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Mandrel pointed

Having established the correct flow of lead, a pipe is first extruded and its wall thickness gauged. Any undue variations may be obviated by radially adjusting the die with the help of the centering screws. The wall thickness of the sheathing is obtained by axially adjusting the mandrel-point and the mandrel-holder respectively, with the help of the rear screwed joint. [Pg.25]

However, this adjustment is limited and depends on the angle ol of the mandrel point. [Pg.25]

If thick-walled tubes with small inside diameters, such as hollow copx)er bars for stud bolts, are to be extruded from the same container, tools with a pointed mandrel, as per sketch b, are employed. The operation is the same as that described above. The stripper stroke is somewhat longer, because the advance motion of the mandrel in this case is shorter than that in sketch a by the length of the mandrel point projecting over the dummy-block. [Pg.148]

Cutting bushing (2) blow mandrel point (3) stripper for neck flash (4) preblow tubing (5) cutting insert (6) cutting ring (striker plate)... [Pg.144]

Figure 17 Viewgraph of the geometrical configuration of an eight-point star mandrel. Figure 17 Viewgraph of the geometrical configuration of an eight-point star mandrel.
The nozzle of original design was fabricated from a niobium alloy coated with niobium silicide and could not operate above 1320°C. This was replaced by a thin shell of rhenium protected on the inside by a thin layer of iridium. The iridium was deposited first on a disposable mandrel, from iridium acetylacetonate (pentadionate) (see Ch. 6). The rhenium was then deposited over the iridium by hydrogen reduction of the chloride. The mandrel was then chemically removed. Iridium has a high melting point (2410°C) and provides good corrosion protection for the rhenium. The nozzle was tested at 2000°C and survived 400 cycles in a high oxidizer to fuel ratio with no measurable corrosion.O l... [Pg.445]

The variable ERRORmj n represents the error in the position of the mandrel over an increment in TIME, in seconds. ERRORman is calculated by subtracting the actual pulses accumulated, PULSEman, from the desired number of pulses that would be generated under perfect control. The desired number of pulses for perfect control is determined by the set point speed, RPSman, revolutions per second and the mechanical gear reduction. The constant 15630 is the product of encoder counts per revolution and the thirty to one gear reduction of the mandrel. [Pg.541]

The speed of the motor for the mandrel is accurately controlled to at least 0.1% of the set point speed. The gain, Kman, was selected to be. 1 by observing an acceptable response to a 10% change in the set-point. [Pg.541]

At the start of the wind, the mandrel is also positioned at a reference point. For the initial pass the change in mandrel position is proportional to the counts. For subsequent peisses, a reference PU LS Em AN REF is determined. It is the count at the start of the pass. The rotational, incremental change of the mandrel can then be determined by subtracting PULSEman REF from the actual count PULSEman-... [Pg.545]

In order to complete the problem, the initial and boundary conditions must be given. The temperature and degree of cine or crystallinity must initially (at time zero) be specified at every point inside the composite and the mandrel. For the latter only the temperature is required. As boundary conditions, the temperatures or heat fluxes at the composite outside diameter and mandrel inner diameter must be specified. [Pg.401]

Fiber jet speed and material elasticity are two of the most important parameters involved in the jet-mandrel interaction and each of these properties are influenced by multiple electrospinning parameters, such as solution conductivity, viscosity, voltage, and feed rate. In addition, material properties cannot be accurately predicted without knowing the exact degree of solvent evaporation at the point when fibers are taken up by the collector. [Pg.180]

For monofilament samples, the apparatus shown in Figure 2 is used to load the sample in tension (11). The monofilament is wound around a split cylindrical mandrel, half attached to the fixed lintel and half attached to the loading rod. The sample is attached to the mandrel at two points and is free to move around the mandrel as the sample is extended under load. [Pg.56]

Most blown film operations extrude the resin in an upward direction. However, blown polypropylene film is generally extruded downwards and water or mandrel quenched. The extruded tube is then reheated, to a point still below its melt temperature, before it is blown. The collapsed bubble can be fed over a series of heated rollers to reheat it and relieve thermal stresses if a heat-stabilized film is wanted or it can be heated and reinflated in what is known as the double bubble process, which will be discussed in Section 7.3.7. In either case, the film is restrained until cooling is complete, to keep it from shrinking. [Pg.228]

Dwell In filament winding, the time that the transverse mechanism is stationary while the mandrel continues to rotate to the appropriate point for the traverse to begin a new pass. [Pg.391]

Some special dies are shown in Fig. 3-20 they produce interesting flow patterns and products such as tubular to flat netting dies. For a circular output, a counter-rotating mandrel and orifice have semicircular-shaped slits through which the melt flow emerges. If one part is held stationary, then a rhomboid or elongated pattern is formed if both parts rotate, then a true rhombic mesh is formed. When the slits overlap, a crossing point is formed... [Pg.125]

It is clearly essential to separate the formed product from the mandrel without damage to the product and, if possible, to the mandrel since it can then be re-used. This is generally accomplished by using a cathode which is covered by a natural or chemically induced thick oxide layer. Suitable materials include titanium, chromium and steel. For some products, their shape predetermines that a permanent mandrel cannot be used. Non-permanent mandrels have to be constructed of a material which can be removed from the inside of the product and several techniques have been used. The non-permanent mandrel may be made from a low-melting-point metal (e.g. Zn, A1 or their alloys), a metal which may be removed by chemically etching or a non-metallic material (e.g. perspex, PVC or epoxy resins) soluble in organic solvents and plated by electrodeless deposition with a layer of silver or copper to make it conducting. [Pg.202]

After cure the component is removed from the mandrel either by collapsing the mandrel or by a mechanical puller device, typically hydraulic to generate sufficient force. Complex shapes may not allow the mandrel to be withdrawn. This problem may be overcome by the use of a collapsible mandrel or by producing the mandrel from a meltable material such as low melting point alloys or wax. [Pg.274]


See other pages where Mandrel pointed is mentioned: [Pg.36]    [Pg.36]    [Pg.420]    [Pg.312]    [Pg.8]    [Pg.718]    [Pg.481]    [Pg.542]    [Pg.542]    [Pg.545]    [Pg.200]    [Pg.806]    [Pg.214]    [Pg.328]    [Pg.31]    [Pg.312]    [Pg.152]    [Pg.292]    [Pg.484]    [Pg.97]    [Pg.200]    [Pg.201]    [Pg.1080]    [Pg.162]    [Pg.291]    [Pg.632]    [Pg.306]    [Pg.219]    [Pg.250]    [Pg.34]    [Pg.108]    [Pg.114]    [Pg.249]    [Pg.66]   
See also in sourсe #XX -- [ Pg.148 ]




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