INFRASTRUCTURE
Projects/Infrastructure
Sludge Tank
In the project, "non-Newtonian" sludge flow in a sludge tank located in a wastewater treatment plant, mixed with static jet nozzles was examined by CFD analysis. Velocity distribution in the tank, active volume, homogenization time, etc. was calculated and it was determined whether the number of mixers, their placement, and pump power were sufficient.
Sludge Tank
In the project, "non-Newtonian" sludge flow in a sludge tank located in a wastewater treatment plant, mixed with static jet nozzles was examined by CFD analysis. Velocity distribution in the tank, active volume, homogenization time, etc. was calculated and it was determined whether the number of mixers, their placement, and pump power were sufficient.
Sludge Tank
In the project, "non-Newtonian" sludge flow in a sludge tank located in a wastewater treatment plant, mixed with static jet nozzles was examined by CFD analysis. Velocity distribution in the tank, active volume, homogenization time, etc. was calculated and it was determined whether the number of mixers, their placement, and pump power were sufficient.
Sludge Tank
In the project, "non-Newtonian" sludge flow in a sludge tank located in a wastewater treatment plant, mixed with static jet nozzles was examined by CFD analysis. Velocity distribution in the tank, active volume, homogenization time, etc. was calculated and it was determined whether the number of mixers, their placement, and pump power were sufficient.
Sludge Tank
In the project, "non-Newtonian" sludge flow in a sludge tank located in a wastewater treatment plant, mixed with static jet nozzles was examined by CFD analysis. Velocity distribution in the tank, active volume, homogenization time, etc. was calculated and it was determined whether the number of mixers, their placement, and pump power were sufficient.
Sludge Tank
In the project, "non-Newtonian" sludge flow in a sludge tank located in a wastewater treatment plant, mixed with static jet nozzles was examined by CFD analysis. Velocity distribution in the tank, active volume, homogenization time, etc. was calculated and it was determined whether the number of mixers, their placement, and pump power were sufficient.