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Title: Wet-air oxidation of TS-1S wastewater

Technical Report ·
OSTI ID:6047836

Tar sand wastewater has been treated using a bench-scale wet air oxidation process. The wastewater, designated TS-1S, was generated during in situ recovery of bitumen from Utah tar sand. After wet-air oxidation at 485/sup 0/F (252/sup 0/C) in the presence of air, the chemical oxygen demand (COD), total organic carbon (TOC), and total suspended solids (TSS) of the wastewater were reduced from 12,800, 3200, and 3860 mg/L to 285, 104, and 2 mg/L, respectively. Smaller reductions in COD, TOC, and TSS were achieved when the wastewater was wet oxidized at 422/sup 0/F (217/sup 0/C) and 466/sup 0/F (230/sup 0/C). The quantity of oxygen charged into the wet-air oxidation reactor was in excess of the amount required for oxidation and hence did not limit the rate of oxidation. The wet-air oxidation system recently developed at WRI was demonstrated to be effective in the destruction of organics at high temperatures and pressures. However, the equipment has limitations for kinetic studies of a low heating rate. A gas leak also occurred around the reactor packing seal. It is recommended that a complete thermal analysis of the reactor be made to identify modifications that will result in efficient heating of the reactor vessel. Improved temperature control will enhance the investigation of wastewater oxidation kinetics. 8 refs., 6 figs., 2 tabs.

Research Organization:
Western Research Inst., Laramie, WY (USA)
DOE Contract Number:
FC21-83FE60177
OSTI ID:
6047836
Report Number(s):
DOE/FE/60177-2424; ON: DE88000141
Resource Relation:
Other Information: Portions of this document are illegible in microfiche products. Original copy available until stock is exhausted
Country of Publication:
United States
Language:
English