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1.
公开(公告)号:AU749888B2
公开(公告)日:2002-07-04
申请号:AU4455499
申请日:1999-08-18
Applicant: DEGUSSA
Inventor: FOERSTER MARTIN , PIROTH JOSEF , SCHLACHTER ULRICH , DOMESLE RAINER , KRAMPE WILLI
Abstract: The coating dispersion is sucked through the flow channels of a monolithic catalyst support at a rate of 0.1-1 m/s. Excess dispersion is removed from the channels by applying a suction impulse from below. Extraction air is sucked at a rate of 40-1 m/s through the channels and the excess coating dispersion removed from the air stream is removed from the air stream within a time from less than 100 ms after leaving the catalyst support. Process for coating the flow channels of a monolithic cylindrical catalyst support with a coating dispersion comprises vertically directing the cylindrical axis, charging a predetermined amount of dispersion from a storage vessel to the upper front surface of the support, sucking the dispersion through the flow channels, removing excess dispersion from the channels, returning the excess dispersion to the storage vessel and fixing the dispersion by calcining. The coating dispersion is sucked through the flow channels of a monolithic catalyst support at a rate of 0.1-1 m/s. Excess dispersion is removed from the channels by applying a suction impulse from below. Extraction air is sucked at a rate of 40-1 m/s through the channels and the excess coating dispersion removed from the air stream is removed from the air stream within a time from less than 100 ms after leaving the catalyst support.
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公开(公告)号:ZA993249B
公开(公告)日:1999-11-11
申请号:ZA993249
申请日:1999-05-11
Applicant: DEGUSSA
Inventor: FOERSTER MARTIN , GUTSCH ANDREAS , DOMESLE RAINER , KIESSLING RALPH , STOEHR OLIVER
IPC: B01J2/00 , B01J2/04 , B01J19/08 , B01J19/12 , B01J20/02 , B01J20/30 , B01J32/00 , B01J37/00 , C01B13/34 , C03B19/00 , C04B35/622 , B01J , B01D , C04B
Abstract: A powdered heterogeneous substance is produced by treating a dispersion, suspension or emulsion in a turbulent or laminar burner under specified conditions, feeding the reaction mixture into a tube where it is further treated and then feeding it to a scrubber, separator or filter for further treatment.
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公开(公告)号:ZA9903249B
公开(公告)日:1999-11-11
申请号:ZA9903249
申请日:1999-05-11
Applicant: DEGUSSA
Inventor: FOERSTER MARTIN , GUTSCH ANDREAS , DOMESLE RAINER , KIESSLING RALPH , STOEHR OLIVER
IPC: B01J2/00 , B01J2/04 , B01J19/08 , B01J19/12 , B01J20/02 , B01J20/30 , B01J32/00 , B01J37/00 , C03B19/00 , C04B35/622 , B01J , B01D , C04B
CPC classification number: B01J2/00 , B01J37/0027
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公开(公告)号:ZA991899B
公开(公告)日:1999-09-27
申请号:ZA991899
申请日:1999-03-09
Applicant: DEGUSSA
Inventor: FOERSTER MARTIN , BIRTIGH GERHARD , MERGNER BERND , HASSELMANN WOLFGANG , DITTRICH EWALD , LEIBOLD WALTER , HOFFMANN MICHAEL , SCHAEFER ROBERT
Abstract: The channels (1) are filled (11) from below, with a quantity up to 10% greater than their empty volume, until the dispersion rises above the upper surface (17). The excess is removed (8, 9) before emptying the channels. Impulsive suction from a low pressure vessel (5) connected with the lower end face of the substrate (1), then clears the passages. The interval between starting to fill and completion of emptying, is no longer than 5 seconds. Preferred Features: The (partial) vacuum vessel (5) has an initial pressure of 150 mbar and a volume 100-1000 times that of the catalyst substrate. During suction, a minimum air velocity of 5 m/s is maintained in the channels. The open flow cross section to the vacuum vessel is adjustable from 0 to a maximum value. When thixotropic or intrinsically-viscous dispersions are used, the interval between filling and sucking-out is so short, that the limit of flowability cannot set in. The substrate is moistened before coating and may be pre-impregnated with acids, bases or salt solutions. Following emptying of the flow channels, before firing, a flow of heated dry air at 50-80 degrees C is passed. This is delivered against the direction of emptying, at a speed of 2-10 m/s, over an interval of 2-60 seconds.
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公开(公告)号:ZA9901899B
公开(公告)日:1999-09-27
申请号:ZA9901899
申请日:1999-03-09
Applicant: DEGUSSA
Inventor: FOERSTER MARTIN , BIRTIGH GERHARD , MERGNER BERND , HASSELMANN WOLFGANG , DITTRICH EWALD , LEIBOLD WALTER , HOFFMANN MICHAEL , SCHAEFER ROBERT
CPC classification number: B05D7/22 , B01J37/0215
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公开(公告)号:AU737238B2
公开(公告)日:2001-08-16
申请号:AU2034299
申请日:1999-03-10
Applicant: DEGUSSA
Inventor: FOERSTER MARTIN , DITTRICH EWALD , BIRTIGH GERHARD , LEIBOLD WALTER , MERGNER BERND , HOFFMANN MICHAEL , HASSELMANN WOLFGANG , SCHAFER ROBERT
IPC: B01D53/86 , B01J35/04 , B01J37/02 , B05D7/22 , B28B11/04 , C04B41/45 , F01N3/28 , B05D7/24 , B05C19/04 , B05C7/04
Abstract: The channels (1) are filled (11) from below, with a quantity up to 10% greater than their empty volume, until the dispersion rises above the upper surface (17). The excess is removed (8, 9) before emptying the channels. Impulsive suction from a low pressure vessel (5) connected with the lower end face of the substrate (1), then clears the passages. The interval between starting to fill and completion of emptying, is no longer than 5 seconds. Preferred Features: The (partial) vacuum vessel (5) has an initial pressure of 150 mbar and a volume 100-1000 times that of the catalyst substrate. During suction, a minimum air velocity of 5 m/s is maintained in the channels. The open flow cross section to the vacuum vessel is adjustable from 0 to a maximum value. When thixotropic or intrinsically-viscous dispersions are used, the interval between filling and sucking-out is so short, that the limit of flowability cannot set in. The substrate is moistened before coating and may be pre-impregnated with acids, bases or salt solutions. Following emptying of the flow channels, before firing, a flow of heated dry air at 50-80 degrees C is passed. This is delivered against the direction of emptying, at a speed of 2-10 m/s, over an interval of 2-60 seconds.
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公开(公告)号:PL334969A1
公开(公告)日:2000-02-28
申请号:PL33496999
申请日:1999-08-18
Applicant: DEGUSSA
Inventor: FOERSTER MARTIN , PIROTH JOSEF , SCHLACHTER ULRICH , DOMESLE RAINER , KRAMPE WILLI
Abstract: The coating dispersion is sucked through the flow channels of a monolithic catalyst support at a rate of 0.1-1 m/s. Excess dispersion is removed from the channels by applying a suction impulse from below. Extraction air is sucked at a rate of 40-1 m/s through the channels and the excess coating dispersion removed from the air stream is removed from the air stream within a time from less than 100 ms after leaving the catalyst support. Process for coating the flow channels of a monolithic cylindrical catalyst support with a coating dispersion comprises vertically directing the cylindrical axis, charging a predetermined amount of dispersion from a storage vessel to the upper front surface of the support, sucking the dispersion through the flow channels, removing excess dispersion from the channels, returning the excess dispersion to the storage vessel and fixing the dispersion by calcining. The coating dispersion is sucked through the flow channels of a monolithic catalyst support at a rate of 0.1-1 m/s. Excess dispersion is removed from the channels by applying a suction impulse from below. Extraction air is sucked at a rate of 40-1 m/s through the channels and the excess coating dispersion removed from the air stream is removed from the air stream within a time from less than 100 ms after leaving the catalyst support.
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8.
公开(公告)号:ZA995303B
公开(公告)日:2000-02-21
申请号:ZA995303
申请日:1999-08-19
Applicant: DEGUSSA
Inventor: FOERSTER MARTIN , SCHLACHTER ULRICH , KRAMPE WILLI , PIROTH JOSEF , DOMESLE RAINER
Abstract: The coating dispersion is sucked through the flow channels of a monolithic catalyst support at a rate of 0.1-1 m/s. Excess dispersion is removed from the channels by applying a suction impulse from below. Extraction air is sucked at a rate of 40-1 m/s through the channels and the excess coating dispersion removed from the air stream is removed from the air stream within a time from less than 100 ms after leaving the catalyst support. Process for coating the flow channels of a monolithic cylindrical catalyst support with a coating dispersion comprises vertically directing the cylindrical axis, charging a predetermined amount of dispersion from a storage vessel to the upper front surface of the support, sucking the dispersion through the flow channels, removing excess dispersion from the channels, returning the excess dispersion to the storage vessel and fixing the dispersion by calcining. The coating dispersion is sucked through the flow channels of a monolithic catalyst support at a rate of 0.1-1 m/s. Excess dispersion is removed from the channels by applying a suction impulse from below. Extraction air is sucked at a rate of 40-1 m/s through the channels and the excess coating dispersion removed from the air stream is removed from the air stream within a time from less than 100 ms after leaving the catalyst support.
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公开(公告)号:CA2271818A1
公开(公告)日:1999-11-12
申请号:CA2271818
申请日:1999-05-11
Applicant: DEGUSSA
Inventor: KIESSLING RALPH , STOEHR OLIVER , FOERSTER MARTIN , GUTSCH ANDREAS , DOMESLE RAINER
IPC: B01J2/00 , B01J2/04 , B01J19/08 , B01J19/12 , B01J20/02 , B01J20/30 , B01J32/00 , B01J37/00 , C01B13/34 , C03B19/00 , C04B35/622 , B01J37/12
Abstract: A suspension, dispersion or emulsion is introduced into a burner. An optionally two-stage after-treatment is then carried out. The resulting powder can be employed as a catalyst.
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公开(公告)号:DE59309706D1
公开(公告)日:1999-09-02
申请号:DE59309706
申请日:1993-11-10
Applicant: DEGUSSA
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