- •1 Level (6 points)
- •History of the need for building materials
- •Cement production in the Republic of Kazakhstan
- •The history of obtaining and production cement
- •Economics of cement production
- •Determination of clinker, cement and additives introduced in the grinding
- •The composition of the raw meal. Equations 1-4
- •The composition of the raw meal. Equations 5-9
- •Portland cement clinker.
- •An overview of phase composition and quality phase of clinker
- •Chemical and mineralogical composition alite
- •Chemical and mineralogical composition of belite
- •Phase aluminate
- •Phase Ferrite
- •Other clinker phases
- •The composition and place of origin of the phases in portland cement clinker
- •Analysis of the raw meal, cement and clinker
- •Microscopic research of clinker
- •Recent developments in the use of X-rays
- •Petrographic analysis of clinker
- •Cement production
- •Raw materials and fuels in cement production
- •The raw materials of cement industry
- •Limestone and clay
- •A natural mixture of clay and limestone
- •Waste and their use in the cement industry
- •2 Level (6 points)
- •Mining, processing of raw materials, grinding of raw meal and homogenisation.
- •The blending warehouse of raw materials and its functions.
- •Development of the pile by rotary excavator
- •The process of burning cement clinker. General concepts
- •Chemical reactions during heat treatment of portland cement raw meal (main reaction clinker burning)
- •The dehydration of kaolinite
- •The reactions during the sintering
- •Reaction with cooling
- •Homogeneity of the raw meal
- •The process of burning cement clinker
- •Procedures for burning cement clinker
- •Decarbonizators with upward vertical gas flue.
- •The fuel in cement production
- •Clinker cooler
- •Cooler sf (Smidth-Fuller).
- •Storage of clinker
- •Cement Grinding
- •Milling equipment
- •The fineness of grinding and particle size distribution (grain) composition of the cement
- •Storage, packing, shipment cement to the consumer
- •The granulated blast furnace slag (s)
- •Pozzolan (p, q)
- •Natural pozzolanic additives (р)
- •Natural volcanic pozzolanic additives (q)
- •3 Level (8 points)
- •Fly ash rich in silica (V)
- •Lime ash dust (w)
- •Calcined shale (t)
- •Limestone (l, ll)
- •The quartz dust (d)
- •Small components
- •Calcium sulphate
- •The cement admixture
- •Cement according to standard
- •Physical and chemical properties of cements according to European standard
- •Cements with special properties
- •Well cement
- •Hydration
- •The reaction of silicates (c3s, c2s)
- •Hydration c3s
- •Hydration c2s
- •Reactions of hydration aluminate without participation of sulfates
- •Reactions hydration aluminate with participation sulphates
- •Hydration ferrite (c4af)
- •Taylor Model
- •Model Stark
- •The cement hydration
- •Reaction of the secondary components
- •Hydration of cement containing granulated slag
- •Reactions pozzolanic materials
- •4 Level (8 points)
- •Slowing solidification
- •Structure of a cement stone
- •Building lime
- •The historical and economic situation. Raw material deposits
- •Production and processing of limestone
- •Burning lime
- •Shaft kiln to coke (coal) and gas fuel
- •The rotary tube kiln
- •Counter current regenerative kiln (ggr-kiln)
- •Shaft ring kiln
- •Grinding and shipment of burnt lime
- •Slaked lime
- •The use of lime products
- •The requirements of stst 9179-79 to building lime
- •Gypsum. History and economy
- •Physical and chemical bases of gypsum binders
- •Phases in the system CaSo4 - h2o
- •The crystal structures, double salts, mixed crystals
- •Natural gypsum, natural anhydrite
- •The chemical gypsum
- •Uddg- gypsum
- •Production of calcium sulphate binders
- •Technological processes in the production of calcium sulphate binders
- •Autoclave method for producing α-hemihydrate
- •Gypsum boiling kettle for the production of ß-hemihydrate
- •5 Level (12 points)
- •The high temperature burning of gypsum method (multiphase gypsum) on the grate
- •Properties capable of hardening calcium sulphates
- •Hydration CaSo4-binding
- •Natural -, uusdg - and chemical anhydrite
- •The properties of the treated gypsum building materials
- •Other areas of application
- •The norms, chemical analysis and phase analysis
- •Gypsum Products
- •The requirements of gost 125-79 for the quality of construction gypsum
- •Other inorganic binding materials
- •Alumina cement
- •Production of alumina cement
- •Chemical and mineralogical composition of the alumina cement
- •Areas of use alumina cement
- •Softeners (plasticizers), added during the production concrete
- •Softeners (plasticizers), added to the concrete mix
- •Concrete
- •Mobile concrete plants
- •Concrete for precast concrete elements
- •Self-compacting concrete
- •Building mortar
- •Cement mortar
- •Plaster
- •Cementing deep wells
Reaction with cooling
An important process is the preparation of cement clinker it is cooled. From the rotary kiln clinker cooling zone out at a temperature of 1100 ... 1300 0C. Final cooling is carried out in its refrigerators.
Cooling the clinker has a significant effect on the structure, the mineralogical composition, grindability and thus the quality of the cement produced from it.
Primarily clinker cooling rate affects the ratio of crystalline and glassy phases. Slow cooling crystallization occurs, and with rapid - it slows down the formation of crystals and substantial portion of the melt solidifies in the form of clinker glass. The proportion of clinker melt in the rotary kiln is 20 ... 25%.
The rate of cooling affects the consistency of clinker cement volume change. Rapid cooling becomes large amounts of MgO in the glassy phase remain a microcrystalline state (grain size up to 5 ... 8 m). On slow cooling crystals of MgO increase in size, up to 30 ... 150 microns, which causes uneven changes in the volume of cement hardening. With a sharp firing and rapid cooling of the clinker formed small crystals alite, which increases the strength of the cement stone.
clinker cooling process also causes the chemical resistance of cement. Rapid cooling of the clinker increases cement sulphate. This is because C3A determining resistance clinker towards sulfate aggression by rapid cooling generally proceeds in a glassy form and becomes less sensitive to the effects against sulfates.
Grindability clinker depends on many factors, including the and the cooling rate. Comparison of grindability data quickly and slowly cooled clinker indicate that the clinker is cooled (slowly) in a drum cooler, requires higher energy consumption for grinding than clinker is cooled (fast) in a grate cooler. A higher content of the glassy phase and the small size of the crystals of clinker minerals grindability increases rapidly cooled clinker compared with cooled slowly. These data demonstrate the need for rapid cooling clinker.
Homogeneity of the raw meal
In the clinker burning process and fuel consumption affect the chemical composition, fineness of grinding, crystal size, nature of raw materials, the type and amount of impurities, the homogeneity of raw muki.Himichesky composition of the raw meal has a significant impact on the required firing time. It is defined as the time it takes to during firing the raw material mixture at a certain temperature the content of free CaO in the clinker should not exceed 2%. Oxides of alkali metals in larger amounts (about 2.5%) retard (inhibit) binding of lime during firing, while the content of MgO (about 2.0%) accelerates the firing.
The homogeneity of the composition of the raw meal is a necessary condition for the uniform clinker mineralogical structure and uniform operation of the kiln system. To do this, you must make sure that the raw material mixture in the smallest volume in the range (<1 mm3) is representative of a composition (thoroughly mixed, homogeneous). If the meal is poorly mixed, the clinker having "nest" of different phases, for example, free lime and belite clusters that formed in non-uniform material with valuable tricalcium silicate - alite. Using mineralizers (such as fluorspar, zinc oxide, manganese sulfide), the firing temperature can be lowered, and thus, can be achieved energy savings in the production of clinker.
