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Inlet materials

A process unit in a chemical process plant performs some operation on the inlet material streams to produce the desired outlet streams. In the design of such a unit the design calculations model the operation of the unit. A process unit and the design equations... [Pg.15]

Space time (r) is usually applied only to flow situations, and is the time required to process one reactor volume of inlet material (feed) measured at inlet conditions. That is, t is the time required for a volume of feed equal to the volume of the vessel (V) to flow through the vessel. The volume V is the volume of the vessel accessible to the fluid, t can be used as a scaling quantity for reactor performance, but the reaction conditions must be the same, point-by-point, in the scaling. [Pg.26]

Moismre content of inlet material should contain a moisture content ranging from 5 to 20% by weight. (A predrying unit can be used in cases where the moismre content of feed material exceeds 20%.)... [Pg.1140]

Ambient temp at blower inlet Material of construction in contact with product... [Pg.730]

The inlet material to the flash drum is liquid at 100°F, with = 8,575.8 Btu/lb mol. The flash Eq. (13.43) applies to this part of the example. The enthalpy balance is... [Pg.335]

In making a heat balance at steady state we use methods similar to those used in making a material balance. The energy or heat coming into a process in the inlet materials plus any net energy added to the process is equal to the energy leaving in the materials. Expressed mathematically. [Pg.19]

Primary sodium temperature (reactor outlet/inlet) Material of primary/secondary coolant pipe Steam eonditions (temperature/pressure) ... [Pg.25]

The refractory wire inside the pipe would be either centered in the flow stream or attached to the inner liner surface. The wire waveguide would remain acoustically isolated from all other components both inside and outside of the pipe. Materials would have been carefully chosen for the internal waveguide and horn that would allow attachment to the internal surface and would not diffuse into the gas stream at elevated temperatures. The horn and waveguide materials on both sides of the inlet should have similar acoustic impedances to the inlet material in order to minimize reflections at the interfaces. [Pg.432]

In describing reactor performance, selectivity is usually a more meaningful parameter than reactor yield. Reactor yield is based on the reactant fed to the reactor rather than on that which is consumed. Clearly, part of the reactant fed might be material that has been recycled rather than fresh feed. Because of this, reactor yield takes no account of the ability to separate and recycle unconverted raw materials. Reactor yield is only a meaningful parameter when it is not possible for one reason or another to recycle unconverted raw material to the reactor inlet. By constrast, the yield of the overall process is an extremely important parameter when describing the performance of the overall plant, as will be discussed later. [Pg.25]

Main steamline section and weld of the same Unit 4 f600 MW3 as above the weld connects 2 steamline sections of different materials (stainless steel and low-alloy steel) through a transition material section, ahead of the Y-piece where branching of the turbine inlet lines takes place (255 mm internal diameter, 44.5 mm thickness). Ultrasonic inspection pointed out potential integrity problems in the weld. The requirement was again that AE could support safe operation of the weld until the next incoming planned maintenance shutdown. [Pg.71]

I) When working with larger quantities of material, it is more convenient (and a better yield is obtained) to purify the air-dried product by distillation under diminished pressure. Use the apparatus pictured in Fig. II, 19, 4, and add a few fragments of porous porcelain to the solid. No air inlet can be employed to prevent bumping since this may lead to explosive decomposition. Collect the pure m-nitrophenol at I60-I65°/I2 mm. always allow the flask to cool before admitting air otherwise the residue may decompose with explosive violence. The recovery is over 90 per cent, of the pure m-nitroplienol. [Pg.615]

Liquid chromatography is a separation method that is often applied to nonvolatile, thermally labile materials such as peptides, and, if their mass spectra are required after the separation step, then a mild method of ionization is needed. Since FAB/LSIMS is mild and works with a liquid matrix, it is not surprising that attempts were made to utilize this ionization source as both an inlet... [Pg.81]

Fundamentally, introduction of a gaseous sample is the easiest option for ICP/MS because all of the sample can be passed efficiently along the inlet tube and into the center of the flame. Unfortunately, gases are mainly confined to low-molecular-mass compounds, and many of the samples that need to be examined cannot be vaporized easily. Nevertheless, there are some key analyses that are carried out in this fashion the major one i.s the generation of volatile hydrides. Other methods for volatiles are discussed below. An important method of analysis uses lasers to vaporize nonvolatile samples such as bone or ceramics. With a laser, ablated (vaporized) sample material is swept into the plasma flame before it can condense out again. Similarly, electrically heated filaments or ovens are also used to volatilize solids, the vapor of which is then swept by argon makeup gas into the plasma torch. However, for convenience, the methods of introducing solid samples are discussed fully in Part C (Chapter 17). [Pg.98]

The hybrid can be used with El, Cl, FI, FD, LSIMS, APCI, ES, and MALDI ionization/inlet systems. The nature of the hybrid leads to high sensitivity in both MS and MS/MS modes, and there is rapid switching between the two. The combination is particularly useful for biochemical and environmental analyses because of its high sensitivity and the ease of obtaining MS/MS structural information from very small amounts of material. The structural information can be controlled by operating the gas cell at high or low collision energies. [Pg.161]

In some inlet devices, the volatile sample materials are first separated from entrained hydrogen gas or air by condensing them in a coolant bath. Subsequently, when all of the volatile sample components have been condensed and the hydrogen or air has been swept away, the sample is reheated and sent to the plasma flame. [Pg.396]

Fig. 25. OxyTech MGC electroly2er a, membrane b, anode assembly c, manifold spacer d, anolyte outlet e, catholyte outlet f, bulkhead g, brine inlet h, NaOH inlet i, insulating channel j, bulkhead insulator k, interface material 1, cathode assembly m, interceU bus n, tie rod o, current distributor p,... Fig. 25. OxyTech MGC electroly2er a, membrane b, anode assembly c, manifold spacer d, anolyte outlet e, catholyte outlet f, bulkhead g, brine inlet h, NaOH inlet i, insulating channel j, bulkhead insulator k, interface material 1, cathode assembly m, interceU bus n, tie rod o, current distributor p,...

See other pages where Inlet materials is mentioned: [Pg.378]    [Pg.177]    [Pg.378]    [Pg.403]    [Pg.378]    [Pg.378]    [Pg.156]    [Pg.895]    [Pg.868]    [Pg.117]    [Pg.188]    [Pg.924]    [Pg.60]    [Pg.704]    [Pg.378]    [Pg.177]    [Pg.378]    [Pg.403]    [Pg.378]    [Pg.378]    [Pg.156]    [Pg.895]    [Pg.868]    [Pg.117]    [Pg.188]    [Pg.924]    [Pg.60]    [Pg.704]    [Pg.276]    [Pg.702]    [Pg.923]    [Pg.38]    [Pg.65]    [Pg.68]    [Pg.68]    [Pg.85]    [Pg.101]    [Pg.106]    [Pg.114]    [Pg.284]    [Pg.437]    [Pg.391]    [Pg.323]    [Pg.397]    [Pg.110]    [Pg.230]    [Pg.398]   
See also in sourсe #XX -- [ Pg.108 ]




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