1.
    发明专利
    未知

    公开(公告)号:DE3343598A1

    公开(公告)日:1985-06-13

    申请号:DE3343598

    申请日:1983-12-02

    Applicant: BASF AG

    Abstract: Rapid in situ estimation of the degree of dispersion in flowing two-phase systems, in particular for determining optimum metering of dispersants or flocculants in concentrated dispersions, is carried out by a method in which assignment of the degree of dispersion is effected by measuring the pressure drop experienced by a flowing dispersion along a defined length during tubular flow.

    DEWATERING OF SEWAGE SLUDGES ON FILTER PRESSES

    公开(公告)号:CA1172390A

    公开(公告)日:1984-08-07

    申请号:CA390301

    申请日:1981-11-18

    Applicant: BASF AG

    Abstract: A process for dewatering sewage sludges by mixing these homogeneously with additives, such as finely divided coal or ash or mixtures thereof, adding organic flocculants, removing the greater part of the water, in a first dewatering step, by gravity filtration without applying a pressure differential and then dewatering more thoroughly in a second dewatering step, by pressure filtration on filter presses, wherein the additives, such as finely divided coal or ash or mixtures thereof, are added in an amount of from 0.5 to 1.5 parts by weight per part by weight of sludge solids and from 1 to 7 kg of organic flocculant/tonne of sludge solids is added to the sewage sludges before or during admixture of the additives.

    METHOD OF DEWATERING SEWAGE SLUDGE IN FILTER PRESSES

    公开(公告)号:DE3162983D1

    公开(公告)日:1984-05-10

    申请号:DE3162983

    申请日:1981-10-12

    Applicant: BASF AG

    Abstract: 1. A multistage process for dewatering sewage sludges by mixing these homogeneously with inert additives, such as finely divided coal or ash or mixtures thereof, adding organic flocculants, removing the greater part of the water, in a first dewatering step, by gravity filtration without applying a pressure differential and then effecting further dewatering in a second dewatering step, by pressure filtration on filter presses, in order to obtain filter cakes which can be combusted, with the utilization of their calorific content, wherein the additives, such as finely divided coal or ash or mixtures thereof, are added in an amount of from 0.5 to 1.5 parts by weight per part by weight of sludge solids and from 1 to 7 kg of organic flocculant/tonne of sludge solids is added to the sewage sludges before or during admixture of the additives.

    DEWATERING OF SEWAGE SLUDGES ON FILTER PRESSES

    公开(公告)号:CA1172391A

    公开(公告)日:1984-08-07

    申请号:CA390331

    申请日:1981-11-18

    Applicant: BASF AG

    Abstract: A process for dewatering sewage sludges of which the sludge solids contain less than 70% of organic matter, and whose dewatering characteristics have been improved by adding organic flocculants, on a filter press, wherein the sewage sludges are concentrated by adding an organic flocculant during thickening by gravity sedimentation from 0.5-5,0% by weight of sludge solids to 6-14, and especially 8-12, % by weight of sludge solids, the sewage sludges are mixed with additives, such as finely divided coal or ash or mixtures thereof, in an amount of from 0.5 to 1.5 parts by weight per part by weight of sludge solids, and the sludges are treated, before, during or after admixture of the additives, with a further 2-8 kg of organic flocculant/tonne of sludge solids and are then dewatered on the filter press.

    METHOD OF DEWATERING SEWAGE SLUDGE IN FILTER PRESSES

    公开(公告)号:DE3163660D1

    公开(公告)日:1984-06-20

    申请号:DE3163660

    申请日:1981-10-12

    Applicant: BASF AG

    Abstract: 1. A multistage process for dewatering sewage sludges of which the sludge solids contain less than 70% of organic matter, and whose dewatering characteristics have been improved by adding organic flocculants, on a filter press, using inert additives, wherein the sewage sludges are concentrated, by adding an organic flocculant during thickening by gravity sedimentation, from 0.5-5.0% by weight of sludge solids to 6-14, and especially 8-12, % by weight of sludge solids, the sewage sludges are mixed with additives, such as finely divided coal or ash or mixtures thereof, in an amount of from 0.5 to 1.5 parts by weight per part by weight of sludge solids, and the sludges are treated, before, during or after admixture of the additives, with a further 2-8 kg of organic flocculant/tonne of sludge solids and are then dewatered on the filter press to produce filter cakes which can be combusted with the utilization of their calorific content.

    6.
    发明专利
    未知

    公开(公告)号:DD202132A5

    公开(公告)日:1983-08-31

    申请号:DD23498581

    申请日:1981-11-19

    Applicant: BASF AG

    Abstract: 1. A multistage process for dewatering sewage sludges by mixing these homogeneously with inert additives, such as finely divided coal or ash or mixtures thereof, adding organic flocculants, removing the greater part of the water, in a first dewatering step, by gravity filtration without applying a pressure differential and then effecting further dewatering in a second dewatering step, by pressure filtration on filter presses, in order to obtain filter cakes which can be combusted, with the utilization of their calorific content, wherein the additives, such as finely divided coal or ash or mixtures thereof, are added in an amount of from 0.5 to 1.5 parts by weight per part by weight of sludge solids and from 1 to 7 kg of organic flocculant/tonne of sludge solids is added to the sewage sludges before or during admixture of the additives.

    7.
    发明专利
    未知

    公开(公告)号:DD201878A5

    公开(公告)日:1983-08-17

    申请号:DD23498781

    申请日:1981-11-19

    Applicant: BASF AG

    Abstract: 1. A multistage process for dewatering sewage sludges of which the sludge solids contain less than 70% of organic matter, and whose dewatering characteristics have been improved by adding organic flocculants, on a filter press, using inert additives, wherein the sewage sludges are concentrated, by adding an organic flocculant during thickening by gravity sedimentation, from 0.5-5.0% by weight of sludge solids to 6-14, and especially 8-12, % by weight of sludge solids, the sewage sludges are mixed with additives, such as finely divided coal or ash or mixtures thereof, in an amount of from 0.5 to 1.5 parts by weight per part by weight of sludge solids, and the sludges are treated, before, during or after admixture of the additives, with a further 2-8 kg of organic flocculant/tonne of sludge solids and are then dewatered on the filter press to produce filter cakes which can be combusted with the utilization of their calorific content.

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