much
as 2892.73 kg/hour.
Type
: Shell and Tube
Heating Load
: 2,068,807.32 kJ/hour
42
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Heat transfer area
: 27.96 m2
Fluid flow
Shell : gas
Tube : Water
Specifications tube
Number of tube
: 70 pieces
Lenght
: 16 ft
OD, BWG, pitch
: ¾ in, 16, 1 in (triangular)
Total flow
: 8 pass
Shell Specification
ID
: 15.25 in
Baffle spacing
: 5 in
Total flow
: 1 pass
Price
: US $ 39,997.28
3.20.Condensor 2
Code
Function
: Cd-02
:.For condensing distillate or products of flash drum.
Type
: Shell and Tube
Heating Load
: 493,805.93 kJ/hour
Heat transfer area
: 3.38 m2
Fluid flow
Shell : gas
Tube : Water
Specifications tube
Number of tube
: 70 pieces
Lenght
: 16 ft
OD, BWG, pitch
: ¾ in, 16, 1 in (triangular)
Total flow
: 8 pass
Specifications shell
ID
: 15,25 in
Baffle spacing
: 5 in
Total flow
: 1 pass
43
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Price
: US $ 20,570.03
3.21.Accumulator 01
Code
: Acc-01
Duties
: Collect as much condensate from the distillation tower as
much as 2892.73 kg/hour
Type
: Horizontal drum
Quantity
: 1 piece
Operating conditions
Temperature
: 118.3oC
Pressure
: 1 atm
Dimensions of tank
Shell :
Lenght : 1.7 m
Diameter : 0.87 m
Thickness : ¼ in
Head
:Type : Torispherical dished head
Thickness
: 36 in
Material
: Stainless steel SA-212 Grade B
Price
: US $ 7,428.07
3.22.Accumulator 02
Code
: Acc-02
Duties
: Collect as much condensate from the flash drum 1893.94
kg/hour
Type
: Horizontal drum
Quantity
: 1 piece
Operating conditions
Temperature
: 196.8oC
Pressure
: 1 atm
Dimensions of tank
Shell
: Lenght : 1.50 m
44
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Diameter : 0.75 m
Thickness : ¼ in
Head
:Type : Torispherical dished head
Thickness
: 32 in
Material
: Stainless steel SA 212 Grade B
Price
: US $ 4,913.95
3.23.Pump-01
Code
: P-01
Duties
: Pumping from the tanker butanol to the tank of material
butanol
Capacity
: 46.09 m3/hour
Total Head
: 8.31 m
Type
:Centrifugal Single Stage 3500 rpm
Motor Standar
: 2 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 19,884.36
3.24.Pump-02
Code
: P-02
Duties
: Transporting raw materials oleic acid from the truck to the
tank Oleic acid reservoir.
Capacity
: 46.09 m3/hour
Total Head
: 3,00 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 2 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 19,884.36
45
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
3.25.Pump-03
Code
: P-03
Duties
: Flowing from the truck to the tank NaOH
Capacity
: 46.09 m3/hour
Total Head
: 4.16 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 2 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 19,884.36
3.26.Pump-04
Code
: P-04
Duties
: Flowing from the truck to the tank Oleic acid
Capacity
: 46.09 m3/hour
Total Head
: 12.19 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 5 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 19,884.36
3.27.Pump-05
Code
: P-05
Duties
: Flowing butanol material to the mixer 02
Capacity
: 0.81 m3/hour
Total Head
: 0.97 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
46
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Price
: US $ 6,628.12
3.28.Pump-06
Code
: P-06
Duties
:Transporting materials sulfuric acid into the reactor
Capacity
: 0.04 m3/hour
Total Head
: 2.98 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 6,628.12
3.29.Pump-07
Code
: P-07
Duties
: To pumping NaOH from NaOH tank to netralizer
Capacity
: 0.10 m3/hour
Total Head
: 1.70 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 6,628.12
3.40.Pump-08
Code
: P-08
Duties
: Pumping oleic acid from oleic acid tank to the mixer 01
Capacity
: 2.57 m3/hour
Total Head
: 0.79 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
47
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 7,656.62
3.41.Pump-09
Code
: P-09
Duties
: Pumping of raw materials to the output of the mixer 02 to
reactor
Capacity
: 6.03 m3/hour
Total Head
: 4.41 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 10,170.74
3.42.Pump-10
Code
: P-10
Duties
: Pumping the output of the mixer 01 to reactor
Capacity
: 3.17 m3/hour
Total Head
: 4.41 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 8,570.85
3.43.Pump-11
Code
: P-11
Duties
: Pumping the output of the reactor to netralizer
Capacity
: 9.08 m3/hour
48
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Total Head
: 0.09 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 11,656.35
3.44.Pump-12
Code
: P-12
Duties
: Pumping output netralizer to decanter
Capacity
: 9.14 m3/hour
Total Head
: 2.35 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 11,656.35
3.45.Pump-13
Code
: P-13
Duties
: Pumping down the decanter to the output of the WTU
Capacity
: 0.29 m3/hour
Total Head
: 3.69 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 6,628.12
3.46.Pump-14
Code
: P-14
49
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Duties
: Pumping on the decanter to the output of the distillation
tower
Capacity
: 8.97 m3/hour
Total Head
: 4.66 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.5 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 11,656.35
3.47.Pump-15
Code
: P-15
Duties
: Pumping output below the results of distillation tower to
Flash drums
Capacity
: 4.02 m3/hour
Total Head
: 7.93 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.5 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 10,170.74
3.48.Pump-16
Code
: P-16
Duties
: Pumping output results on distillation tower is in
accumulator to the mixer 02
Capacity
: 5.77 m3/hour
Total Head
: 0.99 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
50
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Amount
:1
Price
: US $ 10,170.74
3.49.Pump-17
Code
: P-17
Duties
: Pumping output over existing flash drum in accumulator to
the product storage tank
Capacity
: 3.21 m3/hour
Total Head
: 10.19 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 8,570.85
3.50.Pump-18
Code
: P-18
Duties
: Pumping down the output of the mixer to flash drum 01
Capacity
: 0.50 m3/hour
Total Head
: 0.77 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 6,628.12
3.51.Pump-19
Code
: P-18
Duties
: Powering butyl oleate products in the storage tank products
to the distribution trucks.
Capacity
: 46.09 m3/hour
51
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Total Head
: 10.19 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 5 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 19,884.36
52
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
CHAPTER III
SPECIFICATION EQUIPMENTS
1.1 Oleic Acid Storage Tank
Code
: T-01
Duties
: Store raw materials oleic acid as 1,575.31
kg/hour
Type
: Vertical cylindrical tank with torispherical dished
head
Quantity
: 1 Piece
Volume
: 1,415.43 m3
Material
: Carbon steel SA 212 Grade B
Storage conditions
:
Pressure
: 1 atm
Temperature
: 35oC
Dimensions :
The diameter of the tank : 12.17 m
Height tank
Thick tank
: 12.17 m
: Coarse 1
: 0.4375 in
Coarse 2
: 0.375 in
Coarse 3
: 0.3125 in
Coarse 4
: 0.25 in
Coarse 5
: 0.25 in
Coarse 6
: 0.1875 in
Thick Head
: 0.5 in
Total high
: 14.3864 m
Price
: US $ 340,548.30
1.2 Storage Tank Butanol
Code
: T-02
Duties
: store raw materials butanol as 450.11 kg/hour.
29
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Type
: Vertical cylindrical tank with torispherical dished
head
Quantity
: 1 piece
Volume
: 446.14 m3
Material
: Carbon steel SA 212 Grade B
Storage conditions
:
Pressure
: 1 atm
Temperature : 35oC
Dimensions :
The diameter of the tank
: 8.28 m
Height tank
: 8.28 m
Thick tank :
Coarse 1
: 0.25 in
Coarse 2
: 0.25 in
Coarse 3
: 0.1875 in
Coarse 4
: 0.1875 in
Coarse 5
: 0.1875 in
Thick-Head
: 0.3125 in
Overall high
:9.79 m
Price
: US $ 215,985.33
1.3 Tank of Butyl Oleate
Code
: T-05
Duties
: store the product butyl oleate as 1,893.94 kg/hour
Type
: Vertical cylinder with torispherical dished head
Quantity
: 1 piece
Volume
: 826.27 m3
Material
: Carbon steel SA 212 Grade B
Storage conditions :
Pressure
: 1 atm
Temperature
: 35oC
Dimensions :
The diameter of the tank
: 10.17 m
High-tank
: 10.17 m
30
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Thick tank
: Coarse 1
: 0.25 in
Coarse 2
: 0.25 in
Coarse 3
: 0.25 in
Coarse 4
: 0.25 in
Coarse 5
: 0.1875 in
Coarse 6
: 0.1875 in
Thick-Head
: 0.4375 in
Overall high
: 12.02 m
Price
: US $ 270,838.75
1.4 Sulfuric Acid Tank
Code
: T-03
Duties
: To save as much sulfuric acid 47.46 kg/hour
Type
: Vertical cylindrical tank with torispherical dished head
Quantity
: 1 piece
Volume
: 20.69 m3
Material
: Carbon steel SA 212 Grade B
Storage conditions
: Pressure
: 1 atm
Temperature : 35oC
Dimensions :
The diameter of the tank
: 2.98 m
High-tank
: 2.98 m
Thick tank :
Coarse 1
: 0.1875 in
Coarse 2
: 0.1875 in
Thick Head
: 0.1875 in
Overall height
: 3.51 m
Price
: US $ 6,856.68
1.5 Tank Sodium Hydroxide
Code
: T-04
31
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Duties
: To save sodium Hydroxide as much as 96.22 kg/hour
Type
: Upright cylindrical tank covered with the top
torispherical dished head
Quantity
: 1 piece
Volume
: 55.47 m3
Material
: Carbon steel SA 212 Grade B
Storage conditions :
Pressure
: 1 atm
Temperature : 35oC
Dimensions :
The diameter of the tank
: 4.13 m
High-Tank
: 4.13 m
Thick Tank
: Coarse 1
: 0.1875 in
Coarse 2
: 0.1875 in
Thick Head
: 0.1875 in
Overall height
: 4.88 m
Price
: US $ 20,627.17
1.6
Reactor
Code
:R
Duties
: Reacting oleic acid and butanol to produce butyl oleate
with the help of Sulfuric Acid
Type
: Continueous Stirred Tank Reactor (CSTR)
Quantity
: 1 piece
Volume
: 23.39 m3
Material
: Carbon Steel SA 212 Grade B
Condition :
Pressure
: 1 atm
Temperature : 100oC
Dimensions :
The diameter of the tank
: 2.82 m
High-tank
: 3.46 m
Shell thickness
: 0.1875 in
32
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Dimensions head :
Shape
: Elliptical
Thick head
: 0.1875 in
High head
: 0.46 m
Mixer :
Type
: Turbine with 6 blades with 4 baffles
Quantity
: 1 piece
Diameter
: 0.94 m
Speed
: 67.68 rpm
Power
: 7.5 hp
Cooling jacket :
Ingredients
: Water
Diameter
: 3.06 m
Inlet temperature
: 30oC
Outlet temperature
: 40oC
High-jacket
: 2.59 m
Price
: US $ 253,697.05
1.7 Netralizer
Code
:N
Duties
: Neutralize sulfuric acid catalyst with sodium hydroxide
Quantity
: 1 piece
Temperature
: 47.28oC
Pressure
: 1 atm
Diameter
: 1.70 m
Height
: 1.70 m
Volume
: 4.95 m3
Type
: Continueous Stirred Tank Reactor (CSTR)
Type of head
: Torispherical dished head
Construction Materials
: Steel SA-283 Grade C
Mixer
33
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Type
: Blade disk turbine with 6 standard
Speed
: 106.19 rpm
Diameter
: 0.57 m
Power of motor
: 3 hp
Price
: US $ 21,255.70
3.8. Decanter
Code
:D
Function
: Separating butyl oleate and H2O
Operation
: Continuous
Quantity
: 1 piece
Temperature
: 47.28°C
Pressure
: 1 atm
Diameter
: 1.16 m
Lenght
: 3.47 m
Volume
: 3.03 m3
Type
: Horizontal Cylinders
Construction Material : Stainless steel SA-167 (type of 304)
Price
: US $ 5,713.90
3.9 . Mixer Tank 01
Code
Function
: MT-01
: Mixing oleic acid from the recycle of Flash drums and
fresh bait
Operation
: Continuous
Quantity
: 1 piece
Temperature
: 35°C
Pressure
: 1 atm
Diameter
: 0.75 m
Height
: 0.75 m
Volume
: 0.42 m3
34
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Type
: Vertical cylindrical tank stirred
Type of head
: Torispherical dished head
Material of construction
: Steel SA-283 Grade C
Mixer :
Type
: Turbine blade with 6 and 4 baffles
Speed
: 270.05rpm
Diameter
: 0.75 m
Power of motor
: 0.75 hp
Price
: US $ 11,542.07
3.10.Mixer Tank 02
Code
: MT-02
Function
: Butanol from the recycle of Distillation Tower and fresh
bait.
Operation
: Continuous
Quantity
: 1 piece
Temperature
: 35°C
Pressure
: 1 atm
Diameter
: 0.93 m
Height
: 0.93 m
Volume
: 0.84 m3
Type
: Vertical cylindrical tank stirred
Type of head
: Torispherical dished head
Material of construction
: Steel SA-283 Grade C
Mixer
Type
: Turbine blade with 6 and 4 baffles
Speed
: 176.67 rpm
Diameter
: 0.32 m
Power of motor
: 0.75 hp
Cooling Jacket :
35
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Ingredients
: Water
Diameter
: 0.93 m
Inlet temperature
: 25oC
Outlet temperature
: 50oC
High-jacket
: 0.82 m
Price
: US $ 11,542.07
3. 11. Distillation Tower
Code
: DT
Duties
: Separating butanol from the mixture after exit
decanter
Type
: Tower sieve tray
Number plate
: 36 plate
Material
: Low Alloy Steel SA 203 Grade C 2 1/2 Ni
Dimensions :
Diameter Top
: 0.78 m
Diameter Bottom
: 1.26
Height
: 17.121 m
Shell Thickness
: 0.1875 in
Dimensions Head
Type
: Torispherical Dished Head
Thick Head
: 0.1875 in
High Head
: 0.28 m
Operating Conditions:
Top
: Temperature : 118.33oC
Bottom
: Temperature : 146.0937oC Pressure : 1 atm
Price
: US $ 103,421.55
36
Pressure : 1 atm
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
3. 12. Flash Drum
Code
: FD
Duties
: Purify Butyl Oleate as the product of oleic acid
Type
: Vessel Vertical
Quantity
: 1 piece
Volume
: 2.27 m3
Material
: Steel SA-212 Grade B
Condition
: Pressure : 1 atm
Temperature : 196.78oC
Dimensions :
Tank Diameter
: 1.95 m
High-tank
: 7.8 m
Shell thickness
: 0.1875 in
Dimensi Head :
Type
: Elliptical
Thick Head
: 0.1875 m
Price
: US $ 68,566.77
3.13. Heat Exchanger
Code
: HE-01
Function
: Increasing the flow temperature of 10 to MD of
temperature 47.28°C to 121.82°C
Type
: Double pipe heat exchanger
Heating Load
: 1,045,682.80 kJ/hour
Heat transfer area
: 7.19 m2
Pipe Length
: 3.6 m
specifications
:
Anulus,
OD pipe
: 4.55 in
ID
: 4.026 in
37
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Pressure drop : 0,0015 psi
Inner pipe,
OD pipe
: 3.5 in
ID
: 3,068 in
Pressure drop : 0,0119 psi
UC
: 14.26 Btu/hour.ft2.oF
UD
: 13.67 Btu/hour.ft2.oF
Rd
: 0,003 Hour.ft2.oF /Btu
Construction Material : Inner (SS), Anulus (CS)
Total
:1
Price
: US $ 31,997.83
3.14. Heat Exchanger 02
Code
: HE-02
Function
: Increasing the temperature from the bottom of the
distillation tower to flash drums of temperature 146.09oC
to 196.7oC .
Type
: Double pipe heat exchanger
Heating Load
: 319,927.91 kJ/hour
Heat transfer area
: 3.97 m2
Lenght of pipe
: 3.6 m
Specification
:
Anulus,
OD pipe
: 2.38 in
ID
: 2.067 in
Pressure drop : 0,0014 psi
Inner pipe,
38
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
OD pipe
: 1.66 in
ID
: 1.38 in
Pressure drop : 0,1043 psi
UC
: 85.18 Btu/hour.ft2.oF
UD
: 67.84 Btu/hour.ft2.oF
Rd
: 0.003 hour.ft2.oF /Btu
Construction Material : Inner (SS), Anulus (CS)
Total
:1
Price
: US $ 23,998.37
3.15. Heat Exchanger 03
Code
: HE-03
Function
: Raising the temperature of mixing in the mixer 1 (flow 1
+ recycle at flow 14) to the reactor temperature 69.20oC to
100oC.
Type
: Double pipe heat exchanger
Heating Load
: 115,872.63 kJ/hour
Heat transfer area
: 0.78 m2
Pipe Lenght
: 36 m
Specification
:
Anulus,
OD pipa
: 4.5 in
ID
: 4.026 in
Pressure drop : 0.0000489 psi
Inner pipe,
OD pipa
: 3.5 in
ID
: 3.068 in
39
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Pressure drop : 0.0029 psi
UC
: 18.95 Btu/hour.ft2.oF
UD
: 17.93 Btu/hour.ft2.oF
Rd
: 0.003 Hour.ft2.oF /Btu
Construction Material : Inner (SS), Anulus (CS)
Total
:1
Price
: US $ 8,570.85
3.16 Cooler 01
Code
: Co-01
: Decreasing reactor outlet temperature before entering the
Duties
neutralizer of the temperature of 100oC to 40oC as much
as 5,237.06 kg/hour with water cooling medium.
Type
: Double Pipe Heat Exchanger
Cooling Load
: 1,013,420.48 kJ/hour
Heat transfer area
: 6.66 m2
Pipe Lenght
: 3.6 m
Specification
:
Anulus,
OD pipe
: 4.5 in
ID
: 4.026 in
Pressure drop : 0.21 psi
Inner pipe,
OD pipe
: 3.5 in
ID
: 3.068 in
Pressure drop : 0.11 psi
UC
: 74.76 Btu/hour.ft2.oF
UD
: 61.06 Btu/hour.ft2.oF
Rd
: 0.003 Hour.ft2.oF /Btu
Construction Material : Inner (SS), Anulus (CS)
40
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Total
:1
Price
: US $ 34,283.39
3.17. Cooler 02
Code
: Co-02
:.Decreasing flash drum outlet temperature as the product
Duties
of temperature 196,80oC to 35oC as much as 1,893.93
kg/hour with water cooling medium.
Type
: Double Pipe Heat Exchanger
Cooling Load
: 746,495.33 kJ/hour
Heat transfer area
: 4.41 m2
Pipe Lenght
: 3.6 m
Specification
:
Anulus,
OD pipe
: 2.38 in
ID
: 2.067 in
Pressure drop : 0.22 psi
Inner pipe,
OD pipe
: 1.66 in
ID
: 1.38 in
Pressure drop : 6.69 psi
UC
: 136.91 Btu/hour.ft2.oF
UD
: 97.05 Btu/hour.ft2.oF
Rd
: 0.003 Hour.ft2.oF /Btu
Construction Material : Inner (SS), Anulus (CS)
Total
:1
Price
: US $ 23,998.37
1.18. Reboiler
Code
: RB
41
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Function
:.Vaporize
bottom
liquid
distillation
tower
as
2,165.39 kg/h
Type
: Double Pipe
Heating Load
: 2,174,811.45 kJ/hour
Heat transfer area
: 3.31 m2
Pipe Lenght
: 3.6 m
Specification
:
Anulus,
OD pipe
: 4.5 in
ID
: 4.026 in
Pressure drop
: 0.0057 psi
OD pipe
: 3.5 in
ID
: 3.068 in
Pressure drop
: 0.0025 psi
Inner pipe,
UC
: 62.01 Btu/hour.ft2.oF
UD
: 52.28 Btu/hour.ft2.oF
Rd
: 0.003 hour.ft2.oF/Btu
Construction Material : Inner (SS), Anulus (CS)
Total
:1
Price
: US $ 19,427.25
3.19.Condensor 1
Code
Function
: Cd-01
:.For condensing distillation tower top products as much
as 2892.73 kg/hour.
Type
: Shell and Tube
Heating Load
: 2,068,807.32 kJ/hour
42
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Heat transfer area
: 27.96 m2
Fluid flow
Shell : gas
Tube : Water
Specifications tube
Number of tube
: 70 pieces
Lenght
: 16 ft
OD, BWG, pitch
: ¾ in, 16, 1 in (triangular)
Total flow
: 8 pass
Shell Specification
ID
: 15.25 in
Baffle spacing
: 5 in
Total flow
: 1 pass
Price
: US $ 39,997.28
3.20.Condensor 2
Code
Function
: Cd-02
:.For condensing distillate or products of flash drum.
Type
: Shell and Tube
Heating Load
: 493,805.93 kJ/hour
Heat transfer area
: 3.38 m2
Fluid flow
Shell : gas
Tube : Water
Specifications tube
Number of tube
: 70 pieces
Lenght
: 16 ft
OD, BWG, pitch
: ¾ in, 16, 1 in (triangular)
Total flow
: 8 pass
Specifications shell
ID
: 15,25 in
Baffle spacing
: 5 in
Total flow
: 1 pass
43
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Price
: US $ 20,570.03
3.21.Accumulator 01
Code
: Acc-01
Duties
: Collect as much condensate from the distillation tower as
much as 2892.73 kg/hour
Type
: Horizontal drum
Quantity
: 1 piece
Operating conditions
Temperature
: 118.3oC
Pressure
: 1 atm
Dimensions of tank
Shell :
Lenght : 1.7 m
Diameter : 0.87 m
Thickness : ¼ in
Head
:Type : Torispherical dished head
Thickness
: 36 in
Material
: Stainless steel SA-212 Grade B
Price
: US $ 7,428.07
3.22.Accumulator 02
Code
: Acc-02
Duties
: Collect as much condensate from the flash drum 1893.94
kg/hour
Type
: Horizontal drum
Quantity
: 1 piece
Operating conditions
Temperature
: 196.8oC
Pressure
: 1 atm
Dimensions of tank
Shell
: Lenght : 1.50 m
44
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Diameter : 0.75 m
Thickness : ¼ in
Head
:Type : Torispherical dished head
Thickness
: 32 in
Material
: Stainless steel SA 212 Grade B
Price
: US $ 4,913.95
3.23.Pump-01
Code
: P-01
Duties
: Pumping from the tanker butanol to the tank of material
butanol
Capacity
: 46.09 m3/hour
Total Head
: 8.31 m
Type
:Centrifugal Single Stage 3500 rpm
Motor Standar
: 2 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 19,884.36
3.24.Pump-02
Code
: P-02
Duties
: Transporting raw materials oleic acid from the truck to the
tank Oleic acid reservoir.
Capacity
: 46.09 m3/hour
Total Head
: 3,00 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 2 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 19,884.36
45
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
3.25.Pump-03
Code
: P-03
Duties
: Flowing from the truck to the tank NaOH
Capacity
: 46.09 m3/hour
Total Head
: 4.16 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 2 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 19,884.36
3.26.Pump-04
Code
: P-04
Duties
: Flowing from the truck to the tank Oleic acid
Capacity
: 46.09 m3/hour
Total Head
: 12.19 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 5 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 19,884.36
3.27.Pump-05
Code
: P-05
Duties
: Flowing butanol material to the mixer 02
Capacity
: 0.81 m3/hour
Total Head
: 0.97 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
46
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Price
: US $ 6,628.12
3.28.Pump-06
Code
: P-06
Duties
:Transporting materials sulfuric acid into the reactor
Capacity
: 0.04 m3/hour
Total Head
: 2.98 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 6,628.12
3.29.Pump-07
Code
: P-07
Duties
: To pumping NaOH from NaOH tank to netralizer
Capacity
: 0.10 m3/hour
Total Head
: 1.70 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 6,628.12
3.40.Pump-08
Code
: P-08
Duties
: Pumping oleic acid from oleic acid tank to the mixer 01
Capacity
: 2.57 m3/hour
Total Head
: 0.79 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
47
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 7,656.62
3.41.Pump-09
Code
: P-09
Duties
: Pumping of raw materials to the output of the mixer 02 to
reactor
Capacity
: 6.03 m3/hour
Total Head
: 4.41 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 10,170.74
3.42.Pump-10
Code
: P-10
Duties
: Pumping the output of the mixer 01 to reactor
Capacity
: 3.17 m3/hour
Total Head
: 4.41 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 8,570.85
3.43.Pump-11
Code
: P-11
Duties
: Pumping the output of the reactor to netralizer
Capacity
: 9.08 m3/hour
48
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Total Head
: 0.09 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 11,656.35
3.44.Pump-12
Code
: P-12
Duties
: Pumping output netralizer to decanter
Capacity
: 9.14 m3/hour
Total Head
: 2.35 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 11,656.35
3.45.Pump-13
Code
: P-13
Duties
: Pumping down the decanter to the output of the WTU
Capacity
: 0.29 m3/hour
Total Head
: 3.69 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 6,628.12
3.46.Pump-14
Code
: P-14
49
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Duties
: Pumping on the decanter to the output of the distillation
tower
Capacity
: 8.97 m3/hour
Total Head
: 4.66 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.5 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 11,656.35
3.47.Pump-15
Code
: P-15
Duties
: Pumping output below the results of distillation tower to
Flash drums
Capacity
: 4.02 m3/hour
Total Head
: 7.93 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.5 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 10,170.74
3.48.Pump-16
Code
: P-16
Duties
: Pumping output results on distillation tower is in
accumulator to the mixer 02
Capacity
: 5.77 m3/hour
Total Head
: 0.99 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
50
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Amount
:1
Price
: US $ 10,170.74
3.49.Pump-17
Code
: P-17
Duties
: Pumping output over existing flash drum in accumulator to
the product storage tank
Capacity
: 3.21 m3/hour
Total Head
: 10.19 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 8,570.85
3.50.Pump-18
Code
: P-18
Duties
: Pumping down the output of the mixer to flash drum 01
Capacity
: 0.50 m3/hour
Total Head
: 0.77 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 0.25 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 6,628.12
3.51.Pump-19
Code
: P-18
Duties
: Powering butyl oleate products in the storage tank products
to the distribution trucks.
Capacity
: 46.09 m3/hour
51
Final report
Preliminary Design of Butyl Oleate Plant of Oleic Acid and Butanol
Capacity of 15,000 Tons/Year
Total Head
: 10.19 m
Type
: Centrifugal Single Stage 3500 rpm
Motor Standar
: 5 Hp
Material
: Carbon Steel SA 285 Grade C
Amount
:1
Price
: US $ 19,884.36
52