- Page 1: Forschungszentrum Karlsruhe Technik
- Page 4 and 5: Als Manuskript gedruckt Für diesen
- Page 6 and 7: Tagungsband der internationalen GVC
- Page 8 and 9: Table of Contents Polymers Key Lect
- Page 10 and 11: High-pressure apparatus for phase e
- Page 12 and 13: B.E.S.T. Ventil+Fitting GmbH Heinri
- Page 14: Polymers 3
- Page 17 and 18: ) Precipitation thresholds or polym
- Page 19 and 20: solubility of the polymer in the fl
- Page 21: Cationic polymerizations are normal
- Page 25 and 26: 16. M. Super, E. Berluche, C. Coste
- Page 27 and 28: 1-hexene 97 wt% Acros vinyl acetate
- Page 29 and 30: acetate / ethylene / nitrogen decre
- Page 31 and 32: optical high-pressure cell monomer
- Page 33 and 34: 9.5 7,5 '—>—•—I—>—I—>
- Page 35 and 36: use of homogeneous catalysts in scC
- Page 37 and 38: [9] Yakoumis, I.V., Vlachos, K., Ko
- Page 39 and 40: directly related with the nucleatio
- Page 41 and 42: MMA), and stabilizer (5.0358 g). Th
- Page 43 and 44: kg/mol. Table 2 gives the pseudocom
- Page 46 and 47: GVC-Fachausschuß „High Pressure
- Page 48 and 49: adequately described by using the s
- Page 50 and 51: GVC GVC-Fachausschuß „High Press
- Page 52: criterion of successful modificatio
- Page 55 and 56: Silica used for supercritical fluid
- Page 57 and 58: from experiment B21 with the base -
- Page 59 and 60: in different separators. The unit w
- Page 61 and 62: Conclusions The reported results sh
- Page 63 and 64: pressures a part of the solvent eva
- Page 66 and 67: GVC GVC-Fachausschuß,.High Pressur
- Page 68 and 69: Using the SWP EOS one can calculate
- Page 70 and 71: GVC-Fachausschuß,Jügh Pressure Ch
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Results are shown in Figure 3. It c
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Taking into account the fluid mecha
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66 1
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Experimental The complete set-up is
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70 i
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72 !
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GVC-Fachausschuß „High Pressure
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Pressure M e d i u m Firstly, we re
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Extractor 226 Itrs, ID 400, 350 bar
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GVC-Fachausschuß ,Jügh Pressure C
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Tab. 4: Results with industrial was
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Another challenge connected with de
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GVC-Fachausschuß„High Pressure C
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GVC-Fachausschuß „High Pressure
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eflects the supercritical behavior,
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6. Davies, IT.; Chem. Eng. Sei.; 19
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-1.5 T 1 P j—1 1 p 1 1— 1 3 5 !
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100
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The temperature of the reactor mate
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Both process streams, the organic p
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cated slightly above those of the f
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au v + c-b (v + c)(v + c + b) with
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the real ones [24], but the more ad
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Fig. 2: Picture of the tumbling rea
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Table 1: Batch experiments Reactant
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116
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118
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Results and Discussion By changing
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122
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Figure 2. Scheme of experimental ap
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glucose yields are in a narrow rang
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CO Ö O 'S ! o d o O Gas eq Liquid
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mol/gcataiysh, we have achieved rea
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selectivity for mono-alkylation and
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Table 1. Oxide aerogels designation
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hydrogenation of soybean oil. Their
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«2 1X3 1 Stmpti t>
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PYROLYSIS T(C) —•— 0,5 MPa H2
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142
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144
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X hyd=X s(T,p)-XlHT,p t) (5) where
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expansion is obtained. By comparing
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the thermodynamic cycle (Figure 1)
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FIGURE 2: Scheme of the apparatus (
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three phase equilibrium. fi(T,p,y 1
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from a thermostated bath. The screw
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200 100 O 313.1 K + 323.1K • 333.
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summarize briefly, the anthraquinon
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atio vs. time is about constant, th
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0 0 0 ^ ^ Header Cooler P2 Ni Ff# i
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800 S 600 200 300 Pressure [bar] Fi
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Figure 1. A: Buffer Volume B: Press
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40. Figure 6. Experimental (• thi
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available PSRK / UNIFAC parameters
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Results and Discussion Some typical
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lower temperatures to a much strong
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Detennination of solubility For det
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The same phase behaviour show for e
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182
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184
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14 0 2 4 6 8 10 12 14 gC02/g solid
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ed carotenoids (capsanthin and caps
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flowing from top to bottom. The out
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Extraction of Lemon oil O 0 u Men t
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Experimental Methods The high-press
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The size of the phase surface area
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Extraction experiments were carried
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1 1 1 1 1 1 1 1 1 1 1 1 1 r— 0,5
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solid material and therefore also b
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these two substances in the extract
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are mentioned in Table 1. The valve
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Figure A.Mentha M A % area trans-sa
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albumin (purity > 98 %, fatty acid
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& Isobutanol & Acetone & EtOH & MEO
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214
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about 278 K. The 99,9 % carbon diox
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At constant temperature the solubil
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220
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222
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224
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In a pressure vessel, the substance
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mixing process. In fig. 6 a thermog
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A complete release of active ingred
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system. The phase transition pressu
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4 Figure 7. SEM photography of micr
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The primary solution was fed with a
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16 0 1 , , , ~ , 1 40 50 60 70 80 9
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Model In order to elucidate the rol
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1200 1000 £ 800 I eoo I
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the particles by Scanning Electron
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where v is the molecular volume of
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dissolution power of the fluid. Thi
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up to 4 pm. The particles are agglo
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process starts and continues for se
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11. York, P.; Hanna, M. Salmeterol
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256
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258
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The non-ideality of the fluid phase
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262
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11.3 vol%. This low raffinate conce
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temperature lowers the ethanol conc
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hydrodynamic behaviour of packed co
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detected at a pressure of 16.4 MPa,
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) Diketones Zinc chloride (21.6 g,
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alcane N° type Feed (mg.) At (1 >
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• Micell Technologies Corp., Rale
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Under higher pressure the polarity
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Fluid compression Two possible flui
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QU Mass flowmeter -A- Manual valve
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•HxH c=>-tX Modifier Compressed a
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operating point FA. A A. A A . A A
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Kohlensäurewerke Deutschland. Labo
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Fig. 3 shows the liquid hold-up and
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292
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Results Patent view of selected bra
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- chemistry with polymers and react
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asket upper section. At that moment
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Influence of the amount of oil to e
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covers a wide range of metal workin
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[1] J. Schön, N. Dahmen, H. Schmie
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Other chemical-physical processes f
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308
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Lüdemann, H.-D. 173 Luft, G. 15, 4