Document Type

Thesis

Date of Award

5-31-1970

Degree Name

Master of Science in Chemical Engineering - (M.S.)

Department

Chemical Engineering and Chemistry

First Advisor

Deran Hanesian

Second Advisor

John E. McCormick

Third Advisor

Saul I. Kreps

Abstract

The production of Sulfuric Acid at elevated pressures is presented with the economics for operating at one, three, five, seven, nine and thirteen atmospheres. The conventional and pressure plants are compared operating on the same basis.

The basis for a pressure plant design is obtained from an I.B.M. 1130 computer program developed for One Thousand Net Tons per Day of Sulfuric Acid. Recognized operating conditions for a conventional acid plant are incorporated in the pressure plant design program.

Sulfuric Acid manufacture with operating pressures higher than atmospheric, but less than five atmospheres, results in maximum rate of return on investment and operating economy.

A compressor and gas expander arrangement can significantly reduce operating costs in a pressure plant without sacrifice to the steam generation capabilities associated with sulfuric acid production.

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