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Ambient pressure flow cell

Figure 9. Modified Schlenk flask for ambient pressure flow cell system. Figure 9. Modified Schlenk flask for ambient pressure flow cell system.
Addition funnel pressure reactor, 201 Adjustable pressure relief valve, 200 Aerial oxidation, 64 Aerobic product transfer, 193 Aerosol pressure vessel, 198 Air-sensitive materials decomposition, 147 HPLC analysis, 24 recovering, 193 synthesis and handling, 34 Alkyne electron density, 287 Alkyne ligand, 282 Alkyne it donor orbitals, 287 Alkyne levels, 285 Ambient pressure flow cell, 238-244 Ammonia synthesis, 182 Anaerobic column chromatography, 17-18/ Anaerobic transfer, 144 Anionic polymerization, 182 Apparatus design philosophy, 117 Arc lamp... [Pg.290]

There has been an accelerated interest in polymer electrolyte fuel cells within the last few years, which has led to improvements in both cost and performance. Development has reached the point where motive power applications appear achievable at an acceptable cost for commercial markets. Noticeable accomplishments in the technology, which have been published, have been made at Ballard Power Systems. PEFC operation at ambient pressure has been validated for over 25,000 hours with a six-cell stack without forced air flow, humidification, or active cooling (17). Complete fuel cell systems have been demonstrated for a number of transportation applications including public transit buses and passenger automobiles. Recent development has focused on cost reduction and high volume manufacture for the catalyst, membranes, and bipolar plates. [Pg.81]

Influence of PTFE content in the anode DL of a DMFC. Operating conditions 90°C cell temperature anode at ambient pressure cathode at 2 bar pressure methanol concentration of 2 mol dm methanol flow rate of 0.84 cm min. The air flow rate was not specified there was a parallel flow field for both sides. The anode catalyst layer had 13 wt% PTFE, Pt 20 wt%, Ru 10 wt% on Vulcan XC-73R carbon TGP-H-090 with 10 wt% PTFE as cathode DL. The cathode catalyst layer had 13 wt% PTFE, Pt 10 wt% on carbon catalyst with a loading 1 mg cm Pt black with 10 wt% Nafion. The membrane was a Nafion 117. (Reprinted from K. Scott et al. Journal of Applied Electrochemistry 28 (1998) 1389-1397. With permission from Springer.)... [Pg.233]

A modification of the Nelson and Eggertsen method was made by Haley who also used helium and nitrogen in a continuous flow system. Haley s apparatus differs from that described in the previous chapter in that the sample cell can be pressurized while the effluent flows from a pressure regulator through the cell to a flow controller and then to the detector maintained at ambient pressure. [Pg.183]

Figure 8. Ambient pressure glass (macro) flow cell. (Photograph courtesy of Spectra-Tech, Inc.)... Figure 8. Ambient pressure glass (macro) flow cell. (Photograph courtesy of Spectra-Tech, Inc.)...
The pressure is released after a suitable time interval, and the contents of the chambers are sampled using syringes and PTFE tubing. It is important to keep the cell thermally stable during the sampling to avoid temperature-induced flows. The drop in pressure has two effects. It causes a cooling of the cell contents and a small but unavoidable amount of bulk flow of material from top to bottom. It is therefore essential to stir the cell for several minutes after reaching ambient pressure, to attain thermal stability and to ensure a uniform composition of the bottom compartment. The concentrations of labelled material in the compartments are determined by liquid-scintillation techniques. The effects of the bulk flow must be taken into account, and equations have been developed for this purpose. ... [Pg.245]

The most common and useful detector used in SEC is the differential RI. These are simple to use and largely maintenance-free. Unfortunately, they are temperature-sensitive, and should be installed in a room with a reasonably constant ambient temperature and away from draughts and direct sunlight. Some of the more expensive, modern instruments have built-in thermostatic control. If an additional detector is incorporated into the system then this should be installed between the column and RI detector. The flow cells in RI detectors cannot withstand very high pressures and must therefore be connected to the end of the system to avoid excessive back pressure. All tube connections should be made with 0.01" bore s/s tubing, the length of which should be kept to a minimum. [Pg.38]

One of the major advantages of SFC is its compatibility with both GC and HPLC detectors. GC flame detectors, such as the flame ionization detector (FID) [11,12], nitrogen thermionic detector [12,13], and flame photometric detector [14] have all been interfaced with SFC systems using a capillary restrictor which, while maintaining supercritical conditions in the column, also effectively decompresses the fluid to ambient pressure just before it enters the flame tip [10,15]. HPLC detectors such as ultraviolet and fluorescence detectors are employed when pure organic mobile phases or modified mobile phases are used. With these detectors, analytes are detected spectroscopically in a flow-through cell prior to decompression [16]. [Pg.223]

The number of cells nucleated is a function of the supersaturation level relative to the equilibrium concentration at ambient pressure at the processing temperature. The higher the supersaturation level, the greater is the number of cells nucleated. Furthermore, since the amount of dissolved gas that fills the nucleated cells is finite, and since all the cells are nucleated almost simultaneously, the gas distributes more or less evenly among all these cells—a condition for making MCPs. The final bubble size is then determined by the total amount of gas per bubble, and by the flow characteristics of the polymer at the nucleation temperature. [Pg.4654]

Figure 4.65. Performance comparison of DMFC equipped with extended reaction zone anode composed of pressed graphite felt with PtRu and PtRuMo, obtained by electrodeposition from a colloidal solution [86, 250], a) 333 K, b) 343, and 353 K. Anode catalyst characteristics are given in Table 4.4. Anolyte 1 M CH3OH - 0.5 M H2SO4, 5 mL min, ambient pressure. Cathode 4 mg cm Pt black, O2 flow rate 500 nil min at 2 atm (abs). [86]. (Reprinted from Journal of Power Sources, 167(2), Bauer A, Gyenge EL, Oloman CW, Direct methanol fuel cell with extended reaction zone anode PtRu and PtRuMo supported on graphite felt, 281-7, 2007, with permission from Elsevier.)... Figure 4.65. Performance comparison of DMFC equipped with extended reaction zone anode composed of pressed graphite felt with PtRu and PtRuMo, obtained by electrodeposition from a colloidal solution [86, 250], a) 333 K, b) 343, and 353 K. Anode catalyst characteristics are given in Table 4.4. Anolyte 1 M CH3OH - 0.5 M H2SO4, 5 mL min, ambient pressure. Cathode 4 mg cm Pt black, O2 flow rate 500 nil min at 2 atm (abs). [86]. (Reprinted from Journal of Power Sources, 167(2), Bauer A, Gyenge EL, Oloman CW, Direct methanol fuel cell with extended reaction zone anode PtRu and PtRuMo supported on graphite felt, 281-7, 2007, with permission from Elsevier.)...
Once testing was completed, the RD was drained to atmosphere through the Cell 7 heat exchanger (HEX) and vent stack. Residual vapors in the flow system were purged using dry GHe. Then both the ST and RD were brought back to ambient pressure. Videos of the LAD screen were transferred to an external hard drive to be analyzed post-test. [Pg.121]


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See also in sourсe #XX -- [ Pg.238 , Pg.239 , Pg.240 , Pg.241 , Pg.242 , Pg.243 ]




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