Title of Invention

METHOD AND APPARATUS FOR MILLING HOT AND WET RAW MATERIALS

Abstract

The invention is particularly suitable for the cement industry and the grinding and simultaneous drying of cement clinker, slag and aggregates. In order to achieve a throughput increase and energy saving, as well as an improvement in the product quality, particularly with mixed cements, there is a simultaneous grinding and drying through a controlled supply of a cooling gas in the upper mill part with a relatively high hot gas inlet temperature in the lower mill part. The cooling gas supplies ensures a predetermined gas-product temperature downstream of the classifier and replaces or significantly reduces the disadvantageous cooling water injection.

Full Text

1 English translation of the filed PCT-Application METHOD AND DEVICE FOR GRINDING HOT, WET RAW MATERIAL The invention relates to a method for grinding hot, wet raw material according to the preamble of claim 1 and to a device for grinding hot, wet raw material according to the preamble of claim 15. The invention particularly applies to the cement industry for grinding and simultaneously drying raw materials, such as cement clinker, slag and aggregates. It is known that for such mill drying processes vertical mills with integrated or mounted classifiers, particularly Loesche-type air-swept roller mills, are particularly suitable. Grinding systems with vertical mills can be operated in compound with rotary kilns and in addition the waste gases from the heat exchanger and clinker cooler process can be used for mill drying and for the pneumatic conveying of the milled material. DE 198 36 323 C2 describes methods and plants for the production of cement using a vertical mill. New page 2 Besides the mill drying of raw powder in an air-swept roller mill, DE-AS 23 61 060 dis- closes cooling grinding of cement clinker in an air-swept roller mill downstream of a ro- tary tubular kiln. "US patent 4,597,537 discloses a vertical mill having an integrated classifier and a mill housing constructed in a defined manner. For improving classifier efficiency, fitted ele- ments are located in the vicinity of the upper grinding area and upstream of the classi- fier and influence the grinding material-fluid flow. In the vicinity of the classifier there are also tangential gas supplies with which the gas flow in the classifier is regulated. In the wall of the grit cone is provided a further gas supply for the supply of hot gas, in order to bring about a separation of fine particles adhering to the coarse particles with respect to the latter and the return thereof to the classifying area. For the grinding of slag and mixed cements use is advantageously made of modified Loesche-type roller mills, which can be referred to as 2+2 or 3+3 roller mills. In these vertical mills use is made of roller pairs, in each case comprising a precompressing roller or S-roller (slave roller) and a grinding roller, or M-roller (master roller) (EP 406 644 B1). New page 2a When grinding raw material, such as cement clinker, slag and aggregates, the raw ma- terial components have different moisture contents and/or different temperatures. Hot cement clinker, which can have temperatures of 120° C and higher, is ground in cement plants on increasing the capacity of the rotary kilns and when the existing capacity of the clinker cooler is not adequate and/or if the clinker storage in silos or outside storage does not provide an adequate aftercooling time up to the time of grinding, which can particularly arise with on-line production. When grinding hot cement clinker in vertical mills with slag and wet aggregates the nec- essary cooling and drying gases deteriorate in their function as carrying gases. Drying gas or hot gas must be supplied at an adequately high temperature and volume, so that the drying process can take place quickly during grinding. The cooling gas, particularly fresh air, is admixed in regulated manner to the hot gas at corresponding feed tempera- tures, particularly of the cement clinker or slag. 3 In order to achieve the desired gas and product temperature downstream of the classi- fier, it is often necessary to inject water into the grinding chamber, e.g. into the coarse material circulation zone. The disadvantages are an increased energy demand due to the necessary cooling water evaporation, a deterioration of the cement quality and in- creased wear to the grinding parts, together with an increased energy demand at the ~ mill motor. The object of the invention is to provide a method and a device for the simultaneous grinding and drying of hot, wet raw material in a vertical mill, so as to ensure an opti- mum throughput capacity and energy saving and at the same time an improvement in the product quality, particularly in the case of mixed cements. With respect to the method the object is achieved through the features of claim 1 and with respect to the device by the features of claim 15. Appropriate and advantageous developments are contained in the subclaims and the description relative to the draw- ings. It is a fundamental idea of the inventive method to achieve a high grinding/drying effi- ciency, in that the temperature level of the hot gas, which is supplied to the mill via the nozzle ring or vane ring, is so adjusted that the milling and drying speeds are the same. This can lead to a maximum milling throughput capacity with a minimum electrical po- wer consumption of the mill, classifier and blower motors. New page 4 According to the invention hot gas is supplied with a gas inlet temperature which, apart from taking account of the raw material temperature, is significantly determined by the moisture content of the raw material component with the highest moisture level. Accord- ing to the invention, for regulating the predetermined classifier outlet temperature of the gas-product mixture, as the cooling medium a cooling gas is introduced into the vertical mill above the nozzle ring and separately from the hot gas and is admixed with the ground material-gas mixture. An injection of water as the coolant is replaced or at least significantly reduced by the supply of a cooling gas, particularly fresh air from the environment. This leads to the advantage of saving heating energy due to the no longer necessary or reduced cooling water evaporation. It is advantageous that through the subdivision of the mill gas volume or carrying gas into hot gas, which is supplied to the lower part of the mill, and cooling gas which is supplied to the upper part of the mill, the simultaneous grinding and drying is deter- mined by the hot gas supplied here. Due to the high gas inlet temperatures in the lower area of the upper part of the mill a simultaneous grinding and raw material drying and therefore an optimum mill throughput capacity are possible. Simultaneously, due to the replacement of cooling water by cooling gas, particularly by fresh air or at least partially cooled air, in an energy-optimum manner the necessary product and gas temperature can be regulated after the mill and can advantageously be By obviating cooling water injection or injecting only significantly reduced cooling water quantities, there is a heating energy economy and simultaneously an improvement to New page 5 the product quality. In addition, there are process advantages for downstream plant equipment, such as bag filters and blowers. It is appropriate to operate the grinding system with vertical mill, classifier and filter with a mill fan or blower, which produces a necessary volume flow. Generally the grinding system is vacuum-operated, so that advantageously ambient air can be sucked as cool- ing gas into the upper mill area. As a function of the feed temperature of the raw material components and the moisture content, it can be appropriate to supply the vertical mill with hot gas at an inlet tempera- ture > 180° C, e.g. approximately 230° C. It has been found that a subdivision of the overall mill volume or the carrying gas in such a way that up to 70% of the volume flow is supplied as hot gas to the lower part of the mill and up to 30% as cooling gas, particularly fresh air, to the upper part of the mill, is advantageous for optimizing the mill drying efficiency of a cement clinker and slag grinding and supplied aggregates. The total gas quantity of the vertical mill is regulated by a mill fan action and measurements downstream of the filter. Appropriately the cooling gas is introduced into the upper mill part with a swirling flow into the grinding area corresponding to the rising grinding material-gas mixture. Relative to the grinding rollers rolling on the grinding pan and optionally present slave rollers, it is appropriate to have the supply of cooling gas in an area between the grinding rollers or between a grinding roller and a slave roller. New page 6 It is also advantageous to measure the hot gas inlet temperature upstream of the verti- cal mill and to regulate it by a hot gas generator and/or by a gas supply from neighbour- ing processes, e.g. from a clinker cooler, and/or by the return of waste gases down- stream of the filter and mill fan. The inventive device for grinding hot, wet raw material, particularly cement clinker, slag and aggregates, has a grinding system with a vertical mill, a classifier and a feed line for hot gas, as well as at least one supply device for a cooling medium for regulating a pre- determined gas and product temperature downstream of the classifier, the supply de- vices being designed for a cooling gas, preferably fresh air from the environment and above the nozzle ring and positioned upstream of the classifier in the upper mill part and between the grinding rollers or between the grinding rollers and slave rollers. Appropriately the supply devices are swirl boxes equipped with adjustable swirl flaps for regulating the cooling air quantities as a function of the desired temperature value downstream of the classifier. New page 6a Downstream of the classifier the grinding system has a filter, e.g. a bag filter, and a downstream mill fan, which with a relatively high suction capacity ensures a vacuum or suction operation in the mill, classifier and filter and advantageously permits an intake into the upper part of the mill of ambient air. Optionally there can be an additional blo- wer for the cooling gas supply. Appropriately there is a controlled system for cooling gas supply, in which the gas and product temperature downstream of the classifier is a controlled variable. 7 Combined with said controlled system advantageously there is a second controlled sys- tem, which controls the hot gas quantity and temperature in the vertical mill. The con- trolled variables can be the maximum moisture content of a raw material component and the hot gas temperature in the feed line to the vertical mill. Appropriately the swirl flaps of the swirl boxes are set up for a tangential cooling gas supply to ensure that the cooling gas has virtually the same flow direction as the rising grinding material-gas mixture. The invention is described in greater detail hereinafter relative to embodiments and with reference to the attached highly diagrammatic drawings, wherein show: Fig. 1 A plant diagram for a device according to the invention. Fig. 2 A plan view of the grinding pan of an inventive vertical mill. Fig. 3 A plan view of the grinding pan of an inventive 2+2 roller mill. Fig. 1 shows a grinding system with an inventive vertical mill 2 in the form here of a Loesche-type air-swept roller mill and having an integrated classifier 6. In highly dia- grammatic manner is shown a supply of hot gas 4 via a hot gas feed line 14 in the lower mill part 3 and a supply of cooling gas 8 in the upper mill part 5. There is a separate supply, particularly of max 70% hot gas 4 and max 30% cooling gas 8 to the grinding area 7. The hot gas 4 and cooling gas 8 form the supporting or carrying gas for the mill drying process. The hot gas 4 is in per se known manner supplied by means of a nozzle or vane ring (not shown) surrounding a grinding pan in the lower mill part 3 and is used for the drying of the raw materials, e.g. cement clinker, slag and wet aggregates (not shown) supplied via a not shown feed mechanism, as well as proportionally the pneumatic conveying of the grinding material-gas mixture into the classifier 6. A temperature measuring device 21 is positioned upstream of the vertical mill 2 in the hot gas feed line 14 for controlling the hot gas supply, and as a function of the quantity, wetness and temperature of the supplied raw material components and the predeter- mined gas and product temperature downstream of the classifier 6, the temperature and volume of the hot gas 4 are controlled. 8 The hot gas line 14 is connected to a return line 20 for the waste gas from filter 11, which is connected downstream of the vertical mill 2 with classifier 6, so that part of the waste gas can be admixed with the hot gas 4 from a hot gas generator 17. The hot gas 4 fed to the vertical mill 2 together with the cooling gas 8 supplied to the upper mill part 5 and which is in particular fresh or ambient air, forms the carrying gas with which the grinding material is conveyed in the rising grinding material-gas mixture - to the classifier 6 and via a connecting line 22 to filter 11. A mill fan 12 downstream of filter 11 has the necessary suction capacity and ensures a vacuum in vertical mill 2, classifier 6 and filter 11, so that advantageously the cooling air 8 necessary for a predetermined gas and product temperature downstream of the clas- sifier 6 can be sucked in. The cooling air 8 passes via supply devices 18, which are lo- cated in or on the mill housing 13 of the upper mill part 5, into the grinding area or chamber 7. A controlled system with a temperature measuring device 23 is positioned downstream of classifier 6 in connecting line 23 for controlling the cooling gas or fresh air supply. In order in the case of particularly high raw material, e.g. cement clinker inlet tempera- tures to ensure the desired gas and product temperature downstream of the classifier, a cooling water supply 19 is provided in grinding area 7. However, the controllable water injection is greatly reduced and is essentially replaced by the fresh air supply in the up- per mill part 5. Fig. 2 shows in highly diagrammatic form the arrangement of supply devices 18 for the cooling gas 8 in the upper mill part. Here the supply devices 8 are swirl boxes, whose swirl flaps can be set for a controlled tangential supply or swirling flow corresponding to the rising grinding material-gas flow in grinding area 7 (fig. 1). On a grinding pan 10 roll two grinding rollers 15 and in the area between the grinding rollers 15 are provided two swirl boxes 18 as supply devices for fresh air 8 in or on mill housing 13 (cf. fig. 1). -9- Fig. 3 shows in highly diagrammatic form a detail of a 2+2 roller mill, in which two grind- ing rollers 15 and two slave rollers 16 roll on a grinding pan 10. Between each slave roller 16 and each grinding roller 15 are provided in the upper mill part 5 supply devices 18 for a controlled supply of the.cooling gas 8 corresponding to the swirling flow of the rising grinding material-gas mixture. 10 NEW CLAIMS 1 TO 23 1. Method for grinding hot, wet raw material, particularly cement clinker, slag and aggregates, in which the raw material components are fed to a vertical mill (2), ground and simultaneously dried with the aid of hot gas (4) supplied via a nozzle ring to a lower mill part (3) and in which with the aid of a cooling medium a predeterminable gas and product temperature downstream of a classifier (6) is maintained, characterized in that the hot gas (4) is supplied with a gas inlet temperature which is determined by the moisture content of the raw material component with the highest moisture level and above the nozzle ring and separately from the hot gas (4) a cooling gas (8) is introduced into the vertical mill (2) and admixed with the grinding material-gas mixture. 2. Method according to claim 1, characterized in that, relative to the total carrying gas quantity in the vertical mill (2), up to 30% cool- ing gas (8) is supplied to the upper mill part (5) of vertical mill (2). 3. Method according to claim 1 or 2, characterized in that fresh air is supplied as cooling gas (8). 4. Method according to one of the preceding claims, characterized in that at least partially cooled air is supplied as cooling gas (8). 11 5. Method according to one of the preceding claims, characterized in that and this maintained by a controlled supply of cooling gas (8). 6. Method according to one of the preceding claims, characterized in that vacuum is supplied to vertical mill (2), classifier (6) and a filter (11) and ambient air is sucked in as cooling gas (8). 7. Method according to claim 6, characterized in that the vacuum is produced by a mill fan (12) with a necessary volume flow and which is connected downstream of filter (11). 8. Method according to one of the preceding claims, characterized in that hot gas (4) is supplied with an inlet temperature > 180° C, e.g. around 230° C to the vertical mill (2). 9. Method according to one of the preceding claims, characterized in that the hot gas inlet temperature in vertical mill (2) is controlled as a function of the quantity and moisture content of the overall or individual components of the raw material. 10. Method according to one of the preceding claims, characterized in that up to 70% of the volume flow in vertical mill (2) is supplied as hot gas (4). 11. Method according to one of the preceding claims, characterized in that the total gas quantity of vertical mill (2) is controlled by measurement down- stream of filter (11) and action on the mill fan (12). 12 12. Method according to one of the preceding claims, characterized in that cooling gas (8) is introduced into the grinding area (7) with a swirling flow corre- sponding to the rising grinding material-gas mixture. 13. Method according to one of the preceding claims, characterized in that the cooling gas (8) is introduced into grinding area (7) via supply devices (18) in mill housing (13) and which are located in the vicinity of the upper mill part (5) and between grinding rollers (15) or between grinding rollers (15) and slave roll- ers (16). 14. Method according to one of the preceding claims, characterized in that the hot gas inlet temperature is measured upstream of vertical mill (2) and is controlled by a hot gas generator (17) and/or by a gas supply from neighbouring processes and/or a return of the gas downstream of mill fan (12). 15. Device for grinding hot, wet raw material, particularly cement clinker, slag and aggregates, having a vertical mill (2), a classifier (6) and a feed line (14) for hot gas (4), which passes via a nozzle ring in the lower mill part (3) into grinding area (7) and having at least one supply device (18) for a cooling medium with which it is pos- sible to regulate a predeterminable gas and product temperature downstream of the classifier (6), particularly for performing the method according to one of the claims 1 to 14, characterized in that the supply devices (18) are designed for a cooling gas (8) as cooling medium and proportionally carrying gas for the grinding material and are positioned up- stream of classifier (6) in upper mill part (5) and between the grinding rollers (15) or between grinding rollers (15) and slave rollers (16). 13 16. Device according to claim 15, characterized in that as supply devices (18) swirl boxes are provided and have adjustable swirl flaps for the controlled supply of cooling gas (8). 17. Device according to claim 15 to 16, characterized in that there is a controlled system for the supply of fresh air (8) as cooling gas and the gas and product temperature downstream of classifier (6) is a controlled vari- able. 18. Device according to one of the claims 15 to 17, characterized in that there is an additional blower for the supply of fresh air (8). 19. Device according to one of the claims 15 to 18, characterized in that supply devices (19) for cooling water are located above the grinding pan. 20. Device according to one of the claims 15 to 19, characterized in that a controlled system for the inlet temperature of hot gas (4) in vertical mill (2) is provided and the highest moisture content of a raw material component is a controlled variable. 21. Device according to one of the claims 15 to 20, characterized in that a temperature measuring device (21) for the hot gas (4) is provided in feed line (14) upstream of vertical mill (2) and is connected to a hot gas generator (17) for temperature control purposes. 22. Device according to one of the claims 15 to 21, characterized in that the feed line (14) for hot gas (4) is connected to a return line (20) for the hot gas from the mill drying process and downstream of the mill fan (12) and/or with a hot gas supply from neighbouring processes, e.g. from a clinker cooler. 14 23. Device according to one of the claims 16 to 22, characterized in that the swirl flaps of the swirl boxes are adjustable for a tangential supply of cooling gas (8). The invention is particularly suitable for the cement industry and the grinding and simultaneous drying of cement clinker, slag and aggregates. In order to achieve a throughput increase and energy saving, as well as an improvement in the product quality, particularly with mixed cements, there is a simultaneous grinding and drying through a controlled supply of a cooling gas in the upper mill part with a relatively high hot gas inlet temperature in the lower mill part. The cooling gas supplies ensures a predetermined gas-product temperature downstream of the classifier and replaces or significantly reduces the disadvantageous cooling water injection.

Documents:

00680-kolnp-2008-abstract.pdf

00680-kolnp-2008-claims.pdf

00680-kolnp-2008-correspondence others.pdf

00680-kolnp-2008-description complete.pdf

00680-kolnp-2008-drawings.pdf

00680-kolnp-2008-form 1.pdf

00680-kolnp-2008-form 2.pdf

00680-kolnp-2008-form 3.pdf

00680-kolnp-2008-form 5.pdf

00680-kolnp-2008-international exm report.pdf

00680-kolnp-2008-international publication.pdf

00680-kolnp-2008-international search report.pdf

00680-kolnp-2008-pct priority document notification.pdf

00680-kolnp-2008-pct request form.pdf

680-KOLNP-2008-(14-05-2012)-CORRESPONDENCE.pdf

680-KOLNP-2008-(15-10-2013)-ABSTRACT.pdf

680-KOLNP-2008-(15-10-2013)-ANNEXURE TO FORM 3.pdf

680-KOLNP-2008-(15-10-2013)-CLAIMS.pdf

680-KOLNP-2008-(15-10-2013)-CORRESPONDENCE.pdf

680-KOLNP-2008-(15-10-2013)-DESCRIPTION (COMPLETE).pdf

680-KOLNP-2008-(15-10-2013)-DRAWINGS.pdf

680-KOLNP-2008-(15-10-2013)-FORM-1.pdf

680-KOLNP-2008-(15-10-2013)-FORM-2.pdf

680-KOLNP-2008-(15-10-2013)-OTHERS.pdf

680-KOLNP-2008-(15-10-2013)-PETITION UNDER RULE 137.pdf

680-KOLNP-2008-CORRESPONDENCE OTHERS 1.1.pdf

680-KOLNP-2008-CORRESPONDENCE OTHERS 1.2.pdf

680-KOLNP-2008-CORRESPONDENCE OTHERS-1.3.pdf

680-kolnp-2008-form 18.pdf

680-KOLNP-2008-INTERNATIONAL EXM REPORT-1.1.pdf

680-KOLNP-2008-OTHERS.pdf

680-KOLNP-2008-PRIORITY DOCUMENT.pdf

abstract-00680-kolnp-2008.jpg