A new type of impeller for stirred tanks - the convex bladed mixed flow impeller (CBMF) is described. It is a compromise between the disc turbine (Rushton) impeller: the CBMF combines the swept-back blades with a propeller action. The swept-back feature gives lower energy dissipation in the vicinity of the impeller than the disc turbine; the propeller action gives a strong downward liquid motion through the impeller and hence good circulation in the stirred tank. Such a compromise is necessary for a multipurpose mixing vessel. The CBMF impeller was tested comprehensively in comparison with the disc turbine, the marine propeller and the pitched bladed turbine; the comparison includes published data. The tests included measurements of: (1) po...
Abstract Liquid flow in the impeller swept region of vessels with a turbine-type agitator was examin...
The three-blade combined agitator consists of two propulsion blades of the same type (including plan...
The effectiveness of a range of impellers for "stirring as foam disruption" (SAFD) is assessed in a ...
The mixing efficiencies of impellers vary according to their designs. In this work, the effects of 6...
Experiments are carried out in a baffled flat-bottom stirred tank to test live dual-impeller configu...
The fluid mixing process is a common supportive phenomenon that often occurs in a large number of in...
In this paper, the data assembled concerning the agitation of a Newtonian fluid in a cylindrical ves...
The geometry of an impeller is a determining factor in power demand, which in turn determines the co...
Present work compares the mass transfer coefficient (kLa) and power draw capability of stirred tank ...
A study was made of the pumping capacity of pitched blade impellers in a cylindrical pilot plant ves...
Design of the impeller blade is a determining factor in power consumption and mixing quality, which ...
Mixing and mass transfer characteristics of an unbaffled aerated agitation vessel with a liquid heig...
Power consumption of unsteadily forward-reverse rotating multiple impellers, a new cross type of imp...
The rate of gas induction was measured in gas-inducing-type mechanically agitated contactors (GIMAC)...
Rate of gas induction, static pressure, mixing time and power consumption have been measured in 0.57...
Abstract Liquid flow in the impeller swept region of vessels with a turbine-type agitator was examin...
The three-blade combined agitator consists of two propulsion blades of the same type (including plan...
The effectiveness of a range of impellers for "stirring as foam disruption" (SAFD) is assessed in a ...
The mixing efficiencies of impellers vary according to their designs. In this work, the effects of 6...
Experiments are carried out in a baffled flat-bottom stirred tank to test live dual-impeller configu...
The fluid mixing process is a common supportive phenomenon that often occurs in a large number of in...
In this paper, the data assembled concerning the agitation of a Newtonian fluid in a cylindrical ves...
The geometry of an impeller is a determining factor in power demand, which in turn determines the co...
Present work compares the mass transfer coefficient (kLa) and power draw capability of stirred tank ...
A study was made of the pumping capacity of pitched blade impellers in a cylindrical pilot plant ves...
Design of the impeller blade is a determining factor in power consumption and mixing quality, which ...
Mixing and mass transfer characteristics of an unbaffled aerated agitation vessel with a liquid heig...
Power consumption of unsteadily forward-reverse rotating multiple impellers, a new cross type of imp...
The rate of gas induction was measured in gas-inducing-type mechanically agitated contactors (GIMAC)...
Rate of gas induction, static pressure, mixing time and power consumption have been measured in 0.57...
Abstract Liquid flow in the impeller swept region of vessels with a turbine-type agitator was examin...
The three-blade combined agitator consists of two propulsion blades of the same type (including plan...
The effectiveness of a range of impellers for "stirring as foam disruption" (SAFD) is assessed in a ...