Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Continuous crystallizers manipulation

Figure 2 Schematic view of the apparatus used in studies of the steric effects in gas-surface scattering. A detail of the crystal mount with die orientation rod at 1 cm in front of the surface is shown in die right hand corner. A detailed drawing of the hexapole state selector is given below the main figure. The voltage is applied to die six small rods indicated by an arrow. Key Q quadrupole mass spectrometer R Rempi detector M, crystal manipulator SI, beam source for state selected molecules H electric hexapole state selector C mechanical beam chopper V pulsed gas source S2, continuous molecular beam source. From Tenner et al. [34]. Figure 2 Schematic view of the apparatus used in studies of the steric effects in gas-surface scattering. A detail of the crystal mount with die orientation rod at 1 cm in front of the surface is shown in die right hand corner. A detailed drawing of the hexapole state selector is given below the main figure. The voltage is applied to die six small rods indicated by an arrow. Key Q quadrupole mass spectrometer R Rempi detector M, crystal manipulator SI, beam source for state selected molecules H electric hexapole state selector C mechanical beam chopper V pulsed gas source S2, continuous molecular beam source. From Tenner et al. [34].
The final CSD can be dramatically influenced by the temperature at which a continuous crystallizer is operated or by the temperature profile followed over a batch run, because the crystallizer temperature affects the degree of supersaturation and the growth and nucleation rates. Therefore, the manipulation of variables controlling the cooling rate (e.g., crystallizer jacket temperature, evaporation rate) can be used to influence the CSD. The adjustment of the feed rate to a continuous crystallizer has also been suggested as a means of affecting the CSD (Myerson et al. 1987 Han 1969). [Pg.203]

Most of the literature in control of continuous crystallizers is based on a singleinput single output (SISO) control structure. Different controlled variables and manipulations have been suggested based on the relative ease and accuraey of on-line measurements and their efficiency in effectively addressing set-point tracking and disturbance rejections. Both linearized physical models and blackbox models have been suggested for the controller design, as reviewed by Sheikh (1997) as follows. [Pg.291]

One approach which has resulted in experimental implementation is that of Randolph and co-workers f88-92 >. Using a simulation (21) Randolph and Beckman demonstrated that in a complex RTD crystallizer, the estimation of nuclei density could be used to eliminate cycling or reduce transients in the CSD. Randolph and Low (gg) experimentally attempted feedback control by manipulation of the fines dissolver flow rate and temperature in response to the estimated nuclei density. They found that manipulation of fines flow rate upset the fines measurement indicating that changes in the manipulated variable disturbed the measured variable. Partial fines dissolution resulting from manipulation of the fines dissolver temperature appeared to reduce CSD transients which were imposed upsets in the nucleation rate. In a continuation of this work Randolph et. al. < 921 used proportional control of inferred nuclei density to control an 18 liter KCl crystallizer. [Pg.11]

The number of inputs which are available for controlling crystallisation processes is limited. Possible Inputs for a continuous evaporative crystallisation process are, crystalliser temperature, residence time and rate of evaporation. These Inputs affect the crystal size distribution (CSD) through overall changes in the nucleatlon rate, the number of new crystals per unit time, and the growth rate, the increase in linear size per unit time, and therefore do not discriminate directly with respect to size. Moreover, it has been observed that, for a 970 litre continuous crystalliser, the effect of the residence time and the production rate is limited. Size classification, on the other hand, does allow direct manipulation of the CSD. [Pg.130]

In this chapter, we have aimed to present illustrative examples - the success stories. Some of these successes undoubtedly arise by serendipity, essentially by post-mortem analysis of observed crystal structures. Others are indeed the result of inspired design. The continuing challenge for crystal engineers is to tip the balance away from the fortuitous towards the true manipulation of the three-dimensional architecture of molecular crystals. [Pg.436]

Isolated aroma chemicals are aroma-active substances isolated from natural sources mainly by means of crystallization, distillation, and adduct formation/decomposition. Although synthetic materials are in many cases convenient to use, isolated aroma chemicals continue to be advantageous, especially when chirality is the issue. Even if chirality is not a problem, in some cases (eg., 1,8-cineole (1), eugenol (2), and limonene (3)), isolated natural chemicals serve better than their synthetic counterpart (Table 3). 3 Isolated aroma chemicals can be useful as such for the industry, and they are also utilized as starting materials for further synthetic manipulations.34,35... [Pg.599]

One very recently published result must be mentioned. Petukhov et al. have reported the detection of the EPR spectrum of micron-sized crystals of Fe8 via their magnetization response as a function of apphed magnetic field, using a Hall-probe magnetometer under either continuous wave or pulsed microwave irradiation at 118 GHz and between 1.4 and 50 K [53]. Dips are observed in the magnetization vs. field curves corresponding to resonant absorption - that is, EPR transitions. This method offers potentially extraordinary sensitivity and, furthermore, manipulation of the magnetization data in the absence and presence of the microwave radiation allows determination of the spin temperature. [Pg.82]

Figure 9.1 is a schematic of a continuous cooling crystallizer equipped with the measurement devices and manipulated variables that will be discussed subsequently. [Pg.202]

One unique advantage of the current droplet manipulation method is that the actuation can be continued even after a solidification reaction occurred inside a droplet. As shown in Fig. 6, not only a liquid droplet but also droplets containing solid precipitates or hydrogel and even a solid sphere can be actuated on the BCD system. The biochemical solidification reaction inside a droplet is demonstrated as the formation of a calcium carbonate crystal which is related to an in vitro study of biomineralization of marine organisms. When the Na2C03 and CaCla droplets are coalesced, by the BCD actuation of the coalesced droplet, the mixing and solidification reaction is accelerated and completed in... [Pg.942]


See other pages where Continuous crystallizers manipulation is mentioned: [Pg.201]    [Pg.203]    [Pg.1973]    [Pg.12]    [Pg.157]    [Pg.62]    [Pg.297]    [Pg.201]    [Pg.478]    [Pg.113]    [Pg.191]    [Pg.45]    [Pg.168]    [Pg.232]    [Pg.439]    [Pg.934]    [Pg.274]    [Pg.476]    [Pg.45]    [Pg.3442]    [Pg.152]    [Pg.605]    [Pg.427]    [Pg.45]    [Pg.154]    [Pg.442]    [Pg.118]    [Pg.606]    [Pg.1107]    [Pg.1973]    [Pg.201]    [Pg.210]    [Pg.605]    [Pg.261]    [Pg.412]    [Pg.606]    [Pg.329]    [Pg.634]    [Pg.151]    [Pg.4]    [Pg.285]   
See also in sourсe #XX -- [ Pg.225 ]




SEARCH



Continuous crystallizer

Continuous crystallizers

Crystallization continuous

Crystallization manipulation

© 2024 chempedia.info