|
Process parameters |
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|
Project |
Design parameters |
Performance parameters |
||||||
|
|
Shell Side
|
Tube Side
|
Shell Side
|
Tube Side
|
||||
|
MEDIUM |
Fluid name |
Sulfuric Acid
104.5%
|
Cooling Water
|
Sulfuric Acid
104.5%
|
Cooling Water
|
|||
|
|
Temperature (Inlet) ℃ |
70.5
|
33
|
70.5
|
33
|
|||
|
|
Temperature (Outlet)℃ |
50
|
41
|
50
|
40.976
|
|||
|
|
Liquid Kg/h |
382320
|
|
382320
|
345000
|
|||
|
|
Density(inlet/outlet) Kg/m3 |
1855
|
1000
|
1855
|
1000
|
|||
|
|
Viscosity(inlet/outlet)(cp) |
8.69
|
0.76
|
8.69
|
0.76
|
|||
|
|
Inlet pressure Mpa |
0.54
|
0.3
|
0.54
|
0.3
|
|||
|
|
Pressure drop, Mpa |
≤0.1
|
≤0.1
|
0.036
|
0.0042
|
|||
|
PERFORMANCE |
Heat exchanged quantity W |
|
~3185097.3
|
|||||
|
|
Flow rate m/s |
|
0.471
|
0.794
|
||||
|
|
Heat transfer area affluent coefficient |
|
1.15
|
|||||
|
|
Heat transfer coefficient W/m2 ℃ |
|
724.326
|
|||||
|
|
Heat transfer area m2 |
|
200
|
|||||
|
|
Type |
shell and tube
|
The flow form
|
counter-current flow
|
||||
|
|
Sealing form |
welding connection in acid side, flange connection in water side
|
||||||
|
|
Materials and specifications |
shell
|
304L δ= 10
|
|||||
|
|
|
Heat transfer tube
|
316L Φ19×2.0×6000
|
|||||
|
|
|
Tubesheet
|
304L δ= 55
|
|||||
|
|
|
Baffle-crossing
|
304L δ= 10
|
|||||
|
|
|
head
|
Q235-B δ= 12
|
|||||
|
|
Flange standard |
Shell Side
|
Tube Side
|
|||||
|
|
|
HG/T20592-2009(B) PN10 DN 250
|
HG/T20592-2009(B) PN10 DN 300
|
|||||
|
Size |
Φ800×7254×1262
|
|||||||
|
Operating weight |
9451 Kg
|
|||||||
|
The scope of supply |
●Complete set ●Control system
●Special cable ●Random accessories |
|||||||
Anodic protection is an electrochemical corrosion control technique designed to maintain metals in a passive state when exposed to aggressive electrolytes. Unlike cathodic protection, which is suitable for neutral or alkaline environments, anodic protection is specifically engineered for highly corrosive acidic solutions, such as concentrated sulfuric acid and phosphoric acid.
By actively forming and preserving a protective oxide film on metal surfaces, the system virtually eliminates corrosion without altering the process or the product.
The technique capitalizes on the passive-active behavior exhibited by certain metals and alloys. When a metal is polarized into a specific potential range, its surface transforms from an active (corroding) state to a passive (protected) state, characterized by a thin, adherent oxide layer.
An anodic protection system continuously monitors the electrochemical potential of the equipment and applies a controlled anodic current to maintain this passive condition. This proactive approach ensures that even large vessels with complex geometries remain uniformly protected.
A complete anodic protection system consists of four primary elements working in a closed-loop control configuration: