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An experiment on improving tar-distillation technology

Journal Article · · Coke Chem. USSR (Engl. Transl.); (United States)
OSTI ID:6507872
The naphthalene recovery coefficient in the distillation stages amounted to 71% at that time (88% was projected) when the naphthalene content in the naphthalene fraction was low (79.1%). The quality of the absorbent fraction varied greatly. After inspecting the precipitate, a number of projects were undertaken with a view to improving the distillation process, stabilizing conditions, and increasing the efficiency of the distillation columns. The columns were redesigned. Whereas, earlier, the vapor fractions were sent under the fourth tray after the second-level evaporator (i.e., only 56 of the 59 trays in the rectification process were used), after redesign, vapor delivery was effected under the second tray. This increased the number of trays used in rectification to 58 and ensured that they would work continuously without the introduction of supplementary heat. Isolation of the columns and evaporators of the second level was realized using a slab made from a mixture of MgO, CaCO/sub 3/, and asbestos, which was plastered using an asbestos-cement solution. Complete redesign of the monitoring and measuring instrument with a change of the out-of-date devices for new ones was also realized.
Research Organization:
Karaganda Metallurgical Combine
OSTI ID:
6507872
Journal Information:
Coke Chem. USSR (Engl. Transl.); (United States), Journal Name: Coke Chem. USSR (Engl. Transl.); (United States) Vol. 1; ISSN COKCA
Country of Publication:
United States
Language:
English