EP1584820B1 - Pompe à écoulement mixte - Google Patents
Pompe à écoulement mixte Download PDFInfo
- Publication number
- EP1584820B1 EP1584820B1 EP04405214A EP04405214A EP1584820B1 EP 1584820 B1 EP1584820 B1 EP 1584820B1 EP 04405214 A EP04405214 A EP 04405214A EP 04405214 A EP04405214 A EP 04405214A EP 1584820 B1 EP1584820 B1 EP 1584820B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- edge
- blade
- guide vane
- impeller
- screw
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000007787 solid Substances 0.000 claims abstract description 25
- 239000007788 liquid Substances 0.000 claims abstract description 6
- 238000000034 method Methods 0.000 claims abstract description 5
- 238000007792 addition Methods 0.000 claims 5
- 239000012530 fluid Substances 0.000 claims 1
- 239000000654 additive Substances 0.000 abstract 1
- 239000008247 solid mixture Substances 0.000 abstract 1
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 238000009954 braiding Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 239000005060 rubber Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 230000003313 weakening effect Effects 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D7/00—Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts
- F04D7/02—Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts of centrifugal type
- F04D7/04—Pumps adapted for handling specific fluids, e.g. by selection of specific materials for pumps or pump parts of centrifugal type the fluids being viscous or non-homogenous
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
- F04D—NON-POSITIVE-DISPLACEMENT PUMPS
- F04D1/00—Radial-flow pumps, e.g. centrifugal pumps; Helico-centrifugal pumps
- F04D1/04—Helico-centrifugal pumps
Definitions
- the invention relates to a screw centrifugal pump according to the preamble of claim 1.
- the invention further relates to a method for conveying a medium with a fferenzentrifugalradpumpe according to the preamble of claim 8.
- a ringenzentrifugalradpumpe also known as worm gear, known.
- a centrifugal pump comprises a single, helically extending blade, which is rotatably arranged in a pump housing.
- This pump is particularly suitable for the promotion of interspersed with solid admixtures liquids, especially for the promotion of dirty water with langturaigen components.
- the invention has for its object to provide a fferenzentrifugalradpumpe, which has more advantageous properties in the promotion of interspersed with solid admixtures liquids.
- a screw centrifugal wheel pump comprising a pump housing with an inlet opening and an impeller arranged inside the pump housing, which has a spirally running inlet blade edge, wherein in the region of the inlet opening a guide blade protruding into the interior of the impeller is arranged, which has a vane edge, which protrudes increasingly in the direction of rotation of the impeller in the direction of the axis of rotation in the interior of the impeller.
- the screw centrifugal pump according to the invention is particularly advantageous in conveying higher concentrations of fibrous solids prone to plait formation. If the fibrous stranded solids concentration is always higher, this leads to bale formation and increased friction in the suction line in the impeller channel. If a certain limit value is reached, the hydraulic forces alone are no longer sufficient to convey the material, with the result that the screw centrifugal pump clogs and blocks.
- the inventive screw centrifugal pump prevents this blockage by the helical entry vane edge of the worm wheel start rotating with respect to the fixed projecting vane, with the entry vane edge and vane cooperating such that the intervening solid masses are captured by the rotating entry vane edge and loosened along the entry vane edge in the flow direction and / or pressed.
- a mechanical force acting essentially in the conveying direction is exerted on the conveyed medium, which prevents accumulation of solid constituents in the conveying path.
- the guide vane edge forms a fixed space curve and the inlet vane edge rotatable due to the rotatable fferenzentrifugalrades space curve, these two space curves are preferably mutually adapted extending configured that they are when rotating the impeller at mutually short distance or touching each other move past each other.
- the solids located between the two space curves are thereby mechanically moved in the direction of the space curves, and thereby substantially in the flow direction, and thereby loosened or pressed in the flow direction.
- the vane edge and / or the inlet vane edge at least partially on a cutting edge, so that the solids between the mutually moving space curves are also mechanically crushed.
- this causes crushing or dicing of the braids or fibers, which prevents attachment of the braids in the conveying path and thus ensures continuous, reliable operation of the fferenzentrifugalradpumpe without interruption.
- the mutual shear, separation or clamping effect of the two space curves also allows, depending on the design of the vane edge and / or the inlet blade edge, a cutting, crushing or weakening of fibrous solids such as paper, cords, wood or solids such as plastic, rubber, metal or glass.
- the fferenzentrifugalradpumpe 1 comprises a ringenzentrifugalrad 2, which is arranged about a rotation axis 2d rotatably in the direction of rotation 4a in a pump housing 3.
- the fferenzentrifugalrad 2 has a spiral-running inlet blade edge 2a and an outer contour 2c.
- the fferenzentrifugalrad 2 is fixedly connected to a pump shaft 4.
- the pump housing 3 comprises a suction cone housing part 3a, a spiral housing part 3b, an inlet opening 3c and an outlet opening 3d.
- a guide vane 5 with a vane edge 5a protruding into the interior of the pump housing 3 and into the interior of the screw centrifugal wheel 2 is fixedly arranged.
- the term "interior of the impeller 2" in the present document is understood to mean the interior which is bounded by the external contour 2c when the centrifugal centrifugal wheel 2 rotates, so that the guide vane 5 extends at least partially into this internal space, and the centrifugal impeller 2 as shown in FIG. in the region of its tip or within the maximum extent of the helical gear portion 6a, the guide blade 5 is orbited outside.
- the fferenzentrifugalradpumpe 1 also includes a ringradanteil 6a and a Zentrifugalradanteil 6b. The pumped with the pump 1 medium flows in the flow direction S.
- FIG. 2 shows, from the direction indicated by A in FIG. 1, a front view of the inlet opening 3c, the impeller 2 and the guide blade 5 being recognizable inside the pump 1.
- the impeller 2 shows the spiraling inlet blade edge 2a, which falls off against the axis of rotation 2d and grows axially into it. The foremost portion of the inlet blade edge 2a is not directly visible because of the vane 5 and therefore shown in dashed lines.
- the vane 5 is designed in such a way that the vane edge 5 a protrudes progressively in the direction of rotation 4 a in the direction of the axis of rotation 2 d into the interior of the impeller 2, both in the radial and in the axial direction.
- the vane edge 5a forms a fixed space curve, whereas the inlet vane edge 2a forms a space curve rotatable about the wheel axis 2d.
- These two space curves 2 a, 5 a are designed to be mutually adapted in the illustrated exemplary embodiment such that the vane edge 5 a has a vane edge section 5 b and the inlet vane edge 2 a has a vane edge section 2 b within which the vane edge 5 a and the inlet vane edge 2 a depend on the respective position of the impeller 2 have mutually small distance or touch each other.
- the mutually small distance may for example have a value between 0.1 and 30 mm. This position with mutually least distance is shown with the point P1 on the blade edge portion 2b and the P2 on the vane edge portion 5b.
- the guide blade 5 can be arranged and configured in various ways in the pump housing 3 such that the stationary guide blade edge 5a and the rotating inlet blade edge 2a cooperate such that solids are mechanically conveyed by the mutual cooperation of the edges 2a, 5a, in particular in the flow direction S.
- the blade edge section 2b has a tangent T1 at the point P1 and the guide blade edge section 5b has a tangent T2 at the point P2, these two tangents T1, T2 having a cutting angle ⁇ as viewed from the inlet opening 3c.
- This angle ⁇ is at least 10 degrees, and is preferably between 30 degrees and 150 degrees, in particular between 60 degrees and 120 degrees.
- the angle ⁇ is preferably never smaller than the angle at which a sliding of the solid on the inlet blade edge 2a or between the inlet blade edge 2a and the vane edge 5a is no longer guaranteed.
- FIGS. 3 and 4 show, in two detailed views, analogous to the illustration according to FIG. 2, two differently extending space curves or inlet blade edge 2a and guide blade edge 5a, the enclosed angle ⁇ of the tangents T1, T2 of the points P1, P2 in FIG in Figure 4 is about 90 degrees.
- This angle ⁇ is determined by the course of the space curves 2a, 5a, and thus can be selected accordingly in the construction of the fferenzentrifugalradpumpe 1.
- the course of the space curves 2a, 5a can be selected such that the angle ⁇ remains substantially constant during the movement of the points P1, P2 in the direction Q2.
- the angle ⁇ during the movement of the points P1, P2 in the direction Q2 also increase and / or decrease.
- At least part of the blade edge section 2b and / or the blade edge section 5b is designed as an edge, cutting edge or blade in order to weaken or sever a solid which is located between the sections 2b, 5b.
- the length of the effective edge sections 2b, 5b can also be determined by appropriate shaping.
- the fferenzentrifugalradpumpe can be optimized in accordance with the expected solids and admixtures, that the edge portions 2b, 5b and their angle ⁇ is selected to be optimized in order to prevent clogging of the pump and, for example, also to achieve a good pump efficiency.
- FIG. 5 shows a further exemplary embodiment of a screw centrifugal pump 1, in whose inlet opening 3c a wear-resistant sleeve 7 is arranged, which is fixedly connected to the guide blade 5. With a fastening means, not shown, the sleeve 7 can be firmly connected to the pump housing 3.
- the sleeve 7 and thus the vane 5 in the direction of movement R is displaced.
- This arrangement has the particular advantage that the distance between the inlet blade edge 2a and the vane edge 5a, in particular the distance between the points P1, P2 in the direction R and Q1 is adjustable.
- the inlet blade edge 2a and / or the vane edge 5a wears off during operation of the pump, so that the distance between the points P1, P2 increases during operation with time.
- the sleeve 7 thus makes it possible to readjust the position of the guide vane 5 in the direction of displacement R or Q 1 after certain time intervals.
- the sleeve 7 can also be designed such that it can also be rotated in the inlet opening 3c, i. with respect to the wheel axle 2d is rotatable to rotate the sleeve 7 in the released state, and thus also to rotate the position of the guide vane 5.
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Structures Of Non-Positive Displacement Pumps (AREA)
- Centrifugal Separators (AREA)
Claims (9)
- Pompe centrifuge à roue hélicoïdale (1) comprenant un carter de pompe (3) avec un canal d'admission (3c) ainsi qu'une roue à aubes (2) disposée à l'intérieur du carter de pompe (3) et tournant autour d'un axe de rotation (2d) dans le sens de rotation (4a), roue qui présente un bord d'aube d'attaque (2a) en spirale, caractérisée en ce que dans la zone du canal d'admission (3c) est disposée une aube directrice (5) faisant saillie dans l'espace intérieur de la roue à aubes (2), et en ce que l'aube directrice (5) présente un bord d'aube directrice (5a) qui fait progressivement saillie dans l'espace intérieur de la roue à aubes (2), dans le sens de rotation (4a) et en direction de l'axe de rotation (2d), et en ce que la roue à aubes (2) ainsi que l'aube directrice (5) sont conçues d'une manière concourante telle qu'au moins une partie des additifs solides glisse le long du bord d'aube d'attaque.
- Pompe centrifuge à roue hélicoïdale (1) selon la revendication 1, caractérisée en ce que l'aube directrice (5) est logée en direction de l'axe de rotation (2d) de manière à pouvoir être déplacée et fixée.
- Pompe centrifuge à roue hélicoïdale (1) selon l'une quelconque des revendications précédentes, caractérisée en ce que le bord d'aube directrice (5a) forme une courbe spatiale fixe, en ce que le bord d'aube d'attaque (2a) forme une courbe spatiale rotative, et en ce que ces deux courbes spatiales sont conçues avec une adaptation des formes telle que le bord d'aube directrice (5a) présente un segment de bord d'aube directrice (5b) et le bord d'aube d'attaque (2a) présente un segment de bord d'aube (2b) à l'intérieur desquels le bord d'aube directrice (5a) et le bord d'aube d'attaque (2a), selon la position de la roue à aubes (2), présentent un faible écart ou se touchent réciproquement.
- Pompe centrifuge à roue hélicoïdale (1) selon la revendication 3, caractérisée en ce que aussi bien à l'intérieur du segment de bord d'aube (2b) qu'à l'intérieur du segment de bord d'aube directrice (5b) est obtenu à chaque fois un point (P1, P2), deux points qui présentent le plus petit écart entre le segment de bord d'aube (2b) et le segment de bord d'aube directrice (5b), ces points (P1, P2) se déplaçant dans le sens d'écoulement (S) lors de la rotation de la roue à aubes (2).
- Pompe centrifuge à roue hélicoïdale (1) selon la revendication 4, caractérisée en ce que le segment de bord d'aube (2b) présente une tangente (T1) au point (P1), en ce que le segment de bord d'aube directrice (5b) présente une tangente (T2) au point (P2), et en ce que ces deux tangentes (T1, T2) forment un angle de coupe (α) d'au moins 10 degrés par rapport au canal d'admission (3c).
- Pompe centrifuge à roue hélicoïdale (1) selon la revendication 5, caractérisée en ce que l'angle de coupe (α) est situé entre 30 degrés et moins de 180 degrés maximum, en particulier entre 60 degrés et 120 degrés.
- Pompe centrifuge à roue hélicoïdale (1) selon l'une quelconque des revendications 3 à 6, caractérisée en ce que le segment de bord d'aube (2b) ou/et le segment de bord d'aube directrice (5b) est/sont conçu(s) au moins en partie comme un bord coupant.
- Procédé d'alimentation d'un liquide chargé d'additifs solides à l'aide d'une pompe centrifuge à roue hélicoïdale (1) comprenant une roue à aubes (2) avec un bord d'aube d'attaque (2a) en spirale, caractérisé en ce que le liquide est amené, à l'aide d'une aube directrice (5), jusqu'au bord d'aube d'attaque (2a) de la roue à aubes (2) tournante de telle manière qu'au moins une partie des additifs solides glisse le long du bord d'aube d'attaque (2a), si bien que l'additif solide, sous l'effet du bord d'aube d'attaque (2a), est transporté mécaniquement dans le sens d'écoulement du liquide.
- Procédé selon la revendication 8, caractérisé en ce que, lorsque la roue à aubes (2) tourne, un bord d'aube directrice (5a) de l'aube directrice (5) et le bord d'aube d'attaque (2a) concourent de telle manière que l'additif solide se trouvant entre le bord d'aube d'attaque (2a) et le bord d'aube directrice (5a) est broyé de façon mécanique par les bords d'aube (2a, 5a) et/ou poussé dans le sens d'écoulement (S).
Priority Applications (9)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP04405214A EP1584820B1 (fr) | 2004-04-07 | 2004-04-07 | Pompe à écoulement mixte |
DK04405214T DK1584820T3 (da) | 2004-04-07 | 2004-04-07 | Skruecentrifugalpumpe |
AT04405214T ATE330126T1 (de) | 2004-04-07 | 2004-04-07 | Schraubenzentrifugalradpumpe |
DE502004000769T DE502004000769D1 (de) | 2004-04-07 | 2004-04-07 | Schraubenzentrifugalradpumpe |
PCT/CH2004/000664 WO2005098237A1 (fr) | 2004-04-07 | 2004-11-02 | Pompe centrifuge a vis |
CNB2004800426761A CN100419271C (zh) | 2004-04-07 | 2004-11-02 | 螺旋离心泵和使用该螺旋离心泵输送介质的方法 |
RU2006139075/06A RU2358159C2 (ru) | 2004-04-07 | 2004-11-02 | Винтовой центробежный насос |
JP2007506630A JP5070039B2 (ja) | 2004-04-07 | 2004-11-02 | スクリュー遠心ポンプおよびスクリュー遠心ポンプを使用した、固体添加物で満たされた液体の運搬方法 |
US10/588,736 US7510368B2 (en) | 2004-04-07 | 2004-11-02 | Screw-centrifugal pump |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP04405214A EP1584820B1 (fr) | 2004-04-07 | 2004-04-07 | Pompe à écoulement mixte |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1584820A1 EP1584820A1 (fr) | 2005-10-12 |
EP1584820B1 true EP1584820B1 (fr) | 2006-06-14 |
Family
ID=34896183
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP04405214A Expired - Lifetime EP1584820B1 (fr) | 2004-04-07 | 2004-04-07 | Pompe à écoulement mixte |
Country Status (9)
Country | Link |
---|---|
US (1) | US7510368B2 (fr) |
EP (1) | EP1584820B1 (fr) |
JP (1) | JP5070039B2 (fr) |
CN (1) | CN100419271C (fr) |
AT (1) | ATE330126T1 (fr) |
DE (1) | DE502004000769D1 (fr) |
DK (1) | DK1584820T3 (fr) |
RU (1) | RU2358159C2 (fr) |
WO (1) | WO2005098237A1 (fr) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2169234A2 (fr) | 2007-07-17 | 2010-03-31 | Gerardus Augustinus Maria Manshanden | Pompe submersible sans risque pour les poissons |
CN112636910A (zh) * | 2020-12-29 | 2021-04-09 | 北京深思数盾科技股份有限公司 | 临时密码的生成与验证方法、设备及系统 |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5404140B2 (ja) * | 2009-04-01 | 2014-01-29 | 株式会社東芝 | テンプレート及び半導体装置の製造方法 |
US8506236B2 (en) * | 2009-08-03 | 2013-08-13 | Ebara International Corporation | Counter rotation inducer housing |
US8550771B2 (en) * | 2009-08-03 | 2013-10-08 | Ebara International Corporation | Inducer for centrifugal pump |
US20110027071A1 (en) * | 2009-08-03 | 2011-02-03 | Ebara International Corporation | Multi-stage inducer for centrifugal pumps |
US9631622B2 (en) * | 2009-10-09 | 2017-04-25 | Ebara International Corporation | Inducer for centrifugal pump |
EP2397698B1 (fr) * | 2010-06-17 | 2012-09-26 | Frideco AG | Dispositif d'acheminement |
CN102400919A (zh) * | 2011-11-18 | 2012-04-04 | 江苏国泉泵业制造有限公司 | 一种固液两相流螺旋离心泵 |
CN102661282A (zh) * | 2012-04-16 | 2012-09-12 | 杭州萧山美特轻工机械有限公司 | 开式螺旋纸浆泵 |
CN103195755B (zh) * | 2013-04-11 | 2015-10-07 | 南京布鲁克林环保设备有限公司 | 一种单叶片螺旋离心叶轮 |
EP2894342B1 (fr) * | 2014-01-12 | 2016-12-28 | Alfa Laval Corporate AB | Pompe centrifuge à amorçage automatique |
DK2894343T3 (en) | 2014-01-12 | 2017-12-11 | Alfa Laval Corp Ab | SELF-TILTING CENTRIFUGAL PUMP |
US10094384B2 (en) | 2014-01-24 | 2018-10-09 | Mcfinn Technologies, Llc | Radial impeller and casing for centrifugal pump |
KR102231079B1 (ko) * | 2014-07-08 | 2021-03-24 | 엘지전자 주식회사 | 배수 펌프 어셈블리 및 이를 구비하는 의류 건조기 |
KR101588137B1 (ko) * | 2014-10-24 | 2016-01-22 | 엘지전자 주식회사 | 배수 펌프 어셈블리 및 이를 구비하는 의류 건조기 |
DE102020125805A1 (de) * | 2020-10-02 | 2022-04-07 | Frideco Ag | Pumpensystem und Verfahren zum Betrieb eines Pumpensystems |
CN115994394B (zh) * | 2023-02-21 | 2023-11-17 | 上海中韩杜科泵业制造有限公司 | 离心泵叶轮造型方法、装置以及设备 |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
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CH394814A (de) * | 1961-08-29 | 1965-06-30 | Staehle Marin | Schneckenradpumpe |
AT255912B (de) * | 1964-07-01 | 1967-07-25 | Schlesiger & Co Kg Feluwa | Schmutzwasser-Kreiselpumpe |
GB1315547A (en) | 1969-05-23 | 1973-05-02 | Staehle M | Axial flow pump for pumping liquids containing solids in suspension |
JPS5136721Y2 (fr) * | 1973-09-06 | 1976-09-09 | ||
JPS5357507A (en) * | 1976-11-04 | 1978-05-24 | Kubota Ltd | Cutter underwater pumps |
FR2460404A1 (fr) | 1979-07-05 | 1981-01-23 | Schneider Hans Ulrich | Pompe pour le transport de fluides |
SU1132062A1 (ru) | 1983-03-10 | 1984-12-30 | Научно-Исследовательский И Конструкторско-Технологический Институт Городского Хозяйства | Центробежный насос дл перекачивани неоднородных сред |
SU1286817A1 (ru) | 1985-04-09 | 1987-01-30 | Центральный Научно-Исследовательский И Проектно-Технологический Институт Механизации И Электрификации Животноводства Южной Зоны Ссср | Насос |
ES2015517B3 (es) * | 1986-02-14 | 1991-04-16 | Rohren- Und Pumpenwerk Rudolf Bauer Ag | Bomba centrifuga autoaspirante para tratamiento y transporte de liquidos con alto contenido en fibra. |
US4778336A (en) * | 1987-07-09 | 1988-10-18 | Weil Pump Company | Cutter pump subassembly |
SU1677371A1 (ru) | 1989-06-08 | 1991-09-15 | А. Э. Кин, О. В. Дадашев и А. И. Рудштейн | Насос дл перекачивани неоднородных сред |
CN2388377Y (zh) * | 1999-08-06 | 2000-07-19 | 山东青州市南张石油机械厂 | 一种剪切泵预剪切装置 |
-
2004
- 2004-04-07 DK DK04405214T patent/DK1584820T3/da active
- 2004-04-07 AT AT04405214T patent/ATE330126T1/de not_active IP Right Cessation
- 2004-04-07 DE DE502004000769T patent/DE502004000769D1/de not_active Expired - Lifetime
- 2004-04-07 EP EP04405214A patent/EP1584820B1/fr not_active Expired - Lifetime
- 2004-11-02 RU RU2006139075/06A patent/RU2358159C2/ru not_active IP Right Cessation
- 2004-11-02 JP JP2007506630A patent/JP5070039B2/ja active Active
- 2004-11-02 WO PCT/CH2004/000664 patent/WO2005098237A1/fr active Application Filing
- 2004-11-02 US US10/588,736 patent/US7510368B2/en active Active
- 2004-11-02 CN CNB2004800426761A patent/CN100419271C/zh active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2169234A2 (fr) | 2007-07-17 | 2010-03-31 | Gerardus Augustinus Maria Manshanden | Pompe submersible sans risque pour les poissons |
CN112636910A (zh) * | 2020-12-29 | 2021-04-09 | 北京深思数盾科技股份有限公司 | 临时密码的生成与验证方法、设备及系统 |
Also Published As
Publication number | Publication date |
---|---|
US7510368B2 (en) | 2009-03-31 |
WO2005098237A1 (fr) | 2005-10-20 |
RU2006139075A (ru) | 2008-05-20 |
CN100419271C (zh) | 2008-09-17 |
EP1584820A1 (fr) | 2005-10-12 |
DK1584820T3 (da) | 2006-07-31 |
DE502004000769D1 (de) | 2006-07-27 |
JP5070039B2 (ja) | 2012-11-07 |
RU2358159C2 (ru) | 2009-06-10 |
CN1926338A (zh) | 2007-03-07 |
US20070172345A1 (en) | 2007-07-26 |
ATE330126T1 (de) | 2006-07-15 |
JP2007532812A (ja) | 2007-11-15 |
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