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Apparatus, experimental

A schematic diagram of the apparatus for ODMR measurements is shown in Fig. 3. Microwave power is chopped at a low frequency, e.g., 1 kHz,usinga p-i-n diode or applying a rectangular wave to the reflector voltage for the klystron. Emitted li t coming through a monochromator from a sample [Pg.160]

The choice of experimental apparatus is dictated by the question and experimental design, and the test species. An appropriate apparatus will enable the stimuli to be maintained in its original state, allow normal responses by the subject, and permits unobstructed monitoring of responses. Simple is usually better. The literature describes an array of apparatuses for specific tests with specific subjects. This section describes a few inexpensive test apparatuses for simple chemosen-sory bioassays. [Pg.337]

The results are given for pH = 7 in Fig. 5.14a for various total concentrations of H2U added to the system. Surface complex formation progressively increases with [H2Ut] and reaches saturation at concentrations above 10-6 M. [Pg.185]

the net surface charge of the hydrous oxide decreases (it becomes negative when the total ligand added exceeds 10 6 M)  [Pg.185]

2) Effect of Metal Ion. To the hematite suspension already characterized one adds Pb(II). The surface complex formation is characterized by [Pg.185]

The calculations are similar and the result is displayed in Fig. 5.14b for pH = 4.4. Obviously Pb-adsorption is accompanied by an increase in net charge and a marked decrease in surface protonation [sFeOHg]. Plausibly, this reduction in Cji, can decrease the dissolution rate. [Pg.185]

Various devices can be used to determine the kinetics and rates of chemical weathering. In addition to the batch pH-stats, flow through columns, fluidized bed reactors and recirculating columns have been used (Schnoor, 1990). Fig. 5.15a illustrates the fluidized bed reactor pioneered by Chou and Wollast (1984) and further developed by Mast and Drever (1987). The principle is to achieve a steady state solute concentration in the reactor (unlike the batch pH-stat, where solute concentrations gradually build up). Recycle is necessary to achieve the flow rate to suspend the bed and to allow solute concentrations to build to a steady state. With the fluidized bed apparatus, Chou and Wollast (1984) could control the AI(III) concentration (which can inhibit the dissolution rate) to a low level at steady state by withdrawing sample at a high rate. [Pg.185]

Firstly we shall consider the various forms of conventionally determined spectra, as distinct from time-resolved spectra, which can be obtained using continuous excitation. The measurement of emission spectra enables parameters such as the spectral position, spectral width, and spectral intensity to be determined. Moreover, the variation of these parameters with temperature is very important in deciding the origin of spectral bands. Sometimes the luminescence from single crystals is polarized and this can also give information as to the nature of the center. [Pg.37]

The observed excitation spectrum is distorted because the light intensity of the excitation source is a function of the wavelength and the transmission efficiency of the excitation monochromator is a function of wavelength. The emission spectra are distorted by the wavelength-dependent efficiency of the emission monochromator and the photomultiplier (PMP) tubes. Thus both [Pg.37]


Some preliminary tests were performed to set up the experimental apparatus, to check the sensors (pressure and strain gauges) and the SPATE system operation. [Pg.410]

These values were ehosen since they were the best compromise between the possibility to provtde significant amplitudes of the cyclical pressure loading and the experimental apparatus limits. Infact, the cyclical pressure amplitude gets lower as the frequency gets higher. [Pg.412]

Schematic diagrams of modem experimental apparatus used for IR pump-probe by Payer and co-workers [50] and for IR-Raman experiments by Dlott and co-workers [39] are shown in figure C3.5.3. Ultrafast mid-IR pulse generation by optical parametric amplification (OPA) [71] will not discussed here. Single-colour IR pump-probe or vibrational echo experiments have been perfonned with OP As or free-electron lasers. Free-electron lasers use... Schematic diagrams of modem experimental apparatus used for IR pump-probe by Payer and co-workers [50] and for IR-Raman experiments by Dlott and co-workers [39] are shown in figure C3.5.3. Ultrafast mid-IR pulse generation by optical parametric amplification (OPA) [71] will not discussed here. Single-colour IR pump-probe or vibrational echo experiments have been perfonned with OP As or free-electron lasers. Free-electron lasers use...
Wetted wall column An experimental apparatus used to determine the mass transfer that takes place through laminar boundary layers. [Pg.1488]

Fig. 3.1. Mental images of shoek-eompression processes vary eonsiderably depending upon the baekground and experienee of the investigator. The scientifie images are ereated from inputs from theory, numerieal simulation, and experiment. The eritieal nature of the experiment in establishing reality requires unusually eareful study of eritieal aspeets of experimental apparatus. Fig. 3.1. Mental images of shoek-eompression processes vary eonsiderably depending upon the baekground and experienee of the investigator. The scientifie images are ereated from inputs from theory, numerieal simulation, and experiment. The eritieal nature of the experiment in establishing reality requires unusually eareful study of eritieal aspeets of experimental apparatus.
Figure 9.19 Experimental apparatus for feedback control of KCl crystallization after Redman and Rohani, 1992)... Figure 9.19 Experimental apparatus for feedback control of KCl crystallization after Redman and Rohani, 1992)...
Besides shear-induced phase transitions, Uquid-gas equilibria in confined phases have been extensively studied in recent years, both experimentally [149-155] and theoretically [156-163]. For example, using a volumetric technique, Thommes et al. [149,150] have measured the excess coverage T of SF in controlled pore glasses (CPG) as a function of T along subcritical isochoric paths in bulk SF. The experimental apparatus, fully described in Ref. 149, consists of a reference cell filled with pure SF and a sorption cell containing the adsorbent in thermodynamic equilibrium with bulk SF gas at a given initial temperature T,- of the fluid in both cells. The pressure P in the reference cell and the pressure difference AP between sorption and reference cell are measured. The density of (pure) SF at T, is calculated from P via an equation of state. [Pg.56]

MESG is defined in terms of die precise test mediod and apparatus used, of which there are three variants British, lEC, and Underwriters Laboratories, Inc. Each apparatus consists of two combusdon chambers connected by a slot of specified size and variable widdi. The separate chambers are filled with the test mixture. The MESG is die maximum slot widdi that prevents flame propagadoii between die chambers for all composi-doiis of die test gas in air under the specified test coiididoiis. Phillips (1987) describes and compares diese three types of experimental apparatus for determining the MESG. [Pg.100]

The measurements were made using different experimental apparatus such as narrow pipes, diaphragms with a round hole, flat slots, etc. Values of the critical diameter determined using noncircular apertures have been converted to equivalent circular apertures. [Pg.111]

Figure 4.3. Experimental apparatus for investigation of effects of pipe racks on flame propagation (Harrison and Eyre 1986 and 1987). Figure 4.3. Experimental apparatus for investigation of effects of pipe racks on flame propagation (Harrison and Eyre 1986 and 1987).
Figure 4.11. Experimental apparatus for investigating jet ignition of ethylene-air and hydro-gen-air mixtures (Schildknecht et al., 1984). Figure 4.11. Experimental apparatus for investigating jet ignition of ethylene-air and hydro-gen-air mixtures (Schildknecht et al., 1984).
Experiments reported by Harris and Wickens (1989) deserve special attention. They modified the experimental apparatus described in Section 4.1.1—a 45 m long, open-sided apparatus. The first 9 m of the apparatus was modified by the fitting of solid walls to its top and sides in order to produce a confined region. Thus, it was possible to investigate whether a flame already propagating at high speed could be further accelerated in unconfined parts of the apparatus, where obstacles of pipework were installed. The initial flame speed in the unconfined parts of the apparatus could be modified by introduction of obstacles in the confined part. [Pg.87]

FIGURE 21.2 Experimental apparatus used to measure the standard reduction potential of the indicated redox couples (a) the acetaldehyde/ethanol couple, (b) the fumarate/succi-nate couple, (c) the Fe /Fe" couple. [Pg.675]

Figure 7.1 Representation of the phase diagram for a pure fluid such as water. The shaded area is the continuum tlirough wliich we can continuously vary the properties of the fluid. The liigh-pressure and liigh-temperature limits shown here are arbittary. They depend only on the capabilities of the experimental apparatus and the stability of the apparatus and the fluid. Figure 7.1 Representation of the phase diagram for a pure fluid such as water. The shaded area is the continuum tlirough wliich we can continuously vary the properties of the fluid. The liigh-pressure and liigh-temperature limits shown here are arbittary. They depend only on the capabilities of the experimental apparatus and the stability of the apparatus and the fluid.
Smeatnii s elegant experimental technique enabled him to deal with both hydraulic and mechanical friction losses, allowing him to calculate water velocity at the wheel and thereby determine an effective nr virtual head. Smeaton s experimental apparatus was a brilliant device that enabled him to measure the efficiency of the wateiwheel, alone rather than the overall efficiency of the experiment. Smeaton was able to conclusively shov that a water-wheel when driven by the weight of water alone, is about twice as efficient as when driven by the impulse of water. This demonstration ensured that British mills, wherever possible, from then on would be fitted with overshot or breastshot wateiwheels, rather than undershot. [Pg.1049]

Pulse radiolysis requires access to an electron accelerator or similar device. This requirement usually restricts work to specialized laboratories. Thorough descriptions of the experimental apparatus and protocols have been given.23,24... [Pg.269]

Figure 4.8. (a) Experimental apparatus for measuring the catalyst-electrode metal/gas interface area AG- (b) typical yco2 peak obtained upon reacting the preadsorbed O with C2H4 or CO its area gives N0. (c) Plot of N0 vs the 02 desorption time, tHe, to obtain Nc. [Pg.119]

A typical apparatus for electrochemical promotion experiments consists of three parts (a) The gas feed and mixing system (b) the reactor and (c) the analysis and electrochemical measurements system. A detailed schematic of the experimental apparatus is shown in Figure B.l, where the three parts are clearly shown. [Pg.550]

Experimental apparatus and procedures used are essentially those described previously (8). Modifications are described below. [Pg.285]

Experimental Apparatus. The experimental apparatus used in the continuous polymerization reactions of this investigation was constructed and used by Ahmad (27) for earlier studies of isoprene... [Pg.307]

Figure 6. Experimental apparatus for continuous polymerization of styrene ((D) Needle valve (X) t)dlve ( ) pressure regulator check valve (— ) ther-... Figure 6. Experimental apparatus for continuous polymerization of styrene ((D) Needle valve (X) t)dlve ( ) pressure regulator check valve (— ) ther-...
To prevent the optimization procedure from discovering trivial, or nonphysical solutions, the yield must be optimized with respect to a set of constraints. These constraints can take many forms, including details of the experimental apparatus and the physical system [23-30]. [Pg.252]

Fig. 1. Schematic diagram of experimental apparatus 3. Results and discussion... Fig. 1. Schematic diagram of experimental apparatus 3. Results and discussion...
A thermal plasma system has been developed for the decomposition of methane. A schematic diagram of the experimental apparatus is shown in Fig. 1. The system consists primarily of D.C. plasma torch, plasma reactor and filter assembly. Plasma was discharged between a tungsten cathode and a copper anode using N2 gas. All the experiments were carried out at atmospheric pressure at 6 kW input electric power and N2 flow rate of 10 to 12 1/min. The feed gas (CH4) flow rates were varied from 3 to 15 1/min depending on the operating conditions, shown in Table. 1. [Pg.421]

Fig. 1 Schematic diagram of experimental apparatus Co.) and carbon particle size analyzer(LS230, COULTER Co.). Fig. 1 Schematic diagram of experimental apparatus Co.) and carbon particle size analyzer(LS230, COULTER Co.).
A schematic diagram of the experimental apparatus is shown in Fig. 1. A rotating fluidized bed composes of a plenum chamber and a porous cylindrical air distributor (ID400xD100mm) made of stainless sintered mesh with 20(xm openings [2-3]. The horizontal cylinder (air distributor) rotates around its axis of symmetry inside the plenum chamber. There is a stationary cylindrical filter (ID140xD100mm, 20(o.m openings) inside the air distributor to retain elutriated fine particle. A binary spray nozzle moimted on the metal filter sprays binder mist into the particle bed. A pulse air-jet nozzle is also placed inside the filter, which cleans up the filter surface in order to prevent clogging. [Pg.486]


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