Mobile incinerator system for low level radioactive solid waste

Abstract: Mobile incinerating system for low level radioactive solid wastes, consisting of an installation mounted on a mobile platform and consisting of a rotating combustion chamber (3) into which the wastes to be incinerated are to be inserted from a feeder (1) equipped with a loader (2). The rotating chamber (3) communicates with a post-combustion chamber (5). Between these two chambers there is a third gas transit chamber (7) from which the ashes produced drop into a lower collector (9) after having passed a tray (8) fitted with two alternately operating gates. Downstream of the chambers there is a first dilutor (10) followed by a heat exchanger (6) associated with fans (11). Immediately downstream of the heat exchanger (6) is a decanter (12) followed by a second dilutor (13) from which the gas mixture passes through filters (14). The level of activity of the gases is controlled by means of a monitor (15) located downsteam of the filter (14).

Description: The invention described herein is a mobile incinerator system for low level radioactive solid wastes, contemplating both radiological and other conventional aspects, and whose obvious aim is to reduce low level radioactive solid wastes on the basis of a process of pyrolytic incineration. The system may be said to be based on a mobile or transportable installation mounted on platforms with a view to allowing its use in different locations, consequently the overall assembly should be considered as a component integrated into the overall process of treatment and conditioning of solid wastes. The document GB-A-1,037,587 concerns a radioactive residue incineration plant which is a complex static installation. In this plant, the separation of the products to be discharged from the gas is mainly accomplished by a cyclone and the neutralization of the gas is accomplished by a neutralization tower. The discharge system used in this plant is very complicated due to the fact that the wastes to be discharged from the plant are produced at different locations distant from one another. Therefore the complicated structure of the plant disclosed in this document is not adapted for realizing a mobile incinerating system. The document DE-A-3,404,933 discloses a mobile incinerating system for low level radioactive wastes which comprises also a cyclone for the separation of the products to be discharged from the gas and a washer device which is adapted to neutralize the materials eventually produced by thermomechanical reactions and which may damage the filters. One of the objects of the present invention is to provide a mobile incinerator system which comprises a number of devices as small as possible and which should have a structure as simple as possible. Consequently, the mobile incinerating system for low level radioactive solid wastes according to the invention is a system being mounted on a mobile or transportable platform comprising a combustion chamber, a separator system to separate the solid particles from the gas, an ash-collecting tray for the recuperation of the solid particles separated from the gas, a gas neutralizer, a heat exchanger device disposed downstream of the combustion chamber and upstream of the gas neutralizer, a filtration device situated downstream of the gas neutralizer, and a control device of the activity rate of the gas expelled from the filtration device, characterized in that the separator system comprises a gas passage chamber for the decanting and the removal of ash and inert materials, this gas passage chamber being situated at the exit of the combustion chamber, and a gas neutralizer, this gas neutralizer comprising means to spray a neutralizing solution on the hot gas emitted from the combustion chamber and a device to collect the products separated from the gas, this device being connected to the combustion chamber by recycling means for recycling these separated products into the combustion chamber, and in that the ash-collecting tray is situated under the gas passage chamber. Another characteristic of the mobile incinerating system according to the invention is that the gas is expelled from the heat exchanger device at the working temperature of the gas neutralizer. Still another characteristic of the mobile incinerating system according to the invention is that it comprises a post-combustion chamber situated above the gas passage chamber in the flowing path of the gas towards the gas neutralizer. A supplementary characteristic of the mobile incinerating system of the invention is that the combustion chamber is a rotating combustion chamber. A feature of the mobile incinerating system of the invention is that the heat exchanger device is a gas-atmospheric air heat exchanger, the hot air expelled from this heat exchanger being injected into the combustion chamber. Another feature of the mobile incinerating system of the invention is that the hot air expelled from the heat exchanger is injected into both combustion and post-combustion chambers. Furthermore a gas diluter is situated between the post-combustion chamber and the heat exchanger device. The mobile incinerating system of the invention comprises also a second gas diluter situated downstream of the gas neutralizer, the exit of this second gas diluter being connected to the filtration device. The control device of the mobile incinerating system of the invention includes an activity monitor with two actuation signals designed to avoid the permissible limit of activity being exceeded, such that in the case of limit being exceeded the corresponding alarms are generated. In the mobile incinerating system of the invention the gas passage chamber for the decanting and the removal of inert materials is conceived to impart to the high speed gas flow a change of its flow direction. A last characteristic of the mobile incinerating system of the invention is that the passage chamber has a gas flow inlet opening having an horizontal axis, an outlet opening having a vertical axis, located above the inlet opening and substantially vertical particle collecting wall provided opposite to the inlet opening. The solid wastes in question, which may be incinerated using the system described herein, may be for example wood-plastic having a calorific value lower than : 19,37 kJ/kg (4,631 kcal/kg), plastified paper with a calorific value of lower than : 16,89 kJ/kg (4,037 kcal/kg); activated carbon with a calorific value lower than : 23,01 kJ/kg (5,500 kcal/kg); textile materials with a calorific value of less than : 15,05 kJ/kg (3,597 kcal/kg); resins, etc. Given that the production of incinerable low level wastes increases significantly during plant shutdowns for refuelling, optimum use of the system will be during such outages, in order to avoid important increases of the number of drums containing low level incinerable materials. The system described herein allows reductions in the volume of wastes of a proportion of 1/60 to 1/70 to be achieved. The system is made up of a rotating combustion chamber in which the wastes are inserted from an externally mounted independent feeder, into which they are introduced into plastic bags. This rotating chamber communicates with a second, post-combustion chamber in which a thermal reaction with the gases coming from the rotating chamber occurs, this eliminating a large part of the volatile materials not burned by combustion or decanted inert materials. Combustible hot air is injected into both chambers from a gas-air exchanger located downstream of these chambers. A third chamber is located between the two described above into order permit the removal and decanting of ashes and inert materials. Downstream of the post-combustion chamber there is a diluter at whose outlet there is a detector designed to assure a relatively constant temperature in the heat exchanger located downstream of it. This heat exchanger is fed by a fan taking up atmospheric air which is used to cool the gases in such a way that the hot air from the heat exchanger is injected into the combustion chambers, with excess air being expelled from the system. Downstream, there is a dust and ash decanter from which these products are removed to be rechannelled to the combustion chambers. A second dilutor is located downstream of the decanter, and is used to mix the gases with atmospheric air in order to achieve an adequate temperature for the gases as they pass through a filtration stage. Immediately downstream of the filters there is a gas activity control stage based on a detector having two actuation signals and designed in order to prevent the permissible gaseous effluent activity limit being exceeded. In order to facilitate greater understanding of the characteristics of this invention, a detailed description is presented below. This description is based on a sheet of drawings accompanying this report and forming an integral part of it, and which includes an orientative non-limiting general diagram of the installation on which the incineration system described herein is based. The figure shows that the installation begins with a feeder 1 in which the waste materials to be incinerated are inserted in plastic or paper bags weighing approximately 8 kg. This feeder 1 is equipped with an automatic loading device 2 into which the wastes are inserted, and which is totally isolated from the corresponding rotating combustion chamber 3. Access to this chamber is via an opening operated by an electric pulser, which acts on an oleohydraulic cylinder automatically driving the load gate. After inserting the waste into the loader 2, the pushbutton is operated in the closed position until total hermetic closure is achieved. At this moment, and simultaneously, a piston pushes the wastes towards the inside of the furnace while a chopper gate is lifted in order to permit access to the furnace. On completion of the cycle, the piston is withdrawn and the chopper gate is lowered, thus isolating the combustion chamber 3 once more. The wastes are inserted regularly into the combustion chamber 3 in which the combustion phase occurs in a reducing atmosphere, this producing technical pyrolysis of the wastes and the distillation of high combustion power gases. Feed is interrupted when the temperature of the chamber reaches its maximum permissible temperature (approx. 800/900°C). When the system working temperature (approx. 600°C) is reached the auxiliary combustion burner 4 is automatically stopped. The gases produced in the rotating chamber 3 are channelled to a second post-combustion chamber 5 where a thermal reaction takes place in an oxidizing atmosphere, thus eliminating a large part of the volatile materials not burned by combustion and inert materials arising through the settling process that occurs due to the reduction in gas-flow speed. Hot combustion air from the gas-air heat exchanger 6 is injected into both chambers 3 and 5. Located between the rotating combustion chamber 3 and the post-combustion chamber 5 there is a gas passage chamber for the removal and decanting of ash and inert materials. The slag material decanted by gravity drops into an automatic ash-collecting tray 8 which is oleohydraulically driven and fitted with two opening-closure gates which operate alternately in order to empty the tray on a timed basis into a collector 9, which automatically closes when the previously established level is reached. In this collector 9 the ashes are cooled in order to allow subsequent drumming. The gases are then channelled to a metallic chamber or dilutor 10 in which they are mixed with atmospheric air entering via a servo-driven gate operated by means of a signal generated by the detector located at the dilutor outlet. This assures a constant temperature of 900/1,000 °C in the heat exchanger 6 located downstream. At the outlet of the dilutor, or dilution chamber 10, is the gas-air heat exchanger 6 designed to reduce the temperature. A fan 11 uses atmospheric air to cool the gases, achieving a reduction in temperature to 250/300 °C. The hot air from the heat exchanger 6 is exploited as combustion air for injection into the combustion chambers, excess air being expelled from the system. Following the gas temperature reduction process, the gases are neutralized; a controlled liquid solution is sprayed over the gases. The neutralized gas and ash settle at the bottom of the neutralizer 12, from where they are removed and transferred to the combustion chambers for elimination. In order to assure that the temperature of the gases in the filtration stage is adequate, these gases are mixed with atmospheric air in a metallic chamber or dilutor 13. The air is inserted via a servo-driven gate which is operated by means of a signal from the detector located at the outlet of the dilutor. Following dilution of the gases, the resulting mixture is filtered through two series-mounted HEPA filters 14 with a degree of efficiency per filter of 99.9 % for particles of 0.4 micrometres. Following filtration of the gases, their level of activity is controlled. In this respect, an activity monitor 15 is used which provides two actuation signals assuring that the appropriate gaseous effluent permissible activity limits are not exceeded at any time. If the concentration of activity emitted were to reach this limit, the monitor alarm would trip and shut down the system. Finally, the gases are extracted by means of a centrifugal fan which takes the gases resulting from the incineration process and channels them towards the emission stacks 15. The installation described above is mounted on a mobile platform which can be transported at any time to whatever location might be desired or required, this making it possible, for example, for certain companies or factories to avoid the need for a fixed, permanent installation for purely periodical and sporadic use. The system control components are as follows: a.- Temperature : Both the combustion chamber 3 and post-combustion chamber 5 are equipped with a twin setpoint thermocouple detector designed such that the first setpoint automatically shuts down the burners and the second blocks the feed system 1. In order to control the temperature of the smoke at the inlet to the filters 14, a detector is installed which acts on a proportional servo-motor designed to open or close the dilutor 13 air inlet gate, thus maintaining the temperature constant. b.- Dirty filters : These are controlled by means of a pressurestat which generates a signal when the gas pressure through the filters decreases, actuating optical and acoustic alarms and thus indicating the need to change the filters and the corresponding bypass to the standby filter. c.- Activity of emitted smoke : The activity detector 15 makes it possible to control the concentration of activity and total activity of the smoke released. This detector 15 has two setpoints, an initial pre-alarm signal acts on the following elements: Shutdown of the rotating combustion chamber 3 burner 4. Shutdown of the chamber drive system, and automatic closure of the combustion air dumper. Blocking of the waste loading sytem. When the level of activity reduces to the correct limits, all the above elements are automatically reactivated, and the installation is ready for new loads. If in spite of pre-alarm actuations the level of contamination increases, the alarm is generated and shuts down the following elements; Shutdown of the post-combustion burner, and closure of the compressed-air dumper. Opening of the dumper, permitting hot air to be extracted. Total opening of the combustion chamber air inlet gate. Once the levels of contamination reach their permitted values, the installation or system self-regulates and comes into service automatically or manually.

Claims: Mobile incinerating system for low level radioactive solid wastes, the system being mounted on a mobile or transportable platform and comprising: a combustion chamber (3) a separator system to separate the solid particles from the gas, an ash-collecting tray (8) for the recuperation of the solid particles separated from the gas, a gas neutralizer (12), a heat exchanger device (6) disposed downstream of the combustion chamber and upstream of the gas neutralizer (12), a filtration device (14) situated downstream of the gas neutralizer (12), and a control device (15) of the activity rate of the gas expelled from the filtration device (14) characterized in that the separator system comprises: a gas passage chamber (7) for the decanting and the removal of ash and inert materials, this gas passage chamber (7) being situated at the exit of the combustion chamber (3), and the gas neutralizer (12), this gas neutralizer (12) comprising means to spray a neutralizing solution on the hot gas emitted from the combustion chamber (3) and a device to collect the products separated from the gas, this device being connected to the combustion chamber (3) by recycling means for recycling these separated products into the combustion chamber, and in that the ash-collecting tray (8) is situated under the gas passage chamber (7). Mobile incinerating system according to claim 1 characterized in that the gas is expelled from the heat exchanger device (6) at the working temperature of the gas neutralizer (12). Mobile incinerating system according to one of claim 1 or 2 characterized in that it comprises a post-combustion chamber (5) situated above the gas passage chamber (7) in the flowing path of the gas towards the gas neutralizer (12). Mobile incinerating system according to one of the preceding claims, characterized in that the combustion chamber (3) is a rotating combustion chamber. Mobile incinerating system according to one of the preceding claims, characterized in that the heat exchanger device (6) is a gas-atmospheric air heat exchanger, the hot air expelled from this heat exchanger being injected into the combustion chamber (3). Mobile incinerating system according to one of the claims 3 to 5, characterized in that the hot air expelled from the heat exchanger is injected into both combustion and post-combustion chambers (3,5). Mobile incinerating system according to one of the claims 3 to 5, characterized in that the gas diluter (10) is situated between the post-combustion chamber (5) and the heat exchanger device (6) Mobile incinerating system according to one of the preceding claims, characterized in that a second gas diluter (13) is situated downstream of the gas neutralizer (12), the exit of this second gas diluter (13) being connected to the filtration device (14). Mobile incinerating system according to one of the preceding claims, characterized in that the control device (15) includes an activity monitor with two actuation signals designed to avoid the permissible limit of activity being exceeded, such that in the case of limit being exceeded corresponding alarms are generated. Mobile incinerating system according to one of the preceding claims, characterized in that the gas passage chamber (7) for the decanting and the removal of inert materials is conceived to impart to the high speed gas flow a change of its flow direction. Mobile incinerating system according to claim 10, characterized in that the passage chamber (7) has a gas flow inlet opening having an horizontal axis, an outlet opening having a vertical axis, located above the inlet opening and a substantially vertical particle collecting wall provided opposite to the inlet opening.

Inventors: ROVIRA AUGE ANTONIO, ROVIRA AUGE, ANTONIO
Applicants: TECNICAS ESPECIALES DE REDUCCI, TECNICAS ESPECIALES DE REDUCCION, S.A.
Application year: 1988
Main classification: G21F9
IPC codes: G21F9, F23G5