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Simple pressurization

The pressure equipment directive was adopted by the European Parliament and the European Council in May 1997. It harmonises the national laws of the 15 Member States of the European Union relating to equipment subject to the pressure risk. That directive is one of the series of technical harmonisation directives such as for machinery, medical devices, simple pressure vessels, gas appliances and so on, which were foreseen by the Communities programme for the elimination of technical barriers to trade. It therefore aims to ensure the free placing on the market and putting into service of the equipment concerned within the European Union and the European Economic Area. At the same time it permits a flexible regulatory environment, allowing European industry to develop new techniques increasing thereby its international competitiveness. [Pg.937]

Certain types of equipment are specifically excluded from the scope of the directive. It is self-evident that equipment which is already regulated at Union level with respect to the pressure risk by other directives had to be excluded. That is the case with simple pressure vessels, transportable pressure equipment, aerosols and motor vehicles. Other equipment, such as carbonated drink containers or radiators and piping for hot water systems are excluded from the scope because of the limited risk involved. Also excluded are products which are subject to a minor pressure risk which are covered by the directives on machinery, lifts, low voltage, medical devices, gas appliances and on explosive atmospheres. A further and last group of exclusions refers to equipment which presents a significant pressure risk, but for which neither the free circulation aspect nor the safety aspect necessitated their inclusion. [Pg.941]

The pressure versions of the nutsche filter, which falls into this category, are either simple pressurized filter boxes or more sophisticated agitated nutsches, much the same in design as the enclosed agitated vacuum filters described eadier. These are extremely versatile, batch-operated filters, used in many industries, eg, agrochemistry, pharmaceuticals, or dyestuff production. [Pg.402]

Gauge pressure is the pressure indieated on a simple pressure gauge. Simple pressure gauges establish an artificial zero reference at atmo,spheric pressure. The formula is psig = psia - ATM. [Pg.5]

What is more important to us is the differential pressure inside the tire compared to outside the tire (atmospheric pressure). For reasons such as these, the world has adopted a second and artificial zero, at atmospheric pressure as a reference point. This is why a simple pressure gauge will read zero at atmospheric pressure. [Pg.7]

Because simple pressure gauges are made with an artificial zero at atmospheric pressure, this is why the term psig exists, meaning pounds per square inch gauge. As mentioned earlier, the psig is equal to the absolute pressure minus the atmospheric pressure. [Pg.7]

Pressures less than atmospheric are recorded as negative pressures (-psi) on a simple pressure gauge. [Pg.7]

The original steam generators were simple pressure vessels that were prone to caiasirophic failures and loss of life. Due to better boiler design, tube-fired boilers, and boiler inspections, the incidence of catastrophic failure is now to a rare event (about once every 100,000 vessel-years). In Great Britain in 1866, there were 74 steam boiler explosions causing 77 deaths. This was reduced to 17 explo.sions and 8 deaths in 1900 as a result of inspections performed by the Manchester Steam User Association. In the United States, the American Society of Mechanical Engineers established the ASME Pressure Ves.sel Codes with comparable reductions. [Pg.2]

Simple pressure/drag flow. Here we treat an idealization of the down-channel flow in a melt extruder, in which an incompressible viscous fluid constrained between two boundaries of infinite lateral extent (2). A positive pressure gradient is applied in the X-direction, and the upper boundary surface at y - H is displaced to the right at a velocity of u(H) - U this velocity is that of the barrel relative to the screw. This simple problem was solved by a 10x3 mesh of 4-node quadrilateral elements, as shown in Figure 1. [Pg.272]

Figure 7.6 shows a schematic set up for TPD. The crystal, mounted on a manipulator in an ultrahigh vacuum chamber, is heated such that the temperature increases linearly in time. The concentration of desorbing species is monitored with a mass spectrometer or with a simple pressure gauge. [Pg.274]

Gas-expanded liquids (GXLs) are emerging solvents for environmentally benign reactive separation (Eckert et al., op. cit.). GXLs, obtained by mixing supercritical CO2 with normal liquids, show intermediate properties between normal liquids and SCFs both in solvation power and in transport properties and these properties are highly tunable by simple pressure variations. Applications include chemical reactions with improved transport, catalyst recycling, and product separation. [Pg.18]

Drum or simple pressure vessel (basic symbol) ... [Pg.910]

Interest in the pressure dependence of structural relaxation in fluids has been stimulated by recent applications [175, 176] of a simple pressure analogue of the VFTH equation for the relaxation time x at a constant pressure P to the analysis of experimental data at variable pressures. Specifically, x(P) for both polymer and small molecule fluids has been found to extrapolate to infinity at a critical pressure Pg, and this divergence takes the form of an essential singularity,... [Pg.189]

Pressure Test The performance of the LC pump depends on the proper functioning of the pump seal, check valves, and proper connection of the tubing. Properly functioning pump seal check valves and tubing connections are important in maintaining stable mobile-phase flow and system pressure. For pump systems that output the pressure reading in the pump head over time, a simple pressure test can be a useful qualitative test to check the performance of the seals and check valves and to determine whether or not there are any leaks in the system [9]. When performing the pump pressure test, make sure that the system is well primed so that no bubbles are present in the pump system. The pressure fluctuation caused by the presence of air bubbles in the pump will lead to misinterpretation of the test results. [Pg.176]

If you also want to finds, then choose a simple pressure, such as P = 100 torr (so that log/ = 2.000) and the corresponding value of 1/7 (it turns out to be 0.003075), and substitute them into.the basic equation along with the calculated value of the slope (-2.22 x 10 ), t0 glVe ... [Pg.71]

Since homogenous melts are covered in a later account of pressure build-up and power input in the extruder (Chapter 7), this chapter confines itself to the flow behavior of homogenous unfilled polymer melts and on the introduction of the most important rheological parameters such as viscosity, shear thinning, elasticity, and extensional viscosity. The influence of these rheological properties on simple pressure- and drag flows is demonstrated, while the influence of rheological parameters on pressure build-up and power input in the extruder is described in more detail in Chapter 7. [Pg.35]

Really, conducted in present work X-ray diffraction study of HxGaSe crystals at T - 300K shown that parameter Co growth with x and at x = 1.0 increased by 0.031+0.003 A from C0 = 15.94A to Co = 15.971A. It is in 2.5 times greater that one can estimate from our simple pressure extrapolation. At the same time one can observe an unsignificant growth of a crystal lattice parameter a, with x. Thus for... [Pg.328]

Sugden s method appears to combine the advantages of speed, simplicity, and accuracy to a greater extent than any other method and it has the advantage that a fresh liquid surface is formed for each determination, so that there is little risk of contamination. Theoretically the bubbles must be formed slowly, but in practice no change in the pressure reading occurs if the rate is reduced below about two per second, with pure liquids. If a simple pressure controlling device is used to blow the liquids over,... [Pg.375]

The corresponding code for simple pressure vessels in United Kingdom3 is contained in the Statutory Instrument 1991, No. 2749. The schedule 1 consists of essential safety requirements. Some of the essential features covered by the Statutory Instrument are ... [Pg.178]

The British (UK) Simple Pressure Vessels (safety) Regulations, Statutory Instrument, 1991, No. 2749. [Pg.199]

A great advantage of supercritical fluids is the possibility to separate the extracted solute from the solvent by simple pressure reduction to subcritical pressures. The solubility of most solutes in supercritical fluids virtually vanishes and therefore the solutes precipitate at these conditions. For example, pyrene solubil-... [Pg.229]

Figure I shows the overall costs K for Process 3 as a function of the separation pressure p for extraction temperatures between 40 and 100C. As the separation pressure increases, the overall costs K decrease. The saving in mechanical work outweighs the effect of more unfavourable separation conditions at higher separation pressures. The process is more efficient because no heating is necessary, and ftirthermore, simple pressure release results in a temperature favourable for separation. The same trend is observed when energy costs for mechanical work are about 25 % higher or lower, i. e. 0.10 DM/kWh or 0.16 DM/kWh.. Figure I shows the overall costs K for Process 3 as a function of the separation pressure p for extraction temperatures between 40 and 100C. As the separation pressure increases, the overall costs K decrease. The saving in mechanical work outweighs the effect of more unfavourable separation conditions at higher separation pressures. The process is more efficient because no heating is necessary, and ftirthermore, simple pressure release results in a temperature favourable for separation. The same trend is observed when energy costs for mechanical work are about 25 % higher or lower, i. e. 0.10 DM/kWh or 0.16 DM/kWh..
Figure 2.5 The zone 2 concept according to VDE 0165/1991-02. Requirements for electrical apparatus with arcs or sparks in normal operation and/or temperatures exceeding a defined limit/temperature class. Two types of protection are defined here the schwadensicheres Gehause , comparable with a restricted breathing enclosure , and simple pressurization . Figure 2.5 The zone 2 concept according to VDE 0165/1991-02. Requirements for electrical apparatus with arcs or sparks in normal operation and/or temperatures exceeding a defined limit/temperature class. Two types of protection are defined here the schwadensicheres Gehause , comparable with a restricted breathing enclosure , and simple pressurization .

See other pages where Simple pressurization is mentioned: [Pg.403]    [Pg.459]    [Pg.525]    [Pg.382]    [Pg.342]    [Pg.1139]    [Pg.1272]    [Pg.38]    [Pg.1850]    [Pg.813]    [Pg.193]    [Pg.181]    [Pg.285]    [Pg.1936]    [Pg.138]    [Pg.1850]    [Pg.6]    [Pg.324]    [Pg.552]    [Pg.177]    [Pg.924]    [Pg.1172]    [Pg.43]    [Pg.45]    [Pg.45]    [Pg.488]   


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