an example of a deodorizing apparatus made according to the present invention is shown in fig1 and 2 . in fig1 and fig2 the reference character g denotes a gas mixture of a malodorous substance and air and the arrow indicates the flow direction of the gas mixture . the deodorizing apparatus 10 includes a lower 13 and an upper housing 14 on support legs 12 . the housings are hollow , and in the present instance are of sguare configuration to provide an upright flow passage 17 therethrough . upstream in the flow passage 17 , in the flow direction of the gas mixture g , the deodorizing apparatus is provided with a diffuser plate 40 of punched metal to provide a uniform distribution and rectification of the gas mixture of the malodorous substance and air throughout the entire cross section of the flow passage 17 . within the flow passage 17 there is an ozone - generating ultraviolet lamp 20 , generating uv rays below a critical wavelength for producing ozone from oxygen in the air , an ozone - decomposing ultraviolet lamp 30 generating uv rays above a critical wavelength for producing nascent and molecular oxygen from the oxygen , a catalyst layer support 11 for mounting thereon an air - permeable ozone - decomposing catalyst layer , and an axial flow fan 60 employed as means for inducing air streams in a predetermined direction through the passage 17 . at the upper end of the lower housing 13 , the wall of the housing is recessed at 11 to provide a support for an air - permeable ozone - decomposing catalyst layer 18 which can be mounted on the support 11 in a position where the catalyst layer is directly irradiated by the ozone - decomposing ultraviolet lamp 30 . in the preferred embodiment , the lamps 20 and 30 comprise elongated tubes spanning across the flow passages 17 between and generally parallel to the diffuser plate 40 and the layer 17 , the tubes being oriented perpendicular to each as shown . the air - permeable ozone - decomposing catalyst layer 18 consists of , for example , a transition metal oxide , like nickel oxide , a noble metal , like platinum , or a mixture of a transition metal oxide and a noble metal , which is supported on a carrier of cordierite or the like . in the present embodiment , a nickel oxide - base catalyst layer in the form of an air - permeable filter is used . the upper housing 14 is releasably attached to the upper end of the housing 13 to afford ready access to the layer 18 on the support 11 for servicing and / or removal and replacement . the ozone - generating ultraviolet lamp 20 generates an ultraviolet ray of a wavelength smaller than 200 nm , mainly of a wavelength of 185 nm . on the other hand , the ozone - decomposing ultraviolet lamp 30 mainly generates an ultraviolet ray of a wavelength of 254 nm . these two kinds of ultraviolet lamps 20 and 30 each include means for adjusting their intensity as indicated at 25 and 35 in fig2 . a flow of the gas mixture g which consists of a malodorous substance and air is generated by an air flow generating means , in the present case the fan 60 at the upper end of the housing 14 . ozone is produced by the ozone - generating ultraviolet lamp 20 from oxygen in the air to convert the gas mixture into an ozone - prevailing atmosphere . thereafter , the ozone which is produced by the lamp 20 is decomposed by the catalyst layer 17 and the ozone - decomposing ultraviolet lamp 30 to generate nascent state oxygen with extremely strong oxidizing power for oxidation / decomposition of the malodorous substance . as the ozone decomposition proceeds , the above - mentioned catalyst gradually loses its decomposing capacity due to a deteriorating reaction of the catalyst itself . however , according to the present invention the ozone - decomposing ultraviolet lamp 30 not only reduces the ozone to reduce the burden on the catalyst in decomposing the ozone , but also generates , by an ultraviolet ray ( especially of 254 nm wavelength ), nascent state oxygen which reacts inversely to the deteriorating reaction of the catalyst , thereby reactivating the catalyst and preventing its deterioration . thus , the deodorizing apparatus according to the present invention succeeds in advantageously incorporating the synergistic effects of the catalytic and ultraviolet decomposition systems which have been found to be insufficient in function when applied separately . the gas mixture g which is suctioned into the deodorizing apparatus 10 through the plate 40 by the axial flow fan 60 produces ozone as it is irradiated by the ozone - generating ultraviolet lamp 20 . the gas mixture g which now consists of ozone and a malodorous substance is then irradiated by the ozone - decomposing ultraviolet lamp 30 and admitted into the ozone - decomposing catalyst layer 17 which is also irradiated by the ozone - decomposing ultraviolet lamp 30 . as a result , the ozone is forcibly decomposed , thereby generating nascent state oxygen with extremely strong oxidizing power to decompose the malodorous substance in the gas mixture g . the ozone concentration in the gas mixture which is discharged from this operation is preferably smaller than 0 . 1 ppm from the standpoint of safety . for this purpose , the intensity of the ozone - generating ultraviolet lamp 20 of the deodorizer 10 is adjusted so as to maintain the ozone concentration in the gas mixture to a value smaller than 0 . 1 ppm . it is to be understood that the foregoing embodiment of the deodorizing apparatus has been shown and described by way of example , and , needless to say , it should not be construed as limitative of the present invention . the present inventors conducted the following experiments in order to confirm the effects of the deodorizing apparatus as disclosed in the foregoing embodiment , in which the catalyst deterioration was accelerated by the use of ozone in a high concentration of 300 ppm in the experiments for observation of the catalyst deterioration as well as in the experiments for observation of the action of the 254 nm ultraviolet ray on the catalyst . there was firstly conducted an experiment for measuring the variations in ozone decomposing capacity of the catalyst layer . shown in fig3 is an experimental apparatus for forcibly deteriorating the ozone - decomposing catalyst layer by means of high concentration ozone , in which indicated at 50 is an air - permeable ozone decomposing catalyst layer for forcibly decomposing ozone ; at 21 is an ozone - generating ultraviolet lamp for generating ozone from oxygen by the action of the ultraviolet ray ; and at 41 and 42 are diffuser plates of punched metal . a fan 62 is connected to an ozone generating chamber 71 to send air thereinto . the air which has been sent into the ozone generating chamber 71 by the fan 62 is formed into rectified or diffused streams by the diffuser plate 41 and is irradiated by the ozone - generating ultraviolet lamp 21 to generate ozone . the air which contains the generated ozone flows into an ozone - decomposing chamber 72 through a connecting duct 81 , in which the ozone - containing air is formed into rectified streams by the rectifier plate 42 and into contact with the ozone - decomposing catalyst layer 50 . indicated at 82 is a sampling pipe upstream of the ozone - decomposing catalyst layer 50 ; at 83 is a sampling pipe downstream of the ozone - decomposing catalyst layer 50 ; and at 84 a discharge pipe . in this experimental apparatus , the ozone - decomposing catalyst layer 50 employed as a carrier a ceramic filter with a three - dimensional structure of cordierite , supporting thereon a nickel oxide - base catalyst , and air was fed by the fan 62 at a volumetric flow rate of 2 liters / min . samples ( hereinafter s82 and s83 ) were taken through the sampling pipes 82 and 83 in an initial stage of the experiment , after a lapse of 50 hours and after a lapse of 100 hours , respectively , to measure the ozone concentration . in this experiment , the intensity of the ozone - generating ultraviolet lamp 21 was adjusted to generate ozone in a concentration of 300 ppm . the results of the experiments are shown in table 1 below . table 1______________________________________ s 82 ( ppm ) s 83 ( ppm ) ______________________________________initial stage 300 1 . 050 hours later 300 46100 hours later 300 98______________________________________ from these experimental results , it was confirmed that the ozone - decomposing capacity of the catalyst deteriorated with time . next , a comparative experiment was conducted to examine the deodorizing capacity of samples obtained from the layer 50 in the foregoing experiment , namely , a sample i of the ozone - decomposing catalyst layer in the initial stage , a sample ii of the ozone - decomposing catalyst layer after a time lapse of 50 hours , and a sample iii of the ozone - decomposing catalyst layer after a time lapse of 100 hours . fig 4 illustrates an apparatus which was used in the aforementioned comparative experiment . a cross - flow fan 61 is provided within a hermetically sealed chamber 70 of 216 litres in volume . the sealed chamber 70 is provided with a measurement hole 80 to be used for gas injection and sampling . the sample i was mounted in the place of layer 17 on the ozone - decomposing catalyst layer support 11 of the deodorizing apparatus 10 of figs . 1 and 2 and the apparatus was placed in the sealed chamber 70 . turning on the cross - flow fan 61 , hydrogen sulfide was slowly injected by means of an injector 90 while measuring the gas through a gas detector tube ( not shown ) to hold the hydrogen sulfide concentration at about 100 pp . thereafter , the ozone - generating ultraviolet lamp 20 and ozone - decomposing ultraviolet lamp 30 of the deodorizer 10 were energized , and at the same time the axial flow fan 60 was started . at predetermined time intervals , the hydrogen sulfide concentration in the sealed chamber 70 was measured by the gas detector tube . the same experimental procedures were repeated for the samples ii and iii . the results of experiments on the samples i to iii are shown in tables ii to iv , respectively . fig6 shows the hydrogen sulfide removal rates which were obtained from the results of these experiments . table ii______________________________________ ( sample i ) time ( hr ) h . sub . 2 s concentr &# 39 ; n ( ppm ) removal rate (%) ______________________________________0 112 01 21 812 7 943 0 100______________________________________ table iii______________________________________ ( sample ii ) time ( hr ) h . sub . 2 s concentr &# 39 ; n ( ppm ) removal rate (%) ______________________________________0 98 01 38 612 21 793 12 884 5 955 1 99______________________________________ table iv______________________________________ ( sample iii ) time ( hr ) h . sub . 2 s concentr &# 39 ; n ( ppm ) removal rate (%) ______________________________________0 108 01 60 442 43 603 28 744 22 805 14 87______________________________________ it was confirmed from the results of the foregoing experiments that the capacity for decomposing the malodorous substance dropped with deterioration in the ozone decomposing capacity of the catalyst . accordingly , in order to carry out the deodorizing operation effectively , it is necessary to prevent the deterioration of the ozone - decomposing catalyst layer which occurs as a result of ozone decomposition . the following experiment was conducted next to examine the effects of the ultraviolet ray of 254 nm in wavelength which acts as a means for preventing the catalyst deterioration in the ozone decomposition . fig5 shows the apparatus employed for experiment iii , which has a fan 63 attached to one side of an ozone - generating chamber 73 for sending air thereinto . provided within the ozone - generating chamber 73 are a diffuser plate 43 of punched metal and an ozone - generating ultraviolet lamp 22 . provided in an ozone - decomposing chamber 74 are a diffuser plate 44 of punched metal , an ozone - decomposing ultraviolet lamp 32 adapted to generate an ultraviolet ray mainly of 254 nm wavelength , and an ozone - decomposing catalyst holder 52 located in a position which is directly irradiated by the ozone - decomposing ultraviolet lamp . the ozone - decomposing chamber 74 is communicated with the ozone - generating chamber 73 through a connecting duct 85 . denoted at 86 is a sampling pipe upstream of the ozone - decomposing catalyst layer ( not mounted in fig5 ); at 87 is a sampling pipe downstream of the ozone - decomposing catalyst layer ; at 88 is a discharge pipe ; and 89 is a sampling pipe downstream of the ozone - generating chamber 73 , and upstream of the chamber 74 . firstly , without mounting the catalyst on the ozone - decomposing catalyst holder 52 , air was fed by the fan 62 at a volumetric flow rate of 2 liters / min , and simultaneously the ozone - generating ultraviolet lamp 22 was turned on , while adjusting the ozone concentration to 300 ppm . then , the ozone - decomposing ultraviolet lamp 32 was turned in , measuring the ozone decomposing capacity of the 254 nm wavelength ultraviolet ray alone from the ozone concentration . the results are shown in table v below . table v______________________________________downstream of ozone - downstream of ozone - generating chamber decomposing chamber ( at 89 ) ( at 87 ) ______________________________________ozone 300 180concentr &# 39 ; n ( ppm ) ______________________________________ thereafter , a fresh ozone - decomposing catalyst layer ( similar to sample i ) was fitted in the catalyst holder 52 , measuring the ozone decomposing capacity on the basis of the ozone concentration in an initial stage and after a time lapse of 100 hours with the ozone - decomposing ultraviolet lamp 32 in both on - and off - states . the results are shown in table vi below . table vi______________________________________ozone concentration ( ppm ) downstream of catalyst layerupstream of ( at 87 ) catalyst layer initial stagelamp 32 ( at 89 ) of measurement 100 hrs later______________________________________on 300 1 . 0 34off 300 1 . 2 103______________________________________ as a result of this experiment , it has been confirmed that the 254 nm wavelength ultraviolet ray acts not only to reduce the amount of ozone to be treated with the catalyst by decomposing ozone but also to reactivate the catalyst with nascent state oxygen which is produced by the ultraviolet rays , thereby preventing deterioration of the catalyst . according to the present invention , in the deodorization of malodorous substances with nascent state oxygen which occurs as a result of forced decomposition of ozone by an ultraviolet ray , it becomes possible to prevent deterioration of the ozone - decomposing catalyst and conseguently to maintain the deodorizing capacity effectively by irradiating the ozone - decomposing catalyst layer with an ultraviolet ray ( especially of 254 nm in wavelength ) from an ozone - decomposing ultraviolet lamp in an ozone - prevailing atmosphere to reactive the ozone - decomposing capacity of the catalyst . with regard to the action of the ultraviolet ray on malodorous substances ( e . g . sulfides , ammonia , etc . ), the photo energization by the 185 nm wavelength ultraviolet ray decomposes the malodorous substances or renders them easily decomposable , so that it has an effect of promoting the oxidative decomposition of the substances by nascent state oxygen in the next stage . further , since the ozone - generating ultraviolet lamp can generate a 254 nm wavelength ultraviolet ray simultaneously with the 185 nm wavelength ultraviolet ray , the deodorizing capacity can be improved all the more by providing an ozone - generating ultraviolet lamp also in a position which it can directly irradiate the ozone - decomposing catalyst layer . with regard to sterilization , the 254 nm wavelength ultraviolet ray has an excellent sterilizing effect . while a preferred embodiment of the apparatus of the present invention has been illustrated and described , changes and modifications may be made therein and thereto within the scope of the present invention defined in appended claims .