Jenya
Chemical
- Feb 12, 2016
- 1
Hello,
Could you please help me with the following question.
We have a self priming centrifugal pump. The type that retains part of liquid inside the casing such as goulds 3796. We have tested the pump with two liquids, water and hexane. The suction side was blinded off with a blind flange with pressure gauge. Discharge side was also blinded of with a blind flange with pressure gauge and air bleed line. Bleed line is 8mm tube going into hexane tank.
Test 1: water 10C
Casing is filled with initial prime (water). pump started and discharged air through air bleed line. Firther pressure at the suction side dropped to -0.8 barg.
Test 2: hexane 15C
Casing is filled with initial prime (hexane). pump started and discharged air through air bleed line. Firther pressure at the suction side dropped to -0.2 barg. Hexane boiling temperature at -0.2 barg is 50C.
The question is why created suction pressure with water in the casing is lower than with hexane? Density? Viscosity?
Could you please help me with the following question.
We have a self priming centrifugal pump. The type that retains part of liquid inside the casing such as goulds 3796. We have tested the pump with two liquids, water and hexane. The suction side was blinded off with a blind flange with pressure gauge. Discharge side was also blinded of with a blind flange with pressure gauge and air bleed line. Bleed line is 8mm tube going into hexane tank.
Test 1: water 10C
Casing is filled with initial prime (water). pump started and discharged air through air bleed line. Firther pressure at the suction side dropped to -0.8 barg.
Test 2: hexane 15C
Casing is filled with initial prime (hexane). pump started and discharged air through air bleed line. Firther pressure at the suction side dropped to -0.2 barg. Hexane boiling temperature at -0.2 barg is 50C.
The question is why created suction pressure with water in the casing is lower than with hexane? Density? Viscosity?