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dc.contributor.authorElmarghani, Mohamed Abdusalam,en_US
dc.date.accessioned2013-08-16T12:28:56Z
dc.date.available2013-08-16T12:28:56Z
dc.date.issued1983en_US
dc.identifier.urihttps://hdl.handle.net/11244/5158
dc.description.abstractAmmoniacal nickel sulfate solution treated with ferrous sulfate (nucleating agent) was contacted with hydrogen in a continuous countercurrent tubular reactor. Bottom products (liquid-solid) and overflow products (gas-liquid) were separated in individual high pressure separators. Nickel conversion, and ultimately the yield to metallic nickel, were found to depend on: reactor temperature, pressure, residence time, pH, excess hydrogen input and concentrations of ferrous and ammonium sulfates in feed solution. With 25% excess hydrogen, 3580 Kpa and a residence time of 5 minutes, 90 percent yield was obtained at 193(DEGREES)C in a single pass. Several experiments were made to find a suitable nucleating agent for cobalt reduction. The results indicated that colloidal graphite as well as the mixture of sodium sulfide-potassium cyanide nucleated cobalt in 5 minutes of residence time under the conditions of 3580 to 5753 Kpa and 220(DEGREES)C. For essentially complete conversion and 90 percent yield in a single pass, longer residence times (20-30 minutes) were required under the above conditions of temperature and pressure.en_US
dc.format.extentxvi, 234 leaves :en_US
dc.subjectEngineering, Metallurgy.en_US
dc.titleContinuous reduction of nickel and cobalt from ammoniacal sulfate solutions by hydrogen in a tubular reactor /en_US
dc.typeThesisen_US
dc.thesis.degreePh.D.en_US
dc.thesis.degreeDisciplineSchool of Chemical, Biological and Materials Engineeringen_US
dc.noteSource: Dissertation Abstracts International, Volume: 44-06, Section: B, page: 1933.en_US
ou.identifier(UMI)AAI8324886en_US
ou.groupCollege of Engineering::School of Chemical, Biological and Materials Engineering


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