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Powder flow rate

Powder flow rate was determined using a glass funnel. The volume before and after tapping (AF=F10-F500) was measured with an Eberhard Bauer (J.Engelsmann AG) tapping volume meter [14-16]. [Pg.45]

The area under the dissolution curve (AUC=T6), was chosen as the major response to be optimized. Nevertheless, the results showed that it is necessary to study several properties to define the best formulation adequate powder flow, compression behaviour and particularly, a minimal variability of the dissolution parameters [3]. It was noted that good powder flow rate is not always related to an adequate compression behaviour [4]. [Pg.59]

Waste powder Flow rate of gases (1/min) Power (kW) Feed rate (g/min) tfspec (kWh/g)... [Pg.227]

In the continuous drying of BALL POWDER, dewatered powder is fed into a series of vibrating pan conveyors. Fresh air is preheated and blown into an air distribution manifold where tubes direct the air flow into the powder. An aerated bed is obtained by controlling the powder flow rate, the pan conveyor vibration speed, and the heated air supply. The air supplies the heat for evaporating the water. The water vapor is removed with the exhaust air by vacuum transfer. [Pg.176]

Anhydrous citric acid and NaHCOs were granulated with ethanol in a twin-screw extruder at powder flow rates of 60-90 kg/h in a continuous processJ The air suspension coating-reacting technique also is used in the production of effervescent granulates. [Pg.1462]

Crowder, T.M. Hickey, A.J. A semiconductor strain gauge based instrument for rapid powder flow rate measurement. Respiratory Drug Delivery 1998, 6, 297-298. [Pg.3295]

The powder flow rate (a material property) of the API (a material) has an average value of 1 g/s within the range of [0.8, 1.2]. The somce of the reported value was the experiment API Flow Measurement at a given context (78% relative humidity) The collection of the different concepts e.g. material, material property etc and their relation e.g. has Value, comprise an ontology. [Pg.86]

Conical nozzles use deflectors to generate a cone-shaped pattern as shown in the schematic in Fig. 7. Pattern widths can vary from as small as about 2.5 cm (1 in.) to approximately 60 cm (2 ft) in diameter, depending on the size and the radius of the deflector. The size of the pattern also depends on the powder flow rate. Conical nozzles generate a softer spray pattern because the deflector creates a partial vacuum that pulls the inner part of the cone pattern toward itself This reduces the forward velocity of the powder. Conical nozzles are usually used in manual coating operations, where they are used for large flat parts and complex shapes. [Pg.2411]

Figure 8. Pulse adsorptions following sequential injections of 20 pi of 0.01 molar aqueous solution of K2PtCl6 (0.2 pmol) into water percolating throught 25.8 mg of graphitised carbon black mixed with PTFE powder. Flow rate of water - 3 mlh, temperature - 20°C. Figure 8. Pulse adsorptions following sequential injections of 20 pi of 0.01 molar aqueous solution of K2PtCl6 (0.2 pmol) into water percolating throught 25.8 mg of graphitised carbon black mixed with PTFE powder. Flow rate of water - 3 mlh, temperature - 20°C.
Masuda and Matsusaka (1994) have developed a fiow meter to measure powder flow rates using electrostatic measurements. The method depends on the impact of the particles with the inside of the tube wall where a current is generated. The initial charge on the particles can be eliminated by using two metallic pipes whose inner surfaces are coated with different materials. The pipe is 6 mm in diameter and carries fly ash. The powder flow rate and the mean particle-charge value could be measured simultaneously. [Pg.635]

Klinzing GE, Dhodapkar SV, Plasynski SI. NEPTIS-3. Electrostatic Measurement of Powder Flow Rate in Gas-Solids Pipe Flow. Nov. Nisshin Engr, 1994, p 21. [Pg.642]

Polyacrylate superabsorbent powders — Determination of polymer content by powder flow rate and bulk density by timed flow through a defined funnel and gravimetric measurement NWSP 251.0.R2 (15) ISO 17190-8 2001 -f ISO 17190-9 2001. [Pg.207]

Since a powder assembly can generally be regarded as a biphasic system the permeability of a powder, or the ability of a gas to pass through a collection of particles or bed of powder, has now been recognised as a bulk powder property. The magnitude of permeability as a function of bulk density may be used in the determination of the powder flow rate and discharge of powders from hoppers. [Pg.24]

A recommended powder flow rate is between 25 and 32 s for a 100 g sample although higher flow rates can be tolerated for large simple part shapes that do not have a lot of fine surface detail. [Pg.329]


See other pages where Powder flow rate is mentioned: [Pg.23]    [Pg.129]    [Pg.711]    [Pg.47]    [Pg.58]    [Pg.60]    [Pg.182]    [Pg.156]    [Pg.906]    [Pg.21]    [Pg.271]    [Pg.115]    [Pg.116]    [Pg.2346]    [Pg.2409]    [Pg.2410]    [Pg.2411]    [Pg.80]    [Pg.2329]    [Pg.104]    [Pg.582]    [Pg.46]    [Pg.47]    [Pg.459]   
See also in sourсe #XX -- [ Pg.297 ]




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