fig1 shows a storage area ( 1 ) with combustible dust , which represents a silo with a filter ( 2 ) on it . this could be , for instance , a silo for wood chips , wood pellets , wood shavings , grain , feed , fertilizer , or other materials . the filter ( 2 ) separates the ex - zone from the non - ex - zone . it ensures , for example , in the case of storage or transport of wood particles ( wood chips , wood pellets , wood shavings , and similar materials ) a concentration of , for example , 30 g of wood dust per cubic meter for a particular range of particle sizes is not exceeded . detection of a failure of function of the filter ( 2 ) as a result of damage or puncturing which could result in exceeding the ignition limit of the aspirated air - dust mixture must be guaranteed . for this reason the filter ( 2 ) is monitored by the filter monitoring unit ( 4 ), which contains a malfunction monitoring sensor ( 14 ) and a signal processing unit ( not shown ). the air - dust mixture is aspirated via the filter ( 2 ) and the suction pipe ( 3 ) through the aspirator ( 8 ), which is located in the aspirating smoke detector system ( 7 ). in order to ascertain burning characteristics one or more sensors ( 6 ) for detecting burning characteristics are mounted in the aspirating smoke detector system ( 7 ). in the present case , there are three different sensors ( 6 ) which detect different burning characteristics . the air - dust mixture being monitored is led back into the storage area ( 1 ) for combustible dust by means of an air flow return pipe ( 9 ). to the extent required by pressure conditions , by implementing additional appropriate measures such as non - return valves , the direction of flow from the aspirating smoke detector system ( 7 ) to the storage area ( 1 ) can be ensured ( not illustrated ). a fire alarm is set off as soon as burning characteristics are detected by one or more sensors ( 6 ). in this configuration given as an example the entry opening of the suction pipe ( 3 ) is directly connected with the filter ( 2 ). it is advantageous to position the malfunction monitoring sensor ( 14 ) directly at the filter ( 2 ) in the aspirated air - dust mixture in the suction pipe ( 3 ), as shown in fig3 . in an additional advantageous configuration , the filter ( 2 ) is located in the suction pipe ( 3 ) or in a separate filter monitoring unit ( 4 ) between the ex - zone and the aspirating smoke detector system ( 7 ) in the aspirated air flow , as shown in fig2 . the filter ( 2 ) can be replaceable . replacement of the entire filter monitoring unit ( 4 ) is also a configuration variant . a significant feature of the invention is that as soon as the malfunction monitoring sensor ( 14 ) detects that , for instance , the filter ( 2 ) is not working because of damage or a leaky spot , action is taken to ensure that the air - dust mixture with increased dust concentration which may exceed the explosive limit cannot reach the sensors ( 6 ) and cannot enter the aspirating smoke detector system ( 7 ). the malfunction monitoring sensor ( 14 ) is connected to the signal processing unit ( 15 ). this has threshold values stored for ignitable dust concentrations and / or warning threshold values and / or threshold slope values . in the configuration variants shown in fig2 and fig3 this signal processing unit ( 15 ) is mounted separately from the aspirating smoke detector system ( 7 ) in the filter monitoring unit ( 4 ). however , it can also be advantageous that this function of the signal processing unit ( 15 ) is carried out by the signal processing unit ( 15 . 1 ) of the aspirating smoke detector system ( 7 ). this variant is not shown in the figures . the threshold value for an explosive wood dust concentration , for instance , is higher than 30 g of dust per cubic meter of air . it can , however , be advantageous to specify threshold values below the explosive concentration , for example , early warning thresholds of 90 %, or 80 % or 70 % of the explosive dust concentration . in a preferred configuration the malfunction signal is generated when 80 % of the ignition limit value is measured in the aspirated air - dust mixture or a sudden rise of dust concentration is registered . if the malfunction monitoring sensor ( 4 ) indicates that predetermined threshold values have been exceeded , the signal processing unit ( 15 ) generates a malfunction signal . this malfunction signal indicates loss of function of the filter ( 2 ). fig2 shows an advantageous configuration in which the malfunction monitoring sensor ( 14 ) and the signal processing unit ( 15 ), as well as the filter ( 2 ) are integrated into the filter monitoring unit ( 4 ) mentioned above . if the filter ( 2 ) is destroyed , the malfunction signal triggers actions which prevent ingress of the aspirated air - dust mixture with elevated ignitable dust concentration into the aspirating smoke detector system ( 7 ). in the configuration shown schematically in fig2 the subsequent action in case of a malfunction is activation of a valve ( 16 ) such as a flap which seals off entry of air flow from the aspiration process into the aspirating smoke detector system ( 7 ). fig3 is a schematic presentation of a system with a malfunction monitoring sensor ( 4 ) and a signal monitoring unit ( 15 ) in which the malfunction signal from the signal processing unit ( 15 ) is transmitted to the signal processing unit ( 15 . 1 ) of the aspirating smoke detector system ( 7 ) and aspirator ( 8 ) and / or the entire aspirating smoke detector system ( 7 ) is shut down . as a result , the aspirated air - dust mixture , marked here with arrows , comes to a full stop . shutting down can be carried out by means of the switch ( 5 ) or other switching elements , or by means of a fire detection and control cabinet which receives a radio signal from the filter monitoring unit ( 4 ) ( not shown ). this reacts without delay by switching off the aspirator ( 8 ) and / or the entire aspirating smoke detector system ( 7 ) and reports the current state of the equipment to a process control unit ( not shown ). after the shutdown the aspirator ( 8 ) and the aspirated air - dust mixture in the suction pipe ( 3 ) does not suddenly come to a stop . the shutdown time until the aspirator ( 8 ) has come to a full stop has to be taken into account . as a result , in this advantageous configuration ( fig3 ) the length l of the section of the suction pipe ( 3 ) between the filter ( 2 ) and the aspirating smoke detector system ( 7 ) is calculated in such a way that no ignitable atmosphere can enter the aspirating smoke detector system ( 7 ) during and after the shutdown procedure . the length l of this section of the suction pipe ( 3 ) is thus dependent on the transport velocity of the aspirated air - dust mixture and the time until the transport velocity is nearly 0 m / s . with this design length no aspirated air - dust mixture enters the aspirating smoke detector system ( 7 ). with a transport velocity in the suction pipe of , for example , 1 m / s and a shutdown time of 5 s , this section of the suction pipe would have to have a length l of 5 m . the shutdown time is the period of time from the filter damage / filter rupture to cessation of transport of the aspirated air - dust mixture in the suction pipe ( 3 ). in this example it was assumed that the malfunction monitoring sensor ( 14 ) was located directly on the filter ( 2 ). if this malfunction monitoring sensor ( 14 ) is located at a given distance from the filter ( 2 ), the length of the section of the suction pipe ( 3 ) described above is increased by this distance . the length given above as an example is an estimate which assumes a constant velocity until the end of the shutdown time , i . e ., until the aspirator comes to a full stop . in the case of more exact calculations the time dependence of the velocity v ( t ) must be taken into account . a further advantageous configuration in regard to subsequent action is shown in fig4 . here the malfunction signal from the signal processing unit ( 15 ) controls one or several flaps and / or valves ( 16 ) which close the suction pipe ( 3 ) in the direction of the aspirating smoke detector system ( 7 ), and open a bypass pipe ( 17 ) or an emergency valve ( not shown ) for the aspirated air - dust mixture , and lead this into a container ( 18 ) or simply into the surrounding environment . this function can be implemented using two flaps / valves ( 16 ) or through a combined component such as a 3 / 2 - way valve , as shown in fig4 . activation of the flap / valve ( 16 ) prevents ingress of the aspirated air - dust mixture into the aspirating smoke detector system ( 7 ). fig5 demonstrates further development of the device from fig1 , which involves an additional filter ( 10 ) linked to a separator ( 11 ) between the storage area ( 1 ) for combustible materials and the aspirating smoke detector system ( 7 ). here the filter monitoring system is supplemented by the additional specified components . an alarm ( 12 ) such as a siren , a horn , or a fire detection and control cabinet is mounted behind the aspirating smoke detector system ( 7 ). furthermore , in addition to the aspirating smoke detector system ( 7 ) a release valve for an extinguishing agent ( 13 ) with an appropriate fire extinguishing system is mounted , which is an advantageous configuration variant if upon identification of burning characteristics a fire is to be extinguished in the storage area ( 1 ) for combustible materials . when a fire is detected , this extinguishing agent release valve ( 13 ) is directly controlled by the aspirating smoke detector system ( 7 ) or by a fire detection and control cabinet to release the extinguishing agent . a further configuration variant of the device in fig1 is shown in fig6 . in this configuration a signal from the malfunction monitoring sensor ( 14 ) via the signal processing unit ( 15 ) activates a flap and / or valve ( 16 ). this valve opens a pressurized reservoir ( 19 ) containing inerting gas such as nitrogen . this is added to the aspirated air - dust mixture and thus reduces the explosive threshold in the enclosed environment of the aspirating smoke detector system ( 7 ). as a result , continued detection of burning characteristics is made possible . instead of inert gas , uncontaminated air from the ambient atmosphere can also be used with a pump to dilute the aspirated air - dust mixture . enclosed environments with potentially explosive atmospheres ( ex - zone )/ storage and transport areas for combustible materials with dust formation signal processing and controlling unit of the malfunction monitoring sensor ( 14 ) 15 . 1 signal processing and controlling unit of the aspirating smoke detector ( 7 )