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Alite is an impure form of tricalcium silicate , Ca 3 SiO 5 , sometimes formulated as 3CaO·SiO 2 ( C 3 S in cement chemist notation ), typically with 3-4% of substituent oxides. It is the major, and characteristic, phase in Portland cement . The name was given by Törnebohm in 1897 to a crystal identified in microscopic investigation of Portland cement. Hatrurite is the name of a mineral that is substituted C 3 S .

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39-449: C3S may refer to: Alite , in cement chemist notation Chennai Centre for China Studies , an Indian think thank Copernicus Climate Change Service , science service Cultural Commons Collecting Society , music licensing organization Tricarbon monosulfide (C 3 S), substance [REDACTED] Topics referred to by the same term This disambiguation page lists articles associated with

78-450: A limited number of orthosilicate ( SiO 4− 4 ) ions can be replaced with sulfate ( SO 2− 4 ) ions, provided that for each sulfate ion, two aluminate ( AlO 5− 4 ) ions are also substituted. Tricalcium silicate is thermodynamically unstable below 1250°C, but can be preserved in a metastable state at room temperature by fast cooling: on slow cooling it tends to revert to belite ( Ca 2 SiO 4 ) and CaO. As

117-502: A long, relatively cool calcining zone. Fuel consumption is in 4 to 4.5 MJ/kg range and the lime is typically medium burned. Rotary kilns started to be used for lime manufacture at the start of the 20th century and now account for a large proportion of new installations if energy costs are less important. The early use of simple rotary kilns had the advantages that a much wider range of limestone size could be used, from fines upwards, and undesirable elements such as sulfur can be removed. On

156-617: A mass of interlocking needles that provide the strength of the hydrated cement system. High alite reactivity is desirable in Portland cement manufacture, and this is achieved by retaining, as far as possible, high temperature polymorphs, in crystals that are small, distorted and highly defective. Defects provide sites for initial water attack. The composition of alite rich in CaO (71.6 wt. %) and relatively poor in SiO 2 (25.2 wt. %) (see

195-499: A tourist destination. The ruins of the lime kilns can still be seen today. A lime kiln also existed in Wool Bay , South Australia . The large kiln at Crindledykes near Haydon Bridge , Northumbria, was one of more than 300 in the county. It was unique to the area in having four draw arches to a single pot. As production was cut back, the two side arches were blocked up, but were restored in 1989 by English Heritage . The development of

234-431: Is This reaction can take place at anywhere above 840 °C (1,540 °F), but is generally considered to occur at 900 °C (1,650 °F) (at which temperature the partial pressure of CO 2 is 1 atmosphere ), but a temperature around 1,000 °C (1,830 °F) (at which temperature the partial pressure of CO 2 is 3.8 atmospheres ) is usually used to make the reaction proceed quickly. Excessive temperature

273-478: Is a solid solution and contains minor amounts of other oxides besides CaO and SiO 2 . A typical composition is: Based on this, the formula can be expressed as Ca 2.90 Mg 0.06 Na 0.01 Fe 0.03 Al 0.04 Si 0.95 P 0.01 O 5 . In practice, the composition varies with the bulk composition of the clinker , subject to certain limits. Substitution of calcium ions or orthosilicate ions requires that electric charges be kept in balance. For instance,

312-458: Is also ancient, but agricultural use only became widely possible when the use of coal made it cheap in the coalfields in the late 13th century, and an account of agricultural use was given in 1523. The earliest descriptions of lime kilns differ little from those used for small-scale manufacture a century ago. Because land transportation of minerals like limestone and coal was difficult in the pre-industrial era, they were distributed by sea, and lime

351-480: Is around 20 kWh per tonne of lime. This additional input is the equivalent of around 20 kg CO 2 per ton if the electricity is coal-generated. Thus, total emission may be around 1 tonne of CO 2 for every tonne of lime even in efficient industrial plants, but is typically 1.3 t/t. However, if the source of heat energy used in its manufacture is a fully renewable power source, such as solar, wind, hydro or even nuclear; there may be no net emission of CO 2 from

390-674: Is avoided because it produces unreactive, "dead-burned" lime. Slaked lime ( calcium hydroxide ) can be formed by mixing quicklime with water. Because it is so readily made by heating limestone, lime must have been known from the earliest times, and all the early civilizations used it in building mortars and as a stabilizer in mud renders and floors. According to finds at 'Ain Ghazal in Jordan, Yiftahel in Israel, and Abu Hureyra in Syria dating to 7500–6000 BCE,

429-400: Is particularly corrosive. Equipment is installed to trap this dust, typically in the form of electrostatic precipitators or bag filters. The dust usually contains a high concentration of elements such as alkali metals , halogens and sulfur. The lime industry is a significant carbon dioxide emitter. The manufacture of one tonne of calcium oxide involves decomposing calcium carbonate, with

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468-410: Is the "primary" and B the "secondary" shaft, the combustion air is added from the top of shaft A, while fuel somewhat below via burner lances. The flame is top-bottom. The hot gases pass downward, cross to shaft B via the so-called "channel" and pass upward to exhaust of shaft B. At same time in both shafts cooling air is added from the bottom to cool the lime and to make exhaust of gases via the bottom of

507-432: Is unknown if the cathedral builders of this area were aware of the hydraulic properties of their lime mortar or intentionally developed its use after their fortuitous finding. See the article on belite . Lime kiln A lime kiln is a kiln used for the calcination of limestone ( calcium carbonate ) to produce the form of lime called quicklime ( calcium oxide ). The chemical equation for this reaction

546-520: The Black Country Living Museum which opened in 1976, although the kilns were last used during the 1920s. It is now among the last in a region which was dominated by coalmining and limestone mining for generations until the 1960s. The theoretical heat (the standard enthalpy ) of reaction required to make high-calcium lime is around 3.15 MJ per kg of lime, so the batch kilns were only around 20% efficient. The key to development in efficiency

585-569: The medieval epoch in locations where limestone was cemented by amorphous silica or contained chert nodules or a lot of clay impurities. This is likely the reason why some old medieval lime mortars used to build the Tournai cathedral (Belgium) exhibit an unexpected hydraulic character as revealed by a mineralogical study made by Mertens et al . (2006) who evidenced the presence of wollastonite and rankinite along with calcium silicate hydrate phases in lime mortars. The only explanation for

624-404: The base (the "eye"), constructed of brick. Limestone was crushed (often by hand) to fairly uniform 20–60 mm (1– 2 + 1 ⁄ 2  in) lumps – fine stone was rejected. Successive dome-shaped layers of limestone and wood or coal were built up in the kiln on grate bars across the eye. When loading was complete, the kiln was kindled at the bottom, and the fire gradually spread upwards through

663-411: The bottom. The cycling produces a long burning zone of constant, relatively low temperature (around 950 °C) that is ideal for the production of high quality soft burned reactive lime. With exhaust gas temperatures as low as 120 °C and lime temperature at kiln outlet in 80 °C range the heat loss of the regenerative kiln is minimal, fuel consumption is as low as 3.6 MJ/kg. Due to these features

702-401: The charge. The degree of burning can be adjusted by changing the rate of withdrawal of lime. Heat consumption as low as 4 MJ/kg is possible, but 4.5 to 5 MJ/kg is more typical. Due to temperature peak at the burners up to 1200 °C in a shaft kiln conditions are ideal to produce medium and hard burned lime. These typically consist of a pair of shafts, operated alternately. First, when shaft A

741-431: The charge. When burnt through, the lime was cooled and raked out through the base. Fine ash dropped out and was rejected with the "riddlings". Only lump stone could be used, because the charge needed to "breathe" during firing. This also limited the size of kilns and explains why kilns were all much the same size. Above a certain diameter, the half-burned charge would be likely to collapse under its own weight, extinguishing

780-486: The design shown, a circle of shafts (typically 8–15) is arranged around the kiln riser duct. Hot limestone is discharged from the shafts in sequence, by the action of a hydraulic "pusher plate". Kilns of 1000 tonnes per day output are typical. The rotary kiln is the most flexible of any lime kilns able to produce soft, medium, or hard burned as well as dead-burned lime or dolime. All the above kiln designs produce exhaust gas that carries an appreciable amount of dust. Lime dust

819-534: The discovery of these silicate phases not normally expected in lime mortar is that they have been formed by the hydration of calcium silicate such as Ca 3 SiO 5 (C 3 S) or Ca 2 SiO 4 (C 2 S) formed at high temperature along calcium oxide in the lime kiln . In the area of Tournai ( Belgium ), the Tournaisian limestones are particularly rich in amorphous silica and exploited as building stone and for making lime mortar since very ancient ages. It

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858-450: The earliest use of lime was mostly as a binder on floors and in plaster for coating walls. This use of plaster may in turn have led to the development of proto-pottery, made from lime and ash. In mortar, the oldest binder was mud. According to finds at Catal Hüyük in Turkey, mud was soon followed by clay, and then by lime in the 6th millennium BCE. Knowledge of its value in agriculture

897-419: The fire. So kilns always made 25–30 tonnes of lime in a batch. Typically the kiln took a day to load, three days to fire, two days to cool and a day to unload, so a one-week turnaround was normal. The degree of burning was controlled by trial and error from batch to batch by varying the amount of fuel used. Because there were large temperature differences between the center of the charge and the material close to

936-424: The formation of 785 kg of CO 2 in some applications, such as when used as mortar ; this CO 2 is later re-absorbed as the mortar goes off. If the heat supplied to form the lime (3.75 MJ/kg in an efficient kiln) is obtained by burning fossil fuel it will release CO 2 : in the case of coal fuel 295 kg/t; in the case of natural gas fuel 206 kg/t. The electric power consumption of an efficient plant

975-428: The hereabove table) may help to understand why in particular conditions, if a sufficiently high temperature is reached in a lime kiln during enough time, alite can also be directly formed by pyrolizing only siliceous limestone (containing amorphous SiO 2 impurities up to 25 – 30 wt. %). Hydraulic mortar or pre-Portland cement may have been occasionally produced on a small scale in this way during

1014-422: The kiln impossible via maintaining a positive pressure. The combustion air and cooling air leave the kiln jointly via exhaust on top of shaft B, preheating the stone. The direction of flow is reversed periodically (typically 5–10 times per hour) shaft A and B changing the role of "primary" and "secondary" shaft. The kiln has three zones: preheating zone on the top, burning zone in the middle, and cooling zone close to

1053-463: The national rail network made the local small-scale kilns increasingly unprofitable, and they gradually died out through the 19th century. They were replaced by larger industrial plants. At the same time, new uses for lime in the chemical , steel and sugar industries led to large-scale plants. These also saw the development of more efficient kilns. A lime kiln erected at Dudley , West Midlands (formerly Worcestershire ) in 1842 survives as part of

1092-447: The other hand, fuel consumption was relatively high because of poor heat exchange compared with shaft kilns, leading to excessive heat loss in exhaust gases. Old fashioned "long" rotary kilns operate at 7 to 10 MJ/kg. Modern installations partially overcome this disadvantage by adding a preheater, which has the same good solids/gas contact as a shaft kiln, but fuel consumption is still somewhat higher, typically in range of 4.5 to 6 MJ/kg. In

1131-427: The presence of an oxide ion in the lattice. During clinker grinding, first step of partial dissolution of C 3 S involves hydration of superficial oxide ions and leads to a hydroxylated C 3 S surface. It reacts with water (roughly) according to the reaction: Which can also be written in the cement chemist notation as: The hydrate is referred to as the calcium silicate hydrate – "C-S-H-" – phase. It grows as

1170-490: The regenerative kilns are today mainstream technology under conditions of substantial fuel costs. Regenerative kilns are built with 150 to 800 t/day output, 300 to 450 being typical. These contain a concentric internal cylinder. This gathers pre-heated air from the cooling zone, which is then used to pressurize the middle annular zone of the kiln. Air spreading outward from the pressurized zone causes counter-current flow upwards, and co-current flow downwards. This again produces

1209-590: The same title formed as a letter–number combination. If an internal link led you here, you may wish to change the link to point directly to the intended article. Retrieved from " https://en.wikipedia.org/w/index.php?title=C3S&oldid=1180787190 " Category : Letter–number combination disambiguation pages Hidden categories: Short description is different from Wikidata All article disambiguation pages All disambiguation pages Alite The alite found in Portland cement differs in composition from simple tricalcium silicate . It

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1248-422: The temperature changes, it passes through several polymorphic states: The polymorphs differ structurally by minor deformations from the basic hexagonal structure. Alite is the major phase in Portland cement responsible for setting and development of "early" strength. The other silicate, belite contributes "late" strength, due to its lower reactivity. Alite is more reactive because of its higher Ca content, and

1287-504: The top is first dried then heated to 800 °C, where de-carbonation begins, and proceeds progressively faster as the temperature rises. Below the burner, the hot lime transfers heat to, and is cooled by, the combustion air. A mechanical grate withdraws the lime at the bottom. A fan draws the gases through the kiln, and the level in the kiln is kept constant by adding feed through an airlock. As with batch kilns, only large, graded stone can be used, in order to ensure uniform gas-flows through

1326-542: The town of Waratah in Gippsland , Victoria , Australia produced a majority of the quicklime used in the city of Melbourne as well as around other parts of Gippsland. The town, now called Walkerville , was set on an isolated part of the Victorian coastline and exported the lime by ship. When this became unprofitable in 1926 the kilns were shut down. The present-day area, though having no town amenities as such, markets itself as

1365-501: The wall, a mixture of underburned (i.e. high loss on ignition ), well-burned and dead-burned lime was normally produced. Typical fuel efficiency was low, with 0.5 tonnes or more of coal being used per tonne of finished lime (15 MJ/kg). Lime production was sometimes carried out on an industrial scale. One example at Annery in North Devon , England , near Great Torrington , was made up of three kilns grouped together in an 'L' shape and

1404-437: Was alight for several days, and then the entire kiln was emptied of the lime. In a draw kiln, usually a stone structure, the chalk or limestone was layered with wood, coal or coke and lit. As it burnt through, lime was extracted from the bottom of the kiln, through the draw hole. Further layers of stone and fuel were added to the top. The common feature of early kilns was an egg-cup shaped burning chamber, with an air inlet at

1443-426: Was most often manufactured at small coastal ports. Many preserved kilns are still to be seen on quaysides around the coasts of Britain. Permanent lime kilns fall into two broad categories: "flare kilns" also known as "intermittent" or "periodic" kilns; and "draw kilns" also known as "perpetual" or "running" kilns. In a flare kiln, a bottom layer of coal was built up and the kiln above filled solely with chalk. The fire

1482-523: Was situated beside the Torrington canal and the River Torridge to bring in the limestone and coal, and to transport away the calcined lime in the days before properly metalled roads existed. Sets of seven kilns were common. A loading gang and an unloading gang would work the kilns in rotation through the week. A rarely used kiln was known as a "lazy kiln". In the late 19th and early 20th centuries

1521-455: Was the invention of continuous kilns, avoiding the wasteful heat-up and cool-down cycles of the batch kilns. The first were simple shaft kilns, similar in construction to blast furnaces . These are counter-current shaft kilns. Modern variants include regenerative and annular kilns. Output is usually in the range 100–500 tonnes per day. The fuel is injected part-way up the shaft, producing maximum temperature at this point. The fresh feed fed in at

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