. Journal. Pla. Eleojtion tortgfl t;inksII—Gas rooterI Mmrtia No. II>— „ So. 2B—1—Boiler ;.ii-» 1 lit:. Lie ! - K Vaponi lin< a tjnk Fig. 1,—Gasoline Extraction PlantCharcoal recovery process Vol. 24| REVIEW 551 a (rater drips, frequently from sprays in a coolingtower. The radiating area of the coils is usuallyOG—07 sq. ft. per 1000 cb. ft. of plant capacity . Run tank-, which collect the condensate directfrom the coils, are equipped with automatic trapsto discharge the condensate into storage discharge gas should be passed through anabsorption tower, preferably in c
. Journal. Pla. Eleojtion tortgfl t;inksII—Gas rooterI Mmrtia No. II>— „ So. 2B—1—Boiler ;.ii-» 1 lit:. Lie ! - K Vaponi lin< a tjnk Fig. 1,—Gasoline Extraction PlantCharcoal recovery process Vol. 24| REVIEW 551 a (rater drips, frequently from sprays in a coolingtower. The radiating area of the coils is usuallyOG—07 sq. ft. per 1000 cb. ft. of plant capacity . Run tank-, which collect the condensate directfrom the coils, are equipped with automatic trapsto discharge the condensate into storage discharge gas should be passed through anabsorption tower, preferably in contact withnaphtha to extract the last portions of gasoline. The plant, if possible, should he located doB railroad so as to provide for inexpensive shipmenti ili product; but many small plants ship theirproduct in steel drums, of 50 gallons capacity, bymeans of auto-trucks. Tin ii follow data covering lour compressiongasoline plants located in different parts ol theUnited States. less fuel. The i
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Keywords: ., bookcentury1800, bookdecade1880, booksubjectchemist, bookyear1882
