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Orifice multiple

The spinnerets in a production line assembly consist of multiple groupings of orifices thus the number of fibers from a single spinning ceU can vary. AU three spinning techniques mentioned above commonly employ spinning lines that carry as many as 250 fibers (sometimes referred to as a rope) drawn from a single multiorifice spinneret. [Pg.148]

The two principal elements of evaporator control are evaporation rate a.ndproduct concentration. Evaporation rate in single- and multiple-effect evaporators is usually achieved by steam-flow control. Conventional-control instrumentation is used (see Sec. 22), with the added precaution that pressure drop across meter and control valve, which reduces temperature difference available for heat transfer, not be excessive when maximum capacity is desired. Capacity control of thermocompression evaporators depends on the type of compressor positive-displacement compressors can utilize speed control or variations in operating pressure level. Centrifugal machines normally utihze adjustable inlet-guide vanes. Steam jets may have an adjustable spindle in the high-pressure orifice or be arranged as multiple jets that can individually be cut out of the system. [Pg.1148]

Spray characteristics of pressure nozzles depend on the pressure and nozzle-orifice size. Pressure affects not only the spray characteristics but also the capacity. If it is desired to reduce the amount of liquid sprayed by lowering the pressure, then the spray may become coarser. To correct this, a smaller orifice would be inserted, which might then require a higher pressure to produce the desired capacity, and a spray that would be finer than desired might result. Multiple nozzles tend to overcome this inflexible charac teristic of pressure atomization, although several nozzles on a diyer complicate the chamber design and air-flow pattern and risk collision of particles, resulting in nonuniformity of spray and particle size. [Pg.1233]

Bubble sizes at formation generally increase with surface tension and orifice diameter. Prediction of sizes in swarms from multiple orifices is difficult. In aqueous solutions of low surface tension, Bubble diameters of the order of 1 mm are common. Bubbles produced by the more complicated techniques of pressure flotation or vacuum flotation are usually smaller, with diameters of the order of 0.1 mm or less. [Pg.2019]

Sedimentation Tanks These tanks are an integral part of any activated-sludge system. It is essential to separate the suspended solids from the treated liquid if a high-quality effluent is to be produced. Circular sedimentation tanks with various types of hydraulic sludge collectors have become the standard secondary sedimentation system. Square tanks have been used with common-wall construc tion for compact design with multiple tanks. Most secondary sedimentation tanks use center-feed inlets and peripheral-weir outlets. Recently, efforts have been made to employ peripheral inlets with submerged-orifice flow controllers and either center-weir outlets or peripheral-weir outlets adjacent to the peripheral-inlet channel. [Pg.2221]

Number of Valves Required - Normally a manufacturer s standard PR valve with Drifdce area equal to or larger than the calculated requirement is specified. In some cases, e.g., large reheving rates or to prevent chattering, two or more valves are necessary. Likewise, if there is an appreciable difference between the calculated orifice size and the available size, multiple PR valves are desirable to more nearly match the available area to the required orifice area. The column for "spares" indicates the requirement, if any, for spare PR valves installed on the equipment. Normally, this applies only in the case of refinery preference or local regulations, but is required in many European countries. [Pg.195]

Sivakumar and Pandit [13] reported the use of hydrodynamic cavitation for decolorization of dye effluent stream. It has been observed that for same flow area, plate with larger number of small diameter holes gives higher extent of color removal as compared to the plate with smaller number of larger diameter holes. The observed results have been explained on the basis of frequency of turbulence for the two cases. The hydrodynamic cavitation reactor using multiple hole orifice plates has been found to give cavitational yields, which are two times higher than the best acoustic cavitation device (Dual frequency flow cell with capacity of 1.5 L). [Pg.96]

Pipe Orifice Area of a Single Safety Relief in Vapor Service/ Should Not Exceed 2X of the Cross Sectional Area of the Protected Line. 0 Multiple Valves with Staggered Settings May be Required. [Pg.370]

Multiple sprayer ion source with rotatory ion beam chopper (MUX) (performed by instrument maker) Place two to four sprayers in same interface housing each sprayer receives effluent of HPLC spinning chopper protects orifice of MS to allow ions only from one sprayer to enter at a time special MS program separates data from sprayers HPLCs operated in parallel and simultaneously... [Pg.139]

The plates may be any of several types, including sieve, bubble-cap, and valve trays. Valve trays constitute multiple self-adjusting orifices that provide nearly constant gas pressure drop over considerable ranges of variation in gas flow. The gas pressure drop that can be taken across a single plate is necessarily limited, so that units designed for high contacting power must use multiple plates. [Pg.42]


See other pages where Orifice multiple is mentioned: [Pg.1417]    [Pg.101]    [Pg.107]    [Pg.1240]    [Pg.1421]    [Pg.2860]    [Pg.1417]    [Pg.101]    [Pg.107]    [Pg.1240]    [Pg.1421]    [Pg.2860]    [Pg.411]    [Pg.513]    [Pg.135]    [Pg.251]    [Pg.1592]    [Pg.1592]    [Pg.1594]    [Pg.1641]    [Pg.190]    [Pg.190]    [Pg.21]    [Pg.265]    [Pg.148]    [Pg.392]    [Pg.21]    [Pg.245]    [Pg.914]    [Pg.837]    [Pg.79]    [Pg.93]    [Pg.95]    [Pg.96]    [Pg.97]    [Pg.58]    [Pg.81]    [Pg.38]    [Pg.363]    [Pg.11]    [Pg.56]    [Pg.409]   
See also in sourсe #XX -- [ Pg.333 ]




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