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Vessel proportions

Performances of dryers with simple flow patterns can be described with the aid of laboratory drying rate data. In other cases, theoretical principles and correlations of rate data are of value largely for appraisal of the effects of changes in some operating conditions when a basic operation is known. The essential required information is the residence time in the particular kind of dryer under consideration. Along with application of possible available rules for vessel proportions and internals to assure adequate contacting of solids and air, heat and material balances then complete a process design of a dryer. [Pg.231]

This procedure specifically addresses drums but can be made applicable to any kind of vessel. The basic question is What vessel proportions, usually expressed as L/D ratio, will give the lowest weight for a given volume The maximum volume for the least surface area, and weight, is of course a sphere. Unfortunately, spheres are generally more expensive to build. Thus, spheres are not the most economical option until you get to very large volumes and for some process applications where that shape is required. [Pg.89]

Optimum Vessel Proportions for Vessels with (2) 2 1 S.E, Heads... [Pg.91]

Taylor designed and constructed in 1898 the first experimental tank for models of war vessels in the USA. The probably greatest achievement of his career was the T lor Standard Series including 80 models by systematically varying vessel proportions and prismatic coefficients. The results of this series are still currently used for a preliminary determination of ship resistance for twin screw, moderate- to high-speed naval boats. The book was revised in 1933 with the addition of data on 40 new models. The series data were reanalysed using more recent methods in 1954. Both books Speed and power, and the mentioned Reanalysis were pubhshed in 1998 by SNAME, the centennial of the Experimental Model Basin. [Pg.877]

Fig. 1) = Sewer duct 2) = Sewage pump 3) = Collecting vessel = Proportioning pump 3) = Distribution unit 6) = Bottle filler 7) = Control unit 8) = Pressure reducer 9) = Air filter 10) = Compressed air 11) = To sewer... Fig. 1) = Sewer duct 2) = Sewage pump 3) = Collecting vessel = Proportioning pump 3) = Distribution unit 6) = Bottle filler 7) = Control unit 8) = Pressure reducer 9) = Air filter 10) = Compressed air 11) = To sewer...
If it is desired to employ fluoboric acid HBF4, it can be prepared by adding 100 g. of A.R. boric acid in small proportions to 325 g. of A.R. hydrofluoric acid (40 p>er cent. HF) cooled in ice the hydrofluoric acid is contained in a Bakelite beaker, a beaker coated with wax or in a lead vessel. A simple container may also be prepared by cutting of the neck of the wax bottle (in which the hydrofluoric acid is supplied) with a large e.g., a butcher s ) knife which has been slightly warmed. One-third of the above solution should be employed in the preparation. Handle unth great care. [Pg.611]

There are three basic requirements that Hquid level control devices are designed to satisfy alarm functions, pump/valve control, and transmitted output signal to track level continuously. Alarm devices provide warning or shutdown functions when process levels pass a predeterrnined point in the vessel pump /valve control devices turn on/off pumps or open/close valves at predeterrnined levels in the vessel and transmitters provide a proportional output signal over a predetermined span to send to a local meter or signal back to a control room. [Pg.207]

Batch extraction of octanoic acid from water and corn syrup into xylene, paraffin oil, and their mixtures baffled vessel, turbine impeller. proportional to... [Pg.1468]

Refer to Fig. 15-41. The extrartor is an extension of the simple baffled mixing vessel into a multistage column. Although commercial apphcation has been made, data are scarce and are limited to towers of small diameter. The preferred proportions are Zt = 0.5df, d, > dj. [Pg.1483]

Of special interest in scale-control systems is the type in which the motion of the scale beam is sensed by a differential transformer or a group of load cells. The output of such devices is proportional to the displacement of the scale beam, which in turn is proportional to the amount of material in the weigh bucket. Many designs use loadsensing devices such as strain gauges or transducers. These eliminate the need for a scale-beam mechanism. The weigh vessel is mounted directly on the load-sensing devices. This provides many benefits in... [Pg.1941]

The forces applied by an impeller to the material contained in a vessel produce characteristic flow patterns that depend on the Impeller geometry, properties of the fluid, and the relative sizes and proportions of the tank, baffles and impeller. There are three principal types of flow patterns tangential, radial and axial. Tangential flow is observed when the liquid flows parallel to the path described by the mixer as illustrated in Figure 7. [Pg.446]


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Procedure 2-16 Optimum Vessel Proportions

Proportioning and Head Selection for Cylindrical Vessels with Formed Closures

Vertical vessels Vessel proportions

Vessel proportions calculating

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