- •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 dehydration of kaolinite
the dehydration of kaolinite primary product, ranging from approximately 600 ° C, is closest in structure to the kaolinite product metakaolin. Given that the profitability of energy mullite formation is much greater than that of metakaolin. accompanied by a dehydration process kaolinite razrusheniemego complete structure to form a mixture of free oxides. It was found that the endothermic effect of dehydration of kaolinite and its exotherm phase prevrascheniyapo with increasing heating rate of 10 to Bo / min shift toward high temperatur.Prevrascheniya by heating kaolinite were for decades one of the issues subjected to particularly intensive study. There were differing views on the nature of the dehydration of kaolinite product (metakaolin or a mixture of silicon and aluminum), and on the process, which is celebrated on the thermograms ekzotermicheskimeffektom at 900-1000 ° (crystallization from A1., 0z, mullite or spinel).
The reactions during the sintering
In the sintering zone of the most fusible minerals ZSa0-A1203 and 4SaO> Al203 * Fe203 melted. The resulting liquid phase is partially dissolved 2Ca0-Si02 and saturate it with lime to 3Ca0-Si02.
Tricalcium silicate is significantly less soluble in the melt than dicalcium silicate. Therefore, once there its formation, the melt becomes supersaturated with respect to this and tricalcium silicate mineral melt drops in the form of tiny crystalline solid, which under these conditions is then able to increase in size.
Dissolution 2CaO> Si02 and absorption they know is not right in the entire mass of the mixture and its individual portions. Therefore, for a more complete assimilation dvuhkal- tsievym lime silicate materials need to withstand a certain period at the sintering temperature (1300-1450 ° C). The longer this delay is, the more complete will the binding of lime, and at the same time become larger crystals CJSIC - Si02.
However, long withstand the clinker at the sintering temperature or it is not recommended to cool it slowly; Portland cement, which has a Si02 CJSIC fine crystalline structure has higher strength.
The duration of exposure depends on the temperature of the clinker: the higher it is in the sintering zone, the faster formed clinker. However, excessively high, and most importantly a sharp rise in temperature quickly formed a lot of melt and burns the mixture may start komkovatsya. Formed with the large grains are heated and difficult transition process in the C2S C3S violated. As a result, the clinker is badly burned (it will be a little tricalcium silicate).
To accelerate the process of clinker as well as in those cases when it is necessary to obtain high clinker 3Ca0-Si02, apply some substances (calcium fluoride, CaF2, iron oxide, etc.), Having the ability to lower the melting point of the raw mixture. An earlier generation of the liquid phase shifts the clinker formation process to less high temperatures.
The sintering period is sometimes all the lime mixture has no time to fully assimilate silica; this assimilation process is slower due to the depletion of a mixture of lime and 2CaO • Si02. In the clinker with high saturation coefficient, which require maximum absorption in the form of lime CJSIC • Si02, will always be free lime.
1-2% of free lime is not reflected in the quality of Portland cement, but more of its high content of non-uniformity causes changes in the volume of portland cement hardening and therefore inadmissible.
The clinker falls out sintering zone to the cooling zone (VI), where the flows of cold air moving towards the clinker.
