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Modification to the nozzle

Most previous attempts to obtain X-ray diffraction data at very low temperatures (< 80 K) have used custom built systems with closed cycle helium refrigerators mounted on large, robust four circle diffractometers. In order to remove the inherent disadvantages of these systems - cost, single application, absorption and scattering of the windows - we have built an open flow system from mainly off-the-shelf components which uses liquid helium as the cryogen. This is not the first open flow helium system [19, 20] but is the first that is mainly off-the-shelf and is mountable on any diffractometer. It is based on an ADP Helitran ESR cryostat with modifications to the nozzle assembly and to the direction of the gas flow. The lowest temperature is estimated to be <30K. At the current price for liquid helium in... [Pg.230]

If the nozzle cannot be modified for technical flow or economic reasons, the remedial measures will be identical to the measures listed under 2.1 The degree to which possible modifications to the nozzle have to move to compensate the increased pressure level P2 is shown by the straight line AlPl. A/A 1 corresponds to the necessary shortening of the nozzle which has to be carried out to achieve the pressure level PI without extending the screw. [Pg.194]

A liquid draining through a nozzle can initiate a vortex if the liquid level is low and the drainage rate is high. This relationship is quantified in Figure 21-1. If calculations indicate a KO drum is carrying over due to vortexing, a simple modification to the nozzle inside the tower will break the vortex. [Pg.465]

An important consideration in the choice of a dispensing method is the shape of the parts to be bonded. Within the constraints imposed by the performance of the selected adhesive, early considerations of manufacturing problems caused by the shape of the bond area are wise. The engineer should keep in mind that modifications to the adhesive are sometimes possible and these changes may allow the use of a more suitable means of application. For instance, in some cases, solvents may be used to allow the use of spraying methods. Mild application of heat may reduce viscosities so products will flow satisfactorily through rather small nozzles. [Pg.456]

Note that the S-shaped grade efficiency curves do not necessarily start from the origin—in applications with a considerable underflow to throughput ratio (by volume) R, the grade efficiency curves tend to the value G x) = / f as X —> 0. This is a result of the splitting of the flow, or dead flux that carries even the finest solids into the underflow in proportion to the volumetric split of the feed. Section 3.4 discusses possible modifications to the efficiency definitions which account for the volumetric split and illustrate only the net separation effect. Such reduced efficiencies are widely used for hydrocyclones and nozzle-type disc centrifuges where large diluted underflows occur. [Pg.70]

FIG. 33 Modifications in the nozzle design resulting in further reductions in the temperature gradients achieved on the FA controller card with the RSF oven. Not only was the gradient reduced in the reflow zone from 40 to 10°C, but the gradient was reduced from 50 to 25°C in the preheat/soak portion of the profile. (From Ref 22.)... [Pg.617]

This model is a modification of the model developed by Kumar and Kuloor (K18) for bubble formation in inviscid fluids in the absence of surface-tension effects. The need for modification arises because the bubble forming nozzles actually used to collect data on bubble formation in fluidized beds differ from the orifice plates in that they do not have a flat base. Under such conditions the bubble must be assumed to be moving in an infinite medium and the value of 1/2 is more justified than the value 11/16. [Pg.320]

It is apparent that effects of eddy currents and general air turbulence might be approximated by modifying Equations 10 and 14. Modifications of the basic equations could possibly account for solute effects. Extension of the theory to nonaqueous solvents requires the appropriate evaluation of Ap and K. Momentum imparted by vertical spray nozzles affects the time required for droplets to reach terminal fall velocity (II). Helicopter and fixed-wing aircraft impart a downward vector to the bulk of the spray and also produce a turbulent effect on the time of droplet fall and should be accounted for. [Pg.153]

The material in Chapter 4, on finite-rate chemistry in flows with negligible molecular transport, has been amplified to a lesser extent beyond the presentation in the first edition. The discussions of ignition delay and of the well-stirred reactor have been expanded somewhat, and a treatment of two-phase nozzle flow has been added, while elsewhere in the chapter modifications in the writing have been restricted to updating of ideas. [Pg.702]

The internal modifications to retrofit the distillation system consider the distillation column and its internals. In this level of retrofit, some changes are made in the internals or nozzles of the main column and the side strippers. Moreover, the reboilers and pump around loops are examined and adjusted as required. Therefore, more complex modifications are required at this level that lead to higher investments. The objective of these modifications is to find out the ideal distribution of stages for each section in the main column [4]. This ideal design is applied to the existing column by modilying its internal to the niinimrim extent to reduce the costs. [Pg.172]


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