CN205550427U - Half whole grinding of cement grinds and ball -milling combination system immediately - Google Patents
Half whole grinding of cement grinds and ball -milling combination system immediately Download PDFInfo
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Abstract
本实用新型公开了一种水泥半终粉磨立磨,在现有立磨基础上,在立磨壳体上部由外向内分别设有静叶片一、静叶片二、转子、下料管,静叶片一和静叶片二由外向内分别固定在内部壳体上,静叶片一和静叶片二的下部分别接下料锥一和下料锥二,下料锥一的锥部接下料口,下料锥二的锥部接半成品出料口,下料管穿过下料锥二后与下料锥一相通,形成混料腔,转子包括一系列围绕下料管径向分布的动叶片,转子内的空间与出风口相通。本实用新型还公开了包含该立磨的联合系统。本实用新型可实现在立磨内多次分选,提高立磨的粉磨效率和选粉机的选粉效率,同时可控制半成品物料的细度,有利于提高水泥品质。
The utility model discloses a vertical mill for cement semi-final grinding. On the basis of the existing vertical mill, the upper part of the vertical mill housing is respectively provided with a static vane 1, a stationary vane 2, a rotor and a feeding pipe from the outside to the inside. Blade 1 and stator blade 2 are respectively fixed on the inner shell from outside to inside, the lower parts of stator blade 1 and stator blade 2 are respectively connected to feeding cone 1 and feeding cone 2, and the cone part of feeding cone 1 is connected to the feeding port. The cone part of the second feeding cone is connected to the outlet of the semi-finished product. The feeding pipe passes through the second feeding cone and communicates with the first feeding cone to form a mixing chamber. The rotor includes a series of movable blades distributed radially around the feeding pipe. The space in the rotor communicates with the air outlet. The utility model also discloses a combined system comprising the vertical mill. The utility model can realize multiple separations in the vertical mill, improve the grinding efficiency of the vertical mill and the powder selection efficiency of the powder separator, and can control the fineness of semi-finished materials at the same time, which is beneficial to improving the quality of cement.
Description
技术领域 technical field
本实用新型属于水泥粉磨技术领域,具体涉及一种水泥半终粉磨立磨及其与球磨的联合系统。 The utility model belongs to the technical field of cement grinding, in particular to a cement semi-final grinding vertical mill and a combined system with a ball mill.
背景技术 Background technique
目前水泥粉磨主要采用球磨或辊压机+球磨组成的不同粉磨系统。与球磨机相比,立磨具有粉磨效率高、电耗低(比球磨机节电20%~30%),烘干能力大,允许入磨物料粒度大,粉磨工艺流程简单,占地面积小,土建费用低,噪音低,磨损小,寿命长,操作容易等优点,已被广泛应用于粉磨水泥生料和煤粉,但用于生产水泥目前还没有得到普遍推广,主要原因一是立磨用于水泥终粉磨是否真正收到节能效果,二是立磨用于生产水泥可能会改变水泥特性,例如产品细度、颗粒级配、形貌等,从而使其不能达到国家标准要求。 At present, cement grinding mainly adopts different grinding systems consisting of ball mill or roller press + ball mill. Compared with ball mills, vertical mills have high grinding efficiency, low power consumption (20% to 30% power saving compared with ball mills), large drying capacity, large particle size of materials allowed to enter the mill, simple grinding process, and small footprint , low civil construction cost, low noise, low wear, long life, easy operation and other advantages, has been widely used in grinding cement raw materials and coal powder, but for the production of cement has not been widely promoted, the main reason is that Whether the final grinding of cement can really achieve energy-saving effect, and the second is that the use of vertical mills in the production of cement may change the characteristics of cement, such as product fineness, particle gradation, shape, etc., so that it cannot meet the requirements of national standards.
专利ZL201010191141.8公布了一种半终预粉磨立磨和球磨联合粉磨装置,将半终粉磨立磨与球磨结合在一起,物料首先由半终粉磨立磨系统进行半终粉磨,然后由带选粉机的闭路球磨系统进行终粉磨,该工艺能够发挥立磨和球磨的优势,使粉磨后的水泥颗粒形貌较好,粉磨效率提高,但是系统中的立磨若采用常规内循环立磨选粉机,由于需要通入大量热风,喷吹装置吹出的高速向上的气流不能太大,否则会将更多的粗粉随细粉吹入选粉机,从而使增大能耗。同时,如果粗粉和细粉在选粉机内不能进行有效分离,造成进入球磨机的粉料粒度不易控制,部分细粉在球磨机形成过粉磨。 Patent ZL201010191141.8 discloses a semi-final pre-grinding vertical mill and ball mill combined grinding device, which combines the semi-finish vertical mill and ball mill together, and the material is firstly semi-finally ground by the semi-finish vertical mill system , and then the final grinding is carried out by the closed-circuit ball mill system with a classifier. This process can give full play to the advantages of vertical mill and ball mill, so that the shape of cement particles after grinding is better and the grinding efficiency is improved. However, the vertical mill in the system If a conventional internal circulation vertical mill powder separator is used, since a large amount of hot air needs to be introduced, the high-speed upward airflow blown out by the blowing device should not be too large, otherwise more coarse powder will be blown into the powder separator along with the fine powder, thereby increasing the High energy consumption. At the same time, if the coarse powder and fine powder cannot be effectively separated in the powder classifier, the particle size of the powder entering the ball mill is difficult to control, and some fine powders are over-milled in the ball mill.
实用新型内容 Utility model content
本实用新型的目的在于克服现有立磨作为半终粉磨效率低、生产的半成品物料的细度不易控制的缺点,提高选粉机分离效率和水泥品质,提供一种半终粉磨的立磨。 The purpose of this utility model is to overcome the shortcomings of the existing vertical mill as a semi-finish grinding, which has low efficiency and the fineness of the semi-finished materials produced is difficult to control, improve the separation efficiency of the powder classifier and the quality of cement, and provide a semi-finish vertical grinding machine. grind.
本实用新型采用的技术方案为: The technical scheme that the utility model adopts is:
一种水泥半终粉磨立磨,包括减速机、喷吹装置、磨盘、磨盘衬板、磨辊、入料口、出风口,其特征在于,在立磨壳体上部由外向内分别设有位于同一轴心的静叶片一、静叶片二、转子、下料管,入料口位于下料管顶端,静叶片一和静叶片二由外向内分别固定在内部壳体上,静叶片一和静叶片二的下部分别接下料锥一和下料锥二,静叶片一及下料锥一与壳体之间的空间与排渣口相通,下料锥一的锥部接下料口,下料锥二的锥部接半成品出料口,下料管穿过下料锥二后与下料锥一相通,形成混料腔,转子围绕下料管设置,转子包括一系列径向分布的动叶片,转子内的空间与出风口相通。 A cement semi-final grinding vertical mill, comprising a reducer, an injection device, a grinding disc, a grinding disc liner, a grinding roller, a material inlet, and an air outlet. Stationary vane 1, stationary vane 2, rotor, and feeding pipe located on the same axis, the feeding port is located at the top of the feeding pipe, stationary vane 1 and stationary vane 2 are respectively fixed on the inner casing from outside to inside, stationary vane 1 and The lower part of the static vane 2 is respectively connected to the feeding cone 1 and the feeding cone 2. The space between the static blade 1, the feeding cone 1 and the shell is connected to the slag discharge port, and the cone part of the feeding cone 1 is connected to the feeding port. The cone part of the second feeding cone is connected to the outlet of the semi-finished product. The feeding pipe passes through the second feeding cone and communicates with the first feeding cone to form a mixing chamber. The rotor is arranged around the feeding pipe. The rotor includes a series of radially distributed Moving blades, the space in the rotor communicates with the air outlet.
优选地,静叶片的角度可调节;下料锥一的锥角小于下料锥的锥角。 Preferably, the angle of the stationary vanes can be adjusted; the cone angle of the feeding cone 1 is smaller than that of the feeding cone.
本实用新型还公开一种立磨球磨联合系统,所述系统包括如前所述的水泥半终粉磨立磨及球磨,其特征在于,所述水泥半终粉磨立磨的入料口接配料系统,排渣口通过皮带机接配料系统,以将排渣口排出的粗料与配料混合后送入立磨;水泥半终粉磨立磨的半成品出料口通过皮带机接球磨入料口,球磨出料口通过皮带机及提升机接选粉机,选粉机选出的成品细料经收尘器收集后送至成品库,选出的粗料与水泥半终粉磨立磨的半成品出料口排出的粗料混合后再送入球磨;水泥半终粉磨立磨的出风口通过管路接收尘器,细料经收尘器收集后进入成品库。 The utility model also discloses a combined vertical mill and ball mill system. The system includes the cement semi-finish grinding vertical mill and the ball mill described above. It is characterized in that the feed port of the cement semi-finish Batching system, the slag outlet is connected to the batching system through a belt machine, so that the coarse material discharged from the slag outlet is mixed with the ingredients and sent to the vertical mill; the semi-finished product outlet of the cement semi-finishing vertical mill is connected to the ball mill through a belt conveyor. The discharge port of the ball mill is connected to the powder classifier through the belt conveyor and the hoist. The finished fine material selected by the powder classifier is collected by the dust collector and sent to the finished product warehouse. The selected coarse material is mixed with the cement semi-final grinding vertical mill The coarse material discharged from the semi-finished product outlet is mixed and then sent to the ball mill; the air outlet of the cement semi-final grinding vertical mill receives the dust collector through the pipeline, and the fine material enters the finished product warehouse after being collected by the dust collector.
有益效果:本实用新型的半终粉磨立磨及包含该立磨的系统,在立磨内增设了利用静叶片和动叶片对粗细粉进行分离的装置,提高了立磨的粉磨效率和选粉机的选粉效率,同时可控制半成品物料的细度,有利于提高水泥品质。立磨内通过动叶片产生离心力,两级静叶片加动叶片逐级筛选,对不同粒度的粉末及颗粒进行分离,筛选成品,防止过粉磨,半成品送至球磨进一步处理,粗渣再进入配料系统。本实用新型的立磨及联合系统可以极大地提高水泥产品品质,提高粉磨和球磨效率,并且通过静叶片的调节,工艺容易控制。 Beneficial effects: the semi-final grinding vertical mill of the utility model and the system including the vertical mill add a device for separating coarse and fine powder by using the stationary vane and the moving vane in the vertical mill, which improves the grinding efficiency and efficiency of the vertical mill. The powder selection efficiency of the powder separator can control the fineness of semi-finished materials at the same time, which is conducive to improving the quality of cement. The centrifugal force is generated by the moving blades in the vertical mill, and the two-stage stationary blades plus the moving blades are screened step by step to separate the powder and particles of different sizes, and the finished products are screened to prevent over-grinding. The semi-finished products are sent to the ball mill for further processing, and the coarse slag enters the batching system. The vertical mill and the combined system of the utility model can greatly improve the quality of cement products, improve the efficiency of grinding and ball milling, and the process is easy to control through the adjustment of the stationary blades.
附图说明 Description of drawings
图1为立磨结构示意图; Fig. 1 is a schematic diagram of the vertical mill structure;
图2为图1中所示的I-I部位的剖面图; Fig. 2 is a sectional view of the II portion shown in Fig. 1;
图3为本实用新型系统的结构示意图。 Fig. 3 is a structural schematic diagram of the utility model system.
在图中,1、减速机;2、喷吹装置;3、磨盘;4、磨盘衬板;5、磨辊;6、下料锥一;7、下料锥二;8、下料管;9、静叶片一;10、静叶片二;11、转子;12、入料口;13、出风口;14、混料腔;15、下料口;16、半成品出料口;17、排渣口;18、动叶片。 In the figure, 1. Reducer; 2. Injection device; 3. Grinding disc; 4. Grinding disc lining; 5. Grinding roller; 9. Static vane 1; 10. Static vane 2; 11. Rotor; 12. Material inlet; 13. Air outlet; 14. Mixing cavity; Mouth; 18, moving blade.
图1中箭头所示分别代表:x1、粉料1;x2、粉料2;x3、粉料3;c1、粗料1;c2、粗料2;c3、粗料3。 The arrows in Figure 1 represent: x1, powder 1; x2, powder 2; x3, powder 3; c1, coarse material 1; c2, coarse material 2; c3, coarse material 3.
具体实施方式 detailed description
为克服现有技术的若干缺点,提高立磨的粉磨效率和选粉机的选粉效率,同时可控制半成品物料的细度,本实用新型提出了一种半终粉磨立磨,可实现在立磨内多次分选,有利于提高水泥品质。 In order to overcome several shortcomings of the prior art, improve the grinding efficiency of the vertical mill and the powder selection efficiency of the powder separator, and control the fineness of semi-finished materials at the same time, the utility model proposes a semi-final grinding vertical mill, which can realize Multiple sorting in the vertical mill is beneficial to improve the quality of cement.
本实用新型采用的技术方案为:在现有水泥立磨基础上,进一步增设粗细粉分离装置。所述的半终粉磨立磨结构主要包括:磨辊、磨盘、磨盘衬板、喷吹装置、减速机、入料口、出风口、半成品出料口、排渣口、下料锥一、下料锥二、下料管、静叶片一、静叶片二、转子。作为本实用新型半终粉磨立磨的选粉分离装置,在壳体内由外向内分别设有同心的静叶片一、静叶片二、转子、下料管。其中所述的静叶片一和静叶片二的一端分别固定在选粉机壳体上,另一端分别与下料锥一、下料锥二连接。所述的下料锥一的锥部连接下料口。所述的下料锥二位于下料锥一的内部,锥部设有半成品出料管,半成品出料管沿着下料锥二的锥线引出,以防止粉料堆积,且下料锥二的锥部夹角大于下料锥一的锥部夹角,连接下料口。所述的下料管穿过下料锥二后与下料锥一相通。 The technical scheme adopted by the utility model is: on the basis of the existing cement vertical mill, a coarse and fine powder separation device is further added. The semi-finishing vertical mill structure mainly includes: grinding rollers, grinding discs, grinding disc liners, blowing devices, reducers, material inlets, air outlets, semi-finished product outlets, slag discharge ports, and feeding cones. Feed cone 2, feed pipe, stationary vane 1, stationary vane 2, rotor. As the powder selection and separation device of the semi-final grinding vertical mill of the utility model, concentric stationary vane 1, stationary vane 2, rotor, and feeding pipe are respectively arranged in the housing from outside to inside. One end of the stationary vane 1 and the stationary vane 2 are respectively fixed on the shell of the powder separator, and the other ends are respectively connected with the first feeding cone and the second feeding cone. The tapered portion of the first feeding cone is connected to the feeding port. The second feeding cone is located inside the first feeding cone, the cone is provided with a semi-finished discharge pipe, and the semi-finished discharge pipe is drawn out along the cone line of the second feeding cone to prevent powder accumulation, and the second feeding cone The included angle of the cone portion of the feed cone is greater than that of the feed cone one, and is connected to the discharge port. The feeding pipe communicates with the feeding cone 1 after passing through the feeding cone 2.
立磨的喷嘴装置高速向上的热气流对磨辊粉碎的物料进行第一次分选,分选后的粉料被上升气流带至立磨上部的选粉机内,大颗粒物料从下端的排渣口排出。 The high-speed upward hot air flow from the nozzle device of the vertical mill performs the first separation on the materials crushed by the grinding rollers. The slag is discharged.
第一次分选后的粉料与空气的混合物在进入选粉机后由垂直上升变为切向流动,在静叶片一、静叶片二、转子叶片之间的范围内,由转子旋转形成的离心力将粉料和空气混合物进行多次分选。经过静叶片一的大颗粒物料被向外抛出并在重力作用下下沉,离开离心力范围后,落入下料锥一,并经下料口进入立磨;细粉经静叶片二后,进入静叶片与转子间的空间再次进行分选,分选下来的粗粉通过下料锥二的半成品出料口排出,合格成品从选粉机上部的出风口排出。 After the first sorting, the mixture of powder and air changes from vertical rise to tangential flow after entering the powder classifier. In the range between the first stator blade, the second stator blade and the rotor blade, the flow formed by the rotation of the rotor The centrifugal force separates the mixture of powder and air several times. The large-grained material passing through the static vane 1 is thrown out and sinks under the action of gravity. After leaving the range of centrifugal force, it falls into the feeding cone 1 and enters the vertical mill through the feeding port; after the fine powder passes through the stationary vane 2, Enter the space between the stationary vane and the rotor to be sorted again, the sorted coarse powder is discharged through the semi-finished product outlet of the second feeding cone, and the qualified finished product is discharged from the air outlet on the upper part of the powder separator.
在由转子旋转形成的离心力作用下先后经过静叶片一、静叶片二、转子,将粉料和空气混合物分别进行第二次、第三次、第四次分选。由静叶片一的分选后的大颗粒物料落入立磨,另一部分物料进入静叶片二进行第三次分选;第三次分选后的粗料通过下料锥一的下料口进入立磨,另一部分物料进入转子进行第四次分选;第四次分选后的半成品物料通过下料锥二的半成品出料口排出,合格成品从选粉机上部的出风口排出。 Under the action of the centrifugal force formed by the rotation of the rotor, the powder and air mixture are separated for the second, third and fourth times through the stator blade 1, the stator blade 2 and the rotor successively. The large particle material after sorting by the static blade 1 falls into the vertical mill, and another part of the material enters the static blade 2 for the third separation; the coarse material after the third separation enters through the discharge port of the discharge cone 1 In the vertical mill, another part of the material enters the rotor for the fourth sorting; the semi-finished material after the fourth sorting is discharged through the semi-finished product outlet of the feeding cone 2, and the qualified finished product is discharged from the air outlet on the upper part of the powder separator.
参见附图1,本实用新型的半终粉磨立磨主要包括:磨辊5、磨盘3、磨盘衬板4、喷吹装置2、减速机1、入料口12、出风口13、半成品出料口16、排渣口17、下料锥一6、下料锥二7、下料管8、静叶片一9、静叶片二10、转子11,转子11包含一系列径向设置的动叶片18。 Referring to accompanying drawing 1, the semi-final grinding vertical mill of the present utility model mainly comprises: grinding roller 5, grinding disc 3, grinding disc liner 4, blowing device 2, reducer 1, material inlet 12, air outlet 13, semi-finished product outlet Material port 16, slag discharge port 17, feeding cone 1 6, feeding cone 2 7, feeding pipe 8, stationary vane 1 9, stationary vane 2 10, rotor 11, and rotor 11 includes a series of radially arranged moving vanes 18.
所述的立磨工作时电动机通过减速机1带动磨盘3转动,物料通过入料口12经下料管8落到磨盘衬板4中央,在离心力的作用下物料向磨盘3边缘移动并受到磨辊5的碾压,粉碎后的物料从磨盘3边缘溢出,被来自喷嘴装置2高速向上的热气流带起烘干,进行第一次分选,分选后的粉料x1被上升气流带至立磨上部的选粉分离装置内,粗料c1从下端的排渣口17排出,经外循环的斗提机从喂料口重新喂入磨内再次粉磨。 When the vertical mill is working, the motor drives the millstone 3 to rotate through the reducer 1, and the material falls to the center of the millstone liner 4 through the feeding port 12 through the feeding pipe 8, and the material moves to the edge of the millstone 3 under the action of centrifugal force and is ground. Roller 5 crushes, the pulverized material overflows from the edge of the grinding disc 3, is taken up and dried by the high-speed upward hot air flow from the nozzle device 2, and performs the first sorting, and the sorted powder x1 is brought to the In the powder selection and separation device on the upper part of the vertical mill, the coarse material c1 is discharged from the slag outlet 17 at the lower end, and fed into the mill again through the bucket elevator through the external circulation from the feeding port for grinding again.
第一次分选后的粉料与空气的混合物在进入选粉机后由垂直上升变为切向流动。在静叶片一9、静叶片二10和转子11之间的范围内,由转子11旋转形成的离心力将粉料x1和空气混合物在静叶片一9的和静叶片二10形成的通道内进行第二次分选;第二次分选下来的粗料c2落入下料锥一6、下料锥二7与下料管8形成的混料腔14内,再经下料口15返回到磨盘衬板4上,重新粉磨。第二次分选后的粉料x2被气流带至静叶片二10和转子11形成的通道内进行第三次分选;第三次分选出来的粗料c3从下料锥7的半成品出口16排出,第三次分选出来细粉x3随气流向上从选粉机上端的出风口13出磨,在系统的收尘装置中收集下来,即为合格产品。 The mixture of powder and air after the first sorting changes from vertical rise to tangential flow after entering the powder classifier. In the range between the first vane 9, the second vane 10 and the rotor 11, the centrifugal force formed by the rotation of the rotor 11 moves the mixture of powder x1 and air in the passage formed by the first vane 9 and the second vane 10 Secondary sorting; the coarse material c2 from the second sorting falls into the mixing cavity 14 formed by the first feeding cone 6, the second feeding cone 7 and the feeding pipe 8, and then returns to the grinding table through the feeding port 15 On the liner 4, grind again. The powder x2 after the second sorting is brought by the airflow to the channel formed by the second vane 10 and the rotor 11 for the third sorting; the coarse material c3 that is sorted out for the third time is exported from the semi-finished product of the feeding cone 7 16, and the fine powder x3 from the third sorting is discharged from the air outlet 13 on the upper end of the powder classifier with the air flow upward, and collected in the dust collection device of the system, it is a qualified product.
再参见附图2,示出了静叶片和转子的结构。转子11包含一系列围绕下料管8径向设置的动叶片18,转子内部的空间连接出风口13。转子旋转产生离心力,静叶片一9和静叶片二10的角度可调,从而可以实现分离的粒度调节,提高水泥品质。 Referring to accompanying drawing 2 again, the structure of stator blade and rotor is shown. The rotor 11 includes a series of moving blades 18 arranged radially around the feeding tube 8 , and the space inside the rotor is connected to the air outlet 13 . The rotation of the rotor generates centrifugal force, and the angles of the first stationary vane 9 and the second stationary vane 10 can be adjusted, so that the separated granularity can be adjusted and the quality of cement can be improved.
附图3示出了包含本实用新型的半终粉磨立磨的系统。如图所示,配料系统将原料通过提升机送至立磨入料口,原料在立磨内研磨分离后,产生粗料c1、粗料c2、粗料c3及粉料x3,粗料c1从立磨排渣口排出再经过皮带机送至配料系统混合后送至立磨入料口。粗料c2沿下料锥一进入混料腔,与入料口下来的配料一起再进入立磨。进一步经过转子和静叶片二分离出来的粗料c3沿下料锥二从半成品出料口排出,经过皮带机送至球磨。经过转子分离后产生的粉料x3通过立磨出风口送至收尘器收集后送至成品库。球磨的出料通过皮带机及提升机送至选粉机,选粉机选出的成品细料经收尘器收集后送至成品库,选出的粗料与水泥半终粉磨立磨的半成品出料口排出的粗料c3混合后再送入球磨。 Accompanying drawing 3 has shown the system that comprises the semi-finish grinding vertical mill of the utility model. As shown in the figure, the batching system sends the raw materials to the feed inlet of the vertical mill through the elevator. After the raw materials are ground and separated in the vertical mill, coarse material c1, coarse material c2, coarse material c3 and powder x3 are produced. Coarse material c1 is obtained from The slag discharge port of the vertical mill is discharged, and then sent to the batching system through the belt conveyor for mixing, and then sent to the material inlet of the vertical mill. Coarse material c2 enters the mixing chamber along the feeding cone, and then enters the vertical mill together with the ingredients coming down from the feeding port. The coarse material c3 separated from the rotor and the stationary blade 2 is discharged from the semi-finished product outlet along the feeding cone 2, and sent to the ball mill through a belt conveyor. The powder x3 produced after rotor separation is sent to the dust collector through the air outlet of the vertical mill and then sent to the finished product warehouse. The output of the ball mill is sent to the powder separator through the belt conveyor and the hoist. The finished fine material selected by the powder separator is collected by the dust collector and then sent to the finished product warehouse. The coarse material c3 discharged from the semi-finished product outlet is mixed and then sent to the ball mill.
借助于本实用新型的立磨球磨联合系统,物料充分分离,粒度容易受到控制,防止过粉磨的产生。适当粒度的不同物料作不同处理,产品品质和生产效率得到提高。 By means of the combined vertical mill and ball mill system of the utility model, the materials are fully separated, the particle size is easily controlled, and the occurrence of over-grinding is prevented. Different materials with appropriate particle size are treated differently, and product quality and production efficiency are improved.
上面结合附图对本实用新型的实施方式作了详细的说明,但是本实用新型不限于上述实施方式,在所属技术领域普通技术人员所具备的知识范围内,还可以在不脱离本实用新型宗旨的前提下做出各种变化。 The embodiments of the present utility model have been described in detail above in conjunction with the accompanying drawings, but the present utility model is not limited to the above-mentioned embodiments. Various changes are made.
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| CN201620269246.3U CN205550427U (en) | 2016-04-05 | 2016-04-05 | Half whole grinding of cement grinds and ball -milling combination system immediately |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105709883A (en) * | 2016-04-05 | 2016-06-29 | 江苏羚羊水泥工程技术有限公司 | Cement semi-final powder milling vertical milling and ball milling combination system |
| CN107350058A (en) * | 2017-07-06 | 2017-11-17 | 浙江农林大学 | A kind of disintegrating apparatus of high microsteping biological material |
| CN108339656A (en) * | 2018-02-23 | 2018-07-31 | 烟台龙源电力技术股份有限公司 | A kind of coal-burning boiler pulverized coal preparation system and its dynamic separator |
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2016
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105709883A (en) * | 2016-04-05 | 2016-06-29 | 江苏羚羊水泥工程技术有限公司 | Cement semi-final powder milling vertical milling and ball milling combination system |
| CN107350058A (en) * | 2017-07-06 | 2017-11-17 | 浙江农林大学 | A kind of disintegrating apparatus of high microsteping biological material |
| CN108339656A (en) * | 2018-02-23 | 2018-07-31 | 烟台龙源电力技术股份有限公司 | A kind of coal-burning boiler pulverized coal preparation system and its dynamic separator |
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