"Bench scale evaluation of the solid-liquid separation steps in the for" by Darryll Glen Rasnake
 

Masters Theses

Date of Award

5-1989

Degree Type

Thesis

Degree Name

Master of Science

Major

Chemical Engineering

Major Professor

Atul C. Sheth

Committee Members

Lloyd W. Crawford, James N. Chapman

Abstract

Coal-Fired Open-Cycle Magnetohydrodynamics (MHD) power generation system requires the use of a sulfur-free potassium salt as a seed material. This potassium seed when added to the coal before combustion serves the two-fold purpose of increasing plasma conductivity in the MHD channel and removing environmentally offensive sulfur compounds from the flue gas by forming K2SO4. Most of the seed material (over 85%) is collected in the form of potassium sulfate in the downstream particulate collection devices, with the remaining potassium being tied up as potassium aluminosilicates in the radiant furnace slag. Because of the high cost of fresh seed and limited commercial use of K2SO4, the disposal of spent seed is not economically feasible. Thus, a seed reprocessing scheme must be developed to collect and regenerate the spent seed.

In this work, the Formate Process-Based Seed Reprocessing Option is considered. A complete solid-liquid separation (SLS) system to recover the soluble potassium sulfate from spent seed is developed. Additionally, a SLS system to remove the insoluble gypsum formed in the Formate reactor is developed. Preliminary economics of the proposed solid-liquid separation system are completed and related to the overall cost of the Formate Process.

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