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MAINTENANCE CENTRIFUGE

All rotating equipment will exhibit certain harmonic frequencies upon acceleration and deceleration of the unit. It is the speed at which the frequency of rotation equals the natural frequency of the rotating part. They can be [Pg.583]


Ekk, B. Designing and Maintenance Centrifugal and Axial Fans. Translation from German. M. Technical Publishing 1959. [Pg.72]

Gas turbine driven centrifugal compressors are very efficient under the right operating conditions but require careful selection and demand higher levels of maintenance than reciprocating compressors. Compression facilities are generally the most expensive item in an upstream gas process facility. [Pg.253]

A new countercurrent continuous centrifugal extractor developed in the former USSR (214) has the feature that mechanical seals are replaced by Hquid seals with the result that operation and maintenance are simplified the mechanical seals are an operating weak point in most centrifugal extractors. The operating units range between 400 and 1200 mm in diameter, and a capacity of 70 m /h has been reported in service. The extractors have been appHed in coke-oven refining (see Coal conversion processes), erythromycin production, lube oil refining, etc. [Pg.77]

Example 3. A centrifugal pump moving a corrosive Hquid is known to have a time-to-failure that is well approximated by a normal distribution with a mean of 1400 h and a standard deviation of 120 h. A particular pump has been in operation for 1080 h. In order to plan maintenance activities the chances of the pump surviving the next 48 h must be deterrnined. [Pg.9]

The primaiy advantages of a centrifugal pump are simplicity, low first cost, uniform (nonpulsating) flow, smaU floor space, low maintenance expense, quiet operation, and adaptability for use with a motor or a turbine drive. [Pg.902]

Regardless of the machine device, centrifuges are typically maintenance-intensive. Filters can be cheaper in terms of capital and maintenance and should be considered first unless centrifugal equipment already exists. Small facilities (<1000 liters) use filtration, since centrifugation scale-down is constrained by equipment availability. Comparative economics of the two classes of operations are discussed by Datar and Rosen (loc. cit.). [Pg.2058]

The most common maintenance problem with centrifugal pumps is with the seals. Mechanical seal problems account for most of the pump repairs in a chemical plant, with bearing failures a distant second. The absence of an external motor (on canned pumps) and a seal is appeahng to those experienced with mechanical seal pumps. [Pg.2309]

Existing maintenance procedures must be reviewed for several reasons. Typically, these are established based upon manufacturers recommended practices for stock equipment such as pumps, centrifuges and some reactors. However, a new toll can introduce special cleaning and preparation steps as well as possible material of construction incompatibilities. If the toller is using new equipment, special maintenance practices and tools may also be required. [Pg.86]

Since there is only one winding and the poles are already shaded at one particular end, the direction of the rotating flux is fixed and so is the direction of rotation of the rotor. The direction of rotation cannot be altered as in the earlier cases. Since there is only one winding and no need of a speed-operated centrifugal switch, these motors require almost no operational maintenance. [Pg.29]

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]

Intended for graduate engineers, maintenance engineers, end -users and those needing an accessible account of centrifugal pumps, this booh explains it alU... [Pg.253]

Ai the risk of misleading the reader, this section will just touch a few points concerning maintenance. One frequently asked question is, what is critical and what needs special consideration when performing maintenance on the centrifugal compressor While there are many areas that... [Pg.221]


See other pages where MAINTENANCE CENTRIFUGE is mentioned: [Pg.20]    [Pg.317]    [Pg.583]    [Pg.810]    [Pg.20]    [Pg.317]    [Pg.583]    [Pg.810]    [Pg.412]    [Pg.415]    [Pg.153]    [Pg.74]    [Pg.291]    [Pg.404]    [Pg.411]    [Pg.335]    [Pg.322]    [Pg.472]    [Pg.335]    [Pg.91]    [Pg.229]    [Pg.229]    [Pg.926]    [Pg.1110]    [Pg.1117]    [Pg.1565]    [Pg.1590]    [Pg.1714]    [Pg.1743]    [Pg.1743]    [Pg.2058]    [Pg.2222]    [Pg.99]    [Pg.221]    [Pg.48]    [Pg.134]    [Pg.198]    [Pg.198]    [Pg.337]   


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