ROTARY KILN ARRANGEMENTS

Abstract: A rotary kiln in which reaction is to occur between coun­ terflowing reactants and an injector for a reactant extends into a reaction zone in the kiln. The injector is provided with means for adjusting the temperature of the injected reactant to a tem­ perature in the desired range for that zone. Further means are provided for maintaining a temperature in the desired range throughout the zone. The arrangement may be used in the pro­ duction of uranium oxides from uranium hexafluoride.

Description: Rotary Kiln Arrangements This invention relates to kiln arrangements. The invention has particular, although not exclusive, applications in relation to the manufacture of uranium dioxide. A problem that can arise in such manufacture is that, if the kiln arrangement is too hot, the physical properties of the uranium dioxide manufactured can be defective insofar as they do not allow for satisfactory handling in subsequent processes. On the other hand, if the kiln arrangement is too cold, the uranium dioxide can have too high a fluorine content. According to the present invention a rotary kiln arrangement, in which a reaction is to occur between counterflowing reactants, and an injector for at least one reactant extends into a reaction zone of the kiln arrangement, is provided with means for maintaining the temperature throughout that zone within a desired range and said means includes means for adjusting the temperature of the injected reactant to a temperature within the desired range while it is in the injector. Preferably, the injector comprises an elongate tube which contains at least one longitudinally disposed electrical heater. Advantageously, the electrical heater has elements which are adjustable to control the temperature of the injected reactant. Conveniently the kiln arrangement includes a temperature sensing array (which may be disposed in generally parallel relationship to the injector) to provide a signal whereby the temperature of the injected reactant is controlled. An embodiment of the present invention will now be described by way of example only with reference to the accompanying drawings in which: Figure 1 is a general elevation, Figure 2 is an incomplete vertical section looking out of the paper as compared to Figure 1 and including a part which is schematic, Figure 3 is a section on III-III of Figure 2 on a different scale, and Figure 4 is an incomplete section of components shown in Figure 2. Reference is directed first to Figure 1 in which a rotary kiln is shown on a supporting framework 4. The kiln has an inclined barrel 1, and an inlet chamber 2 with an associated disentrainment section 10. The inlet chamber connects with the upper end of the barrel I and is provided with an inlet jet 5 for gaseous reactants. At the lower end of the barrel 1 is a discharge hopper 3 through which extends another reactant inlet 6. A further reactant inlet (not shown) is also provided. The kiln barrel has electrical heater units 7 disposed around its periphery. Three such heater units are shown around its periphery in the Figure. Bearings 8, not shown in detail in Figure 1, allow for rotation of the kiln and also for longitudinal thermal expansion thereof. Filters 9 are provided above the disentrainment section 10. Reference is now directed to Figure 2, which shows in more detail that part of Figure 1 about the discharge hopper 3. Part of bearing 8 attached to this end of the kiln is indicated by 20, and a seal between the kiln and the discharge hopper 3 by 21. The seal 21 is such that relative movement between the discharge hopper 3 and the kiln is allowed without leakage, as would occur during thermal expansion. The direction of such movement of the kiln 1 is indicated by X in the Figure. A steam inlet pipe 22 is supplied with steam via a connecting flange 23. The pipe 22 feeds into a heater tube 24 which contains electrical heating elements 25 and 26. These elements are generally U-shaped, a curved part being seen in connection with heating element 25 at 27, and are supported along the length of the heater tube by spacer grids 28. Also contained within the heater tube 24 and likewise held by the grids is a thermocouple 29 which is sleeved by a protective sleeve 30. Electrical connections for the electrical heaters and thermocouple are provided in a connector box 31, connections for the heaters being seen at 32. Control wires for the electrical heaters 25 and 26 may be operated from a control box 33, whereto may also be fed the output signal from the thermocouple 29. A further thermocouple for use in the kiln is generally indicated by 38. The thermocouple 38 is held in position by a spring bias provided by a spring 39 and a locknut arrangement 40. The tube 24 is sealed in the kiln by a cap 41. Steam emerges from the tube 24 through holes 42. The configuration on the heater elements 25 and 26 can be more clearly seen in Figure 3 in which like references to Figure 2 are used for like parts. Referring now to Figure 4, in which like reference numerals to preceding Figures are used for like parts, there is shown in some detail the joint between the heater tube 24 and the electrical connector box 31. The heater tube 24 is welded to a plate 50 by two welds indicated by 51 and 52. The plate 50 is secured to part of the connector box 31 by means such as bolts (not shown). A gasket 53 is disposed between the plates 50 and box 31 to ensure that the joint is gastight. Sheaths for the heater elements 24 and 25 are indicated by 54. The sheaths 54 are affixed to the box 51. The thermocouple protective sleeve 30 is welded to the box 51 by means of welds 55. The thermocouple 29 does not itself contact the box 51. Operation of the kiln arrangement is now described with reference to. all of the Figures. Uranium hexafluoride and dry steam are injected into the kiln by means of the inlet jet 5. The uranium hexafluoride and dry steam issuing together from the nozzle of the jet react together in the form of a plume which is directed towards the upper end of the kiln barrel 1. Typically the steam temperature is 15O0C, the uranium hexafluoride temperature 900C and, because the reaction between them is exothermic, the temperature in the plume reaches 500-6000C. The uranyl fluoride which is produced by the reaction is deposited in the upper end of the kiln barrel 1 which is rotated in use. In passing down the barrel 1 of the kiln the uranyl fluoride is reacted at a higher temperature (600-7500Celsius) with a steam/hydrogen mixture to produce uranium oxide powder. The required temperature is maintained in the kiln by the heater units 7. The use of a series of heater units enables the establishment of a required temperature gradient along the length of the kiln barrel 1. Steam is fed into the lower end of the kiln barrel 1 through the inlet 6 (described in more detail above with reference to Figure 2 and also below)and hydrogen is passed through an inlet into the discharge hopper 3. Lifting flights (not shown) in the kiln barrel 1 tumble the uranyl fluoride powder and cause it to move in a generally downwards path in countercurrent flow to the steam/hydrogen mixture passing upwards through the kiln barrel. Lifting and tumbling motion of the uranyl fluoride powder ensures efficient solids/gas contacting and rapid and efficient conversion of the uranyl fluoride powder into uranium oxide powder. The uranium oxide produced falls into the discharge hopper 3 and is discharged for further processing. The temperature of steam entering the kiln barrel 1 through the inlet 6 may be controlled by operation of the heater elements 25 and 26, in response to signals from the thermocouples 29 and 38, with or without help from the control unit 33. The object of the control is to limit the radial distribution of heat to a minimum, that is 15-20 Celsius, between the centre of the kiln barrel and the periphery. If steam is allowed to enter the kiln barrel at too low a temperature the input from the heater units 7 has to be increased to compensate if too high a fluorine concentration is to be avoided in the uranium oxide product and a large radial distribution of heat results. The effect is a temperature at the periphery of the kiln barrel, which is so high that desirable physical properties of the uranium oxide product may be impaired. The temperature of the steam as it is injected into the kiln barrel is therefore matched to that which is preferred for the reaction occurring in the region of the kiln barrel about the inlet 6 and the heater units 7 are likewise controlled. The mechanical structure of the heater tube 24 is such that it does not foul any other component in the kiln when thermal expansion of itself or the kiln takes place. Nonetheless, a gas-tight seal is always provided between components in the kiln. The heater tube 24 does not itself rotate as it is secured to the discharge hopper 3. It is also constructed so as not to foul any rotating components of the kiln. With the construction of electrical connector box shown no access is provided for steam to enter within the box 31. This is because all access points are sealed as by the sheaths 54 for the heater elements 25, 26 and the weld 55 between the thermocouple sleeve 30 and the box 31. Steam cannot escape from between the box 31 and plate 52 because of the gasket 53 which blocks this possible escape route.

Claims: Claims. 1. A rotary kiln arrangement in which a reaction is to occur between counter-flowing reactants, and an injector for at least one reactant extends into a reaction zone of the kiln arrangement, characterised in that there is provided means for maintaining the temperature throughout that zone within a desired range and said means includes means for adjusting the temperature of the injected reactant to a temperature within the desired range while it is in the injector. 2. A rotary kiln arrangement as claimed in claim 1 characterised in that the desired range is 600-75O0C. 3 - A rotary kiln arrangement as claimed in claim 1 or claim 2 characterised in that the injector comprises an elongate tube and means for adjusting the temperature of the injected reactant comprises a longitudinally disposed electrical heater contained within the tube. 4. A rotary kiln arrangement as claimed in claim 3 characterised in that a temperature sensing array disposed in generally parallel relationship to the injector is provided to control said heater.

Inventors: HAYES, MICHAEL RICHARD
Applicants: BRITISH NUCLEAR FUELS PLC
Application year: 1982
Main classification: F27B7
IPC codes: F27B7, C01G43, B01J19, F27D21