• Journal of the Korea Concrete Institute
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• v.12 no.1
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• pp.113-125
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• 2000

The purpose of this study was to examine the durability characteristics of controlled low strength material(flowable fill) with high volume fly ash content. Flowable fill refer to self-compacted, cementitious material used primarily as a backfill in lieu of compacted fill. The two primary advantages of flowable fill over traditional methods are its ease of placement and the elimination of settlement. Therefore, in difficult compaction areas or areas where settlement is a concern, flowable fill should be considered. The fly ash used in this study met the requirements of KS L 5405 and ASTM C 618 for Class F material. The mix proportions used for flowable fill are selected to obtain low-strength materials in the 10 to 15kgf/$\textrm{cm}^2$ range. The optimized flowable fill was consisted of 60kg f/$\textrm{m}^3$ cement content, 280kgf/$\textrm{m}^3$ fly ash content, 1400kgf/$\textrm{m}^3$ sand content, and 320kgf/$\textrm{m}^3$ water content. Subsequently, durability tests including permeability, warm water immersion, repeated wetting & drying, freezing & thawing for high volume fly ash-flowable fill are conducted. The results indicated that flowable fill has acceptable durability characteristics.

• KSCE Journal of Civil and Environmental Engineering Research
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• v.14 no.2
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• pp.367-378
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• 1994

The wastewater treatment characteristics of the fluidized bed filled with sand media and intermediately aerated were studied experimentally, and the obtained results were as follows; 1. The formations of biofilm on the media were greatly affected by the recirculation velocities. 2. Under the experimental condition that BOD loading rate was $4.2kg-BOD_5/m^3{\cdot}d$, the optimum media concentration was $261kg/m^3$ and the optimum recirculation velocity 1.35 cm/sec. 3. For the effluent quality of 20 mg-BOD/l and 20 mg-SS/l, the maximum allowable loading rate was about $8kg-BOD_5/m^3{\cdot}d$. 4. The dry density of biofilm was about 5.6% regardless of the filled media quantities and recirculation velocities. 5. Under the experimental conditions, the effluent solids concentration was below 20 mg/l, and the elimination of final clarifier can be expected.