POWER RECOVERY FOR USE IN START-UP OR RE-START OF A PURE TEREPHTHALIC ACID PRODUCTION PROCESS
    1.
    发明申请
    POWER RECOVERY FOR USE IN START-UP OR RE-START OF A PURE TEREPHTHALIC ACID PRODUCTION PROCESS 审中-公开
    电源恢复用于启动或重新启动纯正庚酸生产过程

    公开(公告)号:WO2014189818A1

    公开(公告)日:2014-11-27

    申请号:PCT/US2014/038546

    申请日:2014-05-19

    Abstract: The invention relates to a method and system for recovering power from the gaseous stream produced by a paraxylene - air oxidation reaction. Specifically, the invention is based on heating the gaseous stream from the oxidation reaction to a temperature of at least 600°C, recovering energy through an expander, heating the expander vent stream and recovering heat from the vent stream. The recovered heat is used to maintain the oxidation process, purification process, start-up the process, or re¬ start the process after an interruption.

    Abstract translation: 本发明涉及一种从对二甲苯 - 空气氧化反应产生的气流中回收功率的方法和系统。 具体地,本发明基于将来自氧化反应的气流加热到至少600℃的温度,通过膨胀器回收能量,加热膨胀机排放流并从排气流中回收热量。 回收的热量用于维持氧化过程,净化过程,启动过程,或在中断后重新启动过程。

    POWER RECOVERY
    2.
    发明公开
    POWER RECOVERY 审中-公开
    电源恢复

    公开(公告)号:EP2384394A2

    公开(公告)日:2011-11-09

    申请号:EP09742342.0

    申请日:2009-05-06

    Abstract: The invention relates to a method and apparatus for recovering power from the gaseous stream produced by an oxidation reaction. Specifically, the invention is based on heating the gaseous stream from the oxidation reaction to a temperature of at least 800 °C and recovering energy through a gas turbine. The compressor stage of the gas turbine compresses the oxidant feed to the reactor thereby at least partially offsetting the cost of providing the high temperature and pressure reaction conditions in the reactor. The invention also provides improved control of the power recovery system by optimising the efficiency of the gas turbine by feeding gas to the gaseous stream to modulate the flow of gas to the turbine relative to the compressor discharge flow in order to compensate for the consumption of oxidant in the reactor.

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