The report includes recommendations on flow sketches; 68% nitric acid specifications; dissolver off-gas and ventilation air treatment; installation of standby equipment (details included in Appendix A); schedule of scope drawing specifications and arrangement drawings; mechanical development program (details included in Appendix B); and scope of work on waste disposal facilities (Appendix C).

No administrative or operations significant events are reported. Construction in the pile areas, separations areas, and the technical center is reported. The Southern Railroad connection, Richland paving and related work, and housing work is described. Personnel and visitor data is presented.

Many questions have been raised concerning the advisability of continuing the presently scheduled Redox design and construction program in performance to other uranium recovery processes. In order to answer these questions properly, an extensive re-examination of the Redox process objectives and status and a careful study of other possible alternative uranium recovery processes have been carried out by the Hanford Works. This survey has included consideration of both existing process and facilities for plutonium separations, the Redox process, the Carbide and Carbon Uranyl Ammonium Phosphate process, uranium solvent extraction alone, and various combinations and couplings of parts or entities of the above. Comparative evaluation has been based on the relative assurance of obtaining both plutonium and uranium production; recovery of both ``aged`` and ``current`` metal wastes; timing for developing, design, and construction; economics of capital investment and operating costs; and process complexity, adaptability, and safety. This survey has resulted in conclusions and recommendations for a unified program of separations process development, design, and construction. It is the purpose of this letter to present these conclusions and recommendations, together with a brief summary of the reasons leading to their establishment.

By test duplicating actual operating conditions the average load was found to have a power factor of 95 percent and to be about 75 percent rated load. Since the Sola transformers must be operating into a load having a power factor of 90 percent and about 85 percent rated to attain proper output voltage, power factor corrective networks consisting of inductance and resistance in series were paralleled with the load. When these networks were added, the desired output voltage was attained. Several units have been successfully correction be used on the remaining units.

An experimental range-energy relation in Ilford C-2 emulsion has been obtained for proteins up to 39.5 Mev. In the region from 17 to 33 Mev the relation for dry emulsion is fitted by the empirical equation E{sub (MeV)} = 0.251 R{sub ({mu})} 0.581. Variations in water content due to changes in atmospheric humidity make several percent difference in range. The range in Ilford glass is found to be 18 {+-} 4 percent longer than in dry C-2 emulsion.

None

Apparatus for measuring the resistivity of polonium is described. This equipment has been built and tested. No resistivity measurements were made, however, because the method of determining the purity of the sample has not been perfected.

Experimental use of sodium radiophosphate (P32)in treatment of polycythemia is described. Treatment history is 66 patients treated with P32 alone, 32 patients treated with P32 followed within 4 months by venesections, 21 patients treated with P32 followed more than 4 months later by venesections, 6 patients treated exclusively by venesections, and 9 patients treated and followed elsewhere.