This thesis looks at the implementation of various heat integration designs for a ditertiary butyl peroxide (DTBP) production plant. Heat integration, also known as process integration, is a common industrial practice in the chemical process industry to reduce utility costs. Heat integration is commonly analyzed using pinch technology, which focuses producing a heat exchanger design that pairs hot streams with excess energy with cold streams that need to be heated. These designs usually cut utility costs, but they also require the building of more heat exchangers to place within the process
