ETHYLENE OXIDE PURIFICATION
    2.
    发明申请

    公开(公告)号:US20220348528A1

    公开(公告)日:2022-11-03

    申请号:US17760680

    申请日:2020-09-03

    Inventor: Brian J. Ozero

    Abstract: An improved process for the recovery of high-purity ethylene-oxide water feed streams to EO purification and MEG reaction units when both are operating in EO plants that incorporate EO Stripper bypass technology, by installing a second lights stripper to exclusively degasify the diluted EO feed to the MEG reactor, thus permitting the use of additional bypassed (gasified) EO absorbate as the diluent and resulting in a substantial increase in the total amount of EO absorbate that can bypass the EO Stripper.

    Process and reactor for dehydration of butanol to butylenes
    3.
    发明授权
    Process and reactor for dehydration of butanol to butylenes 有权
    丁醇脱水至丁烯的工艺和反应器

    公开(公告)号:US09340470B2

    公开(公告)日:2016-05-17

    申请号:US13727024

    申请日:2012-12-26

    CPC classification number: C07C1/24 C07C2521/04 C07C11/08

    Abstract: A reactor design and configuration and a process for the catalytic dehydration of butanol to butylenes where the reactor train is comprised of a multi-stage single reactor vessel or multiple reactor vessels wherein each stage and/or vessel has different length, internal diameter, and volume than the other stages and/or vessels and in addition the stages and/or reactor vessels are connected in series or in parallel arrangement, preferably used with an improved means of introducing the butanol feedstock and a heat carrying inert gas to the improved reactor train.

    Abstract translation: 反应器设计和构型以及将丁醇催化脱水至丁烯的方法,其中反应器系由多级单反应器容器或多个反应器容器组成,其中每个级和/或容器具有不同的长度,内径和体积 并且另外阶段和/或反应器容器串联或并联布置连接,优选地与改进的将丁醇原料和携带惰性气体引入到改进的反应器系列中的方法一起使用。

    Ethylene oxide purification
    4.
    发明授权

    公开(公告)号:US11608305B2

    公开(公告)日:2023-03-21

    申请号:US17760680

    申请日:2020-09-03

    Inventor: Brian J. Ozero

    Abstract: An improved process for the recovery of high-purity ethylene-oxide water feed streams to EO purification and MEG reaction units when both are operating in EO plants that incorporate EO Stripper bypass technology, by installing a second lights stripper to exclusively degasify the diluted EO feed to the MEG reactor, thus permitting the use of additional bypassed (gasified) EO absorbate as the diluent and resulting in a substantial increase in the total amount of EO absorbate that can bypass the EO Stripper.

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