- •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
The composition of the raw meal. Equations 5-9
In practice, the composition is characterized by raw materials (also part of PZ clinker) in most cases by the ratio of oxide (so-called modules). They set out certain chemical analyzes oxides. Lime standard (KSt or as it is accepted in Kazakhstan KN saturation ratio) in the majority of cases, is used to calculate the optimum lime component. The high lime component (CaO) allows the formation of rich lime silicate clinker phases during its firing. They are used for quality assurance with regard to the development of high strength cement. CaO content must be agreed with the content of other oxides - SiO2, A12O3, Fe2O3. If there is an excess of CaO (lime CaOsvob free), it can lead to later reaction with water, formation of Ca (OH) 2, and the increase in volume of the cement stone destruction. The optimum proportion of lime should be high, but not be too high. Lime Standard (KN) is used to accurately establish the optimal proportion of lime. It is expressed in the feed (or clinker) shows the available CaO proportion in percent that can bind in the firing process with the existing oxides SiO2, A12O3, Fe2O3 phase in the clinker; those. It expresses actually contained in the raw material or a mixture of CaO in the clinker,% of CaO to the amount that can be caused in the process of clinker burning and cooling.
equation 5
Silicate module characterizes the ratio of silica to the sum of aluminum and iron oxides. With the increase in clinker silicate module increases the content of minerals - silicates alite and belite. Clinker phase with alumina and iron oxide are fusible. The production value of the silicate cements module clinker SMlezhit generally between 1.6 and 4.1 [24], most often, and most favorably between 2.3 and 2.8 [4]. Low modulus silicate leads to easier calcined clinker simultaneously also to accelerate the formation of clinker in the kiln.
Alumina Module (GM, p Alumina Module) - is the ratio of alumina to iron oxide:
equation 6
Alumina module GM characterized clinker melt, since both exist oxide melt formation at a temperature almost entirely in the liquid phase. When aluminum modulus of 1.4 to 1.6 the maximum mass of the melt is formed at a low temperature. When GM <0,638 C3A mineral is formed. Cements with a low C3A exhibit particularly high resistance to the aggressive action of sulphate attack. The cement manufacturing GM value lies between 1.4 and 3.7 [24], in most cases between 1.8 and 2.8 at special cements GM can be reduced to 0.4 [4].
Cement clinker contains some 2% of alkali (Na2O + K2O), an average of about 1%. They are mostly made of raw clay component of the mixture. alkali content is indicated generally as Na2O equivalent [M .-%], and is calculated as follows:
Na2O equivalent [M .-%] = 0,658 K2O [M .-%] + Na2O [M .-%]
equation 7
Further characterization of clinker (SG). In addition, the cement clinker contains up to 2% SO3 (as sulfate). Sulfates arise from the oxidation of sulfur that fall within the furnace with raw material and fuel. When firing sulfate binds with alkalis. The compound to alkali sulfate is designated as (SG).
equation 8
It indicates the percentage of participation in the alkalis, which exists on the basis of the calculation as sulfate alkali. Alkali sulfate by 100% means that all the alkali clinker exist entirely as sulfate. When firing sulfate (SG> 100%) of sulfur is not connected polnostyuK2SO4, Na2SO4, K2SO4 · 2CaSO4 and / or CaSO4 forms as anhydrite. If sulfate firing occurred <100%, the excess alkali can be introduced into the clinker phases [20, 21,22].
Different proportion of alkali is reflected particularly strongly in the aluminate activity. By adding alkali slight (about 0.5%) increased the activity of hydraulic clinker in comparison with non-subsidized aluminate. When subsidized alkali in 1.0% hardly affect the hydraulic activity and if they contain> 1,5% hydraulic activity decreases. Table 1.4 covers the field and averages modules German cement clinkers.
Table - modules in the German Portland cement clinker
Показатель |
Max. |
Средний |
Min. |
KSt |
104,1 |
97,1 |
90,5 |
SM |
4,1 |
2,5 |
1,6 |
TM |
3,7 |
2,3 |
1,4 |
SG |
188,5 |
80,1 |
34,8 |
