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The pumping arrangements

Recycies shown by broken iines are at base pressure [Pg.445]


What effective pumping speed must the pump arrangement maintain to reduce the pressure in a given vessel over a given time to a desired value ... [Pg.66]

Pg j attainable with the pump arrangement is such that Pg p, the... [Pg.67]

Specifically, system characteristic is the relation of discharge Q and the associated head requirements of this system which, again, does not include the pump arrangement. The pump arrangement may be called the pump assembly. In the design of a pumping station, both the pump characteristics and the system characteristic must be considered simultaneously. [Pg.250]

Pump assembly— The pump arrangement in a pumping station. [Pg.253]

In a 1 litre round-bottomed flask provided with an efficient double surface condenser, place 40 g. (39 ml.) of aniline, 50 g. (40 ml.) of carbon sulphide CAUTION inflammable) (1), and 50 g. (63-5 ml.) of absolute ethyl alcohol (2). Set up the apparatus in the fume cupboard or attach an absorption device to the top of the condenser (see Fig. 11, 8, 1) to absorb the hydrogen sulphide which is evolved. Heat upon an electrically-heated water bath or upon a steam bath for 8 hours or until the contents of the flask sohdify. When the reaction is complete, arrange the condenser for downward distillation (Fig. 11, 13, 3), and remove the excess of carbon disulphide and alcohol (CA UTION inflammable there must be no flame near the receiver). Shake the residue in the flask with excess of dilute hydrochloric acid (1 10) to remove any aniline present, filter at the pump, wash with water, and drain well. Dry in the steam oven. The yield of crude product, which is quite satisfactory for the preparation of phenyl iao-thiocyanute (Section IV.95), is 40-45 g. Recrystalhse the crude thiocarbanihde by dissolving it, under reflux, in boiling rectified spirit (filter through a hot water funnel if the solution is not clear), and add hot water until the solution just becomes cloudy and allow to cool. Pure sj/m.-diphenylthiourea separates in colourless needles, m.p, 154°,... [Pg.642]

Cleaners. Cleaner formulations can be classified with respect to the abiUty to emulsify oils, keep them in solution or to reject oils, spHt them out of solution. The latter type loosens the oil, and the separated oil does not dissolve but is rejected, and usually floats to the top of the cleaner solution. For the cleaner that rejects oil, the tank needs to be skimmed constantly. This is most easily accompHshed usiag the overflow weir, sump, and recirculating pump arrangement. OH-rejecting cleaners last longer. [Pg.149]

Jet Mixers Continuous recycle of the contents of a tank through an external pump so arranged that the pump discharge stream appropriately reenters the vessel can result in a flow pattern in the tank which will produce a slow mixing aciion [Fossett, Trans. Jnst. Chem. Eng., 29,322 (1951)]. [Pg.1631]

Development The following discussion relates specifically to the use of what could be called radial-inflow, centrifugal-pump power-recovery turbines. It does not apply to the type of unit nurtured by the hydroelecti ic industry for the 1 ge-horsepower, large-flow, low- to medium-pressure differential area of hydraulic water turbines of the Felton or Francis runner type. There seems to have been little direct transfer of design concepts between these two fields the major manufacturers in the hydroelectric field have thus far made no effort to sell to the process industries, and the physical arrangement of their units, developed from the requirements of the hydroelectric field, is not suitable to most process-plant applications. [Pg.2525]

A more economical alternative is found in a submersible pump where the pump, directly coupled with the prime mover, is slid into the tubewell through narrow pipes. Narrow pipes are easy to sink into rocky terrain or very deep water levels. They are less expensive and are easy to install due to the elimination of the need for a pump house. Once the unit is slid into the well it requires little maintenance. (See Figures 7.5-7.7.) Such pumps have a standard centrifugal multistage arrangement, and the motors are required to work under water or any other liquid. These motors have an exclusive application for submersible pumps. [Pg.170]

Now wc can see the iniporraiiee of rlie eoneenrrie ellipses of effieieney on the pump family eurve. As mueh as possible we should find a pump whose primary effieieney are eovers the needs of the system. Certainly the needs of the system should fall within the seeond or third effieieney ares around the pump s REP. If the system s needs require the pump to eonsistently run too far to the left or right extremes on its eurve, it may be best to eonsider pumps in parallel, or series, or a eombinarion of the two, or some other arrangement, possibly a PD pump. We ll see this later. [Pg.113]

The following pictures show different arrangements of Environmental Controls. These Controls expand the operational range of the mechanical seal, improving the pump service life. [Pg.214]

Many times, the broken part of a pump is replaced when it tails without an effort to understand why the situation happened. Any corrective action that takes place is usually a temporary arrangement. The probability is quite high that the pump will fail again for the same reason. This part replaeement with no analysis practice is not accepstable due to the high cost of the maintenanee, parts, time and lost produetion. [Pg.227]

The pumps may be driven by any of several drivers. For many years the favorite arrangement has been a steam turbine for the main pump and... [Pg.310]

It should be emphasized at this point that the speed of response is cnti-cal. The pressure transient pressure should not fall to less than 50% of the difference in pressure between the standby pump start pressure and the low oil pressure trip pressure. This is normally achievable with good design practice and the use of a switch and direct wiring. There is some tendency to use a transmitter and control through a remote computer. The latter arrangement is difficult to check on a shop test and normally is too slow to meet the requirement. An accumulator can be added and must be used if the requirement cannot be met. This additional hardware contributes to higher initial cost and possible reliability problems in the future. The direct switch method is therefore highly recommended. [Pg.314]

Commercial versions of PR are available. Other contactless methods of electro-modulation are Electron-Beam Electro-reflectance (EBER) and Contacdess Electroreflectance (CER). In EBER the pump beam of Figure 2 is replaced by a modulated low-energy electron beam (- 200 eV) chopped at about 1 kHz. However, the sample and electron gun must be placed in an ultrahigh vacuum chamber. Contactless electroreflectance uses a capacitor-like arrangement. [Pg.390]


See other pages where The pumping arrangements is mentioned: [Pg.47]    [Pg.158]    [Pg.62]    [Pg.757]    [Pg.177]    [Pg.64]    [Pg.445]    [Pg.47]    [Pg.158]    [Pg.62]    [Pg.757]    [Pg.177]    [Pg.64]    [Pg.445]    [Pg.1985]    [Pg.20]    [Pg.485]    [Pg.626]    [Pg.791]    [Pg.315]    [Pg.99]    [Pg.45]    [Pg.55]    [Pg.292]    [Pg.472]    [Pg.1472]    [Pg.1688]    [Pg.2495]    [Pg.2532]    [Pg.170]    [Pg.71]    [Pg.122]    [Pg.125]    [Pg.186]    [Pg.291]    [Pg.299]    [Pg.230]    [Pg.311]    [Pg.312]    [Pg.320]   


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The Pump

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