Research on Online Monitoring of Energy Consumption of Rotary Kiln for Cement Clinker Formation Heat

Author(s):  
Qi Liu ◽  
Hongliang Yu ◽  
Xiaohong Wang ◽  
Shizeng Lu
Refractories ◽  
1962 ◽  
Vol 3 (3-4) ◽  
pp. 111-112
Author(s):  
M. Sh. Sharafiyev ◽  
G. V. Orlova
Keyword(s):  

2013 ◽  
Vol 3 (4) ◽  
pp. 95-98 ◽  
Author(s):  
S. Ya GALITsKOV ◽  
A. S FADEEV

Presents the results of the analysis of efficiency of application of the harmonized automatic control modes of operation of the burner and the drive boot the rotary kiln for firing of expanded clay. On the example of the furnace size of 40 m, in which fired raw clay smushlaevsks Deposit, the possibility to reduce energy consumption for production of 1 m 3 of expanded clay 11-to 15 %.


2009 ◽  
Vol 2 (2) ◽  
pp. 201-210
Author(s):  
B. Simons

The production of cement clinker is an energy consuming process. At about 50% of the energy is associated with grinding and milling of the raw meal, that normally is in the range 100% <200 μm with 90% <90 μm. Question: is it possible to use coarser components of the raw meal without reducing the clinker quality. With synthetic raw meals of various grain sizes the clinker formation was studied at static (1100 - 1450°C) and dynamic conditions (heating microscope). A routine to adjust the grain size of the components for industrial raw meals is developed. The fine fraction <90 μm should mainly contain the siliceous and argileous components, whereas the calcitic component can be milled separately to a grain size between 200-500 μm, resulting in lower energy consumption for milling. Considering the technical and economical realizability the relation fine/coarse should be roughly 1:1. The energy for milling can be reduced significantly, that in addition leads to the preservation of natural energy resources.


2013 ◽  
Vol 652-654 ◽  
pp. 1247-1251 ◽  
Author(s):  
Yang Bai ◽  
Lin Jin Zhang ◽  
Chuan Hui Chen ◽  
Xu Chu Ye

Cement clinker was produced in laboratory using the same ingredient as actual production, comparing with the ones which incineration residue of glyphosate waste mother-liquor was added in. The products were characterized by XRD, and the results showed that the main constituents were not changed. And some of the main performances were tested according to GB standards. After the residue was added in, the water requirement of normal consistency remained no change as 26%; the setting time, both initial set and final set, was extended; the soundness was improved a little. And it could be inferred that within a certain range, the more the residue added in, the longer the setting time was, the better the soundness was. According to all the results, using rotary kiln to dispose the waste mother-liquor was feasible in the actual production.


2021 ◽  
Vol 20 (3) ◽  
pp. 195-206
Author(s):  
V. N. Romaniuk ◽  
A. M. Niyakovskii ◽  
A. N. Chichko ◽  
Yu. V. Yatskevich

Production of concrete and reinforced concrete products in the conditions of the Republic of Belarus and in the countries with similar climatic conditions requires heat treatment in heat-technological installations in order to achieve the desired strength of the products at the appointed time, which consumes a great amount of thermal energy.  In this case, the purpose of equipment operating  modes is associated with a number of difficulties when it comes to new products of complex spatial configuration and structure. The optimality criteria of such modes are, as a rule, the duration and temperature limits of processing, providing the required strength with minimal energy consumption. In the conditions of serial production in the case of structurally simple objects, the assignment of heat treatment modes is carried out empirically. As the analysis shows, the modes obtained in this way do not meet the above criteria, especially from the standpoint of energy saving. The paper, using a mathematical model previously developed by the authors, proposes dependencies for calculating the optimal modes of heat treatment of concrete products that are distinguished by a complex spatial shape and multi-component structure. The method is based on three-dimensional transfer equations, taking into account internal sources of heat release due to the ongoing hydration reaction of the active components of the cement clinker, and the boundary conditions corresponding to the structure of the processed product, as well as the type of heat technology device for accelerated hydration. Equations are proposed for calculating the amount of heat energy supplied to the processed product providing a given strength at a specified time. On the example of a manufactured industrial concrete product and for the conditions of an actually used device for accelerated hydration, a comparison has been made between two limiting modes of heat treatment: with isothermal exposure and in its absence. As a result of the performed calculations, the dependences of energy consumption, temperature fields and the degree of hydration in the product for both modes have been obtained and an energy-saving mode of heat treatment corresponding to the case under consideration has been developed. It is shown that the used numerical method allows to solve problems of this type and to achieve thermal energy savings.


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