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Reactor, schematic

Figure 1. Key elements of the TAP reactor (A) and high pressure fixed bed reactor (B) experimental systems. The TAP reactor schematic shows the heated valve manifold and reactor with the elevated pressure attachment located in the main high vacuum chamber. The fixed bed reactor shows the feed system, liquid vaporizer, oxygen disperser, reactor, and waste recovery system. Figure 1. Key elements of the TAP reactor (A) and high pressure fixed bed reactor (B) experimental systems. The TAP reactor schematic shows the heated valve manifold and reactor with the elevated pressure attachment located in the main high vacuum chamber. The fixed bed reactor shows the feed system, liquid vaporizer, oxygen disperser, reactor, and waste recovery system.
Example 4 Design a flat, perforated-plate grid for the polyethylene reactor schematically shown in Fig. 11, and calculate the gas j et penetration depth. Use a triangular pitch. System parameters are ... [Pg.230]

Figure 2.1 Batch reactor (schematic, liquid-phase reaction)... Figure 2.1 Batch reactor (schematic, liquid-phase reaction)...
FIGURE 2.11 Riser simulator reactor schematics, showing reaction chamber at left and peripherals at right, including a preheated vacuum cylinder linked to a gas chromatograph to drain, quantify and identify reaction products at the end of a rnn. [Pg.32]

Figure 1 Counter-current Bunsen reactor schematics... Figure 1 Counter-current Bunsen reactor schematics...
Figure 3.4. Continuous stirred-tank reactor (schematic). Figure 3.4. Continuous stirred-tank reactor (schematic).
Consider a generic recycle reactor schematically illustrated in Figure 3.5.3. First, denote R as the recycle ratio. The recycle ratio is defined as the volume of fluid returning to the reaction chamber entrance divided by the volume of fluid leaving the system. Simple material balances around the mixing point prior to the entrance of the reaction volunie give ... [Pg.89]

The proper boundary conditions used to solve Equation (8.5.2) have been exhaustively discussed in the literature. Consider the reactor schematically illustrated in Figure 8.5.1. The conditions for the so-called open configuration are ... [Pg.277]

Consider the batch reactor schematically illustrated in Figure 9.3.1. Typically, reactants are charged into the reactor from point (I), the temperature of the reactor... [Pg.288]

Figure El-5.3 Packed-bed reactor. (Schematic and photograph courtesy of Sasol/Sastech FT Limited.)... Figure El-5.3 Packed-bed reactor. (Schematic and photograph courtesy of Sasol/Sastech FT Limited.)...
Figure 10-5 (a) Catalytic packed-bed reactor—schematic (b) different shapes and sizes of catalyst. (Courtesy of the Engelhard Corporation.)... [Pg.591]

Figure l-tits) Tubular reactor schematic. Longitudinal tubular reactor, lExccrpied by special permission from Clieni. Eii/ .. tS.fdO). 211 (Oct. lySb). Copyright 1956 by McCraw-Hill, ine.. New York. NY l()02().]... [Pg.15]

Figure 3-4 Batch reactor. (Schematic with permission by Renwahr.l... Figure 3-4 Batch reactor. (Schematic with permission by Renwahr.l...
Ring closure of nascent CH2=CHCH2CH2CHf within ion-neutral complexes has been studied using a specially designed Electron Bombardment Flow (EBFlow) reactor, schematically drawn in Figure 3. This apparatus has the advantage that the conditions under which ions are formed and react (70 eV electron impact pressure <0.001 mbar) closely parallel those in mass spectrometer sources. The neutral product yields are routinely interpreted with reference to the ionic products observed by the mass spectrometry. Hypotheses based on EBFlow results for ion neutral complexes are further tested by comparison with mass spectrometry. [Pg.239]

The reactor schematic is shown in Figure 1. Continuous stirred tank reactor (CSTR) experiments were conducted in a 50 mL Microclave from Autoclave Engineers, rated to 344 bar and 616 K. Catalyst particles were suspended in the reaction mixture by an impeller operating at 1200 RPM. Fixed-bed reactor experiments were conducted in a 1 I.D. stainless steel tubular reactor from Autoclave Engineers, rated to 1110 bar at 700 K. The catalyst bed was supported on both ends with glass wool (Alltech) and stainless steel mesh screens, which... [Pg.223]

Figure 2. Vortex Reactor Schematic. (Reproduced with permission from ref. 19. Copyright 1985 Solar Energy Research Institute.)... Figure 2. Vortex Reactor Schematic. (Reproduced with permission from ref. 19. Copyright 1985 Solar Energy Research Institute.)...
Figure 3. Lab reactor schematic in which the dynamic experiments were performed. Figure 3. Lab reactor schematic in which the dynamic experiments were performed.
Figure 9.2 Trickle bed reactor schematic (Maiti and Nigam, 2007). Figure 9.2 Trickle bed reactor schematic (Maiti and Nigam, 2007).
Figure 8.6 (a) Concentration profile in a catalytic microstructured film reactor (schematic) and (b) average liquid film thickness profile across a channel at various flowrates [11] (Adapted with permission from Elsevier.)... [Pg.338]


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See also in sourсe #XX -- [ Pg.344 , Pg.346 ]




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