In the starting section of a pneumatic conveyor the material accelerates from the zero starting velocity to the velocity of the uniform conveyance section. In the case of thin flow conveying the pressure drop needed for material acceleration is of a considerable value compared with other pressure drops. In the case of short (15 to 25 m) conveying it forms the greatest part of additional pressure drops. Furthermore, in a vertical starting section the pressure drop needed to lift the weight of the material is higher than in the uniform velocity section
A study was conducted to determine the pressure drop gradient in a straight horizontal pipe for dens...
Experiments are described on the pneumatic conveying of 2.7mm alumina particles up a vertical riser ...
This work is focused on dilute and dense phase pneumatic conveying of bulk solids. The motivation of...
In the starting section of a pneumatic conveyor the material accelerates from the zero starting velo...
In this paper the authors present a procedure for determining pressure drop caused by ...
In this paper a computing method is described for the approximate determination of pressure drop in...
This thesis is a contribution to the dilute-phase pneumatic conveying analysis. The survey of the k...
The main objective of this investigation was to formulate a comprehensive scaling up technique for d...
Pneumatic conveying is being selected for an increasing number of industrial applications and produc...
This study was initiated by the need to improve current techniques used in the design of pneumatic c...
This paper presents a steady state one-dimensional two-fluid model for gas-solid two-phase flow in a...
The main objective of this investigation was to formulate a comprehensive scaling up technique for d...
An accurate estimation of the total pipeline air pressure drop is considered widely to be one of the...
This article results from an ongoing investigation aimed at developing a new validated test-design p...
In this paper physical parameters necessary to dimensioning equipment of pneumatic conveying of grea...
A study was conducted to determine the pressure drop gradient in a straight horizontal pipe for dens...
Experiments are described on the pneumatic conveying of 2.7mm alumina particles up a vertical riser ...
This work is focused on dilute and dense phase pneumatic conveying of bulk solids. The motivation of...
In the starting section of a pneumatic conveyor the material accelerates from the zero starting velo...
In this paper the authors present a procedure for determining pressure drop caused by ...
In this paper a computing method is described for the approximate determination of pressure drop in...
This thesis is a contribution to the dilute-phase pneumatic conveying analysis. The survey of the k...
The main objective of this investigation was to formulate a comprehensive scaling up technique for d...
Pneumatic conveying is being selected for an increasing number of industrial applications and produc...
This study was initiated by the need to improve current techniques used in the design of pneumatic c...
This paper presents a steady state one-dimensional two-fluid model for gas-solid two-phase flow in a...
The main objective of this investigation was to formulate a comprehensive scaling up technique for d...
An accurate estimation of the total pipeline air pressure drop is considered widely to be one of the...
This article results from an ongoing investigation aimed at developing a new validated test-design p...
In this paper physical parameters necessary to dimensioning equipment of pneumatic conveying of grea...
A study was conducted to determine the pressure drop gradient in a straight horizontal pipe for dens...
Experiments are described on the pneumatic conveying of 2.7mm alumina particles up a vertical riser ...
This work is focused on dilute and dense phase pneumatic conveying of bulk solids. The motivation of...