PROCESSES FOR ADJUSTING AT LEAST ONE PROCESS CONDITION OF A CHEMICAL PROCESSING UNIT WITH A TURBINE

    公开(公告)号:US20190284950A1

    公开(公告)日:2019-09-19

    申请号:US15923997

    申请日:2018-03-16

    Applicant: UOP LLC

    Abstract: Processes for controlling at least one process condition of a chemical processing unit with a turbine. In the processes, a flow of a fluid is adjusted with a turbine in order to provide the fluid with a flow associated with at least one process condition of a chemical processing unit. The turbine wheel is rotated within the turbine, and the turbine wheel is configured to transmit rotational movement to an electrical generator. The resistance of the turbine is modulated and adjusts the flow of the fluid through the turbine. A response time of at least one steady state process condition to a new steady state process condition of at least 10% difference is at least one second to reach 50% of the difference between the at least one steady state process condition and the new steady state process condition after modulating the resistance of the turbine.

    HYDROPROCESSING UNIT WITH POWER RECOVERY TURBINES

    公开(公告)号:US20190284488A1

    公开(公告)日:2019-09-19

    申请号:US15923978

    申请日:2018-03-16

    Applicant: UOP LLC

    Abstract: Methods and apparatus for recovering power in a hydroprocessing process are described. The method involves the use of a power-recovery turbine in place of, or in addition to, a control valve. A hydrocarbon feed stream is combined with a portion of a hydrogen stream. The combined stream is heated, and the heated stream is introduced into a hydroprocessing reaction zone having at least two beds. The heated stream is contacted with a first hydroprocessing catalyst to form a first hydroprocessed stream. At least part of a portion of the hydrogen stream is combined with the first hydroprocessed stream to form a first quenched hydroprocessed stream. The first quenched hydroprocessed stream is contacted with a second hydroprocessing catalyst to form a second hydroprocessed stream. At least a portion of the second portion of the hydrogen stream is directed through a power-recovery turbine to generate electric power.

    System and process for recovering products using simulated-moving-bed adsorption
    16.
    发明授权
    System and process for recovering products using simulated-moving-bed adsorption 有权
    使用模拟移动床吸附回收产品的系统和过程

    公开(公告)号:US08992779B2

    公开(公告)日:2015-03-31

    申请号:US13630698

    申请日:2012-09-28

    Applicant: UOP LLC

    CPC classification number: B01D15/1835 C07C7/13 C07C15/08

    Abstract: A process according to various approach includes flushing an intermediate transfer line between the first intermediate transfer line and the extract stream transfer line away from the adsorptive separation chamber to remove residual fluid from intermediate transfer line. The process may include directing the residual fluid flushed from the intermediate transfer line to a recycle stream to introduce the residual fluid into the adsorptive separation chamber.

    Abstract translation: 根据各种方法的方法包括将第一中间转移管线和提取物流输送管线之间的中间转移管线冲洗离开吸附分离室以从中间转移管线去除残留流体。 该方法可以包括将从中间转移管线冲洗的残余流体引导至再循环流,以将剩余流体引入吸附分离室。

    SYSTEM AND PROCESS FOR RECOVERING PRODUCTS USING SIMULATED-MOVING-BED ADSORPTION
    17.
    发明申请
    SYSTEM AND PROCESS FOR RECOVERING PRODUCTS USING SIMULATED-MOVING-BED ADSORPTION 有权
    使用模拟移动式吸盘回收产品的系统和过程

    公开(公告)号:US20130153504A1

    公开(公告)日:2013-06-20

    申请号:US13630698

    申请日:2012-09-28

    Applicant: UOP LLC

    CPC classification number: B01D15/1835 C07C7/13 C07C15/08

    Abstract: A process according to various approach includes flushing an intermediate transfer line between the first intermediate transfer line and the extract stream transfer line away from the adsorptive separation chamber to remove residual fluid from intermediate transfer line. The process may include directing the residual fluid flushed from the intermediate transfer line to a recycle stream to introduce the residual fluid into the adsorptive separation chamber.

    Abstract translation: 根据各种方法的方法包括将第一中间转移管线和提取物流输送管线之间的中间转移管线冲洗离开吸附分离室以从中间转移管线去除残留流体。 该方法可以包括将从中间转移管线冲洗的残余流体引导至再循环流,以将剩余流体引入吸附分离室。

    SYSTEM AND PROCESS FOR RECOVERING PRODUCTS USING SIMULATED-MOVING-BED ADSORPTION
    18.
    发明申请
    SYSTEM AND PROCESS FOR RECOVERING PRODUCTS USING SIMULATED-MOVING-BED ADSORPTION 审中-公开
    使用模拟移动式吸盘回收产品的系统和过程

    公开(公告)号:US20130153502A1

    公开(公告)日:2013-06-20

    申请号:US13630447

    申请日:2012-09-28

    Applicant: UOP LLC

    CPC classification number: B01D15/1828 C07C7/13 C07C15/08

    Abstract: In a process for separating components in a feed stream by simulated countercurrent adsorptive separation, the process according to various aspects includes withdrawing an extract stream through one transfer line that contains residual fluid away from the adsorptive separation chamber. The process also includes directing an initial portion of the extract stream, including at least a portion of the residual fluid withdrawn through the one transfer line toward a first destination. The process further includes directing a subsequent portion of the extract stream withdrawn through the one transfer line toward a second destination.

    Abstract translation: 在通过模拟的逆流吸附分离分离进料流中的组分的方法中,根据各个方面的方法包括通过包含残留流体远离吸附分离室的一条传输管线抽出提取物流。 该方法还包括引导提取物流的初始部分,包括通过一条传送线排出的剩余流体的至少一部分朝向第一目的地。 该过程还包括将通过一条传输线撤销的提取流的后续部分引向第二目的地。

    Processes for adjusting at least one process condition of a chemical processing unit with a turbine

    公开(公告)号:US11131218B2

    公开(公告)日:2021-09-28

    申请号:US15923997

    申请日:2018-03-16

    Applicant: UOP LLC

    Abstract: Processes for controlling at least one process condition of a chemical processing unit with a turbine. In the processes, a flow of a fluid is adjusted with a turbine in order to provide the fluid with a flow associated with at least one process condition of a chemical processing unit. The turbine wheel is rotated within the turbine, and the turbine wheel is configured to transmit rotational movement to an electrical generator. The resistance of the turbine is modulated and adjusts the flow of the fluid through the turbine. A response time of at least one steady state process condition to a new steady state process condition of at least 10% difference is at least one second to reach 50% of the difference between the at least one steady state process condition and the new steady state process condition after modulating the resistance of the turbine.

Patent Agency Ranking