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Experimental device

The device used is an evaporator. This evaporator was initially designed to cany out plating by evaporation under vacuum. [Pg.219]

This device is composed of a glass bell jar, in which a primary vacuum can be achieved using a paddle pump and, if necessary, a diffusion pump. [Pg.220]

This jar contains a cmcible composed of a filament of refractory metal, generally tungsten. This filament, whose diameter is 0.05 mm, is shaped to form a cone made of an unjointed turn of coil. [Pg.220]

Such a source emits in every direction, but not in an isotropic way. Variations have been measured under vacuum using a quartz microbalance. The maximum of these variations depends on the emission angle and can reach 35%. [Pg.220]

In fact, the films will always be deposited at the same place under the source. [Pg.220]

Catal ic reactor is the heart of catal3h ic activity evaluation device, which is considered as the center to organize the experimental process. The reactor is controlled by external conditions, such as the supply of raw materials, analysis and the measurement, preheating or (and) the pressurized device and so on. After reaction, it needs the means of separation, measurement and analysis to provide necessary flow and concentration data of reaction mixture to determine and to calculate the activity, and selectivity of catalysts. At present, the most commonly used device in the evaluation of catalysts is tubular reactor. Here, the high-pressure experimental device of ammonia synthesis catalyst is taken as an example. [Pg.555]

3 Flowsheet of high-pressure test for performance evaluation of ammonia synthesis catalyst [Pg.555]

This device can complete a series of experimental studies and measurement, including the evaluation of the activity, selectivity and stability of catalysts, the study on reduction performance, heat-resistant experiment and antivirus experimental, the study on reaction conditions such as H2/N2, content of inert gases etc, and the study on reaction kinetics and mechanism, and so on. [Pg.557]


Application of experimental devices allows to perform NDT of products, made out of materials of low density (Al-Mg - alloys, Be, plastics) with high defectoscopic sensitivity up to 0,5 %. Inch-size X-ray vidicons used complete with microfocal X-ray tubes and X-ray image enlargement method allow to obtain resolution up to SO pairs of lines per mm. [Pg.449]

Figure la Schematic diagram of the experimental device axial translation of length Xa... [Pg.661]

From a reaction engineering viewpoint, semiconductor device fabrication is a sequence of semibatch reactions interspersed with mass transfer steps such as polymer dissolution and physical vapor deposition (e.g., vacuum metallizing and sputtering). Similar sequences are used to manufacture still experimental devices known as NEMS (for nanoelectromechanical systems). [Pg.425]

If the turbulent flame is ever proven to have asymptotically a constant flame brush thickness and constant speed in constant, i.e., nondecaying, turbulence, then the aforementioned turbulent flame speed and the flame brush thickness (5 give a well-defined sufficient characterization of the flame in its asymptotic behavior. However, it is not proven up to now that the studied experimental devices have been large enough to ensure that this asymptotic state can be reached. Besides, the correct definitions for the turbulent flame speed or flame brush thickness, as given above, are far from... [Pg.140]

RPLC-FTTR of an Irganox 1010, Irganox PS800 containing polyolefin extract was reported with a thermospray /moving belt/DRIFT interface [483] detection limits of 100 ng were reported for this experimental device. LC-TSP-FTTR has also been used for the identification of other antioxidants, as shown in Figure 7.25 [500]. [Pg.494]

The experimental device for photometric measurements is shown schematically in Fig. 7. The device includes a measuring box (1) in which a mobile platform (2) is situated with two windows (3), into which plates (3 ) are inserted, each plate having 9 holes with paper matrixes. [Pg.160]

The microwave power could be adjusted in order to allow constant pressure within the vessel. A incorporated pressure release valve permits to use this experimental device routinely and safely. Furthermore, an inert gas as argon could be introduced within the reactor to avoid sparking risk with flammable solvents. This experimental device is able to raise temperature from ambient to 200 °C in less than 20 s (pressure is close to 1.2 Mpa and heating rate is close to 7° s 1). The RAMO system has been designed for nanoparticles growing and elaboration [59-62]. The RAMO system is a batch system. It could be easily transpose to continuous process with industrial scale (several hundred kilograms by seconds). [Pg.28]

Fig. 7 A molecular switch made of the leg of a legged Cu-porphyrin adsorbed on a Cu(211) surface, (a) An idealized version of such a molecular switch where the switching leg is exactly interconnected to two atomic wires in a Fig. la like configuration. The device resistance is maximum for a perpendicular = 0 conformation, (b) The real experimental device where the STM tip apex can be maintained at 0.7 nm or 0.9 nm separation between the tip and the surface in between the leg switching. In this case, the resistance is minimum for perpendicular to the Cu(211) surface = 0 conformation. The energetic of the switching mechanism can be calculated and the switching barrier height was also determined experimentally... Fig. 7 A molecular switch made of the leg of a legged Cu-porphyrin adsorbed on a Cu(211) surface, (a) An idealized version of such a molecular switch where the switching leg is exactly interconnected to two atomic wires in a Fig. la like configuration. The device resistance is maximum for a perpendicular = 0 conformation, (b) The real experimental device where the STM tip apex can be maintained at 0.7 nm or 0.9 nm separation between the tip and the surface in between the leg switching. In this case, the resistance is minimum for perpendicular to the Cu(211) surface = 0 conformation. The energetic of the switching mechanism can be calculated and the switching barrier height was also determined experimentally...
Physics and chemistry are carried out in laboratory frames using coordinate systems to set up experimental devices. Before discussing quantum mechanical processes let us recall the form of the total Hamiltonian for a set of particles having charges qa and masses ma interacting with an electromagnetic field A. This Hamiltonian is given by ... [Pg.313]

We now have to make the definition of x more explicit and decide where to locate the origin (the Matano interface) for the conservation condition above to hold. In the laboratory, one would use an arbitrary coordinate X, such as the distance to one end of the experimental device, then... [Pg.425]

Analytical-operational Difficulties. In order to work close to the conditions in natural waters, very low concentrations of metal ions (in the nanomolar range) and of particles as well as pH values in the neutral range have to be used. Analytical difficulties occur because of undesired adsorption of metal ions to the experimental devices (walls of beakers, glass filtration devices, etc.) and of insufficient separation of the particulate and dissolved phase (particles in the colloidal size range). [Pg.374]

Table 11.2. An Assessment of Various Experimental Devices Based on Solid State... Table 11.2. An Assessment of Various Experimental Devices Based on Solid State...
The main schemes and experimental devices used for the detection of signals within this time range are briefly described below. In Section 3.7 we will also introduce the instrumentation used to measure optical signals in the picosecond-femtosecond range. [Pg.107]

Figure 5.32 Solids conveying rate data calculate using the modified Campbell-Dontula model for the Dow solids conveying process using the shallow screw, 75 °C barrel and screw temperatures, and a screw speed of 50 rpm. The solids conveying rates measured from the experimental device are provided... Figure 5.32 Solids conveying rate data calculate using the modified Campbell-Dontula model for the Dow solids conveying process using the shallow screw, 75 °C barrel and screw temperatures, and a screw speed of 50 rpm. The solids conveying rates measured from the experimental device are provided...
Five biomass samples (hazelnut shell, cotton cocoon shell, tea factory waste, olive husk and sprace wood) were pyrolyzed in a laboratory-scale apparatus designed for the purpose of pyrolysis (Demirbas, 2001, 2002a). Figure 6.4 shows the simple experimental setup of pyrolysis. The main element of the experimental device is a vertical cylindrical reactor of stainless steel, 127.0 nun in height, 17.0 nun iimer diameter and 25.0 mm outer diameter inserted vertically into an electrically heated tubular furnace and provided with an electrical heating system power source, with a heating rate of about 5 K/s. The biomass samples ground... [Pg.180]

This method, which has been developed and extensively utilized in Russia [22,23], deals with nonstirred liquid phases and is based on measurements of the electrical conductivity of the aqueous phase and of its changes during extraction. In the experimental device, the two phases are initially kept separated inside a theimostated cell and then instantaneously contacted through a known contact area. At this moment, the concentration variation in one phase is recorded as a function of time, generally using conductometry. [Pg.254]

Bennett and Barter (1997) discuss the effect of partitioning-dissolution in an aqueous phase of alkylphenol. Specifically, they show that the depletion of this crude oil component affects the chemical composition of the original pollutant. Partitioning at equilibrium can be considered the maximum dissolution value of a compound under optimal solvation conditions. Partitioning-dissolution is obtained by washing the crude oil with saline water at variable temperature and pressure conditions, similar to those in the subsurface. The data reported were obtained using a partition device able to simulate the natural environmental conditions of a crude oil reservoir. The alkylphenol partition coefficients between crude oil and saline subsurface water were measured as a function of variation in pressure, temperature, and water salinity. Preliminary trials proved that the experimental device did not allow alkylphenol losses due to volatilization. [Pg.346]

Open Vessel. This represents a convenient and commonly used experimental device, a section of long pipe (see Fig. 13.9). It also happens to be the only physical situation (besides small D/wL) where the analytical expression for the E curve is not too complex. The results are given by the response curves shown... [Pg.300]

The experimental strategy in studying catalytic kinetics usually involves measuring the extent of conversion of gas passing in steady flow through a batch of solids. Any flow pattern can be used, as long as the pattern selected is known if it is not known then the kinetics cannot be found. A batch reactor can also be used. In turn we discuss the following experimental devices ... [Pg.396]

Experimental devices for studying deactivating catalysts fall into two classes those which use a batch of solids, and those which use a through flow of solids. Figure 21.1 shows some of these devices. [Pg.477]

We treat these two classes of experimental devices in turn. [Pg.478]

As long as the deactivation is concentration independent, the activity and concentration effects can be decoupled and any of the above experimental devices will give simple easy-to-interpret results. Thus the above analyses can be extended with no difficulty to any reaction order n and any deactivation order d, as long as m = 0, or for... [Pg.483]

On the other hand, if the deactivation is concentration dependent, or m 0, then the concentration and activity effects do not decouple and analysis becomes difficult unless the proper experimental device is used, one deliberately chosen so as to decouple these factors. Reactors which keep constant by slowing the flow rate of feed, as treated above, are such devices. They can be used to find the rate constants for the reactions... [Pg.483]

Shah (1979) evaluation of the mass transfer coefficients in various types of equipment. Also experimental devices for finding these coefficients. [Pg.535]


See other pages where Experimental device is mentioned: [Pg.327]    [Pg.328]    [Pg.1]    [Pg.397]    [Pg.612]    [Pg.738]    [Pg.1183]    [Pg.604]    [Pg.141]    [Pg.150]    [Pg.160]    [Pg.192]    [Pg.439]    [Pg.418]    [Pg.21]    [Pg.440]    [Pg.127]    [Pg.370]    [Pg.370]    [Pg.131]    [Pg.113]    [Pg.114]    [Pg.222]    [Pg.211]    [Pg.398]   
See also in sourсe #XX -- [ Pg.26 , Pg.555 ]




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