US 4,043,746 AGrant
Method for the Heat Treatment of Fine-Grained Materials Containing Alkali Compounds
Issue Date:1977-08-23
•8 Claims
•1 Drawing Sheets
Abstract
A method for the heat treatment of fine-grained materials containing alkali compounds which liquify at critical temperatures comprises pre-heating the materials and discharging them to a rotary kiln in counterflow to the kiln exhaust gases, and introducing cooling air to the kiln in such quantity and at such temperature as to reduce the temperature of the exhaust gases to a level lower than that required for the compounds to liquify.
Metadata
Assignee
- Polysius AG
Inventor
- Horst Ritzmann
Application Information
Application Number:US 6798063
Filing Date:1976-04-23
Priority Date:1974-09-19
Art Unit:344
Classifications
IPC:
F27B 720
Field of Search:
1064323410014;58;106;109;105135;137
Patent Drawings (1 sheets)
Description
One embodiment of the invention is disclosed in the drawing which is a diagrammatic elevational view of apparatus for practicing the method.
The plant for firing raw cement meal comprises a pre-heater or first heat-treatment stage 1 to which the material is introduced, preheated, and subsequently discharged to a rotary kiln 6. The pre-heater may consist, for example, of two cyclones 2, 3 and 4, 5.
The second heat-treatment stage is formed by the rotary kiln 6, through which hot sintering gases (arrow 8) produced by a burner 7 pass in counterflow to the material (arrow 9). The sintering temperature of cement meal is of course known.
In the rear part of the rotary kiln 6 adjacent the pre-heater 1 additional air (arrow 11) is forcibly blown in by a number of variable speed fans 10 disposed on the outer periphery of the kiln and rotating with the kiln; this air is of such temperature and in such quantity as to reduce the temperature of the exhaust gases (arrow 12) at the rear end of the kiln so that no undesirable deposits from liquid compounds of alkalis, chlorine, sulphur and the like can occur either in the pre-heater 1 or in the transition 13 between the pre-heater 1 and the rotary kiln 6.
Reference works such as "The Behaviour of Alkalis in Cement Burning", a thesis by Goes, C., submitted at the Bergakademie Clausthal, 1959, list critical temperatures for alkali compounds of the kind referred to herinbefore. For example, the critical temperature of K.sub.2 SO.sub.4 is 1069.degree. C. and that of Na.sub.2 SO.sub.4 is 884.degree. C. In the practice of the present process,the exhaust gases leaving the kiln enroute to the preheater should be cooled to less than 1069.degree. C. to prevent the liquification of K.sub.2 SO.sub.4. To prevent the liquification of Na.sub.2 SO.sub.4, the exhaust gas should be cooled to a temperature less than 884.degree. C. The quantity of the cooling air admitted via the cooling fans 10 can be adjusted, inasmuch as their speed is variable, to regulate closely the temperature of the exhaust gases so that they will preheat the material in the preheater but will not liquify the alkali compounds. The temperature of the exhaust gas adjacent the material inlet end of the kiln may of course be determined in the usual way by means of known temperature sensing devices.
The following examples illustrate the disclosed process.
Example I
Raw cement meal having a sintering temperature of 1450.degree. C. was analysed and found to contain a quantity of K.sub.2 SO.sub.4, the critical temperature of which is 1069.degree. C. The temperature of the exhaust gas at the material inlet end of the kiln was measured to be 1100.degree. C. and the temperature of the meal discharged from the preheater to the kiln was measured to be 820.degree. C. Liquification of the K.sub.2 SO.sub.4 was prevented by introducing standard atmosphere air into the kiln via the blowers at a rate (about 0.14 m.sup.3 per kg of clinker) sufficient to lower the temperature of the exhaust gas to 1000.degree. C.
Example Ii
Raw cement meal having a sintering temperature of 1400.degree. C. was analysed and found to contain a quantity of Na.sub.2 SO.sub.4, the critical temperature of which is 884.degree. C. The temperature of the exhaust gas at the material inlet end of the kiln was measured to be 950.degree. C. and the temperature of the meal discharged from the preheater to the kiln was measured to be 800.degree. C. Liquification of the Na.sub.2 SO.sub.4 was prevented by introducing standard atmosphere air into the kiln via the blowers at a rate (about 0.13 m.sup.3 per kg of clinker) sufficient to lower the temperature of the exhaust gas to 870.degree. C.
By analysing the content of any cement meal its constituency can be determined. Then by measuring the temperature of the kiln exhaust gas, as much cooling air may be introduced to the kiln via the variable speed blowers 10 as is required to lower the temperature of the exhaust gas temperature to one only a little below the critical temperature of the deposit-forming material. Typical of the kinds of deposit-forming materials with which the process is applicable are SiO.sub.2, Al.sub.2 O.sub.3, TiO.sub.2, Fe.sub.2 O.sub.3, Mn.sub.2 O.sub.3, CaO, MgO, SO.sub.3, P.sub.2 O.sub.5, Na.sub.2 O, K.sub.2 O, Cl, and mixtures thereof .
Claims
What is claimed is:
1. A two-stage method of sintering fine-grained raw cement meal containing a solid compound which at a critical temperature lower than the sintering temperature of said material tends to liquify and form deposits, said solid compound being from the group composed of SiO.sub.2, Al.sub.2 O.sub.3, TiO.sub.2, Fe.sub.2 O.sub.3, Mn.sub.2 O.sub.3, CaO, MgO, SO.sub.3, P.sub.2 O.sub.5, Na.sub.2 O, K.sub.2 O, Cl, and mixtures thereof, said method comprising discharging said material from a preheater to one end of a sintering kiln; directing through said kiln from the other end thereof toward said one end hot gases at a temperature sufficiently high to sinter said material; exhausting the gases from said kiln to said preheater to preheat said material prior to its discharge to said one end of said kiln; and introducing cooling air into said kiln adjacent said one end thereof in sufficient quantity and at such temperature to ensure that the temperature of the gases exhausted from said kiln to said preheater is lower than that of said critical temperature.
2. A two-stage heat treatment method of treating fine-grained raw material having a sintering temperature and containing a solid compound which at a critical temperature lower than said sintering temperature tends to liquify and form deposits, said method comprising directing through a sintering kiln from one end thereof toward the other hot gases at a temperature higher than said critical temperature; preheating said material by exhausting the gases from said kiln to a preheater to which said material is introduced and subsequently delivered to said other end of said kiln; and introducing cooling air into said kiln adjacent said other end thereof in sufficient quantity and at such temperature as to ensure that the temperature of the gases exhausted from said kiln to said preheater is at a temperature lower than said critical temperature.
3. A method according to claim 2 including introducing said air to said kiln at a sufficient distance from said other end thereof that a substantially homogeneous mixture of air and exhaust gases exists at said other end of said kiln.
4. A method according to claim 2 including introducing said air to said kiln at a distance from said other end thereof which is between about two to three times the diameter of said kiln.
5. A method according to claim 2 including forcibly blowing said air into said kiln.
6. A method according to claim 2 including varying the quantity of air introduced to said kiln.
7. A method according to claim 2 wherein said raw material is cement meal.
8. A method according to claim 2 including maintaining the temperature of said gases adjacent said one end of said kiln at least as high as the sintering temperture of said material.
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