EP1064133B1 - Method for producing foaming substances, especially foaming cement substances, and corresponding device - Google Patents
Method for producing foaming substances, especially foaming cement substances, and corresponding device Download PDFInfo
- Publication number
- EP1064133B1 EP1064133B1 EP99916759A EP99916759A EP1064133B1 EP 1064133 B1 EP1064133 B1 EP 1064133B1 EP 99916759 A EP99916759 A EP 99916759A EP 99916759 A EP99916759 A EP 99916759A EP 1064133 B1 EP1064133 B1 EP 1064133B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- flow
- product flow
- product
- jet pump
- mixing reactor
- 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
- 239000004568 cement Substances 0.000 title claims abstract description 27
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 21
- 239000000126 substance Substances 0.000 title claims abstract 9
- 238000005187 foaming Methods 0.000 title claims abstract 8
- 239000004088 foaming agent Substances 0.000 claims abstract description 27
- 230000036961 partial effect Effects 0.000 claims description 43
- 238000000034 method Methods 0.000 claims description 22
- 230000001681 protective effect Effects 0.000 claims description 8
- 230000001105 regulatory effect Effects 0.000 claims description 4
- 238000001739 density measurement Methods 0.000 claims description 2
- 230000003068 static effect Effects 0.000 claims description 2
- 239000006260 foam Substances 0.000 description 61
- 239000003570 air Substances 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000003795 chemical substances by application Substances 0.000 description 9
- 239000000203 mixture Substances 0.000 description 7
- 239000004570 mortar (masonry) Substances 0.000 description 5
- 239000011148 porous material Substances 0.000 description 4
- 230000002829 reductive effect Effects 0.000 description 4
- 238000005259 measurement Methods 0.000 description 3
- 230000000717 retained effect Effects 0.000 description 3
- 239000011362 coarse particle Substances 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000002411 adverse Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000011381 foam concrete Substances 0.000 description 1
- 239000006261 foam material Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 239000008240 homogeneous mixture Substances 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000003380 propellant Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C5/00—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
- B28C5/38—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions wherein the mixing is effected both by the action of a fluid and by directly-acting driven mechanical means, e.g. stirring means ; Producing cellular concrete
- B28C5/381—Producing cellular concrete
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/29—Mixing systems, i.e. flow charts or diagrams
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/30—Injector mixers
- B01F25/31—Injector mixers in conduits or tubes through which the main component flows
- B01F25/311—Injector mixers in conduits or tubes through which the main component flows for mixing more than two components; Devices specially adapted for generating foam
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/82—Combinations of dissimilar mixers
- B01F33/821—Combinations of dissimilar mixers with consecutive receptacles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C5/00—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
- B28C5/38—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions wherein the mixing is effected both by the action of a fluid and by directly-acting driven mechanical means, e.g. stirring means ; Producing cellular concrete
- B28C5/381—Producing cellular concrete
- B28C5/386—Plants; Systems; Methods
Definitions
- the invention relates to a method of manufacture of foam materials, in particular foam cement materials, which are essentially from a starting product, in particular cement paste, and a foaming agent, in one over one Feed pump with a storage container for the starting product related mixing reactor and an apparatus therefor.
- Foam masses or foam cement masses are used in modern Building technology, especially when renovating old buildings as well as in the construction of new buildings, often used.
- In the production of walkable floors, screeds, etc. must usually to compensate for height differences on the bare floor, Depressions, cavities and the like applied in order to manufacture the further floor structure. This balance is generally achieved by installing foamed sheets and / or the use of loose fillings of insulation materials accomplished.
- these are known compensation procedures very labor intensive and therefore expensive. in the they are also questionable from an occupational medical point of view.
- foam mass in which a different binder is used instead of cement, or foam cement mass is carried out by mixing air, water and a foaming agent into a foam.
- This foam is fed to a mixing device at the processing site and introduced into a cement paste consisting of cement and water.
- This manufacturing process is almost exclusively suitable for the production of a so-called heavy foam with a foam density of more than 800kg / m 3 .
- DE 41 18 537 C1 discloses a method for producing a so-called lightweight foam with a foam density between 250 and 400kg / m 3 and an apparatus for carrying out the method.
- cement paste is injected into a mixing chamber under high pressure and mixed with a foaming agent. Due to the high pressure, this mixture is fed to an expansion nozzle into which compressed air is blown in to foam.
- DE 36 31 223 A1 shows a device for Production of a hardening foam mass with a fine pore structure, in particular a cement foam mass that a Pipe supplied and arranged in the pipe transport and Mixing tools both transported and mixed becomes.
- the water and foaming agent Foam mass is via the transport path formed by the tube distributed from outside. This is intended to reduce the water content the foam mass that adversely affects curing the same affects, are reduced.
- DE 32 22 033 A1 describes a process for the production a pore mortar with a low specific Weight described using compressed air.
- the device is used to carry out the method Perforated plates exist in a row in a pipe are arranged and through which the mortar mass flows. By appropriate connections, the compressed air is introduced into the pipe, where it mixes with the mortar.
- DE-A-23 48 915 discloses a plant for the production of foam cement, each with a volumetric pump for pumping water, foam, air and cement paste or mortar. Pumps for water, foam and the air is connected to a foam-forming sling, which is connected to a collector in which the cement or mortar is promoted. The mixture is from the collector transported to a mixing machine at the point of use.
- the known devices and methods are disadvantageous in that than the consistency and thus the quality of the Foam masses or foam cement masses through the multitude of consecutive mixing and conveying units changed. Furthermore, the known systems are only for production of foam masses in a very restricted density range suitable and very complex using a variety built by auxiliary units.
- UA-A-5 556 033 describes a device for manufacturing a sprayable foam mass for a weatherproof Protective cover known to cover a waste dump (Landfill).
- the device comprises a storage container in which an agitator is arranged with a mixer is connected and to promote the foam mass is coupled with a pumper that blends the mixture into one Control valve transported. From this regulator valve an outlet leads to an injection device, on the one hand via a pipeline to the storage container and to the other via an inlet channel in connection with a foam generator stands.
- the foam generator comprises a foam agent tank which is coupled to an injector, the injector to make a foam with a Compressor for generating compressed air is connected.
- the one with Compressed air produced foam is through a nozzle of the injection device fed and passes through the pipeline into the storage container in which the foam with the agitator is mixed into a slurry, which in turn is from the Pump is fed to the regulating valve. From the regulating valve a partial flow is coupled through a pipeline Jet nozzle discharged and a product stream in turn passed to the injector in which the product flow Foam is fed, after which the product flow through the pipeline again gets into the storage container.
- DE-A-31 32 667 discloses a method and a device for producing porous or foam concrete or the like, with foaming agents, water and Compressed air for producing a raw material to be mixed Foam can be merged.
- the foam agent supply is controlled by the inflowing water.
- to Carrying out the process is the water inflow as a jet pump trained for the liquid foaming agent, its inflow opens directly at the jet pump nozzle.
- the course is the supply of compressed air for processing of the foaming agent provided, which is then a Foam lance gets into a mixing vessel, where the now formed Foam is mixed with the starting product.
- From US-A-2 733 053 is a mixing machine for manufacturing a foam cement mass known, the principle of which is based on to circulate a solid material in a mixing reactor and with to mix different components, being in the mixing reactor a rotating agitator is arranged.
- the components are a water tank 16 and a cement tank 20 provided.
- the object is thereby achieved solved that a product stream taken from the mixing reactor under Supply of the foaming agent and atmospheric air in the Circulation the storage container kept at a minimum level is supplied via a jet pump, the product stream after a mixing phase, a partial flow for processing is removed and the product stream in the jet pump the foaming agent is added.
- the product stream flowing continuously through the mixing reactor essentially from that stored in the storage container
- Starting product, the foaming agent and atmospheric Air exists in an empirically determined mixing phase mixed with the starting product until one homogeneous foam mass of high quality is present.
- the mixing phase ended and the product stream becomes a partial stream taken for processing.
- the starting product for example cement glue
- the Product stream is with a truck mixer to the storage container at the processing point transported, its transport capacity not through the foaming agent is reduced because it is provided separately becomes.
- by adding the foaming agent pollution to the product stream in the jet pump greatly reduced during the production of the foam mass.
- a compressed gas is preferably added to the product stream.
- the compressed gas becomes the product stream in the jet pump added. This will cause excessive dust formation or contamination during the production of the foam mass greatly reduced and occupational health concerns always can occur as far as possible if there is a lot of dust be excluded.
- the amount of the product stream is expediently mixed Foam agent and / or the compressed gas measured and regulated. This measure allows the foam mass to be adjusted to a desired density, which is required for processing is. Furthermore, the foam agent is expediently and / or the compressed gas from a metering pump through a Flow meter conveyed to the jet pump.
- the partial flow a density measuring device. This continuously working facility serves to monitor the quality of the Partial flow.
- the density of the partial stream is preferably volumetric or determined gravimetrically.
- the partial flow is also preferred depending on the result of the density measurement of the processing point or fed to the storage container. A partial flow that does not meet the quality requirements therefore not for processing, but is together with the Product stream reprocessed.
- the task is done in a constructive way with a device for the production of foam compositions, in particular foam cement compositions, which essentially consists of a starting product, in particular cement paste, and a foaming agent, with one via a feed pump with a storage container for the Starting product related mixing reactor, in particular to carry out the aforementioned method according to the invention solved in that the mixing reactor one to one Jet pump leading outlet for a product stream, a outlet leading to a processing point for a Partial stream of the product stream and an inlet for the product stream from the reservoir, the product stream above the fill level of the storage container from the with an inlet for the jet pump exits and within the mixing reactor at least one static Mixing element is arranged.
- the mixing reactor is relatively compact constructed and can be in the immediate vicinity of a processing point place.
- the fact that the mixing reactor a separate outlet and an inlet for the product stream and an outlet for the partial stream of the product stream is the separate circulation of these streams possible. Only then is a partial stream removed from the product stream, which is supplied to the processing point when the Product stream has the required quality.
- the Outlet of the product flow above the fill level of the storage container the jet pump becomes a homogeneous mixture achieved to increase the quality of the foam mass is.
- the mixing element causes one Swirling of the product flow and thus the generation of a uniform mass in the mixing reactor.
- Fine protection screen fixed.
- the fine protection screen is expedient arranged before the outlet for the product stream, where the outlet for the product flow at one of the inlet for the product stream opposite side of the mixing reactor located. Because of this measure, larger particles of the product stream retained in the mixing reactor and the jet pump is protected from damage from these particles protected.
- the invention of the mixing reactor with an external vibrator in connection.
- the vibrator is to be set so that an already generated foam structure of the foam mass does not Damage suffers, after which an even and finely divided Air pore structure is retained in the foam mass.
- the vibrations of the mixing reactor are not full size to be transferred to the storage container is expedient the mixing reactor via a pipeline and a Hose with the intermediate feed pump with the Reservoir connected.
- the pipe inside with at least one Provide mixing element is preferred.
- the jet pump with an inlet for the Provide compressed gas. This measure makes the compressed gas direct into the jet pump or into the jet pump flowing through it Product flow initiated and pollution through uncontrolled escaping products is largely excluded.
- the jet pump is preferably each density Dosing pump for supplying the flow through a flow meter Foam agent and / or compressed gas assigned.
- connection line to the outlet for the partial flow of the product flow with interposed density measuring device assigned. It is also used to control the quantity discharged of the partial flow at the processing point the connecting line with a flow meter downstream of the density measuring device Mistake.
- This prevents the entry of coarse particles into the device is preferably the storage container with a Protective screen covered.
- Jet pump for the product stream a dosing jet pump for assigned a partial product stream that the foaming agent and / or the compressed gas feeds the partial product stream, after which the partial product stream enters the mixing reactor. by virtue of this measure becomes a certain density of the partial product flow set. After mixing the partial product stream with the product stream in the mixing reactor, a resulting density required for processing.
- the device for producing a foam composition comprises Fig. 1 essentially a storage container 1 for receiving of a starting product A, which is covered by a protective screen 2 is and via a feed pump 3 with a mixing reactor 4 communicates.
- the feed pump 3 is on the one hand via a hose 5 to the storage container 1 and to the other by means of a pipeline 6 to an inlet 7 of the Mixing reactor 4 connected for a product stream B.
- the Inner wall of the pipeline 6 is with mixing elements, not shown Mistake.
- the mixing reactor 4 carries 8 mixing elements on its inner walls 9 and is connected to an external vibrator 10. At the inlet 7 for the product stream B opposite The mixing reactor 4 faces one side Jet pump 11 leading outlet 12 for the product stream B as well an outlet 14 leading to a processing point 13 for a partial stream C of the product stream B. Before leaving 12 a fine protection screen 15 is fixed, which the passage prevents coarse particles. In the further is between the departure 12 and the jet pump 11, a shut-off valve 16 is arranged.
- the jet pump 11 has an inlet on its suction side 17 provided for a foam agent 18, which is via a metering pump 19 with downstream flow meter 20 the product stream B is added.
- the jet pump 11 also has a Inlet 21 for a compressed gas 22, which also has a Metering pump 23 with a downstream flow meter 24 Product stream B is supplied.
- the jet pump 11 is such arranged that the product stream B above the level 25 of the starting product A reaches the storage container 1.
- the partial stream C of the product stream B is through a connecting line 26 to a density measuring device 27 with a upstream shut-off valve 28 out.
- a density measuring device 27 In dependence of the measurement result of the density measuring device 27 reaches Partial flow C via a flow meter 29 the processing point 13 or via a return line 30 the reservoir 1.
- the jet pump 11 is for the product stream B. assigned a metering jet pump 31 for a partial product stream D.
- the product stream B reaches via a shut-off valve 32 provided supply line 33 a propellant nozzle 34.
- the product stream B is mixed with air or Gas 35 instead of the open entered in the jet pump 11 becomes.
- the jet pump 11 is followed by a diffuser 36, which opens into the mixing reactor 4.
- the partial product stream D is included the foam agent 18 and the compressed gas 22 intimately mixed, after which he also via the feed 37 in the mixing reactor 4 arrives.
- the mixing reactor 4 in turn becomes a product stream B in the reservoir 1 and a partial stream C to the processing point 13 headed.
- the method is carried out using a truck mixer the starting product A, consisting of cement and water, delivered that over the protective sieve 2 in the reservoir 1 arrives.
- the shut-off valve 28 for the partial flow C is closed and the product stream B is supplied with foam agent 18, Compressed gas 22 and atmospheric air are pumped into the circuit and mixed in the process.
- the product stream B by means of the feed pump 3 removed from the reservoir 1, through the pipeline 6 provided with mixing elements to the mixing reactor 4 transported and via the jet pump 11 into the reservoir 1 headed.
- the shut-off valve opens after the mixing phase 28 and the partial flow C flows through the density measuring device 27. Does the measurement result meet the requirements for Foam mass, the partial flow C via the flow meter 29th fed to the processing station 13. If the measurement result does not meet the requirements for the foam mass the partial flow C via the return line 30 into the storage container 1 initiated, after which further mixing takes place. During the removal of the partial stream C, the product stream B promoted in the cycle described above.
- a foam mass is produced from 3.8 m 3 of starting product A with a density between 1500 and 2500 kg / m 3 , which after a mixing phase of 60 seconds has a density between 100 and 1000 kg / m 3 with a uniformly distributed pore structure.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Structural Engineering (AREA)
- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Porous Artificial Stone Or Porous Ceramic Products (AREA)
Abstract
Description
Die Erfindung bezieht sich auf ein Verfahren zur Herstellung von Schaummassen, insbesondere Schaumzementmassen, die im wesentlichen aus einem Ausgangsprodukt, insbesondere Zementleim, und einem Schaummittel bestehen, in einem über eine Förderpumpe mit einem Vorratsbehälter für das Ausgangsprodukt in Verbindung stehenden Mischreaktor und eine Vorrichtung dazu.The invention relates to a method of manufacture of foam materials, in particular foam cement materials, which are essentially from a starting product, in particular cement paste, and a foaming agent, in one over one Feed pump with a storage container for the starting product related mixing reactor and an apparatus therefor.
Schaummassen bzw. Schaumzementmassen werden in der modernen Bautechnologie, insbesondere bei der Renovierung von Altbauten sowie bei der Erstellung von Neubauten, häufig verwendet. Bei der Herstellung von begehbaren Böden, Estrichen usw. muß in der Regel auf den Rohboden ein Ausgleich für Höhendifferenzen, Vertiefungen, Hohlräume und dergleichen aufgebracht werden, um den weiteren Bodenaufbau zu fertigen. Dieser Ausgleich wird im allgemeinen durch den Einbau geschäumter Platten und/oder die Verwendung loser Schüttungen von Dämmaterialien bewerkstelligt. Allerdings sind diese bekannten Ausgleichsverfahren sehr arbeitsintensiv und damit teuer. Im weiteren sind sie aus arbeitsmedizinischer Sicht bedenklich.Foam masses or foam cement masses are used in modern Building technology, especially when renovating old buildings as well as in the construction of new buildings, often used. In the production of walkable floors, screeds, etc. must usually to compensate for height differences on the bare floor, Depressions, cavities and the like applied in order to manufacture the further floor structure. This balance is generally achieved by installing foamed sheets and / or the use of loose fillings of insulation materials accomplished. However, these are known compensation procedures very labor intensive and therefore expensive. in the they are also questionable from an occupational medical point of view.
Die Herstellung einer solchen Schaummasse, bei der statt Zement ein anderes Bindemittel verwendet wird, bzw. Schaumzementmasse erfolgt durch das Vermischen von Luft, Wasser und einem Schaummittel zu einem Schaum. Dieser Schaum wird einer am Verarbeitungsort stehenden Mischvorrichtung zugeführt und in einen Zementleim, bestehend aus Zement und Wasser, eingebracht. Dieses Herstellungsverfahren eignet sich nahezu ausschließlich zur Produktion eines sogenannten Schwerschaums mit einem Schaumdichte von mehr als 800kg/m3.The production of such a foam mass, in which a different binder is used instead of cement, or foam cement mass is carried out by mixing air, water and a foaming agent into a foam. This foam is fed to a mixing device at the processing site and introduced into a cement paste consisting of cement and water. This manufacturing process is almost exclusively suitable for the production of a so-called heavy foam with a foam density of more than 800kg / m 3 .
Die DE 41 18 537 C1 offenbart ein Verfahren zur Herstellung eines sogenannten Leichtschaumes mit einer Schaumdichte zwischen 250 und 400kg/m3 sowie eine Vorrichtung zur Durchführung des Verfahrens. Hierbei wird Zementleim unter hohem Druck in eine Mischkammer eingespritzt und mit einem Schaummittel vermischt. Diese Mischung wird aufgrund des hohen Druckes einer Expansionsdüse zugeleitet, in die dosiert Druckluft zum Aufschäumen eingeblasen wird.DE 41 18 537 C1 discloses a method for producing a so-called lightweight foam with a foam density between 250 and 400kg / m 3 and an apparatus for carrying out the method. Here, cement paste is injected into a mixing chamber under high pressure and mixed with a foaming agent. Due to the high pressure, this mixture is fed to an expansion nozzle into which compressed air is blown in to foam.
Des weiteren zeigt die DE 36 31 223 A1 eine Vorrichtung zur
Herstellung einer härtenden Schaummasse mit einer feinen Porenstruktur,
insbesondere einer Zementschaummasse, die einem
Rohr zugeführt und durch im Rohr angeordnete Transport- und
Mischwerkzeuge sowohl zwangstransportiert als auch zwangsgemischt
wird. Die aus Wasser und Schaumbildner bestehende
Schaummasse wird über den von dem Rohr gebildeten Transportweg
verteilt von außen zugegeben. Hierdurch soll der Wasseranteil
der Schaummasse, der sich negativ auf das Aushärten
derselben auswirkt, verringert werden.Furthermore,
Weiterhin ist in der DE 32 22 033 A1 ein Verfahren zur Herstellung eines Porenmörtels mit einem geringen spezifischen Gewicht unter Verwendung von Druckluft beschrieben. Zur Durchführung des Verfahrens dient eine Vorrichtung, die aus Lochblechen besteht, die in einer Rohrleitung hintereinander angeordnet sind und durch die die Mörtelmasse strömt. Durch entsprechende Anschlüsse wird die Druckluft in das Rohr eingeleitet, wo sie sich mit dem Mörtel vermischt.Furthermore, DE 32 22 033 A1 describes a process for the production a pore mortar with a low specific Weight described using compressed air. to The device is used to carry out the method Perforated plates exist in a row in a pipe are arranged and through which the mortar mass flows. By appropriate connections, the compressed air is introduced into the pipe, where it mixes with the mortar.
Ferner offenbart die DE-A-23 48 915 eine Anlage zur Herstellung von Schaumzement mit jeweils einer volumetrischen Pumpe zum Fördern von Wasser, Schaummittel, Luft und Zementleim oder Mörtel. Die Pumpen für das Wasser, das Schaummittel und die Luft sind mit einer schaumbildenden Schleuder verbunden, die an einen Sammler angeschlossen ist, in den der Zement bzw. Mörtel gefördert wird. Von dem Sammler wird das Gemisch zu einer Mischmaschine an der Verwendungsstelle transportiert.Furthermore, DE-A-23 48 915 discloses a plant for the production of foam cement, each with a volumetric pump for pumping water, foam, air and cement paste or mortar. Pumps for water, foam and the air is connected to a foam-forming sling, which is connected to a collector in which the cement or mortar is promoted. The mixture is from the collector transported to a mixing machine at the point of use.
Die bekannten Vorrichtungen und Verfahren sind insofern nachteilig, als sich die Konsistenz und damit die Qualität der Schaummassen bzw. Schaumzementmassen durch die Vielzahl der hintereinander geschalteten Misch- und Fördereinheiten verändert. Ferner sind die bekannten Anlagen nur zur Herstellung von Schaummassen in einem stark eingeschränkten Dichtebereich geeignet und sehr aufwendig unter der Verwendung einer Vielzahl von Hilfsaggregaten aufgebaut. The known devices and methods are disadvantageous in that than the consistency and thus the quality of the Foam masses or foam cement masses through the multitude of consecutive mixing and conveying units changed. Furthermore, the known systems are only for production of foam masses in a very restricted density range suitable and very complex using a variety built by auxiliary units.
Aus der UA-A-5 556 033 ist eine Vorrichtung zur Herstellung einer sprühbaren Schaummasse für einen wetterbeständigen Schutzüberzug bekannt, der zur Abdeckung einer Abfallhalde (Mülldeponie) dient. Die Vorrichtung umfaßt einen Vorratsbehälter in dem ein Rührwerk angeordnet ist, das mit einem Mischer in Verbindung steht und der zur Förderung der Schaummasse mit eine Pumper gekoppelt ist, die die Mischung zu einem Regulierventil transportiert. Von diesem Regulierventil führt ein Abgang zu einer Einspritzeinrichtung, die zum einen über eine Rohrleitung mit dem Vorratsbehälter und zum anderen über einen Einlaßkanal mit einem Schaumerzeuger in Verbindung steht. Der Schaumerzeuger umfaßt einen Schaummitteltank, der mit einer Einspritzeinrichtung gekoppelt ist, wobei die Einspritzeinrichtung zur Herstellung eines Schaums mit einem Kompressor zur Erzeugung von Druckluft verbunden ist. Der mit Druckluft hergestellte Schaum wird über eine Duse der Einspriteinrichtung zugeführt und gelangt über die Rohrleitung in den Vorratsbchälter, in dem der Schaum mit dem Rührwerk unter eine Aufschlämmung gemischt wird, die wiederum von der Pumpe zu dem Regulierventil gefördert wird. Von dem Regulierventil wird ein Teilstrom durch eine Rohrleitung mit gekoppeltor Strahldüse ausgetragen und ein Produktstrom wiederum zu der Einspritzeinrichtung geleitet, in der dem Produktstrom Schaum zugeführt wird, wonach der Produktstrom über die Rohrleitung wiederum in den Vorratsbehälter gelangt.UA-A-5 556 033 describes a device for manufacturing a sprayable foam mass for a weatherproof Protective cover known to cover a waste dump (Landfill). The device comprises a storage container in which an agitator is arranged with a mixer is connected and to promote the foam mass is coupled with a pumper that blends the mixture into one Control valve transported. From this regulator valve an outlet leads to an injection device, on the one hand via a pipeline to the storage container and to the other via an inlet channel in connection with a foam generator stands. The foam generator comprises a foam agent tank which is coupled to an injector, the injector to make a foam with a Compressor for generating compressed air is connected. The one with Compressed air produced foam is through a nozzle of the injection device fed and passes through the pipeline into the storage container in which the foam with the agitator is mixed into a slurry, which in turn is from the Pump is fed to the regulating valve. From the regulating valve a partial flow is coupled through a pipeline Jet nozzle discharged and a product stream in turn passed to the injector in which the product flow Foam is fed, after which the product flow through the pipeline again gets into the storage container.
Die DE-A-31 32 667 offenbart ein verfahren und eine Einrichtung zum Erzeugen von Poren- oder Schaumbeton oder dergleichen, wobei in dosierten Mengen Schaummittel, Wasser und Druckluft zur herstellung eines einem Ausgangsprodukt beizumischenden Schaums zusammengeführt werden. Die Schaummittelzufuhr wird durch das zuströmende Wasser gesteuert. Zur Durchfuhrung des Verfahrens ist der Wasserzufluß als Strahlpumpe für das flüssige Schaummittel ausgebildet, dessen Zufluß unmittelbar an der Düse der Strahlpumpe mündet. Im weiteren Verlauf ist die Zufuhr von Druckluft zur Aufbereitung des Schaummittels vorgesehen, das anschließend über eine Schaumlanze in ein Mischgefäß gelangt, wo der nunmehr gebildete Schaum mit dem Ausgangsprodukt vermischt wird.DE-A-31 32 667 discloses a method and a device for producing porous or foam concrete or the like, with foaming agents, water and Compressed air for producing a raw material to be mixed Foam can be merged. The foam agent supply is controlled by the inflowing water. to Carrying out the process is the water inflow as a jet pump trained for the liquid foaming agent, its inflow opens directly at the jet pump nozzle. In the further The course is the supply of compressed air for processing of the foaming agent provided, which is then a Foam lance gets into a mixing vessel, where the now formed Foam is mixed with the starting product.
Aus der US-A-2 733 053 ist eine Mischmaschine zur Herstellung
einer Schaumzementmasse bekannt, deren Prinzip darauf beruht,
ein festes Material in einem Mischreaktor umzuwälzen und mit
verschiedenen Komponenten zu vermischen, wobei in dem Mischreaktor
ein umlaufendes Rührwerk angeordnet ist. Zur Bevorratung
der Komponenten sind ein Wassertank 16 und ein Zementtank
20 vorgesehen. From US-A-2 733 053 is a mixing machine for manufacturing
a foam cement mass known, the principle of which is based on
to circulate a solid material in a mixing reactor and with
to mix different components, being in the mixing reactor
a rotating agitator is arranged. For storage
the components are a
Es ist Aufgabe der Erfindung, ein Verfahren zur Herstellung von Schaummassen, insbesondere Schaumzementmassen, der eingangs genannten Art und eine Vorrichtung zur Durchführung des Verfahrens zu schaffen, das bzw. die an einer Verarbeitungsstelle zum Einsatz kommt und eine hohe Qualität der hergestellten Schaummassen gewährleistet.It is the object of the invention to produce a method of foam masses, especially foam cement masses, of the beginning mentioned type and a device for performing the Process to create that at a processing point is used and a high quality of the manufactured Foam masses guaranteed.
Die Aufgabe wird nach der Erfindung verfahrensgemäß dadurch gelöst, daß ein dem Mischreaktor entnommener Produktstrom unter Zuführung des Schaummittels und atmosphärischer Luft im Kreislauf dem auf einem Mindestfüllstand gehaltenen Vorratsbehälter über eine Strahlpumpe zugeführt wird, wobei dem Produktstrom nach einer Einmischphase ein Teilstrom für die Verarbeitung entnommen wird und dem Produktstrom in der Strahlpumpe das Schaummittel beigemischt wird.According to the invention, the object is thereby achieved solved that a product stream taken from the mixing reactor under Supply of the foaming agent and atmospheric air in the Circulation the storage container kept at a minimum level is supplied via a jet pump, the product stream after a mixing phase, a partial flow for processing is removed and the product stream in the jet pump the foaming agent is added.
Der den Mischreaktor kontinuierlich durchstromende Produktstrom, der im wesentlichen aus dem im Vorratsbehälter gelagerten Ausgangsprodukt, dem Schaummittel sowie atmosphärischer Luft besteht, wird in einer empirisch ermittelten Einmischphase solange mit dem Ausgangsprodukt vermischt, bis eine homogene Schaummasse hoher Qualität vorliegt. Nachdem der Produkrstrom eine homogene Konsistenz aufweist, ist die Einmischphase beendet und dem Produktstrom wird ein Teilstrom für die Verarbeitung entnommen. Auch nach der Einmischphase wird der Produktstrom im Kreislauf durch den Mischreaktor geleitet, wodurch dessen hohe Qualität und damit die Qualität des Teilstroms für die Verarbeitung erhalten bleibt. Das Ausgangsprodukt, beispielsweise Zementleim, wird mit einem Fahrmischer zu dem Vorratsbehälter an der Verarbeitungsstelle transportiert, wobei dessen Transportkapazität nicht durch das Schaummittel reduziert ist, da dieses separat bereitgestellt wird. Zur Sicherstellung einer intensive Vermischung des Produktstromes mit der atmosphärischen Luft, wird der Produktstrom über eine Strahlpumpe in den Vorratsbehälter geleitet. Darüberhinaus wird durch das Beimischen des Schaummittels zu dem Produktstrom in der Strahlpumpe die Verschmutzung während der Herstellung der Schaummasse stark reduziert.The product stream flowing continuously through the mixing reactor, essentially from that stored in the storage container Starting product, the foaming agent and atmospheric Air exists in an empirically determined mixing phase mixed with the starting product until one homogeneous foam mass of high quality is present. After the Product flow has a homogeneous consistency, is the mixing phase ended and the product stream becomes a partial stream taken for processing. Even after the mixing phase the product stream is circulated through the mixing reactor, whereby its high quality and thus the quality of the substream for processing is retained. The starting product, for example cement glue, is with a truck mixer to the storage container at the processing point transported, its transport capacity not through the foaming agent is reduced because it is provided separately becomes. To ensure intensive mixing of the product flow with the atmospheric air, the Product stream fed into the storage container via a jet pump. In addition, by adding the foaming agent pollution to the product stream in the jet pump greatly reduced during the production of the foam mass.
Insbesondere zur Herstellung einer Schaummasse mit einer geringen Dichte werden neben dem Schaummittel weitere Zuschläge benötigt. Bevorzugt wird dem Produktstrom ein Druckgas beigemischt.In particular for the production of a foam mass with a low In addition to the foaming agent, additional densities become dense needed. A compressed gas is preferably added to the product stream.
Nach einer vorteilhaften Ausgestaltung des Erfindungsgedankens wird in der Strahlpumpe dem Produktstrom das Druckgas beigemischt. Hierdurch wird eine übermäßige Staubbildung bzw. eine Verschmutzung während der Herstellung der Schaummasse stark reduziert und arbeitsmedizinische Bedenken, die stets bei einer starken Staubbildung auftreten, können weitestgehend ausgeschlossen werden.According to an advantageous embodiment of the inventive concept the compressed gas becomes the product stream in the jet pump added. This will cause excessive dust formation or contamination during the production of the foam mass greatly reduced and occupational health concerns always can occur as far as possible if there is a lot of dust be excluded.
Zweckmäßigerweise wird die Menge des dem Produktstrom beidemischten Schaummittels und/oder des Druckgases gemessen und geregelt. Diese Maßnahme erlaubt das Einstellen der Schaummasse auf eine gewünschte Dichte, die zur Verarbeitung erforderlich ist. Weiterhin wird zweckmäßigerweise das Schaummittel und/oder das Druckgas von einer Dosierpumpe durch einen Durchflußmesser zu der Strahlpumpe gefördert.The amount of the product stream is expediently mixed Foam agent and / or the compressed gas measured and regulated. This measure allows the foam mass to be adjusted to a desired density, which is required for processing is. Furthermore, the foam agent is expediently and / or the compressed gas from a metering pump through a Flow meter conveyed to the jet pump.
Nach einer weiteren Ausgestaltung der Erfindung durchläuft der Teilstrom eine Dichtemeßeinrichtung. Diese kontinuierlich arbeitende Einrichtung dient zur Überwachung der Qualität des Teilstroms. According to a further embodiment of the invention the partial flow a density measuring device. This continuously working facility serves to monitor the quality of the Partial flow.
Bevorzugt wird die Dichte des Teilstroms volumetrisch oder gravimetrisch ermittelt. Ferner wird bevorzugt der Teilstrom in Abhängigkeit von dem Ergebnis der Dichtemessung der Verarbeitungsstelle oder dem Vorratsbehälter zugeleitet. Ein Teilstrom, der nicht den Qualitätsanforderungen genügt, gelangt sonach nicht zur Verarbeitung, sondern wird gemeinsam mit dem Produktstrom erneut aufbereitet.The density of the partial stream is preferably volumetric or determined gravimetrically. The partial flow is also preferred depending on the result of the density measurement of the processing point or fed to the storage container. A partial flow that does not meet the quality requirements therefore not for processing, but is together with the Product stream reprocessed.
Die Aufgabe wird in konstruktiver Hinsicht bei einer Vorrichtung zur Herstellung von Schaummassen, insbesondere Schaumzementmassen, die im wesentlichen aus einem Ausgangsprodukt, insbesondere Zementleim, und einem schaummittel bestehen, mit einem über eine Förderpumpe mit einem Vorratsbehälter für das Ausgangsprodukt in Verbindung stehenden Mischreaktor, insbesondere zur Durchführung des vorgenannten Verfahrens erfindungsgemäß dadurch gelöst, daß der Mischreaktor einen zu einer Strahlpumpe führenden Abgang für einen Produktstrom, einen zu einer Verarbeitungsstelle führenden Auslaß für einen Teilstrom des Produktstroms und einen Einlaß für den Produktstrom aus dem Vorratsbehälter aufweist, wobei der Produktstrom oberhalb des Füllstandes des Vorratsbehälters aus der mit einem Eingang für das Schaummittel versehenen Strahlpumpe austritt und innerhalb des Mischreaktors mindestens ein statisches Mischelement angeordnet ist.The task is done in a constructive way with a device for the production of foam compositions, in particular foam cement compositions, which essentially consists of a starting product, in particular cement paste, and a foaming agent, with one via a feed pump with a storage container for the Starting product related mixing reactor, in particular to carry out the aforementioned method according to the invention solved in that the mixing reactor one to one Jet pump leading outlet for a product stream, a outlet leading to a processing point for a Partial stream of the product stream and an inlet for the product stream from the reservoir, the product stream above the fill level of the storage container from the with an inlet for the jet pump exits and within the mixing reactor at least one static Mixing element is arranged.
Aufgrund dieser Maßnahmen ist der Mischreaktor relativ kompakt aufgebaut und läßt sich in unmittelbarer Nähe einer Verarbeitungsstelle plazieren. Dadurch, daß der Mischreaktor jeweils einen separaten Abgang und einen Einlaß für den Produktstrom sowie einen Auslaß für den Teilstrom des Produktstroms aufweist, ist die getrennte Umwälzung dieser Ströme möglich. Dem Produktstrom wird erst dann ein Teilstrom entnommen, der der Verarbeitungsstelle zugeführt wird, wenn der Produktstrom die erforderliche Qualität aufweist. Durch den Austritt des Produktstroms oberhalb des Füllstandes des Vorratsbehälters aus der Strahlpumpe wird eine homogene Vermischung erzielt, die zur Steigerung der Qualität der Schaummasse beträgt.Because of these measures, the mixing reactor is relatively compact constructed and can be in the immediate vicinity of a processing point place. The fact that the mixing reactor a separate outlet and an inlet for the product stream and an outlet for the partial stream of the product stream is the separate circulation of these streams possible. Only then is a partial stream removed from the product stream, which is supplied to the processing point when the Product stream has the required quality. By the Outlet of the product flow above the fill level of the storage container the jet pump becomes a homogeneous mixture achieved to increase the quality of the foam mass is.
Zweckmäßigerweise ist innerhalb des Mischreaktors mindestens ein Mischelement angeordnet. Das Mischelement bewirkt eine Verwirbelung des Produktstroms und somit die Erzeugung einer einheitlichen Masse in dem Mischreaktor.It is expedient within the mixing reactor at least a mixing element arranged. The mixing element causes one Swirling of the product flow and thus the generation of a uniform mass in the mixing reactor.
Bevorzugt ist innerhalb des Mischreaktors mindestens ein Feinschutzsieb festgelegt. Das Feinschutzsieb ist zweckmäßigerweise vor dem Abgang für den Produktstrom angeordnet, wobei sich der Abgang für den Produktstrom an einer dem Einlaß für den Produktstrom gegenüberliegenden Seite des Mischreaktors befindet. Aufgrund dieser Maßnahme werden größere Partikel des Produktstroms in dem Mischreaktor zurückgehalten und die Strahlpumpe wird vor einer Beschädigung durch diese Partikel geschützt.At least one is preferred within the mixing reactor Fine protection screen fixed. The fine protection screen is expedient arranged before the outlet for the product stream, where the outlet for the product flow at one of the inlet for the product stream opposite side of the mixing reactor located. Because of this measure, larger particles of the product stream retained in the mixing reactor and the jet pump is protected from damage from these particles protected.
Um die Vermischung des Produktstroms in dem Mischreaktor zu intensivieren, steht nach einer vorteilhaften Ausgestaltung der Erfindung der Mischreaktor mit einem außenseitigen Rüttler in Verbindung. Hierbei ist der Rüttler so einzustellen, daß eine bereits erzeugte Schaumstruktur der Schaummasse keinen Schaden erleidet, wonach eine gleichmäßige und feinverteilte Luftporenstruktur in der Schaummasse erhalten bleibt. In order to mix the product stream in the mixing reactor intensify stands for an advantageous embodiment the invention of the mixing reactor with an external vibrator in connection. Here the vibrator is to be set so that an already generated foam structure of the foam mass does not Damage suffers, after which an even and finely divided Air pore structure is retained in the foam mass.
Da die Schwingungen das Mischreaktors nicht in voller Größe auf den Vorratsbehälter übertragen werden sollen, ist zweckmäßigerweise der Mischreaktor über eine Rohrleitung sowie einen Schlauch mit der zwischengeschalteten Förderpumpe mit dem Vorratsbehälter verbunden.Because the vibrations of the mixing reactor are not full size to be transferred to the storage container is expedient the mixing reactor via a pipeline and a Hose with the intermediate feed pump with the Reservoir connected.
Zur Erzielung einer innigen Vermischung des Produktstroms unter der Ausnutzung einer vorhandenen Förderstrecke, ist bevorzugt die Rohrleitung in ihrem Inneren mit mindestens einem Mischelement versehen.To achieve an intimate mixing of the product flow under the use of an existing conveyor line is preferred the pipe inside with at least one Provide mixing element.
Nach einer weiteren vortellhaften Ausgestaltung des Erfindungagedankens ist die Strahlpumpe mit einem Einlaß für das Druckgas versehen. Das Druckgas wird durch diese Maßnahme direkt in die Strahlpumpe bzw. in den die Strahlpumpe durchströmenden Produktstrom eingeleitet und eine Verschmutzung durch unkontrolliert austretende Produkte ist weitgehend ausgeschlossen.According to another exemplary embodiment of the inventive idea is the jet pump with an inlet for the Provide compressed gas. This measure makes the compressed gas direct into the jet pump or into the jet pump flowing through it Product flow initiated and pollution through uncontrolled escaping products is largely excluded.
Zur Herstellung einer Schaummasse mit einer definierten, regulierbaren Dichte ist bevorzugt der Strahlpumpe jeweils eine Dosierpumpe zur Zuführung des einen Durchflußmesser durchströmenden Schaummittels und/oder Druckgases zugeordnet.For the production of a foam mass with a defined, adjustable The jet pump is preferably each density Dosing pump for supplying the flow through a flow meter Foam agent and / or compressed gas assigned.
Um die kontinuierliche oder stichprobenartige Überprüfung der Dichte des Teilstroms sicherzustellen, ist zweckmäßigerweise dem Auslaß für den Teilstrom des Produktstroms eine Verbindungsleitung mit zwischengeschalteter Dichtemeßeinrichtung zugeordnet. Ferner ist zur Kontrolle der ausgetragenen Menge des Teilstroms an der Verarbeitungsstelle die Verbindungsleitung mit einem der Dichtemeßeinrichtung nachgeschalteten Mengenmesser versehen.In order to continuously or randomly review the Ensuring the density of the partial flow is expedient a connection line to the outlet for the partial flow of the product flow with interposed density measuring device assigned. It is also used to control the quantity discharged of the partial flow at the processing point the connecting line with a flow meter downstream of the density measuring device Mistake.
Da ein Teilstrom, der nicht die vorbestimmten Eigenschaften aufweist, nicht der Verarbeitung zugeführt werden soll, steht die Dichtemeßeinrichtung mit einer Rückleitung in Verbindung, die zu dem Vorratsbehälter führt. Somit wird ein derartiger Teilstrom in das Ausgangsprodukt bzw. den Produktstrom eingeleitet und erneut aufbereitet.Because a partial flow that does not have the predetermined properties has, should not be processed, stands the density measuring device with a return line in connection, that leads to the reservoir. Thus such a Partial stream introduced into the starting product or the product stream and reprocessed.
Damit das Eintragen grober Partikel in die Vorrichtung verhindert wird, ist bevorzugt der Vorratsbehälter mit einem Schutzsieb abgedeckt.This prevents the entry of coarse particles into the device is preferably the storage container with a Protective screen covered.
Nach einer alternativen Ausgestaltung der Erfindung ist der Strahlpumpe für den Produktstrom eine Dosierstrahlpumpe für einen Teilproduktstrom zugeordnet, die das Schaummittel und/oder das Druckgas dem Teilproduktstrom zuleitet, wonach der Teilproduktstrom in den Mischreaktor gelangt. Aufgrund dieser Maßnahme wird eine bestimmte Dichte des Teilproduktstroms eingestellt. Nach dem Vermischen des Teilproduktstroms mit dem Produktstrom in dem Mischreaktor ergibt sich eine resultierende, zur Verarbeitung benötigte Dichte.According to an alternative embodiment of the invention Jet pump for the product stream a dosing jet pump for assigned a partial product stream that the foaming agent and / or the compressed gas feeds the partial product stream, after which the partial product stream enters the mixing reactor. by virtue of this measure becomes a certain density of the partial product flow set. After mixing the partial product stream with the product stream in the mixing reactor, a resulting density required for processing.
Es versteht sich, daß die vorstehend genannten und nachstehend noch zu erläuternden Merkmale nicht nur in der jeweils angegebenen Kombination, sondern auch in anderen Kombinationen verwendbar sind, ohne den Rahmen der vorliegenden Erfindung zu verlassen. It is understood that the above and below Features to be explained not only in each case specified combination, but also in other combinations are usable without the scope of the present invention to leave.
Die Erfindung wird im folgenden anhand eines Ausführungsbeispieles unter Bezugnahme auf die zugehörigen Zeichnungen näher erläutert. Es zeigen:
- Fig.1
- eine schematische Darstellung einer erfindungsgemäßen Vorrichtung und
- Fig.2
- eine schematische Darstellung eines Teils der erfindungsgemäßen Vorrichtung in einer alternativen Ausgestaltung.
- Fig.1
- a schematic representation of a device according to the invention and
- Fig.2
- a schematic representation of part of the device according to the invention in an alternative embodiment.
Die Vorrichtung zur Herstellung einer Schaummasse umfaßt nach
Fig. 1 im wesentlichen einen Vorratsbehälter 1 zur Aufnahme
eines Ausgangsproduktes A, der von einem Schutzsieb 2 überdeckt
ist und der über eine Förderpumpe 3 mit einem Mischreaktor
4 in Verbindung steht. Die Förderpumpe 3 ist zum einen
über einen Schlauch 5 an den Vorratsbehälter 1 und zum anderen
mittels einer Rohrleitung 6 an einen Einlaß 7 des
Mischreaktors 4 für einen Produktstrom B angeschlossen. Die
Innenwand der Rohrleitung 6 ist mit nicht dargestellten Mischelementen
versehen.The device for producing a foam composition comprises
Fig. 1 essentially a
Der Mischreaktor 4 trägt an seinen Innenwänden 8 Mischelemente
9 und steht mit einem außenseitigen Rüttler 10 in Verbindung.
An der dem Einlaß 7 für den Produktstrom B gegenüberliegenden
Seite weist der Mischreaktor 4 einen zu einer
Strahlpumpe 11 führenden Abgang 12 für den Produktstrom B sowie
einen zu einer Verarbeitungsstelle 13 führenden Auslaß 14
für einen Teilstrom C des Produktstroms B auf. Vor dem Abgang
12 ist ein Feinschutzsieb 15 festgelegt, das den Durchtritt
grober Partikel verhindert. Im weiteren ist zwischen dem Abgang
12 und der Strahlpumpe 11 ein Absperrventil 16 angeordnet.The mixing
Die Strahlpumpe 11 ist an ihrer Saugseite mit einem Eingang
17 für ein Schaummittel 18 versehen, das über eine Dosierpumpe
19 mit nachgeschaltetem Durchflußmesser 20 dem Produktstrom
B beigemischt wird. Ferner weist die Strahlpumpe 11 einen
Einlaß 21 für ein Druckgas 22 auf, das ebenfalls über eine
Dosierpumpe 23 mit nachgeschaltetem Durchflußmesser 24 dem
Produktstrom B zugeführt wird. Die Strahlpumpe 11 ist derart
angeordnet, daß der Produktstrom B oberhalb des Füllstandes
25 des Ausgangsproduktes A in den Vorratsbehälter 1 gelangt.The
Der Teilstrom C des Produktstromes B wird durch eine Verbindungsleitung
26 zu einer Dichtemeßeinrichtung 27 mit einem
vorgeschalteten Absperrventil 28 geführt. In Abhängigkeit von
dem Meßergebnis der Dichtemeßeinrichtung 27 erreicht der
Teilstrom C über einen Mengenmesser 29 die Verarbeitungsstelle
13 oder über eine Rückleitung 30 den Vorratsbehälter 1.The partial stream C of the product stream B is through a connecting
Gemäß Fig. 2 ist der Strahlpumpe 11 für den Produktstrom B
eine Dosierstrahlpumpe 31 für einen Teilproduktstrom D zugeordnet.
Der Produktstrom B erreicht über eine mit einem Absperrventil
32 versehene Zuleitung 33 eine Treibdüse 34. Hier
findet eine Vermischung des Produktstromes B mit Luft bzw.
Gas 35 statt, das offen in die Strahlpumpe 11 eingetragen
wird. Der Strahlpumpe 11 ist ein Diffusor 36 nachgeschaltet,
der in den Mischreaktor 4 mündet.2, the
In der Dosierstrahlpumpe 31 wird der Teilproduktstrom D mit
dem Schaummittel 18 und dem Druckgas 22 innig vermischt, wonach
er über die Einspeisung 37 ebenfalls in den Mischreaktor
4 gelangt.In the
Aus dem Mischreaktor 4 wird wiederum ein Produktstrom B in
den Vorratsbehälter 1 und ein Teilstrom C zu der Verarbeitungsstelle
13 geleitet.The mixing
Zur Durchführung des Verfahrens wird mittels eines Fahrmischers
das Ausgangsprodukt A , bestehend aus Zement und Wasser,
angeliefert, das über das Schutzsieb 2 in den Vorratsbehälter
1 gelangt. In einer Einmischphase des Produktstromes B
ist das Absperrventil 28 für den Teilstrom C geschlossen und
der Produktstrom B wird unter Zufuhr von Schaummittel 18,
Druckgas 22 sowie atmosphärischer Luft im Kreislauf gepumpt
und dabei vermischt. Hierbei wird der Produktstrom B mittels
der Förderpumpe 3 dem Vorratsbehälter 1 entnommen, durch die
mit Mischelementen versehene Rohrleitung 6 zu dem Mischreaktor
4 befördert und über die Strahlpumpe 11 in den Vorratsbehälter
1 geleitet.The method is carried out using a truck mixer
the starting product A, consisting of cement and water,
delivered that over the
Nach der Einmischphase erfolgt das Öffnen des Absperrventils
28 und der Teilstrom C durchfließt die Dichtemeßeinrichtung
27. Entspricht das Meßergebnis den Anforderungen an die
Schaummasse, wird der Teilstrom C über den Mengenmesser 29
der Verarbeitungsstelle 13 zugeführt. Falls das Meßergebnis
den Anforderungen an die Schaummasse nicht entspricht, wird
der Teilstrom C über die Rückleitung 30 in den Vorratsbehälter
1 eingeleitet, wonach eine weitere Vermischung erfolgt.
Während der Entnahme des Teilstroms C wird der Produktstrom B
in dem zuvor beschriebenen Kreislauf gefördert. The shut-off valve opens after the
Mittels dieses Verfahrens wird aus 3.8 m3 Ausgangsprodukt A mit einer Dichte zwischen 1500 und 2500 kg/m3 eine Schaummasse hergestellt, die nach einer Einmischphase von 60 Sekunden eine Dichte zwischen 100 und 1000 kg/m3 mit einer gleichmäßig verteilten Porenstruktur aufweist. Using this process, a foam mass is produced from 3.8 m 3 of starting product A with a density between 1500 and 2500 kg / m 3 , which after a mixing phase of 60 seconds has a density between 100 and 1000 kg / m 3 with a uniformly distributed pore structure.
- AA
- Ausgangsproduktstarting product
- BB
- Produktstromproduct flow
- CC
- Teilstrompartial flow
- DD
- TeilproduktstromPartial product stream
- 1.1.
- Vorratsbehälterreservoir
- 2.Second
- Schutzsiebprotective screen
- 3.Third
- Förderpumpefeed pump
- 4.4th
- Mischreaktormixing reactor
- 5.5th
- Schlauchtube
- 6.6th
- Rohrleitungpipeline
- 7.7th
- EinlaßInlet
- 8.8th.
- Innenwandinner wall
- 9.9th
- Mischelementmixing element
- 10.10th
- RüttlerJogger
- 11.11th
- Strahlpumpejet pump
- 12.12th
- Abgangleaving
- 13.13th
- Verarbeitungsstelleprocessing Agent
- 14.14th
- Auslaßoutlet
- 15.15th
- FeinschutzsiebFeinschutzsieb
- 16.16th
- Absperrventilshut-off valve
- 17.17th
- Eingangentrance
- 18.18th
- Schaummittelfoaming agent
- 19.19th
- Dosierpumpemetering
- 20.20th
- Durchflußmesserflowmeter
- 21.21st
- EinlaßInlet
- 22.22nd
- Druckgascompressed gas
- 23.23rd
- Dosierpumpemetering
- 24.24th
- Durchflußmesserflowmeter
- 25.25th
- Füllstandlevel
- 26.26th
- Verbindungsleitungconnecting line
- 27.27th
- Dichtemeßeinrichtungdensity measuring
- 28.28th
- Absperrventilshut-off valve
- 29.29th
- Mengenmesserflow meter
- 30.30th
- Rückleitungreturn
- 31.31st
- DosierstrahlpumpeDosierstrahlpumpe
- 32.32nd
- Absperrventilshut-off valve
- 33.33rd
- Zuleitungsupply
- 34.34th
- Treibdüsepropelling nozzle
- 35.35th
- Gasgas
- 36.36th
- Diffusordiffuser
- 37.37th
- Einspeisungfeed
Claims (21)
- Method for producing foaming substances, especially foaming cement substances, which substantially comprise a starting product (A), especially cement paste, and a foaming agent (18), in a mixing reactor (4) connected via a feed pump (3) to a supply container (1) for the starting product (A), characterised in that a product flow (B) taken from the mixing reactor (4) is conveyed in a circuit via a jet pump (11) to the supply container (1) which is kept at a minimum level, foaming agent (18) and atmospheric air being added, a partial flow (C) being removed for processing from the product flow (B) after a mixing phase, and the foaming agent (18) being mixed into the product flow (B) in the jet pump (11).
- Method according to claim 1, characterised in that a compressed gas (22) is mixed into the product flow (B).
- Method according to claims 1 and 2, characterised in that the compressed gas (22) is mixed into the product flow (B) in the jet pump (11).
- Method according to one of claims 1 to 3, characterised in that the amount of the foaming agent (18) mixed into the product flow (B) and/or the amount of compressed gas (22) is measured and regulated.
- Method according to one of claims 1 to 4, characterised in that the foaming agent (18) and/or the compressed gas (22) are/is conveyed from a metering pump (19, 23) through a flow-meter (20, 24) to the jet pump (11).
- Method according to claim 1, characterised in that the partial flow (C) flows through a density measuring device (27).
- Method according to claim 6, characterised in that the density of the partial flow (C) is determined by volumetric or gravimetric means.
- Method according to claims 6 and 7, characterised in that the partial flow (C) is led in dependence on the result of the density measurement to the processing location (13) or to the supply container (1).
- Device for producing foaming substances, especially foaming cement substances, which substantially comprise a starting product (A), especially cement paste, and a foaming agent (18), having a mixing reactor (4) connected via a feed pump (3) to a supply container (1) for the starting product (A), in particular for accomplishing the method according to claim 1, characterised in that the mixing reactor (4) has an exit (12) for a product flow (B), leading to a jet pump (11), an outlet (14), leading to a processing location (13), for a partial flow (C) of the product flow (B) and an intake (7) for the product flow (B) from the supply container (1), the product flow (B) emerging above the filling level (25) of the supply container (1) from the jet pump (11), which is provided with an entrance (17) for the foaming agent (18), and at least one static mixing element (9) being disposed inside the mixing reactor (4).
- Device according to claim 9, characterised in that at least one fine protective screen (15) is fixed inside the mixing reactor (4).
- Device according to claim 10, characterised in that the fine protective screen (15) is disposed in front of the exit (12) for the product flow (B), the exit (12) for the product flow (B) being located on a side of the mixing reactor (4) opposite the intake (7) for the product flow (B).
- Device according to one of claims 9 to 11, characterised in that the mixing reactor (4) is connected to an external shaking device (10).
- Device according to claim 9, characterised in that the mixing reactor (4) is connected to the supply container (1) via a pipeline (6) and a hose (5) with the interposed feed pump (3).
- Device according to claim 13, characterised in that the pipeline (6) is provided in its interior with at least one mixing element.
- Device according to one of claims 9 to 14, characterised in that the jet pump (11) is provided with an intake (21) for the compressed gas (22).
- Device according to one of claims 9 to 15, characterised in that there is associated with the jet pump (11) in each case a metering pump (19, 23) to supply the foaming agent (18) flowing through a flow-meter (20, 24) and/or the compressed gas (22).
- Device according to claim 9, characterised in that a connecting line (26) with an interposed density measuring device (27) is associated with the outlet (14) for the partial flow (C) of the product flow (B).
- Device according to claim 17, characterised in that the connecting line (26) is provided with a quantity meter (29) connected downstream of the density measuring device (27).
- Device according to claims 17 and 18, characterised in that the density measuring device (27) is connected to a return line (30) which leads to the supply container (1).
- Device according to one of claims 9 to 19, characterised in that the supply container (1) is covered with a protective screen (2).
- Device according to one of claims 9 to 13, characterised in that there is associated with the jet pump (11) for the product flow (B) a metering jet pump (31) for a partial product flow (D), which leads the foaming agent (18) and/or the compressed gas (22) to the partial product flow (D), after which the partial product flow (D) reaches the mixing reactor (4).
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19808506 | 1998-02-27 | ||
| DE19808506A DE19808506A1 (en) | 1998-02-27 | 1998-02-27 | Device and method for producing foam masses |
| PCT/DE1999/000520 WO1999043478A1 (en) | 1998-02-27 | 1999-02-26 | Method for producing foaming substances, especially foaming cement substances, and corresponding device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP1064133A1 EP1064133A1 (en) | 2001-01-03 |
| EP1064133B1 true EP1064133B1 (en) | 2002-12-11 |
Family
ID=7859226
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP99916759A Expired - Lifetime EP1064133B1 (en) | 1998-02-27 | 1999-02-26 | Method for producing foaming substances, especially foaming cement substances, and corresponding device |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US6425950B1 (en) |
| EP (1) | EP1064133B1 (en) |
| AT (1) | ATE229412T1 (en) |
| AU (1) | AU3515299A (en) |
| CA (1) | CA2322280C (en) |
| DE (2) | DE19808506A1 (en) |
| WO (1) | WO1999043478A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107097352A (en) * | 2017-05-15 | 2017-08-29 | 南通海高数控机械有限公司 | A kind of cement foam board injection molding mechanism with heat sinking function |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102005014704B4 (en) * | 2004-03-26 | 2010-04-01 | Suspensionsbeton Ltd. | Material processing plant for the production of lightweight materials |
| US8408781B2 (en) * | 2006-02-21 | 2013-04-02 | Charles D. Welker | System, method and apparatus for entraining air in concrete |
| RU2336999C1 (en) * | 2007-02-14 | 2008-10-27 | Государственное образовательное учреждение высшего профессионального образования "Кубанский государственный технологический университет" (ГОУВПО "КубГТУ") | Line for foam concrete products manufacturing |
| CN102527266A (en) * | 2011-12-29 | 2012-07-04 | 多维联合集团有限公司 | Method for statically mixing raw materials for banding production line of sandwich panel |
| US10189180B2 (en) * | 2014-01-15 | 2019-01-29 | United States Gypsum Company | Foam injection system with variable port inserts for slurry mixing and dispensing apparatus |
| WO2015191494A1 (en) * | 2014-06-09 | 2015-12-17 | The Procter & Gamble Company | Dispensers for delivering a consistent consumer experience |
| CN106313324B (en) * | 2015-06-16 | 2018-08-21 | 中国石油化工股份有限公司 | A kind of device being used to prepare foam slurry |
| CN112843544B (en) * | 2020-12-29 | 2022-04-15 | 天津润木科技有限公司 | Portable high-efficient foaming device |
| CN115259795B (en) * | 2022-08-09 | 2023-05-12 | 武汉理工大学 | Preparation method of slag soil-based foam concrete block |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2733053A (en) | 1956-01-31 | dug as | ||
| DE2348915A1 (en) | 1973-09-28 | 1975-04-17 | Luigi Leandri | Foamed concrete mix producer - has volumetric pumps beneath the site surface, with foam-forming sling and collector |
| DE3100443A1 (en) * | 1981-01-09 | 1982-08-12 | Dietrich Dipl.-Ing. 6240 Königstein Maurer | METHOD AND DEVICE FOR PRODUCING AND, IF NECESSARY, CONVEYING FOAMED MIXTURES MADE OF BINDING AGENTS OR BINDING AGENTS WITH ADDITIVES |
| DE3132667A1 (en) | 1981-08-14 | 1983-02-24 | Lehmann & Co GmbH, 2120 Lüneburg | Process and device for producing porous concrete or foam concrete or the like |
| DE3222033A1 (en) | 1982-06-11 | 1983-12-15 | KBI Klöckner-Becorit Industrietechnik GmbH, 4224 Hünxe | Process and device for producing porous mortar |
| DE3631223A1 (en) | 1986-09-13 | 1988-04-07 | Heinz Josef Krause | Process for producing a curing foam composition of fine pore structure |
| US4764019A (en) * | 1987-09-01 | 1988-08-16 | Hughes Tool Company | Method and apparatus for mixing dry particulate material with a liquid |
| US5556033A (en) * | 1989-05-10 | 1996-09-17 | New Waste Concepts, Inc. | Apparatus for forming a foamed outdoor protective cover layer |
| JPH06144953A (en) | 1992-10-30 | 1994-05-24 | Sumitomo Cement Co Ltd | Method for controlling quality of air mortar preparing bubble-containing liquid and method and device for controlling execution of air mortar |
-
1998
- 1998-02-27 DE DE19808506A patent/DE19808506A1/en not_active Withdrawn
-
1999
- 1999-02-26 WO PCT/DE1999/000520 patent/WO1999043478A1/en not_active Ceased
- 1999-02-26 DE DE59903743T patent/DE59903743D1/en not_active Expired - Fee Related
- 1999-02-26 EP EP99916759A patent/EP1064133B1/en not_active Expired - Lifetime
- 1999-02-26 US US09/623,089 patent/US6425950B1/en not_active Expired - Fee Related
- 1999-02-26 AT AT99916759T patent/ATE229412T1/en not_active IP Right Cessation
- 1999-02-26 CA CA002322280A patent/CA2322280C/en not_active Expired - Fee Related
- 1999-02-26 AU AU35152/99A patent/AU3515299A/en not_active Abandoned
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107097352A (en) * | 2017-05-15 | 2017-08-29 | 南通海高数控机械有限公司 | A kind of cement foam board injection molding mechanism with heat sinking function |
Also Published As
| Publication number | Publication date |
|---|---|
| DE59903743D1 (en) | 2003-01-23 |
| WO1999043478A1 (en) | 1999-09-02 |
| ATE229412T1 (en) | 2002-12-15 |
| CA2322280A1 (en) | 1999-09-02 |
| AU3515299A (en) | 1999-09-15 |
| DE19808506A1 (en) | 1999-09-02 |
| US6425950B1 (en) | 2002-07-30 |
| EP1064133A1 (en) | 2001-01-03 |
| CA2322280C (en) | 2007-07-10 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| EP1064133B1 (en) | Method for producing foaming substances, especially foaming cement substances, and corresponding device | |
| CH657844A5 (en) | METHOD AND DEVICE FOR PRODUCING FOAMED MIXTURES. | |
| DE69513525T2 (en) | METHOD AND DEVICE FOR MIXING, SPRAYING AND APPLYING CEMENT MATERIALS | |
| DE102005037080A1 (en) | Method and apparatus for cooling cement or cementitious powders | |
| EP0698419B1 (en) | Installation for spraying dry building material | |
| WO2020039021A1 (en) | Device for producing foamed construction materials | |
| CH674869A5 (en) | ||
| AT2027U1 (en) | SPRAY NOZZLE AND METHOD FOR DRY SPRAYING SPRAY CONCRETE | |
| DE3408007C2 (en) | Spray nozzle for foam concrete, foam mortar or the like and method for spraying foam concrete | |
| DE4443594A1 (en) | Plaster or screed, mortar for this purpose, a method for producing the same and apparatus for carrying out the method | |
| DE4120409A1 (en) | METHOD FOR APPLYING QUICK-SET SPRAYING MATERIALS | |
| DE2617741C3 (en) | Process for the production of fiber-reinforced, hydraulically hardening masses, in which the matrix and the fibers are sprayed against a surface by spraying one above the other with the effect of a mixing effect in the fiber spraying process | |
| DE10110917C2 (en) | Method and device for producing a binder foam | |
| DE10124247A1 (en) | Heat and/or sound insulation foamed cement manufacture involves circulation and premixing of cement glue and foaming agent, then addition of foamed polymer | |
| DE3132667A1 (en) | Process and device for producing porous concrete or foam concrete or the like | |
| AT410420B (en) | System to convey and dry shotcrete of building material mixtures | |
| DE19537239C2 (en) | Device and method for producing a foamed binder | |
| AT526383B1 (en) | Device for producing foam concrete and conveying the foam concrete to various pouring locations on a construction site | |
| DE10310599A1 (en) | Spraying concrete spray onto an object via nozzles with addition of carbon dioxide to the concrete useful as a safety measure in tunnel and side wall construction and for construction of mine walls | |
| DE19512098C1 (en) | Control device for multi-phase flow such as "ready-mixed" concrete used in construction industry | |
| DE3328898A1 (en) | Dry mix for a screed, and process and equipment for producing it | |
| EP1198287A1 (en) | Method and device for producing foams, especially foamed porous light-density materials | |
| DE19932247C2 (en) | Process and arrangement for supplying consumption points with Si-containing raw material in vapor form | |
| AT322189B (en) | DEVICE FOR CONTINUOUS MIXING OF FINE-GRAIN BUILDING MATERIALS WITH WATER | |
| WO2022135714A1 (en) | Apparatus for producing co2-enriched concrete |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| 17P | Request for examination filed |
Effective date: 20000822 |
|
| AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE |
|
| GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
| 17Q | First examination report despatched |
Effective date: 20020320 |
|
| GRAG | Despatch of communication of intention to grant |
Free format text: ORIGINAL CODE: EPIDOS AGRA |
|
| GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
| GRAH | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOS IGRA |
|
| GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
| AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED. Effective date: 20021211 Ref country code: IE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20021211 Ref country code: GB Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20021211 Ref country code: FI Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20021211 |
|
| REF | Corresponds to: |
Ref document number: 229412 Country of ref document: AT Date of ref document: 20021215 Kind code of ref document: T |
|
| REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D Free format text: NOT ENGLISH |
|
| REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP |
|
| REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D Free format text: GERMAN |
|
| REF | Corresponds to: |
Ref document number: 59903743 Country of ref document: DE Date of ref document: 20030123 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20030226 Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20030226 Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20030226 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20030228 Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20030228 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20030228 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20030311 Ref country code: PT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20030311 Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20030311 |
|
| REG | Reference to a national code |
Ref country code: GR Ref legal event code: EP Ref document number: 20030400922 Country of ref document: GR |
|
| GBV | Gb: ep patent (uk) treated as always having been void in accordance with gb section 77(7)/1977 [no translation filed] |
Effective date: 20021211 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20030627 |
|
| REG | Reference to a national code |
Ref country code: IE Ref legal event code: FD4D Ref document number: 1064133E Country of ref document: IE |
|
| ET | Fr: translation filed | ||
| REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
| PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
| REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
| 26N | No opposition filed |
Effective date: 20030912 |
|
| REG | Reference to a national code |
Ref country code: FR Ref legal event code: RN |
|
| REG | Reference to a national code |
Ref country code: FR Ref legal event code: FC |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GR Payment date: 20080229 Year of fee payment: 10 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: LU Payment date: 20090303 Year of fee payment: 11 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 20090225 Year of fee payment: 11 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 20090202 Year of fee payment: 11 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20090404 Year of fee payment: 11 |
|
| PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20090224 Year of fee payment: 11 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20090902 |
|
| BERE | Be: lapsed |
Owner name: *LEITSCH FERDINAND Effective date: 20100228 |
|
| REG | Reference to a national code |
Ref country code: NL Ref legal event code: V1 Effective date: 20100901 |
|
| REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST Effective date: 20101029 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100901 Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100301 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100901 Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100228 |
|
| PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20100226 |