Device for a ring section furnace

Abstract: Device for a ring section furnace for the calsination of carbon bodies, comprising a number of chambers (K1-Kn) wherein the carbon bodies are placed when performing the calsination process. During the calsination process, a part of the furnace comprising a minor number of chambers is divided into a preheating zone (K3-K2), a combustion zone (K7-K14), and a cooling zone (K8-K10) that together in a successive manner are advanced as to the furnace, whereby flue gases formed under the process are sucked out from the first chamber (K2) in the preheating zone through a pipe connection to a common ring duct (10). To eliminate the entrance of false air from the first chamber (K1) adjacent the preheating zone, a counterpressure fan (17) is arranged in connection with the first chamber (K1).

Description: The present invention relates to a ring section furnace device for the calcination of carbon bodies, which consists of a number of chambers wherein the carbon bodies are placed when performing the calsination process. During the calcination process, a part of the furnace comprising a minor number of chambers is divided into a preheating zone, a combustion zone, and a cooling zone that together in a successive manner are advanced as to the furnace, whereby flue gases formed in the combustion zone under the process are sucked out from the first chamber in the preheating zone through a pipe connection to a common ring duct. The purpose of the calcination process is to carbonise the binding agent in the carbon blocks, to obtain homogenised carbon blocks with properties that make them suitable for the use e. g. in aluminium electrolysis cells. The carbon blocks are produced in the required shape from a mixture of crushed coke or anthracite and a binding agent as, for example, pitch. Carbon blocks of this type may be of a considerable weight of several tonnes and of lengths of 1,5 metres or more, dependent on the use as anode- or cathode elements in the electrolysis cells. The carbon blocks are placed in the furnace in deep shafts known as cassettes, that are built of fireproof bricks. The gap between the carbon blocks and the cassette walls is filled with coke that serves as a packing material for the support of the carbon blocks. The coke also serves to protect the carbon blocks from burning. A number of cassettes are connected to each other and constitute in this manner a chamber. The walls between the cassettes are fitted with flue gas channels, and heat is transferred to the carbon blocks by the gases being passed through these channels. The space above each chamber is covered with a lid. The flue gases from one chamber are led through channels to an adjacent chamber. In this manner the flue gases can be led through a number of serially connected chambers in a preheating, combustion and cooling zone. The most frequently used fuels are oil or gas. Flue gas discharge and burner equipment are successively moved from one chamber to the next. A ring section furnace is fitted with two rows with the chambers connected to each other as parallel rows. At the end of a chamber row the gas flows are connected with channels to the parallel chamber row. In this way the chambers form a ring. For this reason this type of furnace is known as a ring section furnace. Due to the special properties of the carbon bodies, it is necessary to avoid excessive temperature gradients during calcination that will result in cracks in the finished product. Each chamber must consequently be operated in accordance with an exact time and temperature programme defined for the ring furnace. The first phase of heat supply to a chamber takes place in the preheating zone, where the carbon blocks are heated up to 600°C by using the gas heat from the last part of the combustion zone. At a later stage in the temperature interval from 600°C to the required maximum temperature 1200-1300°C, it becomes necessary to add heat through the above mentioned combustion of gas or oil. The combustion zone is moved by moving the oil or gas burners from one chamber to the next. The frequency of this relocation is known as the heating progress and determines the capacity of the ring section furnace. As mentioned, each chamber must have provisions to be connected to an exhaust system partly for the removal of exhaust gases from the combustion zone, and partly for the supply of oxygen to the combustion zone, to obtain a complete combustion of gas or oil. This connection is generally established by fitting an exhaust pipe, possibly with a fan, between a chamber in the preheating zone and a ring duct. Ambient air is sucked through the combustion zone and serves to support this with a sufficient amount of oxygen. The gas is further sucked through the preheating zone before it is transported through the pipe and the exhaust fan to the ring duct and a purifying plant. There are horizontal flue gas channels in the room below the chamber, whereas there is free gas flow in the room below the chamber lid above the cassettes. The flue gas channels in the cassette walls connect the room below the chamber lid and the rooms below the chamber. In closed ring section furnaces the fuel may be supplied either in separate vertical furnace shafts, or preferably the fuel may be added fully or in part to the room above and/or below the cassettes as shown in the applicant's own Norwegian patents no. 152.029 and no. 174.364 (EP 0 541 165 A). In ring section furnaces the channels in each cassette wall are divided into two by a dividing wall in the room below the cassettes. The flue gases are consequently led up through one half of the wall and down through the other half of the wall. A ring section furnace is controlled on the basis of the temperature of the gas that flows through the chambers. The temperature of the carbon blocks is lower than the gas temperature, and is a result of the heat transfer conditions in the furnaces. The heat transfer conditions depend mainly on the following parameters: Chamber- and cassette size, the size of the carbon block, the particle size of the coke (the packing material) and the packing factor of the same, gas quantity and -speed together with the alignment of the carbon blocks in the cassettes. A common feature concerning these parameters is that they should be kept at a constant value in the course of time, such that the difference between gas temperature and carbon block temperature may be kept at an approximately constant level. The ability of controlling a ring section furnace on the basis of the gas temperature depends on the above mentioned condition. In practice, if in case the values of the above mentioned parameters change in the course of time, e. g. as a result of wear in the brickwork and thereby allowing the entrance of false air, this have to be compensated for when following the time/temperature curve. To obtain a good utilisation of the energy value (heat value) in the fuel, it is required that all parts of the combustion zone receive a sufficient amount of oxygen, securing that the combustion will be complete. Further, under unfavourable conditions, incomplete combustion results in formation of gases that may cause an explosion in the furnace. Thus, the content of oxygen in the gas at the various locations in the calcinating process, is of great importance as to the quality of the process. A balanced process control serves to avoid thermal shocks, i. e. rapid changes of temperature in the carbon blocks and in the refractory construction of the furnace which could lead to crack formation and deformation and, consequently, an increase in the amount of wrecked carbon blocks and extended maintenance work on the refractory constructions. A substantial weakness in the existing ring section furnaces is that they are constructed as a continuos brickwork of refractory bricks and mortar that forms chambers, walls and channels. Constructions of this type will, in the course of time, become degraded due to the thermal stresses being present as the construction is repeatedly heated and cooled. This degradation comprises cracks and displacements that results in unwanted passage of air and gases. As mentioned initially, flue gases formed in the combustion zone are sucked out of the first chamber (K2) in the preheating zone through a pipe connection to a common ring duct. As a result, the uncovered cold chamber (K1) adjacent the chamber (K2) where the exhaust fan is placed, is exposed to an sub-pressure in the A-part of the chamber leading to the entrance of false air from said part to the preheating zone. Following this, the capability of the exhaust fan to suck air in the opposite direction, i. e. from the cooling zone, through the combustion zone and to the preheating zone, is substantially reduced. It has been an object of the present invention to provide a device that substantially eliminates the entrance of false air in the preheating zone (K2), and thereby gaining an increase in the efficiency of the ring section furnace together with a reduction in the amount of gases exhausted from the furnace. According to the invention, this is achieved by a device characterised in that the entrance of false air from the first chamber adjacent the preheating zone is eliminated by the arrangement of a counterpressure fan in connection with the first chamber. In the following a more detailed description of the invention will be made by the use of an example and with reference to the attached drawings in which: Fig. 1 shows the principles of a ring section furnace with a cooling zone, a combustion zone and a preheating zone. Fig. 2 shows in perspective a ring section furnace on an enlarged scale with a cut through a chamber. Fig. 3 shows a ring section furnace with a cut through a chamber, and with a counterpressure fan arranged according to the invention. Fig. 1 shows a principal drawing that describes the course of events in the process. An exhaust fan 3 in a pipe connection 1, or possibly an exhaust fan (not shown) connected to a ring duct (not shown) at a distant location, sucks combustion air through the cooling zone K10-K8 and further through the combustion zone K7-K4 where it is combusted together with fuel. The combustion gases that are formed in the combustion zone are then sucked through the preheating zone K3-K2 and led to the ring duct 10. The exhaust fan 3 is connected to K2, and thus the sub-pressure is strongest in this area. Followed by this, the exhaust fan sucks false air from the A-part 8 in the chamber K1, and consequently an underpressure is formed in the A-part 8. Fig. 2 shows a ring section furnace with a cut through a chamber having chamber walls 15, cassettes 18, cassette walls 2 and flue gas channels 5. Below the bottom of the cassettes 18 there is arranged a dividing wall 6 that divides the room below the cassettes in two parts, a A-part 8 and a B-part 7. Hereby, the flue gases in the flue gas channels are led upwards in the A-part 8 and downwards in the B-part 7 in the chambers K10-K2, and in the opposite direction in chamber K1, where false air is sucked from chamber K1 to chamber K2. In the example shown in figure 2, the lid 16 above the chamber is connected to the ring duct 10 through the pipe connection 1, wherein there is arranged a closing device 11, together with the exhaust fan 3. Fig. 3 shows the exhaust fan 3, together with a counterpressure fan arranged according to the invention, either provided with a pipe connection exhausting the gases above the roof (not shown), or to the ambient environment. In case the exhaust from the counterpressure fan contains gases, these gases may be led through a pipe connection and the ring duct (not shown) to a purifying plant. The counterpressure fan 17 is equipped with a differential pressure sensor (not shown) that is connected to the A- and B-part in chamber K1 through lines or hoses 9. The top of the chamber is covered with a sheet of plastic material. The counterpressure fan 17 connected to the furnace shaft in the chamber wall adjacent the B-part in chamber K1, is controlled by the pressure difference in the A- and the B-part in chamber K1 by means of a frequency converter (not shown). The application of the counterpressure fan leads to a substantial elimination of the sucking of false air from chamber K1 to chamber K2 by the exhaust fan 3. This results in that a better control with the combustion process, and thus the temperatures in the furnace, is achieved. Further, with this provisions, the total amount of gas sucked through the ring duct 10 is substantially reduced, and thereby the amount of gas to be purified is decreased. Finally, this leads to a reduction in the investment-and the operation costs of the exhaust gas purifying plant.

Claims: Device for a ring section furnace for the calcination of carbon bodies, comprising a number of chambers (K1-Kn) wherein the carbon bodies are placed when performing the calsination process, and where, during said process, a part of the furnace that comprises a minor number of chambers is divided into a preheating zone (K3-K2), a combustion zone (K7-K14), and a cooling zone (K8-K10) that together and in a successive manner are advanced as to the furnace, whereby flue gases formed under the process are sucked out from the first chamber (K2) in the preheating zone through a pipe connection to a common ring duct (10), characterised in that a counterpressure fan (17) is arranged in connection with the first chamber (K1) to eliminate the entrance of false air from the first chamber (K1) adjacent the preheating zone. Device in accordance with claim 1, characterised in that the counterpressure fan (17) is controlled on the basis of the pressure difference in the A- and the B-part in the first chamber by means of an frequency converter.

Inventors: ASPERHEIM MAGNE, BOSDAL AUDUN, WERGE-OLSEN ARNE, ASPERHEIM, MAGNE, BOSDAL, AUDUN, WERGE-OLSEN, ARNE
Applicants: NORSK HYDRO AS, NORSK HYDRO ASA
Application year: 1996
Main classification: F27B13
IPC codes: C04B35, F27B13, F27B3