Source: http://www.patentsencyclopedia.com/app/20100043675
Timestamp: 2020-07-09 07:46:00
Document Index: 332878674

Matched Legal Cases: ['art 3', 'art 5', 'art 3', 'art 5', 'art 5', 'art 5', 'art 5']

Method and Device for Grinding Hot, Wet Raw Material - Patent application
Patent application title: Method and Device for Grinding Hot, Wet Raw Material
Inventors: Willy Lohle (Neuss, DE) Hans Bonk (Muehlheim, DE) Franz-Josef Heuken (Moenchengladbach, DE)
IPC8 Class: AC04B2808FI
USPC Class: 106789
Class name: Coating or plastic compositions inorganic settable ingredient containing slag
Patent application number: 20100043675
Method and Device for Grinding Hot, Wet Raw Material - Patent application <?php require_once('/home/patents/php/mtc.config.php'); require_once('/home/patents/php/mtc.class.php'); $MTC = new MTC(); $MTC->init(); ?>
Inventors: Willy Lohle Hans Bonk Franz-Josef Heuken
The invention relates to a method and a device for grinding hot, wet raw material. 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.
24. 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) andin which with the aid of a cooling medium a predeterminable gas and product temperature downstream of a classifier (6) is maintained,whereinthe 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 andabove 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.
25. Method according to claim 24,wherein,relative to the total carrying gas quantity in the vertical mill (2), up to 30% cooling gas (8) is supplied to the upper mill part (5) of vertical mill (2).
26. Method according to claim 24,whereinfresh air is supplied as cooling gas (8).
27. Method according to claim 24,whereinat least partially cooled air is supplied as cooling gas (8).
28. Method according to claim 24,wherein≦95.degree. C. is preset as gas and product temperature downstream of classifier (6) and this maintained by a controlled supply of cooling gas (8).
29. Method according to claim 24,whereinvacuum is supplied to vertical mill (2), classifier (6) and a filter (11) and ambient air is sucked in as cooling gas (8).
30. Method according to claim 29,whereinthe vacuum is produced by a mill fan (12) with a necessary volume flow and which is connected downstream of filter (11).
31. Method according to claim 24,whereinhot gas (4) is supplied with an inlet temperature >180.degree. C., e.g. around 230.degree. C. to the vertical mill (2).
32. Method according to claim 24,whereinthe 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.
33. Method according to claim 24,whereinup to 70% of the volume flow in vertical mill (2) is supplied as hot gas (4).
34. Method according to claim 24,whereinthe total gas quantity of vertical mill (2) is controlled by measurement downstream of filter (11) and action on the mill fan (12).
35. Method according to claim 24,whereincooling gas (8) is introduced into the grinding area (7) with a swirling flow corresponding to the rising grinding material-gas mixture.
36. Method according to claim 24,whereinthe 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 rollers (16).
37. Method according to claim 24,whereinthe 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).
38. Device for performing the method according to claim 24, the device: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) andhaving at least one supply device (18) for a cooling medium with which it is possible to regulate a predeterminable gas and product temperature downstream of the classifier (6),whereinthe supply devices (18) are designed for a cooling gas (8) as cooling medium and proportionally carrying gas for the grinding material and are positioned upstream of classifier (6) in upper mill part (5) and between the grinding rollers (15) or between grinding rollers (15) and slave rollers (16).
39. Device according to claim 38,whereinas supply devices (18) swirl boxes are provided and have adjustable swirl flaps for the controlled supply of cooling gas (8).
40. Device according to claim 38,whereinthere 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 variable.
41. Device according to claim 38,whereinthere is an additional blower for the supply of fresh air (8).
42. Device according to claim 38,whereinsupply devices (19) for cooling water are located above the grinding pan.
43. Device according to claim 38,whereina 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.
44. Device according to claim 38,whereina 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.
45. Device according to claim 38,whereinthe 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.
46. Device according to claim 39,whereinthe swirl flaps of the swirl boxes are adjustable for a tangential supply of cooling gas (8).
[0001]This is a national stage of International application No. PCT/EP2006/007122 filed on Jul. 19, 2006 and published in German.
[0003]The invention relates to a method for grinding hot, wet raw material according and to a device for grinding hot, wet raw material.
[0004]The invention particularly applies to the cement industry for grinding and simultaneously drying raw materials, such as cement clinker, slag and aggregates.
[0006]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.
[0007]DE 198 36 323 C2 describes methods and plants for the production of cement using a vertical mill.
[0008]Besides the mill drying of raw powder in an air-swept roller mill, DE-AS 23 61 060 discloses cooling grinding of cement clinker in an air-swept roller mill downstream of a rotary tubular kiln.
[0009]U.S. Pat. No. 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 elements are located in the vicinity of the upper grinding area and upstream of the classifier 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.
[0010]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).
[0011]When grinding raw material, such as cement clinker, slag and aggregates, the raw material 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.
[0012]When grinding hot cement clinker in vertical mills with slag and wet aggregates the necessary 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 temperatures, particularly of the cement clinker or slag.
[0013]In order to achieve the desired gas and product temperature downstream of the classifier, 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 increased wear to the grinding parts, together with an increased energy demand at the mill motor.
[0014]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 optimum throughput capacity and energy saving and at the same time an improvement in the product quality, particularly in the case of mixed cements.
[0015]With respect to the method the object is achieved through the raw material components being fed to a vertical mill, ground and simultaneously dried with the aid of hot gas supplied via a nozzle ring to a lower mill part and a predeterminable gas and product temperature downstream of a classifier being maintained with the aid of a cooling medium, wherein the hot gas 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 a cooling gas is introduced into the vertical mill and admixed with the grinding material-gas mixture; and with respect to the device having a vertical mill, a classifier and a feed line for hot gas, which passes via a nozzle ring in the lower mill part into grinding area and having at least one supply device for a cooling medium with which it is possible to regulate a predeterminable gas and product temperature downstream of the classifier, wherein the supply devices are designed for a cooling gas as cooling medium and proportionally carrying gas for the grinding material and are positioned upstream of classifier in upper mill part and between the grinding rollers or between grinding rollers and slave rollers.
[0016]It is a fundamental idea of the inventive method to achieve a high grinding/drying efficiency, 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 power consumption of the mill, classifier and blower motors.
[0017]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. According 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.
[0018]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.
[0019]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 determined 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 ≦95° C.
[0020]By obviating cooling water injection or injecting only significantly reduced cooling water quantities, there is a heating energy economy and simultaneously an improvement to the product quality. In addition, there are process advantages for downstream plant equipment, such as bag filters and blowers.
[0021]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 cooling gas into the upper mill area.
[0022]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 temperature >180° C., e.g. approximately 230° C.
[0023]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.
[0024]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.
[0025]It is also advantageous to measure the hot gas inlet temperature upstream of the vertical mill and to regulate it by a hot gas generator and/or by a gas supply from neighbouring processes, e.g. from a clinker cooler, and/or by the return of waste gases downstream of the filter and mill fan.
[0026]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 predetermined gas and product temperature downstream of the classifier, the supply devices 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.
[0027]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.
[0028]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 blower for the cooling gas supply.
[0029]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.
[0030]Combined with said controlled system advantageously there is a second controlled system, which controls the hot gas quantity and temperature in the vertical mill. The controlled 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.
[0031]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.
[0032]The invention is described in greater detail hereinafter relative to embodiments and with reference to the attached highly diagrammatic drawings, wherein show:
[0033]FIG. 1 A plant diagram for a device according to the invention.
[0034]FIG. 2 A plan view of the grinding pan of an inventive vertical mill.
[0035]FIG. 3 A plan view of the grinding pan of an inventive 2+2 roller mill.
[0036]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 diagrammatic 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.
[0037]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.
[0038]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 predetermined gas and product temperature downstream of the classifier 6, the temperature and volume of the hot gas 4 are controlled.
[0039]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.
[0040]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.
[0041]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 classifier 6 can be sucked in. The cooling air 8 passes via supply devices 18, which are located in or on the mill housing 13 of the upper mill part 5, into the grinding area or chamber 7.
[0042]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.
[0043]In order in the case of particularly high raw material, e.g. cement clinker inlet temperatures 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 upper mill part 5.
[0044]FIG. 2 shows in highly diagrammatic form the arrangement of supply devices 18 for the cooling gas 8 in the upper mill part.
[0045]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).
[0046]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).
[0047]FIG. 3 shows in highly diagrammatic form a detail of a 2+2 roller mill, in which two grinding 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.
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