[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

EP3074137B1 - Method for producing cement - Google Patents

Method for producing cement Download PDF

Info

Publication number
EP3074137B1
EP3074137B1 EP14805222.8A EP14805222A EP3074137B1 EP 3074137 B1 EP3074137 B1 EP 3074137B1 EP 14805222 A EP14805222 A EP 14805222A EP 3074137 B1 EP3074137 B1 EP 3074137B1
Authority
EP
European Patent Office
Prior art keywords
cage
classifiers
bar
cement
ground
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.)
Not-in-force
Application number
EP14805222.8A
Other languages
German (de)
French (fr)
Other versions
EP3074137A1 (en
Inventor
Jörg BINNER
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
KHD Humboldt Wedag AG
Original Assignee
KHD Humboldt Wedag AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by KHD Humboldt Wedag AG filed Critical KHD Humboldt Wedag AG
Publication of EP3074137A1 publication Critical patent/EP3074137A1/en
Application granted granted Critical
Publication of EP3074137B1 publication Critical patent/EP3074137B1/en
Not-in-force legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C23/00Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
    • B02C23/08Separating or sorting of material, associated with crushing or disintegrating
    • B02C23/14Separating or sorting of material, associated with crushing or disintegrating with more than one separator

Definitions

  • the invention relates to a method for producing a cement, wherein at least one millbase is ground in at least two devices for grinding to different ground millbase with mutually different grain size distributions, the ground millbase separated from each of the at least two devices for grinding separately, each with its own classifying air stream is supplied to one of at least two rod sifters, in each of the at least two rod sifter classified a fine material fraction and a coarse grain fraction is discharged.
  • a device for grinding regrind For the production of cement and / or cement raw meal suitable for cement production regrind such as cement clinker, metallurgical or slag sand, limestone and / or gypsum is placed in a device for grinding regrind.
  • regrind such as cement clinker, metallurgical or slag sand, limestone and / or gypsum
  • HPGR 'high-pressure roller press'
  • the material to be removed from the roller presses consists of still existing coarse material and a fine material produced during comminution. For the production of the fine material, it is separated from the coarse material in classifiers.
  • a broadened particle size distribution can be achieved by operating at least two similar Kreislaufmahlanlagen. Differences in the roller presses used (in particular in the contact forces) and the rod basket sifters (in particular with regard to speed and dimensions) make it possible to produce different, steep particle size distributions.
  • DE 10 2008 019 830 A1 a Umkylzmahlstrom with roller press, static caution and dynamic classifier is known, it being possible to operate in parallel to increase the throughput of several similar systems.
  • WO 2009/068465 A1 is a Kreislaufmahlstrom known, which is composed of several roller presses and corresponding classifiers. With such systems, the desired grain size influencing and distribution can be achieved by bringing together the respective light goods.
  • the object of the invention is therefore to provide a method for producing a cement, which overcomes the disadvantages of the prior art.
  • At least two grinders at least one grindable material suitable for cement production is ground and that the ground grindbase suspended in separate classifying air streams is in each case supplied pneumatically to a dynamic rod basket sifter.
  • a separation of a coarse grain fraction (grits) and a fine grain fraction is achieved.
  • the grits are taken away.
  • the fine material fractions which are located in the rod basket sifters are discharged from the respective classifying air streams into a common discharge device.
  • the classifying air streams flow together.
  • the resulting flow field inside the discharge device swirls the fine material particles and leads to a uniform mixing of the fine material fractions from the individual rod basket separators.
  • the at least two devices for grinding mutually different millbase for example cement clinker, metallurgical or slag sand, limestone and / or gypsum, is supplied. If at the same time different starting materials are supplied to the devices for grinding as the respective ground material, this can influence the composition of the cement or cement raw meal.
  • roller presses As devices for grinding.
  • Operating characteristics of roller presses and the nature of the comminuted fresh produce are well known in cement production.
  • roller presses lead to steep particle size distribution curves.
  • the desired broadened particle size distribution can easily be achieved for the common fine product product.
  • two roller presses and two Stabkorbsichtern a composition of a coarser and a finer fines content in the common fines product is produced, resulting in a high strength of cement.
  • the inventive method is not limited to the use of roller presses. It is possible, in their place, to use other devices known from cement production for grinding regrind, in particular ball mills (tube mills), vertical mills and impact hammer mills. This makes it possible, not least for testing and development purposes, to carry out additional influencing of the particle size distribution in the common fine product product that is fundamentally made possible by the method according to the invention.
  • the ground material to be ground from the at least two devices for grinding is not directed directly into the dynamic rod basket sifter, but first subjected to a pre-seal.
  • the crushed regrind is in each case in a static Caution entered.
  • Caregivers are used in the process of cement production to separate coarse material located in the material to be ground. These are coarse material residues that were not crushed during the grinding process.
  • the coarse grain fractions discharged from the at least two rod basket sifters are again supplied to the devices for grinding.
  • Such a recirculation of Gr manstrags offers the known economic advantages of Kreislaufmahlanlagen.
  • the individual grinding cycles are run separately from each other, i. the coarse grain fraction from a rod basket sifter is returned to the corresponding apparatus for grinding, from which forth this Stabkorbsichter also flows the reformgut.
  • the at least two rod cage separators are separately but in only one housing. This allows an economical material cost for the housing construction of the rod basket sifter and takes up the least space for the devices for sifting.
  • two rod cage sifters are preferably coaxially stacked for dynamic reasons.
  • FIG. 1 the method according to the invention for the production of cement is shown schematically for the exemplary embodiment in which two roller presses 1, 2 are used as devices for comminuting the at least one ground material.
  • the Austragsgut from the roller presses 1, 2 is pneumatically introduced in each case with a crusher poverty 3a, 3b in the housing 6a, 6b each of a dynamic Stabkorbsichters 4, 5.
  • Each of the two rod sifter 4, 5 has its own, speed-adjustable drive 24a, 24b, which puts him about its longitudinal axis in a rotational movement.
  • Speed and direction of rotation of the two rod basket sifter 4, 5 can be controlled independently.
  • the millbase suspended in the classifying air flows laterally toward the respective rod basket classifier 4, 5 and is accelerated by the rotational movement of the rod basket classifier 4, 5 into its zone of vision.
  • the centrifugal forces acting on the particles of the prepareguts lead in cooperation with the frictional force of the air flow to a separation of the prepareguts in each case a coarse grain fraction 7, 8 (Grape) and each a fine material fraction 9, 10.
  • the coarse grain fractions 7, 8 are from the Stabkorbsichtern 4, 5 discharged due to gravity down from the respective reformzone (Gr manstrag).
  • the classified fines 9, 10 are pneumatically transported by the respective classifying air stream from the respective rod basket sifter 4, 5 and both arrive in the discharge device 11.
  • a substantial phase of the method according to the invention for the production of a cement occurs in the discharge device 11 to a club so far separate classifying air streams.
  • the merger of the classifying air flows leads to a turbulent flow dynamics in the interior of the discharge device 11. This results in a turbulence and in its consequence a uniform mixing of suspended in the classifying air streams fine material fractions 9, 10 to a homogeneous finished product with a correspondingly composed particle size distribution.
  • the separation device here a cyclone
  • the fine material 14 separated from the classifying air stream 15 can be stored in silos in the further process of cement production (not in the picture).
  • FIGS. 4a and 4b are exemplary embodiments of the inventive method for producing a cement with a roller press 1 and a ball mill 16 ( FIG. 4a ) or with a vertical mill 17 and an impact hammer mill 18 (FIG. FIG. 4b ).
  • procedures and structure are as in FIG. 1 ,
  • FIG. 2 is based on the embodiment of FIG. 1 schematically illustrates an inventive method for producing a cement, in which the Austragsgut from the roller presses 1, 2 each undergoes a Vorsichtung before it is passed into one of the rod basket classifier 4, 5.
  • the Austragsgutstrom 20a, 20b from each roller press 1, 2 is to each a static caution 21, 22, respectively.
  • the discharged into a static cauterizer 21, 22 Austragsgut is separated into this in a fraction of fines 27a, 27b of the static Beicassers 21, 22 and a coarse material fraction, which leaves on the way Grobgutab Entry 26a, 26b, the static cautery 21, 22.
  • the separated fines 27a, 27b of the static cauterizer 21, 22 is pneumatically with a classifying air stream 19a, 19b in each one of the rod basket classifier 4, 5 passed.
  • FIG. 3 is based on the embodiment of FIG. 2 an extended to a grinding cycle, inventive method for producing a cement shown.
  • the Gr maneaustrag from the Stabkorbsichtern 4, 5 each returned to the devices for grinding 1, 2.
  • the recirculation takes place separately and to the respectively corresponding roller press 1, 2:
  • the feed 25b of the coarse grain fraction takes place back to the roller press 2.
  • the roller presses 1, 2 grind the recirculated coarse grain fractions 7, 8 together with that in the fresh material feeds 23a, 23b each supplied grinding stock.
  • the Austragsgutströme 20a, 20b from the roller presses 1, 2 are each passed into the corresponding static caution 21, 22.
  • the coarse material discharge discharged into the coarse material removal lines 26a, 26b of the static cauterizers 21, 22 can - not shown in the figure - be brought together with fresh material directly or after further pre-grinding and likewise fed back into the grinding cycle by way of the fresh material feeds 23a, 23b.
  • FIG. 5 shows a detail of an embodiment of the method according to the invention, in which the two rod basket viewers 4, 5 are arranged in only one housing 6c. For dynamic reasons, a coaxial arrangement of the rod basket sifter 4, 5 is favorable, as shown.
  • the rod basket separators 4, 5 are separated from each other by the respective prepare for the production of the rod basket sifter 4, 5 .
  • the fines 9, 10 are separated from each other in the discharge 11, in which combines the classifying air streams and the two fines 9, 10 are uniformly mixed.

Landscapes

  • Engineering & Computer Science (AREA)
  • Food Science & Technology (AREA)
  • Crushing And Grinding (AREA)
  • Combined Means For Separation Of Solids (AREA)
  • Disintegrating Or Milling (AREA)

Description

Die Erfindung betrifft ein Verfahren zur Herstellung eines Zements, wobei mindestens ein Mahlgut in mindestens zwei Vorrichtungen zum Mahlen zu verschiedenem gemahlenen Mahlgut mit voneinander verschiedenen Korngrößenverteilungen vermahlen wird, das gemahlene Mahlgut aus jeder der mindestens zwei Vorrichtungen zum Mahlen getrennt voneinander mit je einem eigenen Sichtluftstrom je einem von mindestens zwei Stabkorbsichtern zugeführt wird, in jedem der mindestens zwei Stabkorbsichter eine Feingutfraktion ausgesichtet und eine Grobkornfraktion abgeführt wird.The invention relates to a method for producing a cement, wherein at least one millbase is ground in at least two devices for grinding to different ground millbase with mutually different grain size distributions, the ground millbase separated from each of the at least two devices for grinding separately, each with its own classifying air stream is supplied to one of at least two rod sifters, in each of the at least two rod sifter classified a fine material fraction and a coarse grain fraction is discharged.

Zur Herstellung von Zement und/oder Zementrohmehl wird ein für die Zementherstellung geeignetes Mahlgut wie Zementklinker, Hütten- bzw. Schlackensand, Kalkstein und/oder Gips in eine Vorrichtung zum Mahlen von Mahlgut aufgegeben. Insbesondere werden zur Zerkleinerung des Mahlguts Rollenpressen eingesetzt, die auch 'Gutbettwalzenmühle', 'Hochdruck-Walzenpresse' oder englisch ,High Pressure Grinding Roller Press' (HPGR) genannt werden. Das Austragsgut aus den Rollenpressen besteht aus noch vorhandenem Grobgut und einem bei der Zerkleinerung entstandenen Feingut. Zur Gewinnung des Feinguts wird es in Sichtern vom Grobgut abgeschieden. Für die Trennung von körnigen Feststoffen in Fraktionen mit verschiedenen Korngrößen ist bei der Zementherstellung der Einsatz von dynamischen Stabkorbsichtern bekannt, in denen Zementrohmehl und/oder Zement als Feingut abgeschieden wird. Zur Erzielung einer hohen Mahlfeinheit ist es bekannt, das Mahlgut im Verfahren einer Kreislaufmahlanlage solange im Umlauf zu führen, bis es aufgrund hinreichender Zerkleinerung aus dem Kreislauf durch Sichten entfernt wird.For the production of cement and / or cement raw meal suitable for cement production regrind such as cement clinker, metallurgical or slag sand, limestone and / or gypsum is placed in a device for grinding regrind. In particular, for the crushing of the material to be ground roller presses are used, which are also called 'high-grade roller mill', 'high-pressure roller press' (HPGR). The material to be removed from the roller presses consists of still existing coarse material and a fine material produced during comminution. For the production of the fine material, it is separated from the coarse material in classifiers. For the separation of granular solids into fractions of different grain sizes, the use of dynamic rod basket separators is known in cement production in which cement raw meal and / or cement is precipitated as fines. In order to achieve a high grinding fineness, it is known to circulate the millbase in the process of a Kreislaufmahlanlage until it is removed due to sufficient comminution from the circulation by sifting.

Für die Festigkeit des Baustoffes Zement ist dessen Korngrößenverteilung ein wesentlicher Parameter. Insbesondere kann sich eine sehr steile Korngrößenverteilungskurve negativ auf die Festigkeit von Zement auswirken. So ist es aus der Praxis bekannt, dass die Vermahlung von Zementklinker mit Rollenpressen zu steilen Korngrößenverteilungen führt, da hierbei nur ein geringer Feingutanteil mit einer im Vergleich zur mittleren Partikelgröße signifikant kleineren Partikelgröße entsteht. Von Vorteil sind daher Verfahren, die eine Verbreiterung der Korngrößenverteilung bewirken bzw. grundsätzlich eine Beeinflussung der Korngrößenverteilung zulassen, um eine hohe Qualität von Zement zu erreichen. Beispielsweise kommt es zu einer sehr hohen Zementfestigkeit, wenn eine Feingutfraktion von möglichst kleinen Körnern und eine Feingutfraktion aus größeren Körnern zusammen eine sehr kompakte Partikelanordnung bilden.For the strength of the building material cement whose particle size distribution is an essential parameter. In particular, a very steep grain size distribution curve can negatively impact the strength of cement. Thus, it is known from practice that the milling of cement clinker with roller presses leads to steep particle size distributions, since in this case only a small proportion of fines is formed with a particle size that is significantly smaller than the average particle size. Therefore, processes which cause a widening of the particle size distribution or, in principle, allow the particle size distribution to be influenced in order to achieve a high quality of cement are advantageous. For example, a very high cement strength occurs when a fines fraction of grains as small as possible and a fines fraction of larger grains together form a very compact particle arrangement.

Ausgehend vom Stand der Technik kann eine verbreiterte Korngrößenverteilung durch das Betreiben von mindestens zwei gleichartigen Kreislaufmahlanlagen erreicht werden. Durch Unterschiede bei den dabei eingesetzten Rollenpressen (insbesondere bei den Anpresskräften) und den Stabkorbsichtern (insbesondere bzgl. Drehzahl und Abmessungen) lassen sich unterschiedliche, steile Korngrößenverteilungen erzeugen. Aus DE 10 2008 019 830 A1 ist eine Umwälzmahlanlage mit Rollenpresse, statischem Vorsichter und dynamischem Sichter bekannt, wobei es möglich ist, zur Steigerung des Durchsatzes mehrere gleichartige Anlagen parallel zueinander zu betreiben. Auch aus WO 2009/068465 A1 ist eine Kreislaufmahlanlage bekannt, die sich aus mehreren Walzenpressen und korrespondierenden Sichtern zusammensetzt. Mit solchen Anlagen können durch Zusammenführung der jeweiligen Feinsichtgüter die gewünschte Korngrößenbeeinflussung und -verteilung erreicht werden. Es ist für die Zusammenführung jedoch kein anderes Verfahren bekannt gemacht, als einen Verschnitt der je für sich aus den Sichtluftströmen abgeschiedenen Feingutfraktionen der Teilanlagen vorzunehmen. Eigens einen Verschnitt des schon abgeschiedenen Feinguts vorzunehmen, bedeutet mit dem Bau und Betreiben einer Vorrichtung, die eine homogene Mischung der Feingutfraktionen der Teilanlagen erreicht, einen nachteiligen wirtschaftlichen, energetischen und baulichen Aufwand im Gesamtprozess der Zementherstellung.Starting from the prior art, a broadened particle size distribution can be achieved by operating at least two similar Kreislaufmahlanlagen. Differences in the roller presses used (in particular in the contact forces) and the rod basket sifters (in particular with regard to speed and dimensions) make it possible to produce different, steep particle size distributions. Out DE 10 2008 019 830 A1 a Umwälzmahlanlage with roller press, static caution and dynamic classifier is known, it being possible to operate in parallel to increase the throughput of several similar systems. Also from WO 2009/068465 A1 is a Kreislaufmahlanlage known, which is composed of several roller presses and corresponding classifiers. With such systems, the desired grain size influencing and distribution can be achieved by bringing together the respective light goods. However, no other method is known for the merger, as to make a waste of each separated from the classifying air streams fine material fractions of the units. Especially to make a blend of the already deposited fine material, means with the construction and operation of a device that is a homogeneous Mixture of the fine material fractions of the units achieved, a disadvantageous economic, energetic and structural complexity in the overall process of cement production.

Aufgabe der Erfindung ist es daher, ein Verfahren zur Herstellung eines Zements zur Verfügung zu stellen, welches die Nachteile aus dem Stand der Technik überwindet.The object of the invention is therefore to provide a method for producing a cement, which overcomes the disadvantages of the prior art.

Die erfindungsgemäße Aufgabe wird durch das Verfahren zur Herstellung eines Zements mit den Merkmalen des Anspruchs 1 gelöst. Weitere vorteilhafte Ausgestaltungen sind in den Unteransprüchen zu Anspruch 1 angegeben.The object of the invention is achieved by the method for producing a cement having the features of claim 1. Further advantageous embodiments are specified in the subclaims to claim 1.

Nach der Erfindung ist vorgesehen, dass in mindestens zwei Vorrichtungen zum Mahlen mindestens ein für die Zementherstellung geeignetes Mahlgut vermahlen wird und dass das in voneinander getrennten Sichtluftströmen suspendierte gemahlene Mahlgut jeweils einem dynamischen Stabkorbsichter pneumatisch zugeführt wird. In jedem Stabkorbsichter wird eine Trennung einer Grobkornfraktion (Grieße) und einer Feinkornfraktion erreicht. Die Grieße werden abgeführt. Die in den Stabkorbsichtern ausgesichteten Feingutfraktionen werden von den jeweiligen Sichtluftströmen in eine gemeinsame Austragsvorrichtung ausgetragen. In der Austragsvorrichtung strömen die Sichtluftströme zusammen. Das hierbei entstehende Strömungsfeld im Inneren der Austragsvorrichtung verwirbelt die Feingutpartikel und führt zu einer gleichmäßigen Durchmischung der Feingutfraktionen aus den einzelnen Stabkorbsichtern. Durch das Verfahren, die Feingutfraktionen aus den einzelnen Stabkorbsichtern schon durch Vereinen der Sichtluftströme zu durchmischen und nicht erst nach Abscheidung aus den jeweiligen Sichtluftströmen zu verschneiden, wird kein weiterer Schritt eines Verschnitts im Verfahren benötigt. Dies bietet bauökonomische und nicht zuletzt hinsichtlich der Energiekosten auch wirtschaftliche Vorteile, da auf eine zusätzliche Vorrichtung für einen solchen Verschnitt im Gesamtprozess der Zementherstellung verzichtet werden kann.According to the invention, it is provided that in at least two grinders at least one grindable material suitable for cement production is ground and that the ground grindbase suspended in separate classifying air streams is in each case supplied pneumatically to a dynamic rod basket sifter. In each rod basket sifter a separation of a coarse grain fraction (grits) and a fine grain fraction is achieved. The grits are taken away. The fine material fractions which are located in the rod basket sifters are discharged from the respective classifying air streams into a common discharge device. In the discharge device, the classifying air streams flow together. The resulting flow field inside the discharge device swirls the fine material particles and leads to a uniform mixing of the fine material fractions from the individual rod basket separators. By the method of mixing the fine material fractions from the individual rod sifter already by unifying the classifying air streams and not to be blended only after separation from the respective classifying air streams, no further step of a blending in the process is needed. This offers economic advantages, and not least in terms of energy costs also economic benefits, as can be dispensed with an additional device for such a blend in the overall process of cement production.

Nach der Erfindung kann es vorgesehen sein, dass den mindestens zwei Vorrichtungen zum Mahlen voneinander verschiedenes Mahlgut, beispielsweise Zementklinker, Hütten- bzw. Schlackensand, Kalkstein und/oder Gips, zugeführt wird. Werden den Vorrichtungen zum Mahlen zugleich unterschiedliche Ausgangsprodukte als jeweiliges Mahlgut zugeführt, kann damit Einfluss auf die Zusammensetzung des Zements bzw. Zementrohmehls genommen werden.According to the invention it can be provided that the at least two devices for grinding mutually different millbase, for example cement clinker, metallurgical or slag sand, limestone and / or gypsum, is supplied. If at the same time different starting materials are supplied to the devices for grinding as the respective ground material, this can influence the composition of the cement or cement raw meal.

Nach konkreter Ausgestaltung der Erfindung ist vorgesehen, als Vorrichtungen zum Mahlen vorzugsweise Rollenpressen einzusetzen. Betriebseigenschaften von Rollenpressen und die Beschaffenheit des von ihnen zerkleinerten Frischguts sind in der Zementherstellung gut bekannt. Insbesondere führen Rollenpressen zu steilen Korngrößenverteilungskurven. Durch unterschiedliche Einstellung der Zerkleinerungseigenschaften der verwendeten zwei oder mehr Rollenpressen mit jeweils nachfolgendem Stabkorbsichter kann für das gemeinsame Feingutprodukt leicht die gewünschte verbreiterte Korngrößenverteilung erreicht werden. Insbesondere ist damit im Falle von zwei Rollenpressen und zwei Stabkorbsichtern eine Zusammensetzung aus einem gröberen und einem feineren Feingutanteil im gemeinsamen Feingutprodukt erzeugbar, was zu einer hohen Festigkeit von Zement führt.According to a concrete embodiment of the invention, it is provided to use preferably roller presses as devices for grinding. Operating characteristics of roller presses and the nature of the comminuted fresh produce are well known in cement production. In particular, roller presses lead to steep particle size distribution curves. By varying the setting of the crushing properties of the two or more roller presses used, each with a following rod basket sifter, the desired broadened particle size distribution can easily be achieved for the common fine product product. In particular, in the case of two roller presses and two Stabkorbsichtern a composition of a coarser and a finer fines content in the common fines product is produced, resulting in a high strength of cement.

Das erfindungsgemäße Verfahren ist nicht auf den Einsatz von Rollenpressen begrenzt. Es ist möglich, an ihrer Stelle auch andere, aus der Zementherstellung bekannte Vorrichtungen zum Mahlen von Mahlgut, insbesondere Kugelmühlen (Rohrmühlen), Vertikalmühlen und Prallhammermühlen einzusetzen. Dies ermöglicht es nicht zuletzt zu Test- und Entwicklungszwecken, zusätzliche, durch das erfindungsgemäße Verfahren prinzipiell ermöglichte Beeinflussungen der Korngrößenverteilung im gemeinsamen Feingutprodukt vorzunehmen.The inventive method is not limited to the use of roller presses. It is possible, in their place, to use other devices known from cement production for grinding regrind, in particular ball mills (tube mills), vertical mills and impact hammer mills. This makes it possible, not least for testing and development purposes, to carry out additional influencing of the particle size distribution in the common fine product product that is fundamentally made possible by the method according to the invention.

Gemäß einer Ausführungsform der Erfindung ist es vorgesehen, das gemahlene Mahlgut aus den mindestens zwei Vorrichtungen zum Mahlen nicht direkt in die dynamischen Stabkorbsichter zu leiten, sondern zunächst einer Vorsichtung zu unterziehen. Dazu wird das zerkleinerte Mahlgut jeweils in einen statischen Vorsichter eingegeben. Vorsichter werden im Verfahren der Zementherstellung eingesetzt, um im Mahlgut befindliches Grobgut abzutrennen. Dabei handelt es sich um Grobgutreste, die im Mahlvorgang nicht zerkleinert wurden. Darüber hinaus gibt es einen Anteil an Agglomeraten im Austragsgut der Rollenpressen, die durch den hohen Anpressdruck bei der Gutbettzerkleinerung in den Rollenpressen aus den Partikeln des Zementklinkers gebildet wurden. Es ist bekannt, statische Vorsichter (z.B. Kaskadensichter) zur Desagglomeration dieser sogenannten Schülpen bei der Zementproduktion einzusetzen. Das in den statischen Vorsichtern abgetrennte Grobgut wird abgeführt. Das ausgesichtete Feingut jedes statischen Vorsichters wird mit einem eigenen Sichtluftstrom pneumatisch zur weiteren Aussichtung je einem dynamischen Stabkorbsichter zugeführt.According to one embodiment of the invention, it is provided that the ground material to be ground from the at least two devices for grinding is not directed directly into the dynamic rod basket sifter, but first subjected to a pre-seal. For this purpose, the crushed regrind is in each case in a static Caution entered. Caregivers are used in the process of cement production to separate coarse material located in the material to be ground. These are coarse material residues that were not crushed during the grinding process. In addition, there is a proportion of agglomerates in the Austragsgut the roller presses, which were formed by the high contact pressure in the Gutbettzerkleinerung in the roller presses from the particles of cement clinker. It is known to use static cautionary (eg Cascade classifier) for deagglomeration of these so-called scabs in cement production. The coarse material separated in the static cauterizers is removed. The screened fines of each static cauterizer are pneumatically fed with their own classifying air stream for further viewing of each dynamic bar cage sifter.

Gemäß einer weiteren Ausführungsform der Erfindung ist vorgesehen, die aus den mindestens zwei Stabkorbsichtern abgeführten Grobkornfraktionen (Grießeaustrag) erneut den Vorrichtungen zum Mahlen zuzuführen. Eine solche Rezirkulation des Grießeaustrags bietet die bekannten wirtschaftlichen Vorteile von Kreislaufmahlanlagen. Für eine bessere Kontrollierung der Korngrößenverteilungen ist vorgesehen, dass die einzelnen Mahlkreisläufe getrennt voneinander durchlaufen werden, d.h. die Grobkornfraktion aus einem Stabkorbsichter wird zur korrespondierenden Vorrichtung zum Mahlen zurückgeführt, von der her diesem Stabkorbsichter auch das Sichtgut zuströmt.According to a further embodiment of the invention, the coarse grain fractions discharged from the at least two rod basket sifters are again supplied to the devices for grinding. Such a recirculation of Grießeaustrags offers the known economic advantages of Kreislaufmahlanlagen. For a better control of the grain size distributions, it is provided that the individual grinding cycles are run separately from each other, i. the coarse grain fraction from a rod basket sifter is returned to the corresponding apparatus for grinding, from which forth this Stabkorbsichter also flows the Sichtgut.

Gemäß zumindest einer Ausführungsform der Erfindung ist es ferner vorgesehen, die mindestens zwei Stabkorbsichter zwar getrennt voneinander, aber in nur einem Gehäuse anzuordnen. Dies ermöglicht einen wirtschaftlich günstigen Materialaufwand für die Gehäusekonstruktion der Stabkorbsichter und nimmt den geringsten Raum für die Vorrichtungen zum Sichten ein. Im typischen Fall von zwei Stabkorbsichtern werden diese aus dynamischen Gründen vorzugsweise koaxial übereinander angeordnet.In accordance with at least one embodiment of the invention, it is further provided to arrange the at least two rod cage separators separately but in only one housing. This allows an economical material cost for the housing construction of the rod basket sifter and takes up the least space for the devices for sifting. Typically, two rod cage sifters are preferably coaxially stacked for dynamic reasons.

Die Erfindung wird anhand der folgenden Figuren näher erläutert. Es zeigt:

Figur 1:
ein erfindungsgemäßes Verfahren zur Herstellung eines Zements im Ausführungsbeispiel mit zwei als Rollenpressen ausgeführten Vorrichtungen zum Mahlen und zwei im Vertikalschnitt dargestellten Stabkorbsichtern in getrennten Gehäusen;
Figur 2:
ein erfindungsgemäßes Verfahren zur Herstellung eines Zements im Ausführungsbeispiel mit zwei als Rollenpressen ausgeführten Vorrichtungen zum Mahlen, zwei im Vertikalschnitt dargestellten Stabkorbsichtern in getrennten Gehäusen und mit Vorsichtung in zwei statischen Vorsichtern;
Figur 3:
ein erfindungsgemäßes Verfahren zur Herstellung eines Zements in einer Ausführungsform als Kreislaufmahlanlage, im Ausführungsbeispiel mit zwei als Rollenpressen ausgeführten Vorrichtungen zum Mahlen, zwei im Vertikalschnitt dargestellten Stabkorbsichtern in getrennten Gehäusen und mit Vorsichtung in zwei statischen Vorsichtern;
Figur 4a:
ein erfindungsgemäßes Verfahren zur Herstellung eines Zements im Ausführungsbeispiel mit zwei Vorrichtungen zum Mahlen, von denen eine eine Rollenpresse und die zweite eine Kugelmühle ist, und zwei im Vertikalschnitt dargestellten Stabkorbsichtern in getrennten Gehäusen;
Figur 4b:
ein erfindungsgemäßes Verfahren zur Herstellung eines Zements im Ausführungsbeispiel mit zwei Vorrichtungen zum Mahlen, von denen eine eine Vertikalmühle und die zweite eine Prallhammermühle ist, und zwei im Vertikalschnitt dargestellten Stabkorbsichtern in getrennten Gehäusen;
Figur 5:
Ausschnitt aus dem erfindungsgemäßen Verfahren zur Herstellung eines Zements, im Vertikalschnitt darstellend das Ausführungsbeispiel mit zwei Stabkorbsichtern in einem gemeinsamen Gehäuse.
The invention will be explained in more detail with reference to the following figures. It shows:
FIG. 1:
an inventive method for producing a cement in the embodiment with two executed as roller presses devices for grinding and two shown in vertical section Stabkorbsichtern in separate cases;
FIG. 2:
an inventive method for producing a cement in the embodiment with two executed as roller presses devices for grinding, two shown in vertical section Stabkorbsichtern in separate housings and with caution in two static Cautioners;
FIG. 3:
an inventive method for producing a cement in one embodiment as Kreislaufmahlanlage, in the embodiment with two designed as roller presses devices for grinding, two shown in vertical section Stabkorbsichtern in separate housings and with caution in two static cautionary;
FIG. 4a
an inventive method for producing a cement in the embodiment with two devices for grinding, one of which is a roller press and the second is a ball mill, and two shown in vertical section Stabkorbsichtern in separate cases;
FIG. 4b:
an inventive method for producing a cement in the embodiment with two devices for grinding, one of which is a vertical mill and the second is an impact hammer mill, and two in vertical sections shown Stabkorbsichtern in separate housings;
FIG. 5:
Section of the inventive method for producing a cement, in vertical section representing the embodiment with two rod basket sifters in a common housing.

In Figur 1 ist das erfindungsgemäße Verfahren zur Herstellung von Zement schematisch für das Ausführungsbeispiel dargestellt, in dem als Vorrichtungen zum Zerkleinern des mindestens einen Mahlguts zwei Rollenpressen 1, 2 eingesetzt werden. Das Austragsgut aus den Rollenpressen 1, 2 wird jeweils mit einem Sichtluftstrom 3a, 3b pneumatisch in das Gehäuse 6a, 6b je eines dynamischen Stabkorbsichters 4, 5 eingeführt. Jeder der beiden Stabkorbsichter 4, 5 verfügt über einen eigenen, drehzahlregelbaren Antrieb 24a, 24b, der ihn um seine Längsachse in eine Rotationsbewegung versetzt. Drehzahl und Drehrichtung der beiden Stabkorbsichter 4, 5 können unabhängig voneinander geregelt werden. Das in der Sichtluft suspendierte Mahlgut strömt den jeweiligen Stabkorbsichter 4, 5 wie dargestellt seitlich an und wird durch die Rotationsbewegung des Stabkorbsichters 4, 5 in dessen Sichtzone beschleunigt. Die auf die Teilchen des Sichtguts wirkenden Zentrifugalkräfte führen im Zusammenwirken mit der Reibungskraft der Luftströmung zu einer Auftrennung des Sichtguts in jeweils eine Grobkornfraktion 7, 8 (Grieße) und jeweils eine Feingutfraktion 9, 10. Die Grobkornfraktionen 7, 8 werden aus den Stabkorbsichtern 4, 5 aufgrund der Schwerkraft nach unten aus der jeweiligen Sichtzone ausgetragen (Grießeaustrag).In FIG. 1 the method according to the invention for the production of cement is shown schematically for the exemplary embodiment in which two roller presses 1, 2 are used as devices for comminuting the at least one ground material. The Austragsgut from the roller presses 1, 2 is pneumatically introduced in each case with a Sichtluftstrom 3a, 3b in the housing 6a, 6b each of a dynamic Stabkorbsichters 4, 5. Each of the two rod sifter 4, 5 has its own, speed-adjustable drive 24a, 24b, which puts him about its longitudinal axis in a rotational movement. Speed and direction of rotation of the two rod basket sifter 4, 5 can be controlled independently. The millbase suspended in the classifying air flows laterally toward the respective rod basket classifier 4, 5 and is accelerated by the rotational movement of the rod basket classifier 4, 5 into its zone of vision. The centrifugal forces acting on the particles of the Sichtguts lead in cooperation with the frictional force of the air flow to a separation of the Sichtguts in each case a coarse grain fraction 7, 8 (Grape) and each a fine material fraction 9, 10. The coarse grain fractions 7, 8 are from the Stabkorbsichtern 4, 5 discharged due to gravity down from the respective Sichtzone (Grießeaustrag).

Die ausgesichteten Feingutfraktionen 9, 10 werden pneumatisch von dem jeweiligen Sichtluftstrom aus dem jeweiligen Stabkorbsichter 4, 5 transportiert und gelangen beide in die Austragsvorrichtung 11. In einer wesentlichen Phase des erfindungsgemäßen Verfahrens zur Herstellung eines Zements kommt es in der Austragsvorrichtung 11 zu einem Vereinen der bislang getrennten Sichtluftströme. Die Zusammenführung der Sichtluftströme führt zu einer turbulenten Strömungsdynamik im Innenraum der Austragsvorrichtung 11. Hieraus resultiert eine Verwirbelung und in ihrer Folge eine gleichmäßige Durchmischung der in den Sichtluftströmen suspendierten Feingutfraktionen 9, 10 zu einem homogenen Fertiggut mit entsprechend zusammengesetzter Korngrößenverteilung. Dieses verlässt als Feingutstrom 12 die Austragsvorrichtung 11 und gelangt zur Abscheideeinrichtung (hier ein Zyklon) 13. In der Abscheideeinrichtung 13 wird das Feingut 14 vom Sichtluftstrom 15 getrennt und kann so im weiteren Verfahren der Zementherstellung in Silos eingelagert werden (nicht im Bild).The classified fines 9, 10 are pneumatically transported by the respective classifying air stream from the respective rod basket sifter 4, 5 and both arrive in the discharge device 11. In a substantial phase of the method according to the invention for the production of a cement occurs in the discharge device 11 to a club so far separate classifying air streams. The merger of the classifying air flows leads to a turbulent flow dynamics in the interior of the discharge device 11. This results in a turbulence and in its consequence a uniform mixing of suspended in the classifying air streams fine material fractions 9, 10 to a homogeneous finished product with a correspondingly composed particle size distribution. This leaves as the fine material flow 12, the discharge device 11 and reaches the separation device (here a cyclone) 13. In the separator 13 is the fine material 14 separated from the classifying air stream 15 and can be stored in silos in the further process of cement production (not in the picture).

In den Figuren 4a und 4b sind Ausführungsbeispiele des erfindungsgemäßen Verfahrens zur Herstellung eines Zements mit einer Rollenpresse 1 und einer Kugelmühle 16 ( Figur 4a ) bzw. mit einer Vertikalmühle 17 und einer Prallhammermühle 18 ( Figur 4b ) dargestellt. Darüber hinaus sind Verfahren und Aufbau so wie in Figur 1 . In the FIGS. 4a and 4b are exemplary embodiments of the inventive method for producing a cement with a roller press 1 and a ball mill 16 ( FIG. 4a ) or with a vertical mill 17 and an impact hammer mill 18 (FIG. FIG. 4b ). In addition, procedures and structure are as in FIG. 1 ,

In Figur 2 ist basierend auf dem Ausführungsbeispiel aus Figur 1 schematisch ein erfindungsgemäßes Verfahren zur Herstellung eines Zements dargestellt, bei dem das Austragsgut aus den Rollenpressen 1, 2 jeweils eine Vorsichtung erfährt, bevor es in einen der Stabkorbsichter 4, 5 geleitet wird. Der Austragsgutstrom 20a, 20b aus jeder Rollenpresse 1, 2 wird dazu jeweils einem statischen Vorsichter 21, 22 zugeführt. Das in einen statischen Vorsichter 21, 22 aufgegebene Austragsgut wird in diesem getrennt in eine Fraktion von Feingut 27a, 27b des statischen Vorsichters 21, 22 und eine Grobgutfraktion, die auf dem Wege der Grobgutabführung 26a, 26b den statischen Vorsichter 21, 22 verlässt. Das abgeschiedene Feingut 27a, 27b des statischen Vorsichters 21, 22 wird pneumatisch mit einem Sichtluftstrom 19a, 19b in je einen der Stabkorbsichter 4, 5 geleitet.In FIG. 2 is based on the embodiment of FIG. 1 schematically illustrates an inventive method for producing a cement, in which the Austragsgut from the roller presses 1, 2 each undergoes a Vorsichtung before it is passed into one of the rod basket classifier 4, 5. The Austragsgutstrom 20a, 20b from each roller press 1, 2 is to each a static caution 21, 22, respectively. The discharged into a static cauterizer 21, 22 Austragsgut is separated into this in a fraction of fines 27a, 27b of the static Bewässers 21, 22 and a coarse material fraction, which leaves on the way Grobgutabführung 26a, 26b, the static cautery 21, 22. The separated fines 27a, 27b of the static cauterizer 21, 22 is pneumatically with a classifying air stream 19a, 19b in each one of the rod basket classifier 4, 5 passed.

In Figur 3 ist basierend auf dem Ausführungsbeispiel aus Figur 2 ein zu einem Mahlkreislauf erweitertes, erfindungsgemäßes Verfahren zur Herstellung eines Zements dargestellt. Bei ansonsten gleichem Verfahrensablauf wird in dieser Ausführungsform der Grießeaustrag aus den Stabkorbsichtern 4, 5 jeweils zu den Vorrichtungen zum Mahlen 1, 2 zurückgeführt. Die Rezirkulation erfolgt getrennt und zu der jeweils korrespondierenden Rollenpresse 1, 2: Für die Grobkornfraktion 7 aus dem Stabkorbsichter 4 erfolgt eine Zuführung 25a der Grobkornfraktion zurück zur Rollenpresse 1; analog erfolgt die Zuführung 25b der Grobkornfraktion zurück zur Rollenpresse 2. Die Rollenpressen 1, 2 vermahlen die rezirkulierten Grobkornfraktionen 7, 8 zusammen mit dem in den Frischgutzuführungen 23a, 23b jeweils zugeführten Mahlgut. Die Austragsgutströme 20a, 20b aus den Rollenpressen 1, 2 werden jeweils in die entsprechenden statischen Vorsichter 21, 22 geleitet. Der in den Grobgutabführungen 26a, 26b der statischen Vorsichter 21, 22 abgeführte Grobgutaustrag kann - in der Figur nicht dargestellt - direkt oder nach einer weiteren Vormahlung mit Frischgut zusammengeführt und auf dem Wege der Frischgutzuführungen 23a, 23b ebenfalls wieder in den Mahlkreislauf eingespeist werden.In FIG. 3 is based on the embodiment of FIG. 2 an extended to a grinding cycle, inventive method for producing a cement shown. With otherwise the same procedure in this embodiment, the Grießeaustrag from the Stabkorbsichtern 4, 5 each returned to the devices for grinding 1, 2. The recirculation takes place separately and to the respectively corresponding roller press 1, 2: For the coarse grain fraction 7 from the rod basket sifter 4, a feed 25a of the coarse grain fraction takes place back to the roller press 1; Similarly, the feed 25b of the coarse grain fraction takes place back to the roller press 2. The roller presses 1, 2 grind the recirculated coarse grain fractions 7, 8 together with that in the fresh material feeds 23a, 23b each supplied grinding stock. The Austragsgutströme 20a, 20b from the roller presses 1, 2 are each passed into the corresponding static caution 21, 22. The coarse material discharge discharged into the coarse material removal lines 26a, 26b of the static cauterizers 21, 22 can - not shown in the figure - be brought together with fresh material directly or after further pre-grinding and likewise fed back into the grinding cycle by way of the fresh material feeds 23a, 23b.

Figur 5 zeigt in einer Ausschnittsskizze ein Ausführungsbeispiel des erfindungsgemäßen Verfahrens, bei dem die zwei Stabkorbsichter 4, 5 in nur einem Gehäuse 6c angeordnet sind. Aus dynamischen Gründen ist eine koaxiale Anordnung der Stabkorbsichter 4, 5 günstig, wie dargestellt. Dabei werden die Stabkorbsichter 4, 5 getrennt voneinander vom jeweiligen Sichtluftstrom 3a, 3b angeströmt. Die Feingutfraktionen 9, 10 gelangen getrennt voneinander in die Austragsvorrichtung 11, in der die Sichtluftströme vereint und die beiden Feingutfraktionen 9, 10 gleichmäßig durchmischt werden. Darüber hinaus sind Verfahren und Aufbau so wie in einer der Figuren 1 bis 4b . BEZUGSZEICHENLISTE 1 Rollenpresse 16 Kugelmühle 2 Rollenpresse 17 Vertikalmühle 3a, 3b Sichtluftstrom 18 Prallhammermühle 4 Stabkorbsichter 19a, 19b Sichtluftstrom 5 Stabkorbsichter 20a, 20b Austragsgutstrom 6a, 6b, 6c Gehäuse 21 Statischer Vorsichter 7 Grobkornfraktion 22 Statischer Vorsichter 8 Grobkornfraktion 23a, 23b Frischgutzuführung 9 Feingutfraktion 24a, 24b Antrieb 10 Feingutfraktion 25a, 25b Zuführung der Grobkornfraktion 11 Austragsvorrichtung 12 Feingutstrom 26a, 26b Grobgutabführung 13 Abscheideeinrichtung 27a, 27b Feingut des statischen Vorsichters 14 Feingut 15 Sichtluftstrom FIG. 5 shows a detail of an embodiment of the method according to the invention, in which the two rod basket viewers 4, 5 are arranged in only one housing 6c. For dynamic reasons, a coaxial arrangement of the rod basket sifter 4, 5 is favorable, as shown. The rod basket separators 4, 5 are separated from each other by the respective Sichtluftstrom 3a, 3b flows. The fines 9, 10 are separated from each other in the discharge 11, in which combines the classifying air streams and the two fines 9, 10 are uniformly mixed. In addition, procedures and structure are as in one of Figures 1 to 4b , <I> LIST OF REFERENCES </ i> 1 roller Press 16 ball mill 2 roller Press 17 vertical mill 3a, 3b Classifying air stream 18 Impact hammer mill 4 Rod basket sifter 19a, 19b Classifying air stream 5 Rod basket sifter 20a, 20b Austragsgutstrom 6a, 6b, 6c casing 21 Static Caution 7 Coarse particle fraction 22 Static Caution 8th Coarse particle fraction 23a, 23b fresh material 9 fines fraction 24a, 24b drive 10 fines fraction 25a, 25b Feeding the coarse grain fraction 11 discharge 12 fine material 26a, 26b Grobgutabführung 13 separating 27a, 27b Fines of static caution 14 fines 15 Classifying air stream

Claims (6)

  1. Method for producing cement, wherein
    - at least one material to be ground is ground in at least two grinding devices (1, 2, 16, 17, 18) into differently ground material with grain size distributions that are different from one another,
    - the ground material from each of the at least two grinding devices (1, 2, 16, 17, 18) is fed separately from one another by its own respective classifying air stream (3a, 3b) to one of at least two bar-cage classifiers (4, 5),
    - in each of the at least two bar-cage classifiers (4, 5) a fine material fraction (9, 10)is separated out and a coarse grain fraction (7, 8) is discharged,
    characterized by
    combining the classifying air streams, emerging from the at least two bar-cage classifiers (4, 5) and supporting the fine material fractions (9, 10), inside a common discharge device (11), wherein a uniform mixing of the fine material fractions (9, 10) takes place.
  2. Method as claimed in claim 1, characterized in that the at least two grinding devices (1, 2, 16, 17, 18) are preferably roller presses(1, 2).
  3. Method as claimed in one of claims 1 to 2,
    characterized in that
    - the ground material is discharged from the at least two grinding devices (1, 2, 16, 17, 18) and is supplied in discharged material flows (20a, 20b) separately from one another each to one of at least two static preliminary sifters (21, 22),
    - in the static preliminary sifters (21 22) a coarse material discharge (26a, 26b) and a separating out of the fine material (27a, 27b) of the static preliminary sifters (21, 22) takes place,
    - the fine material (27a, 27b) of the at least two static preliminary sifters (21, 22) is supplied separated from one another by its own classifying air stream (19a, 19b) into one each of the at least two bar-cage classifiers (4, 5).
  4. Method as claimed in one of claims 1 to 3,
    characterized in that
    the coarse grain fractions (7, 8) are discharged from the at least two bar-cage classifiers (4, 5) and are supplied separately from one another to the respective corresponding device of the at least two grinding devices (1, 2, 16, 17, 18).
  5. Method as claimed in one of claims 1 to 4,
    characterized in that
    at least two of the at least two bar-cage classifiers (4, 5) are arranged in only one housing (6c).
  6. Method as claimed in one of claims 1 to 5,
    characterized in that
    at least one of the at least two grinding devices (1, 2, 16, 17, 18) is a ball mill (16), a vertical mill (17) or an impact hammer mill (18).
EP14805222.8A 2013-11-26 2014-11-21 Method for producing cement Not-in-force EP3074137B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102013019840.2A DE102013019840A1 (en) 2013-11-26 2013-11-26 Process for the production of cement
PCT/EP2014/075308 WO2015078787A1 (en) 2013-11-26 2014-11-21 Method for producing cement

Publications (2)

Publication Number Publication Date
EP3074137A1 EP3074137A1 (en) 2016-10-05
EP3074137B1 true EP3074137B1 (en) 2017-10-25

Family

ID=51999410

Family Applications (1)

Application Number Title Priority Date Filing Date
EP14805222.8A Not-in-force EP3074137B1 (en) 2013-11-26 2014-11-21 Method for producing cement

Country Status (4)

Country Link
EP (1) EP3074137B1 (en)
DE (1) DE102013019840A1 (en)
DK (1) DK3074137T3 (en)
WO (1) WO2015078787A1 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102014015654B4 (en) * 2014-10-22 2016-08-11 Khd Humboldt Wedag Gmbh Plant for grinding and sifting cement clinker
DE102015001404B3 (en) 2015-02-04 2016-08-04 Khd Humboldt Wedag Gmbh Kreislaufmahlanlage with two grinders and method for operating the Kreislaufmahlanlage
CN108043511A (en) * 2018-01-16 2018-05-18 海安海太铸造有限公司 A kind of raw materials for cement crushes dispensing mixing arrangement
CN108554507A (en) * 2018-01-16 2018-09-21 海安海太铸造有限公司 Efficient centrifugal, mixing apparatus in a kind of manufacture of cement

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4334904A1 (en) * 1993-10-13 1995-04-20 Kloeckner Humboldt Deutz Ag Circulating grinding plant
DE10333361A1 (en) * 2003-07-23 2005-02-10 Gebr. Pfeiffer Ag Process for preparation of cement e.g. Portland cement involves milling cement clinker with sulfate containing carrier material and other components in a roller mill
DE202007016785U1 (en) 2007-11-29 2009-04-02 Khd Humboldt Wedag Gmbh Kreislaufmahlanlage
DE102008019830B4 (en) 2008-04-11 2019-01-24 Khd Humboldt Wedag Gmbh Circulation meter with external risers

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
None *

Also Published As

Publication number Publication date
EP3074137A1 (en) 2016-10-05
DK3074137T3 (en) 2018-01-29
DE102013019840A1 (en) 2015-05-28
WO2015078787A1 (en) 2015-06-04

Similar Documents

Publication Publication Date Title
EP0603481B1 (en) Method and arrangement for milling grinding stock
EP0650763B1 (en) Closed circuit grinding plant
EP2271428A1 (en) Circulating mill system with external rising pipes
DE102007046834B4 (en) Process for the production of cements containing granulated blastfurnace
WO2015086554A1 (en) Closed-circuit grinding plant having a pre-classifier and a ball mill
EP3074137B1 (en) Method for producing cement
EP0406591B1 (en) Method and arrangement for milling material to be milled
WO2010072276A1 (en) Method and apparatus for comminuting mineral ground product
DE102014010065B3 (en) Kreislaufmahlanlage with second grinding circuit and method for operating the Kreislaufmahlanlage
DE102015001404B3 (en) Kreislaufmahlanlage with two grinders and method for operating the Kreislaufmahlanlage
DE19514971A1 (en) Energy efficient grinding, esp. of cement clinker
EP3665133B1 (en) Method and plant for producing cement
DE19526040A1 (en) Installation in which grains of material are reduced in size
EP0366759B1 (en) Process for size reduction of brittle grinding material
EP2407244B1 (en) Method for comminution of material by a tube mill
DE3710602A1 (en) Apparatus and method for processing granular material, in particular wheat
EP0648539B1 (en) Closed circuit grinding plant
DE4307230A1 (en) Process and plant for comminuting the bed of brittle regrind
EP3368222B1 (en) Pneumatically connected cascade classifier and circulating grinding plant with pneumatically connected cascade classifiers
EP3655164B1 (en) Two-stage milling circuit and method for producing a milled product by means of a two-stage milling
EP1640070B1 (en) Apparatus and method for grinding material
DE10147591A1 (en) Process for crushing regrind and grinding plant
DE102014015654B4 (en) Plant for grinding and sifting cement clinker
DE102014015161A1 (en) Plant for grinding and sifting cement clinker
DE102014006429B4 (en) Plant and method for grinding and sifting cement clinker with impermeability

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: 20160519

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

AX Request for extension of the european patent

Extension state: BA ME

DAX Request for extension of the european patent (deleted)
GRAP Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOSNIGR1

INTG Intention to grant announced

Effective date: 20170707

GRAS Grant fee paid

Free format text: ORIGINAL CODE: EPIDOSNIGR3

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AL AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO RS SE SI SK SM TR

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: AT

Ref legal event code: REF

Ref document number: 939430

Country of ref document: AT

Kind code of ref document: T

Effective date: 20171115

REG Reference to a national code

Ref country code: IE

Ref legal event code: FG4D

Free format text: LANGUAGE OF EP DOCUMENT: GERMAN

REG Reference to a national code

Ref country code: DE

Ref legal event code: R096

Ref document number: 502014005994

Country of ref document: DE

REG Reference to a national code

Ref country code: FR

Ref legal event code: PLFP

Year of fee payment: 4

REG Reference to a national code

Ref country code: DK

Ref legal event code: T3

Effective date: 20180122

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DK

Payment date: 20171212

Year of fee payment: 4

Ref country code: FR

Payment date: 20171213

Year of fee payment: 4

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20171212

Year of fee payment: 4

REG Reference to a national code

Ref country code: NL

Ref legal event code: MP

Effective date: 20171025

REG Reference to a national code

Ref country code: LT

Ref legal event code: MG4D

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 FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20171025

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NO

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: 20180125

Ref country code: LT

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: 20171025

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: 20171025

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: 20171025

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: 20171025

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BG

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: 20180125

Ref country code: GR

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: 20180126

Ref country code: RS

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: 20171025

Ref country code: IS

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: 20180225

Ref country code: HR

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: 20171025

Ref country code: LV

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: 20171025

REG Reference to a national code

Ref country code: DE

Ref legal event code: R119

Ref document number: 502014005994

Country of ref document: DE

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: CZ

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: 20171025

Ref country code: MC

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: 20171025

Ref country code: EE

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: 20171025

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: 20171025

Ref country code: SK

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: 20171025

Ref country code: CH

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20171130

Ref country code: LI

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20171130

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: 20171121

Ref country code: RO

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: 20171025

Ref country code: PL

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: 20171025

Ref country code: SM

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: 20171025

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

Effective date: 20171025

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: IE

Ref legal event code: MM4A

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: MT

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: 20171025

26N No opposition filed

Effective date: 20180726

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: 20180602

Ref country code: IE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20171121

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: SI

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: 20171025

REG Reference to a national code

Ref country code: DK

Ref legal event code: EBP

Effective date: 20181130

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: HU

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT; INVALID AB INITIO

Effective date: 20141121

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20181121

REG Reference to a national code

Ref country code: BE

Ref legal event code: MM

Effective date: 20181130

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20181130

Ref country code: DK

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20181130

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: BE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20181130

Ref country code: MK

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: 20171025

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20181121

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: TR

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: 20171025

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

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: 20171025

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AL

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: 20171025

REG Reference to a national code

Ref country code: AT

Ref legal event code: MM01

Ref document number: 939430

Country of ref document: AT

Kind code of ref document: T

Effective date: 20191121

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: AT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20191121