OPERATING EXPERIENCE OF VERTICAL ROLLER MILL FOR SLAG GRINDING
Dr. Heinz Ulrich Schaefer
 
 
 
SUMMARY  

Vertical roller mills are very well introduced for grinding and drying of raw materials for cement production all over the world. 
  
The high reliability and the perfect operational availability of the vertical roller mill leaves no alternative presently. Therefore it was a consequent step to develop this system further for the application in grinding plants for clinker, slag, pozzolana and other materials used for cement production nowadays.   
 
By introducing the vertical roller mill of the LM ... 2+2 C/S design into the market a most reliable mill has been offered to cement producers. The newly designed mill uses the well proven components of roller mills for raw materials, but the installation of different sized master and slave rollers allows the mill to grind such fine products like cements and slag. The material bed on the grinding table is stabilized perfectly without using additives like limestone or spraying of water into the mill.  
  
Low energy consumption, low costs for civil construction and low maintenance costs due to the simplicity of the system makes the LM ... 2+2 C/S an ideal tool in the cement industry. Perfect cement quality comparable to other grinding systems and very good quality of concrete produced with the cement made in the vertical roller mill emphasizes, that the system meets the requirements of the cement industry.   
 

INTRODUCTION  

Many efforts have been made throughout the last years to improve the efficiency of clinker grinding systems. High efficiency separators have been developed in order reduce the circulation load in the grinding system. Roller presses are used in various set - ups together with ball mills for decreasing the energy consumption.  
  
Roller press systems in connection with high efficiency separators without ball mills have been installed for cement production. However many of those solutions did not reach their aim either in respect of their reliability and operational availability or in respect of the quality requirements of the product.   
 
During the last years intensive research and developments were made for the application of vertical roller mills for grinding of clinker, slag and related materials. Besides the consideration of mechanical problems due to the hardness and the abrasive properties of those materials the quality aspect had to be kept seriously in mind.  
  
No change in quality of the product was allowed when comparing it with conventional grinding systems. The result of these efforts was the development of  2+2 C/S design of the Loesche mill for cement and slag grinding.  
 

DESIGN FEATURES OF MILL TYPE LM .. 2+2 C/S  

Basically the well proven components of the vertical roller mills for raw materials and coal have been used. The physical properties of clinker and slag however and the high fineness compared to raw meal or coal dust required a new design in order to stabilize the relatively thin material bed on the grinding table and in order to run the mill smoothly without vibrations.   
 
The 2+2 system provided the most favourable solution for this application. Two different sized sets of rollers are installed (picture no. 1). 
  

  
  
One set of rollers of small diameter - the so-called slave rollers - is used for perparation of the material bed. These slave rollers are of a light steel sheet design. By means of a hydraulic system their position above the grinding table is kept on a certain level. No pressure is applied on the slave rollers themselves, except the counterpressure of the material passing underneath the rollers. The slave rollers smoothen the surface of the material bed on the grinding table and they consolidate it and deaerate it slightly. After the material bed has been prepared in such manner it is easily nipped by the large sized master rollers.  
  
The master rollers are of heavy design. Their tires are casted from high wear resistant alloys. A hydraulic system is used for creating high pressure on the material bed to be ground. A hydro-pneumatic spring system provides uniform loading. The 2+2-system is applicable up to capacities of 140 - 150 t/h cement. For higher capacities, which might exceed 200 t/h the same principle as above is used but the two sets of different sized rollers consist of 3 slave and 3 master roller each.  
 
A high efficiency separator is incorporated in the upper part of the mill housing. Mass related surfaces of cement or ground granulated blast furnace slag between 2800 cm²/g and more than 4500 cm²/g can be achieved. Particle size distributions with slopes between 0,8 and 1,2 according to the RRSB - grit are common.  

Besides the above highlighted features many aspects for easy operation and low maintenance have been considered, like wear protection in the housing, provisions to avoid metal to metal contact  between grinding table and rollers and the hydraulic swing - out device.   
 

GRINDING PLANTS WITH LM .. 2+2 C/S TYPE MILLS  

Grinding plants with this new generation of cement mills are of very simple design. The matrial is fed by means of weigh feeders into the mill. A hydraulically operated feed gate is used for preventing the intrusion of false air into the system.  
  
The material is dried and ground  and after it is discharged from the grinding table it is lifted by the process air flow  to the classifier where grits and product are separated. The product leaves the mill with the air flow and is collected in a jet pulse filter. Depending on the heat requirements in the system the air can be recirculated back to the mill or it can be discarded through the stack. In case of high heat demands due to drying operation, e.g. in cases of  slag or pozzolana grinding, a hot gas generator might be used as heat source , if no other sources like cooler waste gases or similar are available. In case of clinker grinding the hot gas generator will be used for start-up only. Verse vice the system can be operated with ambient air in case of excessive clinker temperatures and cement cooling can be done in the grinding circuit.  
  
Coarse particles which leave the grinding table and fall down through the nozzle ring are collected in the lower part of the mill and conveyed to the mill feeder by means of an external recirculation system (picture no. 2). 
  

 
 
  
  
This system is used as well for the extraction of metallic iron in case of slag grinding.  
  
Picture no. 3 shows the general arrangement for a grinding plant with a LM ...2+2 C/S mill. 
 
  
The building structure can be of a very simple design. The mill is relocated on the ground. Only the jet pulse filter needs the support of a steel structure. The fan is located on ground level as well. It is working downstream of the filter in a clean air enviroment.  
  
The whole grinding system is completely closed, as the transport of material takes place inside the ductwork. No open transfer points, conveyors or elevators are required except for the feeding system. Therefore the whole plant can be kept open without any building except for the small tower which accomodates the feed system. Costs for civil construction are considerably low for this reason.  
 
QUALITY OF CEMENT PRODUCED IN A LM .. 2+2 C MILL  

Experience with other sophisticated grinding systems showed in the past, that the cement quality changed compared to existing ball mill systems. Therefore this matter has been studied in all details.  
  
In December 1994 the first LM 46 2+2 C world wide for cement production has been started up.  During the first months of operation clinker from various sources has been imported for cement production in this plant. From the day of start  - up no problems on the cement quality have been encountered. Later on the clinker came from a cement plant in which two ball mills grind this clinker type as well, which provided a perfect chance for a direct comparison of the quality of the products of both systems.  
  
However 4 -5 % of blast furnace slag were added into the vertical roller mill at the time of sampling.-The particle size distributions of both samples have been determined by means of a CILAS 850 lasergranulometer using alcohol as dispersive agent. The characteristic parameters of the particle size distriubutions in the RRSB grit are :  
  

  LM 46.2+2 C Ball Mill
slope 0,86 0,96
position parameter 17,3 µm 15,3 µm
  
The slope of the cement ground in the Loesche mill is much lower compared to the slope of the cement produced in the ball mill system (picture no. 4).  
 
 
 
  
This is more favourable in respect to the water demand of the cement. Compared to other cements with such a slope the position parameter (63,2 % by mass passing) is slightly low however.  
  
The mass related surface area has been determined according to BLAINE:  
 
  LM 46.2+2 C Ball Mill
surface area 3.320 cm²/g 3.580 cm²/g
 
 
The relatively low position parameters in respect of the mass related surface areas are required under the consideration that both cements are cements of high early strength according to the local requirements.   
 
The chemical composition of the cement samples used for comparison is listed in table no. 1.   
 
It is obvious that both cements are made out of the same type of clinker. The slight differences originate from the addition of blast furnace slag.  
 
 
sample
LM 46.2+2 C
Ball Mill
sample no.
1
2
lab no.
96/068
96/069
Loi
1,50
1,40
SiO2
20,90
20,20
Al2O3
5,20
4,80
Fe2O3
3,60
3,60
TiO2
0,60
0,50
CaO
61,70
63,10
CaO, free
n.d.
1,70
MgO
3,40
2,80
SO3
2,30
2,20
K2O
0,50
0,60
Na2O
0,40
0,40
Na-Eq.
0,73
0,79
Summ.
100,10
99,60
 
Table No.1: Chemical analyses of cement samples
 
The physical properties of both cement samples have been tested according to DIN EN 196 part 1 and part 3. Regarding the water demand and the setting time the following results have been obtained:  
  
 
LM 46.2+2 C
Ball Mill
water demand
27,0 %
29,0 %
initial setting
120 min.
180 min.
final setting
180 min.
210 min.
  
The lower water demand of the cement produced in the vertical roller mill can be related to the lower slope value compared to the cement produced in the ball mill. The setting times of both tested cements are within the usual range. The development of strength of both cements has been determined on mortar specimens according to the above mentioned standards. The development of compressive strength of both tested cements is fairly good (picture no. 5).  
 
  
  
The early strength of the cement produced in the vertical roller mill is slightly less compared to the ball mill cement, but it must be kept in mind that the first one contains 4 - 5 % by mass of granulated blast furnace slag and that the particle size distribution shows a lower slope and that the cement has a lower mass related surface area. The relatively great difference in the 7 days strength of both cements is most probably related to the addition of slag. After 28 days the compressive strength of both cements is on the same level.   
 
Both cements meet the requirements of a high early strength cement class CEM I 42,5 R according to DIN EN 197.  
 
QUALITY OF CONCRETE PRODUCED WITH A CEMENT GROUND IN A LM 46.2+2C  

In order to investigate in the influence of the cement properties on the properties of concrete produced of the cements ground in different grinding systems a series of concrete batches have been prepared. Special attention has been drawn on the workability of the concrete and the possibility of unfavourable early setting of the concrete. For the preparation of the concrete batches aggregates of particle size distribution curve A/B32 have been use (picture no.6).  
 

Picture No. 6: Particle size distribution of aggregates
 
The general aim was to use a cement quantity of 300 kg/m³ concrete and to achieve a slump of approx. 48 cm. Alltogether 4 concrete batches have been prepared, each of about 25 l.  
 
The concrete batches have been mixed for 120 s and after that the slump has been determined according to DIN 1048 after 3 minutes, after 30 minutes and after 60 minutes. After the last slump test each concrete batch was taken back into the mixer and after mixing the slump has been determined again (marked as" ## 60 min "). Picture no. 7 shows the results. 
  
  
  
  
  
Concerning early setting a difference in slump of 3 ± 2 cm after 30 minutes (refered to the result after 3 minutes ) and of 5 ± 2 cm after 60 minutes ( refered to the result after 3 minutes ) can be considered as normal.  
 
In this particular case the concrete made of cement ground in the ball mill shows a significantly higher trend for early setting than the concrete made with cement produced in the vertical roller mill. This phenomenon has been encoutered in many of similar tests before.  
 
Finally water was added to one of each batches of concrete until the original slump value has been obtained. After the slump tests specimens for the determination of compressive strength have been prepared from the concrete batches LM 1, LM 2, BM 1 and BM 2. The actual compositions of the concrete specimens is shown in  table no. 2. 
 
 
concrete LM 1 LM 2 BM 1 BM 2
cement [kg/m³] 305 302 304 302
water [kg/m³] 168 178 168 179
aggregates [kg/m³] 1.927 1.908 1.921 1.911
concrete density [kg/m³] 2.400 2.388 2.393 2.392
water/cement ratio 0,551 0,591 0,551 0,591
 
Table No. 2: Composition of concrete specimens
used for comprehensive strength testing
 
The results of the tests of compressive strength of the concrete specimens is shown in picture no. 8. The results resemble clearly what could be expected from the tests described before.  
  
The strength development after 7 days of the concrete made with cement ground in the vertical roller mill is slightly less compared to the concrete made with the ball mill  cement. The reason for that is the addition of blast furnace slag into the cement ground in the LM 46 2+2 C, the lower mass related surface area  and the less steep particle size distribution.  
  
The results obtained after 28 days however show clearly that the concretes made out of cements of the same clinker but have been produced in different grinding systems reach easily the same level of compressive strength.  
 
 
 
ENERGY CONSUMPTION OF DIFFERENT GRINDING SYSTEMS  

The comparison of the specific energy consumptions between the vertical roller mill and the ball mill system has been carried out for this particular case. For the energy consumption figures of the ball mill system two cases can be shown, as this particular ball mil can be operated with a roller press as a pregrinder if required.   
 
The result is shown in table no. 3. The table is self - explanatory.  
  

CONCLUSION  

Grinding plants with LOESCHE mills of the new LM ... 2+2 C/S generation provide cement producers with grinding systems, which offer perfect cement quality, a wide range of flexibility and which are very energy efficient systems.  
  
The combination of grinding and of a perfect drying capability of this type of mill makes it suitable to grind all kinds of cements, such as cements with granulated blast furnace slag, pozzolana cements, fly ash cements and other blended cements.  
  
The possibility to switch within less than one hour from one type of product to the other is a unique feature of this grinding technology.