Power recovery for use in start-up or re-start of a pure terephthalic acid production process
a technology of pta and power recovery, which is applied in the direction of machines/engines, gas turbine plants, steam engine plants, etc., can solve the problems of adding additional complexity to the normal operation of the production process, and additional sources of high-grade heat, so as to improve the overall cost-effectiveness of the pta production process, improve the power and energy recovery system, and add additional complexity
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[0058]The following examples further illustrate the various aspects of the disclosed processes and systems. The mass and heat balances have been calculated based on the schematics shown in FIG. 1 for normal operation and FIG. 2 for interrupted operation, but other aspects show similar results.
[0059]Table 1 (below) assumes the use of high pressure (“HP”) steam and shows the relative mass flows, compared to the normal generation of high pressure steam, for the two modes of operation. For normal operation, ambient air is compressed and heated to about 365° C. before flowing to the combustor feed interchanger, where it is cooled, before feeding to the oxidation reactor. The gaseous stream vented from the oxidation reactor flows to a condenser to remove condensables, before the gaseous stream temperature is increased in the combustor feed interchanger and heater. The heated gaseous stream flows to the catalytic combustor, where volatile organics and other gaseous components are combusted...
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