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| Titel: |
GAS HOLD-UP AND BACKMIXING IN A BUBBLE-COLUMN REACTOR UNDER COAL-HYDROLIQUEFACTION CONDITIONS |
| Auteur: |
Sangnimnuan, A. Prasad, G. N. Agnew, J. B. |
| Verschenen in: |
Chemical engineering communications |
| Paginering: | Jaargang 25 (1984) nr. 1-6 pagina's 193-212 |
| Jaar: |
1984-01-01 |
| Inhoud: |
Gas hold-up and the extent of liquid-phase backmixing have been investigated experimentally at room temperature and under coal hydroliquefaction conditions (viz. temperature 164 to 384°C and pressure between 4.5 to 15 MPa) using a continuous tubular bubble-column reactor of small diameter (1.9 cm) and large length to diameter ratio. Gas hold-up is affected by superficial gas velocity and temperature particularly above 300°C. The effects of superficial liquid velocity, gas molecular weight and pressure are negligible. Liquid-phase dispersion coefficient and Peclet number are strongly dependent on superficial gas velocity. The modified correlation of Hikita et al. (1980) for the fractional gas hold-up is found to fit the experimental data at high temperatures after corrections have been applied for dissolution of gas and liquid vaporization. Literature correlations derived from two- and three-phase systems are found to be inapplicable under coal hydroliquefaction conditions for vˆG < 1 cm/s. EL is found to vary proportionally with vˆG1.53. |
| Uitgever: |
Taylor & Francis |
| Bronbestand: |
Elektronische Wetenschappelijke Tijdschriften |
Details van artikel 10 van 24 gevonden artikelen
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