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Clinker well burned

Well-burned clinkers are less porous and contain better-crystallized colorless alite and dirty-green to muddy belite. [Pg.3]

Burning too near the discharge end of the kiln, where the temperature change is 1400°C to 1000°C, also produces small alite, and the clinker is usually poorly burned. Alite sizes of less than 15 pm in a 1000 tons-per-day kiln can be indicative of poor burning a 20-pm alite size is typical of poor burning in a 4000 tons-per-day kiln (Ono, 1980c). A well burned clinker (f-CaO < 0.6%) does not have alite crystals under 20 pm (Ono, 1995). [Pg.47]

Poorly burned clinker frequently contains many small belite clusters. If the raw mix contains coarse quartz grains, belite clusters appear even in well-burned clinker, and the alite size has a wide range. [Pg.53]

Ono (1991) listed some of the characteristics of poorly burned clinker free lime greater than 4.5%, tightly packed large free lime nests, belite nests with a surrounding of small alites, high porosity, a loose framework of free lime and alkali aluminate, and a flow pattern of matrix into the free-lime nest. Well-burned clinker was said to contain small free lime and octahedral periclase from dolomite and coarse aluminate and ferrite, resulting from equilibrium crystallization. [Pg.54]

Well-burned clinker with a high VW, volume weight, is difficult in coarse grinding (getting it to pass the 1-2 mm sieve), but soft in fine grinding (<88 microns). VW is the weight of clinker nodules, 5-10 mm diameter, in a liter container. Opti mum VW is approximately 1.35 kg/L. [Pg.54]

Flame formation must be favorable to a dense, stable coating on the brick refractory lining in the burning zone of the kiln as well as to a nodular clinker formation with low dust content and correctly developed clinker phases. [Pg.640]

The desirable characteristics of Class H well cement were listed by Arbelaez (1990) free lime levels less than 0.5% with a uniform distribution, CjA less than 6.5%, no weathered clinker, using only the 12.7-to 38.1-mm clinker fraction for the cement, relatively hot burning without production of cannibalistic alite, and avoidance of ragged belite by rapid cooling. [Pg.6]

Relatively large alite crystals, typically corroded well-differentiated matrix Clinker burned under oxidizing conditions and cooled to 1250 C in the kiln (Sylla, 1981)... [Pg.74]

Relatively wide and more numerous belite borders on alite which shows lamellar structure, the latter well-developed upon withdrawal from kiln at temperatures lower than 1200°C Clinker burned under reducing conditions, removed from kiln at1200 C, aircooled. Similar texture when removed at 1150°C and quenched in water (Sylla, 1981)... [Pg.77]

Photograph 7-25 Experimental laboratory burn with raw mix containing marl instead of quartz as a silica source. Resulting belite was well scattered in clinker and, to a minor extent, as nests. 1000°C for 30 min, 1425°C for 10 min. Very rapid temperature change. Average alite size = 20 pm. Clinker courtesy of Joe Garcia, Capitol Cement, San Antonio, Texas. (S A6645)... [Pg.88]

Relatively rapid set of cement Clinker burned and cooled under reducing conditions highly reactive, well-crystallized, more abundant C3A, slowly cooled (Sylla, 1981)... [Pg.116]

A relatively "hard-to-burn" feed from the western U.S., with a very impure dolomitic limestone, has 6.7% >125 pm and an acetic-acid insoluble residue of 9.5% >45 pm, the latter comprised of quartz, feldspar, medium to finely crystalline igneous and metamorphic rock fragments, and an abundance of ferro-magnesian minerals (mainly amphiboles and pyroxenes). = 1.6% and = 4.5%. Belite nests (many with tightly packed crystals), solitary belite, and periclase are abundant in this fine- to medium-crystalline clinker. Nevertheless, a high-compressive strength mortar (44.8 to 48.3 MPa) is made, mainly because of the small alite size and the well-scattered solitary belite. [Pg.146]

The chemical enthalpy of the formation of sulfobelitic clinkers is lower than that of ordinary Portland clinkers and even of belitic clinkers. This is due mainly to a lower overall CaO content in the clinker to be produced, as well as to the fact that a fraction of the needed CaO is introduced in the form of calcium sulfate rather than calcium carbonate. The thermal losses are also reduced because of the lower burning temperature... [Pg.68]


See other pages where Clinker well burned is mentioned: [Pg.30]    [Pg.43]    [Pg.47]    [Pg.54]    [Pg.55]    [Pg.75]    [Pg.92]    [Pg.31]    [Pg.5]    [Pg.13]    [Pg.30]    [Pg.38]    [Pg.63]    [Pg.200]    [Pg.969]    [Pg.184]    [Pg.14]    [Pg.17]    [Pg.68]    [Pg.159]   
See also in sourсe #XX -- [ Pg.47 , Pg.54 , Pg.55 ]




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