The invention relates to a shaft preheater for preheating material in lump form with at least one shaft for receiving the material as well as a bridge disposed in the shaft for delivering hot gases which flow through the material from the bottom upwards.
Known shaft preheaters for preheating material in lump form ahead of downstream kilns frequently consist of a chamber which is formed as an annular shaft and in which the stock which is to be preheated is distributed. The stock is as a rule delivered into the preheater from a silo chamber lying above. The width of the annular shaft is limited to approximately 1.30 m in order to prevent segregation phenomena of the individual grain-size fractions. The preheated stock is discharged from the preheater via a plurality of rams disposed at the circumference. The flue gases from the downstream kilns are generally used for the preheating process by being delivered to the fill via horizontal bridges disposed in the annular shaft. However it has in this case been found that the material is heated relatively unevenly over the depth of the shaft, in particular when the shafts are relatively deep, due to the varying length of the fill through which the flue gases flow.
The object of the invention is therefore to further develop the shaft preheater so as to enable the material located in the shaft to be preheated as evenly as possible.
The shaft preheater according to the invention for preheating material in lump form consists substantially of at least one shaft for receiving the material as well as a bridge disposed in the shaft for delivering hot gases which flow through the material from the bottom upwards. The bridge is in this case disposed at an inclination.
According to a preferred embodiment, the bridge is disposed at an inclination corresponding to the angle of repose of the material. The length of the fill through which the flue gases flow is thus approximately uniform over the entire depth of the shaft.
According to a further configuration of the invention, a device for filling is provided which is disposed such that the shaft is charged centrally and a filling cone develops in the process. This method of delivering the material into the individual shafts results in the development of the shortest possible slope lengths, so that segregation phenomena of the individual grain-size fractions can largely be prevented. In this configuration the bridge is advantageously formed according to the developing filling cone.
According to a further aspect of the invention, the device for filling the shaft comprises a vertically adjustable feed chute. The mouth of the feed chute is in this case expediently set such that the filling height of the stock in the shaft meets the requirements according to the material grain size and type of material used. The chute is of a length such that it simultaneously serves as an air seal with respect to the flue gases emerging from the preheater shaft.
The shaft preheaters which are represented in
One of the shafts is represented in greater detail in
The material in lump form which is to be preheated is delivered via a device 2 for filling the shaft. This device consists of a pre-silo 2a and a feed chute 2b, with the mouth 2c of the feed chute 2b being vertically adjustable according to the double arrow 3.
A bridge 4, which extends over the entire depth of the shaft 1, is disposed in the lower part of the shaft 1.
Means 6 are provided in the upper region of the shaft 1 to carry off the hot gases. The bottom of the shaft 1 is formed by a slope 1b which is inclined towards the center of the shaft preheater and on which the preheated material can be conveyed to a central discharge opening 8 with the assistance of a ram system 7 which can be actuated.
Because of the vertically adjustable feed chute 2b, the mouth 2c can always be brought into line with the tip of the filling cone. The chute 2b thereby simultaneously also provides an air seal with respect to the hot gases 5 emerging from the preheater shaft. The bridge 4, which extends over the entire depth of the shaft, is inclined relative to the horizontal.
In order to obtain flow-through lengths which are as uniform as possible, the inclination of the bridge is expediently adapted according to the angle of repose of the material. The bridge therefore extends from the center of the shaft obliquely downwards on both sides to the respective outer wall.
Otherwise the bridge is configured such that the hot waste gases are introduced into the fill in such a way that the gases are distributed as evenly as possible over the width and depth of the shaft.
The gases emerging from the fill are collected in the upper part of the shaft, drawn off via the means 6 and delivered to a collecting main which connects all the shafts. From here the hot gases, in particular the flue gases of a downstream kiln, can be passed on to a dust removal device.
Although the invention is described herein with reference to the preferred embodiment, one skilled in the art will readily appreciate that various modifications and variations may be made without departing from the spirit and scope of the present invention. Such modifications and variations are considered to be within the purview and scope of the appended claims and their equivalents.
Number | Date | Country | Kind |
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103 52 764 | Nov 2003 | DE | national |
Number | Name | Date | Kind |
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4042226 | Beggs | Aug 1977 | A |
4289481 | Yano | Sep 1981 | A |
4668184 | Dorman | May 1987 | A |
4797092 | Pieper | Jan 1989 | A |
5125943 | Cole | Jun 1992 | A |
5401166 | Mallek et al. | Mar 1995 | A |
5460517 | Scheibenreif et al. | Oct 1995 | A |
Number | Date | Country | |
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20050098071 A1 | May 2005 | US |