- •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
Cementing deep wells
In principle, all portland cement the well borehole. They differ from conventional standard cements requirement that they should be produced without the addition of recycled fuel and distillate. They can not even be used intensify the additive. Cements are usually manufactured in a batch mode with fineness of 3000 cm2 / g Blaine, i.e. they are relatively coarse. Today Base uses two class G cement and Class H. Tampon Their technical properties controlled can be adjusted with suitable retardants for use in almost any desired downhole temperature to 250 ° C and thus, they are universal cements. According to API standard mortar class G is tested with W / C ratio is 0.44, Class H cement tested at the W / C ratio is 0.38. These indicators are only slightly deflected by praktike.Skvazhinnoe pressure increases the temperature and results in faster hardening of Portland cement and, therefore, accelerates well cementing accelerates hydration product formation. As a result, at a temperature of about 110 ° C C-S-H gel forms a highly-S2SH crystallinity and, thus, most of the hydration products becomes denser. This conversion process requires a strong shrinkage and partial loss of strength of the hardened cement paste, with devastating consequences for the well density. In a class of standardized G- slurries reduction in compressive strength may be 80%, and 100-fold increase in permeability (typically 0.1 mDarsy) is observed at 230 ° C. This is "the power of regression." The marked technical problem is solved by reducing the ratio CaO: SiO2 - solution ratio is about 1. For this purpose, for oil wells, operating at temperatures above 110 ° C, prepared slurries containing 30-40% quartz flour. Under these conditions, it is obtained as the preferred phase C-S-H - tobermoritopodobny (C5S6H5) mineral which is not formed at normal temperature and elevated temperature.Pri calcium aluminates and others in hydrated form products. It turns C3A at a temperature of about 80 ° C instead of hexagonal C2AH8 cubic C3AH6 (Kato). Ettringite at about 110 ° C becomes unstable and decomposes with the formation of C-A-N phase CaSO4.Burovoy hemihydrate and cement, in particular, two basic Class G Cement and Class H iz-za fit their well-defined composition and preparation method as for manufacturing of complex building structures is responsible oil and gas wells. Their purity and quality make them particularly interesting for research.
