TITLE: Hydrodynamics of Fischer-Tropsch Synthesis in Slurry Bubble Column Reactors: Final Report.

AUTHOR: D. B. Bukur; J. G. Daly; S. A. Patel; M. L. Raphael; G. B. Tatterson.

INST.  AUTHOR: Texas A and M Univ., College Station.

SPONSOR: Department of Energy, Washington, DC.

LANGUAGE: English

PUB.  TYPE: Technical Report

PUB.  COUNTRY: United States

SOURCE: Department of Energy [DE],  Jun 87,  329p.

NTIS ORDER NO.: DE88000383/INW

ABSTRACT:

This report describes studies on hydrodynamics of bubble columns for Fischer-Tropsch synthesis. These studies were carried out in columns of 0.051 m and 0.229 m in diameter and 3 m tall to determine effects of operating conditions (temperature and gas flow rate), distributor type (sintered metal plate and single and multi-hole perforated plates) and liquid media (paraffin and reactor waxes) on gas hold-up and bubble size distribution. In experiments with the Fischer-Tropsch (F-T) derived  paraffin wax (FT-300) for temperatures between 230 and 280 sup 0 C there is a range of gas velocities (transition region) where two values of gas hold-up (i.e., two flow regimes) are possible. Higher hold-ups were accompanied by the presence of foam (''foamy'' regime) whereas lower values were obtained in the absence of foam (''slug flow'' in the 0.051 m column, or ''churn-turbulent'' flow regime in the 0.229 m column). This type of behavior has been observed for the first time in a system with molten paraffin wax as the liquid medium. Several factors which have significant effect on foaming characteristics of this system were identified. Reactor waxes have much smaller tendency to foam and produce lower hold-ups due to the presence of larger bubbles. Finally, new correlations for prediction of the gas hold-up and the specific gas-liquid interfacial area were developed on the basis of results obtained in the present study. 49 refs., 99 figs., 19 tabs. (ERA citation 13:010674)

REPORT  NUMBER: DOE/PC/70027-10

CONTRACT  NUMBER: AC22-84PC70027