PROCESS AND APPARATUS FOR THE SIMULATED COUNTER-CURRENT PRODUCTION OF PARA-XYLENE, CONSTITUTED BY TWO ADSORBERS IN SERIES WITH A TOTAL NUMBER OF 22 OR FEWER BEDS
    14.
    发明申请
    PROCESS AND APPARATUS FOR THE SIMULATED COUNTER-CURRENT PRODUCTION OF PARA-XYLENE, CONSTITUTED BY TWO ADSORBERS IN SERIES WITH A TOTAL NUMBER OF 22 OR FEWER BEDS 有权
    用于模拟对流生产对二甲苯的方法和装置,由两个共22个或更少的床上的两个吸烟者组成

    公开(公告)号:US20140121436A1

    公开(公告)日:2014-05-01

    申请号:US14064884

    申请日:2013-10-28

    CPC classification number: C07C7/12 B01D15/1828 C07C7/13 C07C15/08

    Abstract: The present invention describes a novel configuration for simulated counter-current para-xylene production units, constituted by two adsorbers, characterized in that the volume occupied by the solid adsorbent is reduced by at least 8% compared with the volume of solid adsorbent contained in the adsorbers of a prior art unit. This novel configuration can be used to minimize the quantity of solid adsorbent necessary to produce a given quantity of para-xylene.

    Abstract translation: 本发明描述了由两个吸附器构成的模拟逆流对二甲苯生产单元的新型结构,其特征在于固体吸附剂占据的体积与包含在固体吸附剂中的固体吸附剂的体积相比降低了至少8% 现有技术单元的吸附器。 这种新颖的结构可以用于最小化产生给定量的对二甲苯所必需的固体吸附剂的量。

    METHOD FOR OBTAINING A PURIFIED DIESTER EFFLUENT BY DEPOLYMERISING A POLYESTER COMPRISING OPAQUE POLYETHYLENE TEREPHTHALATE

    公开(公告)号:US20230028123A1

    公开(公告)日:2023-01-26

    申请号:US17786101

    申请日:2020-12-07

    Abstract: The present invention relates to a process for depolymerizing a polyester feedstock comprising opaque PET, which comprises: a) a conditioning step; b) a step of glycolysis, operated at between 180 and 400° C., a residence time of from 0.1 to 10 h in the presence of diol; c) a diol separation step, at a temperature of between 100 and 250° C., a pressure lower than that of step b) and producing a diol effluent and an effluent rich in monomers; d) a step of separating into a heavy impurities effluent and a prepurified monomers effluent, at a temperature of less than 250° C. and a pressure of less than 0.001 MPa and a residence time of less than 10 min; e) a step of decolourizing the prepurified monomers effluent, by adsorption of a mixture comprising between 20% and 90% by weight of the prepurified monomers effluent and a solvent, at a temperature of between 100 and 200° C., a pressure of between 0.1 and 1.0 MPa and in the presence of at least one adsorbent.

    SIMULATED MOVING BED SEPARATION METHOD AND DEVICE WITH BYPASS FLUID FLOW

    公开(公告)号:US20190388801A1

    公开(公告)日:2019-12-26

    申请号:US16441547

    申请日:2019-06-14

    Abstract: Method for the simulated moving bed separation of a feedstock (F), in which when a fluid/effluent (feedstock F, desorbent D, extract E, raffinate R) is injected/withdrawn into/from a chosen plate (Pi) using an external bypass line (Li−1/i, Li+1/i) connected to said chosen plate (Pi), the flow rate within the said external bypass line (Li−1/i, Li+1/i) is controlled in such a way that: a major proportion of the fluid/effluent (F, D, E, R) is injected/withdrawn into/from the chosen plate (Pi); and a minor proportion of the fluid/effluent (F, D, E, R) is injected/withdrawn into/from the adjacent plate (Pi−1, Pi+1) connected to the said external bypass line (Li−1/i, Li+1/i).

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