![]() ANMA CONTAINER WITH SEVERAL STIRRERS
专利摘要:
The invention relates to a mixing container (1) having a bottom (5), a container wall (3) and a cover (7) with at least one obliquely mounted first agitator (9), the second agitator (11) having a substantially vertically arranged stirring shaft (15) is provided. 公开号:AT510522A2 申请号:T1436/2011 申请日:2011-10-04 公开日:2012-04-15 发明作者:Peter Rohn 申请人:Roehm Gmbh;Streisal Gmbh; IPC主号:
专利说明:
4. OK '. 2011 13:05 ROHN FACTORY REPRESENTATIVES NO. 036 * · · · · · · · · · · S: IB5DUP DUPDKA 201010 12070004EN-2010072l39.doc applicant; Rohn GmbH Hauptetr. 38 91610 Insingen streisal GmbH and Pettermandstr. 2 88239 cheeks 35690001DE 08.10.2010 THE / JLG Title: Intake container with several agitators description The invention relates to pre-wells or hydrolysis and / or Anmiachbehälter and a stirrer, such as those used in biogas production. In the context of the invention, the following is always spoken of mixing containers; This term encompasses all containers from the field of biogas production and sewage treatment. 04/10/2011 14:11 No .: R205 P.005 / 020 4. 0 <T. 2011 13:06 ROHM FACTORY REPRESENTATIVES MR, 036 S, 6 • · · * «% * m 2 Mixing containers serve to provide substrate for the feeding of fermenters. Substrate is a mixture of renewable raw materials (Nawaro) such as silage of maize and grass, cereals - GPS, solid manure, etc. and slurry or recirculation of fermented substrate (recirculate) from repository, Nachgärer or fermenter. The uniform distribution of the solids contained in the components, which is necessary for optimum biogas production, places special demands on the mixing technique for the following reasons: severe miscibility due to temporarily very high dry matter content (nonaqueous, since liquid fraction is bound in the cell structure), Sinking and floating layers and resulting rapid separation, preferably large amounts in a short time (from the wheel loader in a corresponding large chute), but also cyclically via solids metering with plug screw or conveyor belts or pumps and / or changing levels in the container (eg filling 1 x per day and then cyclical emptying over 24 hours), but also constant levels (with cyclic filling and emptying) 04/10/2011 14:11 No .: R205 P.006 / 020 L-OCT. 2011 13:06 ROHN FACTORY REPRESENTATIVES NO. 0 36 p. 7 3 So far, only submersible agitators, obliquely installed Stabrührverke or vertical agitators are used in pre-pits, slurry pits / containers, mixing tanks, etc. Submersible mixers can normally be adjusted in height on a vertical guide rail. The disadvantage is the high power consumption and the tendency to form caverns (stirring in their own juice) at high dry matter contents (TS contents) .The working height must also be adjusted manually (labor-intensive) to the frequently changing fill levels. In the known obliquely installed Stabrührwerken the storage of these agitators takes place on one side of the concrete ceiling of the container. Accordingly, due to the design, only limited bending moments can be absorbed by the stirrer shaft or by the entire receiving / ceiling construction, which in turn only permits small propeller diameters. This results in a higher operating speed and a high power consumption. The so-called vertical agitators, for example, individually installed either in the middle or classically on the half radius of the container. This arrangement has proven very useful in aqueous as well as higher viscosity, homogeneous liquids in the past. The use in mixing containers with the mentioned difficult conditions of use has at least a very high energy requirement in a full mixing of the container to result. Also 04/10/2011 14:11 No .: R205 P.007 / 020 4. OCT. 2011 13:06 ROHN FACTORY REPRESENTATIVES NO. 036 p. 8 4 the use in large containers with a diameter of more than 6 m is no longer possible, because in the external area (wall friction) "dead zones" are created. form where the aufaufwimmende silage collects. The invention has for its object to provide a Anmiechbehälter with at least one agitator, which at least partially overcomes the disadvantages of the prior art and in particular is optimized in terms of energy requirements and the use in large containers of z. B. 9m diameter allowed. The inventive combination of preferably an inclined and a vertically mounted agitator adapted to the particular Rühraufgabe, and therefore usually also different types of propellers, it is possible on the one hand to generate a vertical flow for intermixing 'newly introduced substrate and on the other hand, a circulation effect in the container, so that the entire contents of the container is repeatedly pushed to the point of the strongest flow and as a result, the mixing is improved. 04/10/2011 14:12 No .: R205 P.008 / 020 4. OCT. 2011 13: 0 ROHM FACTORY REPRESENTATIVES NO. 036 p. 9 5 The inclined agitator ensures a circulation in the tank due to its large horizontal flow components, the vertically installed agitator predominantly takes over the mixing and avoidance of the dissolution of sinking and floating echoes. Both or one of the two agitators become close (approx. 0.5 m) installed at the filling opening. The combination of other pairings is also conceivable (for example two inclined stirrers). Another important aspect of the claimed invention is the very small margin of one or more propellers from the vessel wall. As a result, the increased wall friction can be better overcome and thus the adhesion of substrate can be prevented. Thus, it is also possible to stir containers with diameters of, for example, 8 or 9 m also in the edge region without, for example, comes to the formation of silage carpets. The stirrer shafts of the stirrers are preferably mounted with an abutment on the bottom of the container, so that the stability and the load capacity of the stirrers are increased by the double storage / which is particularly advantageous at high TS levels and changing levels. There are, preferably, large diameter and low speed propellers to produce maximum thrust at 04/10/2011 14:12 No .: R205 P.009 / 020 4th OCT, 201 1 13:07 ROHN WORKS 'RESPONSIBILITY NO. 036 $. 10 * · «6 Preferably, large diameter, low speed propellers are used to produce maximum thrust with the least possible energy input. Different shapes and diameters for adaptation to the specific container geometry and mixing task. In particular, Streisal large-wing propellers can be used, which are characterized in that the propeller blades can be separated or folded away from the propeller hub, so that an assembly even with small openings in the ceiling of the container is possible. The installation and removal takes place in disassembled or folded state. In order to minimize the detrimental effect of especially unilaterally drowning propellers obliquely mounted agitators, for example, with decreasing levels, preferably the Streisal SAFEGUARD is used. This device identifies impermissible torque peaks, which occur as a result of striking the propeller blade against the substrate surface) and automatically reduces the speed of the affected agitator until safe operation is ensured. Increasing the reduced speed to the preset speed setpoint is also automatic. Hereinafter, embodiments of the claimed invention are shown with reference to the accompanying drawings and the associated reference numerals. Regarding constructive details of the agitators is on the utility model DE 20 2006 Oll 144 and DE 20 2006 013 548 04/10/2011 14:12 No .: R205 P.010 / 020 4. OCT. 2011 13:07 ROHN WORKSVERREAM NO. 036 p. 11 t · 4 · fc * " * * «·· ♦ *« J 7 streisal GmbH. The content of this utility model is hereby incorporated in the disclosure of the present patent application. FIG. 1 a to f) FIG. 2 a) to f) v_ / I (mixing) container 3 container wall 5 bottom 7 ceiling 9 first agitator with inclined agitator shaft 15 II second agitator with vertically arranged agitator shaft 15 13 drive motor 15 agitator shaft 17.1. 17.2 Propeller 19 Bearing unit at the bottom 5 of the container 21 gearbox (at the same time upper bearing of agitator shaft 15J 04/10/2011 14:13 No .: R205 P.011 / 020
权利要求:
Claims (7) [1] 4th OCT. 2011 13:07 ROHN FACTORY REPRESENTATIVES NO. 036 p. 12 * · · * * ·· ·· * · ** · »I * I *: ΐ * * * * t *. Claims 1. A mixing container (1) having a bottom (5), a container wall (3) and a cover (7) with at least one obliquely installed first stirrer (9), characterized in that a second agitator (11) is provided with a substantially vertically arranged RUhrwelle (15). [2] 2. Mixing container according to one of the preceding claims, characterized in that a further agitator is provided with obliquely or vertically arranged agitator shaft (15). [3] 3. Mixing container according to one of the preceding claims, characterized in that the stirring shaft (15) of at least one agitator (9, 11) in the region of the ceiling (7) and on the bottom () of the container (l) is mounted. [4] 4. A method for operating the agitators (9, 11) of a mixing container (1), wherein the mixing container (1) comprises a first agitator (9) with an inclined stirring shaft (15) and a second agitator (11) having a substantially vertical arranged stirrer shaft (15), characterized in that the first agitator (9) and / or the second agitator (11) time-controlled and / or event-controlled switched on and / or off 04/10/2011 14:13 No .: R205 P. 012/020 [5] 4th OCT. 2011 13:08 ROHN FACTORY REPRESENTATIVES NO. 036 p. 13 * * · · · * «· 9 [6] 5. The method according to claim 4, characterized in that the control takes place in dependence on the loading and / or unloading of the mixing container (1). [7] 6. The method according to claim 4 or 5, characterized in that the first agitator (9) and the second agitator (11) are operated simultaneously or with a time offset. Ί. Method according to one of claims 4 to 1, characterized in that the control comprises a control, in particular a power control and / or a speed control. 04/10/2011 14:13 No .: R205 P.013 / 020
类似技术:
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同族专利:
公开号 | 公开日 DE102011114793A1|2012-04-12| AT510522A3|2014-06-15|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题 CH695239C1|2000-01-21|2009-11-30|Rosenmund Vta Ag|Device for treating substances.| DE10123637B4|2001-05-07|2008-02-28|Thomas Falkenstein Gewerbliche Vermietung Und Verpachtung E.K.|Propeller agitator for stirring crude oil| DE102004027077B4|2004-06-02|2007-05-31|Schmack Biogas Ag|Heatable agitator for fermentation tanks| DE202006020195U1|2005-09-02|2008-01-31|Agraferm Technologies Ag|Agitator for a fermenter and fermenter| DE202006011144U1|2006-07-13|2007-11-29|Envicon Klärtechnik GmbH & Co. KG|Hollow shaft for a stirrer| DE202006013548U1|2006-09-01|2008-01-10|Envicon Klärtechnik GmbH & Co. KG|Stirring device for a gas-tight sealed container|DE102012222589A1|2012-12-07|2014-06-12|Planungsbüro Rossow Gesellschaft für erneuerbare Energien mbH|SUBSTRATE CIRCUIT FOR BIOGAS PLANTS IN A CONNECTION AND COMBI HYDROLYSIS CONTAINER| SE538527C2|2014-06-17|2016-09-06|Xylem Ip Man S À R L|Plant for the treatment of liquid and method for controlling such a plant| DE102014116239A1|2014-11-07|2016-05-12|Uts Biogastechnik Gmbh|Method for operating a stirring device and a fermenter| DE102015106419A1|2015-04-27|2016-10-27|Stefan Steverding Sondermaschinen- und Vorrichtungsbau GmbH|Agitator and container with stirrer| DE102018133226A1|2018-12-20|2020-06-25|Jean-Marc Peters|Container and method for installing an agitator in a container|
法律状态:
2016-05-15| REJ| Rejection|Effective date: 20160515 |
优先权:
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