METHOD FOR PRODUCING HIGHLY PURE MONOETHYLENE GLYCOL

    公开(公告)号:CA2345140C

    公开(公告)日:2009-06-16

    申请号:CA2345140

    申请日:1999-09-21

    Applicant: BASF AG

    Abstract: The invention relates to a method for obtaining highly pure monoethylene glycol from the product of hydrolysis of ethylene oxide by distillation, by means of dehydration under pressure, preferably in a cascade, vacuum dehydration and subsequent pure distillation. According to the inventive method, the pressure dehydration column or at lea st the first pressure dehydration column of the cascade (2, 3, 4) has a stripping section with at least one separation stage, preferably 2- 10 separation stages, especially 3-6 stages, and in that part of the top flow of the dehydration column(s) (2, 3, 4) is sluiced out with the stripping section.

    طريقة لانتاج احادي ايثلين جليكول Monoethylene glycol عالي النقاء

    公开(公告)号:SA1102B1

    公开(公告)日:2006-08-12

    申请号:SA99200783

    申请日:1999-11-30

    Applicant: BASF AG

    Abstract: الملخص: عمليةللتقطيرالاستخلاصلاحاديايثيلينجيكول monoethylene glycol عاليالنقاءمنناتجالتحللالمائيلاكسيدالايثيلين ethylene oxide بواسطةنزعالماءبالضغط،ويفضلفيمجموعةمتواحدة،مننزعالماءبالتفريغوالتقطيرالمنقىالتالي،حيثيتماثناءنزعالماءبالتفريغحسبتيارمائييحتويعلىاحاديايثيلينجيكول monoethylene glycol بتركيزاقلمن 1% بالوزن،ويفضلاقلمن 0,1% بالوزن،ومركباتمتوسطةالغليانومركباتمنخفضةالغليان . ويتمازالةالتيارالمائيالذيتمسحبةاختياريابعدالمعالجةمرةأخرىمنالنظام.20 ،

    23.
    发明专利
    未知

    公开(公告)号:ES2212671T3

    公开(公告)日:2004-07-16

    申请号:ES99969405

    申请日:1999-09-21

    Applicant: BASF AG

    Abstract: A process for the distillative recovery of high purity monoethylene glycol from the hydrolysis, product of ethylene oxide by pressure dewatering, preferably in a battery, vacuum dewatering and subsequent purifying distillation, wherein during the vacuum dewatering an aqueous stream is withdrawn which contains-monoethylene glycol in a concentration below 1% by weight, preferably below 0.1% by weight, medium boilers and low boilers. The withdrawn aqueous stream is, optionally after further workup, removed from the system.

    24.
    发明专利
    未知

    公开(公告)号:DE59909416D1

    公开(公告)日:2004-06-09

    申请号:DE59909416

    申请日:1999-09-20

    Applicant: BASF AG

    Abstract: In the preparation of ethylene oxide by direct oxidation of ethylene with air or oxygen using water as heat carrier to dissipate the heat of reaction, with water vapor being formed, a process for optimizing the specific energy consumption is proposed. In this, the water vapor is first expanded in one or more backpressure steam turbine(s) T for operating working machines M, before it is fed to one or more consumers, such as bottoms reboilers or steam injectors, for further utilization.

    25.
    发明专利
    未知

    公开(公告)号:ES2194518T3

    公开(公告)日:2003-11-16

    申请号:ES99952457

    申请日:1999-09-21

    Applicant: BASF AG

    Abstract: A process for the distillative recovery of high purity monoethylene glycol from the hydrolysis product of ethylene oxide by pressure dewatering, vacuum dewatering and subsequent purifying distillation, which includes the pressure dewatering columns or at least the first pressure dewatering column of the battery (2, 3, 4) having a stripping section with at least one separating stage, preferably with from 2 to 10 separating stages, particularly preferably with from 3 to 6 stages, and a portion of the overhead stream of the pressure dewatering column(s) (2, 3, 4) having a stripping section being removed from the system.

    METHOD FOR PRODUCING HIGHLY PURE MONOETHYLENE GLYCOL

    公开(公告)号:PL347580A1

    公开(公告)日:2002-04-08

    申请号:PL34758099

    申请日:1999-09-21

    Applicant: BASF AG

    Abstract: A process for the distillative recovery of high purity monoethylene glycol from the hydrolysis, product of ethylene oxide by pressure dewatering, preferably in a battery, vacuum dewatering and subsequent purifying distillation, wherein during the vacuum dewatering an aqueous stream is withdrawn which contains-monoethylene glycol in a concentration below 1% by weight, preferably below 0.1% by weight, medium boilers and low boilers. The withdrawn aqueous stream is, optionally after further workup, removed from the system.

    METHOD FOR PRODUCING HIGHLY PURE MONOETHYLENE GLYCOL

    公开(公告)号:PL346752A1

    公开(公告)日:2002-02-25

    申请号:PL34675299

    申请日:1999-09-21

    Applicant: BASF AG

    Abstract: A process for the distillative recovery of high purity monoethylene glycol from the hydrolysis product of ethylene oxide by pressure dewatering, vacuum dewatering and subsequent purifying distillation, which includes the pressure dewatering columns or at least the first pressure dewatering column of the battery (2, 3, 4) having a stripping section with at least one separating stage, preferably with from 2 to 10 separating stages, particularly preferably with from 3 to 6 stages, and a portion of the overhead stream of the pressure dewatering column(s) (2, 3, 4) having a stripping section being removed from the system.

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