referring now to fig1 the apparatus and method of this invention is illustrated specifically in unloading used catalyst from a catalytic vessel 1 into a drum 40 or series of drums or other containers . while the dust control equipment has been described for use in unloading spent catalysts from catalytic vessels it may also be employed in founderies , mineral processing plants , coal processing plants , oil refineries , chemical plants and other industries in which dust containing discrete solids require transfer from one vessel or container to another . further , while the invention has been described primarily as a portable method , it can be installed as a permanent unit for continuous or semi - continuous operation . however , one of the major advantages of the equipment and of the method is that they lend themselves readily for transportation from one area to another for intermittent or infrequent usage . referring , now to fig1 a catalyst vessel 1 is shown having a dump chute 2 and a dump chute valve 3 . a normally limp transfer hose 4 is connected to the dump chute 2 by use of a clamp ( not shown ) and the discharge end of the hose is operatively connected to the dust control hood 6 . the dust control hood 6 , as shown best in fig2 and 3 , has a top 7 , a wall portion 8 and a rim 9 . rim 9 contains a depending skirt 10 which in the embodiment shown in fig2 contains a sealing ring 21 . at the top 7 of the dust control hood there is a dip pipe 11 having an opening 12 and a discharge end 13 which terminates at about the level of the depending skirt 10 . the dip pipe can terminate at a point slightly above or below this level depending upon the natural angle of repose 27 of the materials being loaded . as illustrated , the transfer hose 4 can be fitted over the opening 12 of dip pipe 11 , or merely inserted into the opening . in the embodiment illustrated in fig2 and 3 there is a gas inlet 14 which has an adjustable cover 15 in the form of a rubber flap which is pivotably attached at point 16 with a rivet for manipulation to either side . however , in the devices shown in fig1 and 10 , the gas inlet is in the form of an inlet tube 17 which may be connected to a recycle line 30 for purposes to be described hereinafter . furthermore , as illustrated in fig4 through 9 , the gas inlet opening 14 can be completely eliminated by the elimination of the sealing ring 21 which allows for air to flow between the depending skirt 10 and the upper rim 41 of the drum 40 . in any event , all that is required is that air or other gases be allowed to enter into the hood area while the dust laden materials are being loaded . as will be apparent , the dust which evolves from the discrete dust laden pieces being loaded into the drum 40 is entrained into the air stream flowing across plenum 23 between the hood 6 and the drum and which escapes via outlet 18 through outlet tube 19 into the outlet line 22 . this air is pulled by means of fan 26 through the dust collector 25 , preferably in the form of a bag filter , and the exhaust air thereafter is discharged to the atmosphere ( or recycled in the case of inert gases ). referring now to drawings 4 through 9 , the air is shown by the arrows entering between the depending skirt 10 and the upper rim 41 of the drum 40 and sweeping across the plenum 23 of the hood through the outlet tube 19 into outlet line 22 to the filtering apparatus ( not shown ). the transfer hose 4 is shown in limp condition as the pulverulent solids and dust are loaded into the bottom of the drum . however , as is shown in fig5 once the solids 28 have reached the discharge end 13 of the dip pipe 11 , the normally limp transfer hose 4 becomes rigid and is readily observable by the operator . thereafter , as is shown in fig4 the operator can manually squeeze off or close off the transfer hose 4 thus stopping the flow of materials 28 into the drum 40 . the natural angle of repose of the loaded materials ( indicated at 27 ) allows for additional material to be loaded into the drum without overfilling and this is accomplished when the operator pulls the hood 6 and attached hoses 4 and 22 away from the drum . this is shown in fig7 as allowing the materials in the dip pipe 13 and in the transfer hose 4 past the point of constriction to fall into the drum 40 . thereafter the lid 42 can be easily placed onto the drum as is shown in fig8 and the hood 6 and attached hoses are immediately transferred to a waiting container as is shown in fig9 . handles have been provided for this purpose . as has previously been mentioned , the transfer hose 4 need not be physically attached to the dip pipe 11 but can merely be inserted therein . thus , in this case , the operator will provide two or more dust control hoods 6 for two or more drums 40 and merely lift the transfer hose upwardly after applying constricting pressure and thus allow the residual materials to flow into the drum through the open dip pipe 11 . thereafter , the hose is inserted into the dip pipe 11 of a waiting hood 6 on an adjacent drum 40 and the pressure released so as to allow the flow to again resume to the new drum . as will be obvious to artisans in this art , slide valves can be used rather than manually squeezing off the transfer hose or other methods can be devised for stopping the flow when the transfer hose shows , through its rigidity , that the drum is filled . furthermore , the outlet line 22 may be through a manifold , with closure valves in the case of multiple hoods for multiple drums . since all of this is within the skill of the art , further description is not deemed necessary . in some instances , as has previously been alluded to , the materials being transferred are pyrophoric and will burst into flame upon exposure to air . in these instances , a method such as that disclosed in fig1 , may be used wherein an inert gas is used to blanket the materials being loaded to the container . the inert gas , as for example nitrogen or carbon dioxide , can be fed through the inlet tube 17 to purge the drum 40 . the inert gas is then fed through exhaust tube 19 through exhaust line 22 to the dust collector 25 . in this instance , however , the fan 26 rather than exhausting to the atmosphere propels the gases back through recycle line 30 which is connected to the inlet tube 17 . a make up of nitrogen or co 2 can be fed from cylinder 33 via line 34 to the recycle line through a t arrangement , ( not shown ). thus it is possible , with the use of the method and apparatus of this invention , to safely and successfully transfer dangerous pyrophoric materials containing pyrophoric dust to drums without danger of conflagration . in some instances , in the transfer of extremely highly pyrophoric materials , such as raney nickel and the catalytic rich gas ( crg ) catalysts , the dust is so highly pyrophoric , that there is a danger of a fire in the filter bags in the &# 34 ; bag house &# 34 ;. this would occur , when the hood , is lifted from the drum and oxygen in the area would be withdrawn through the outlet line 22 to the filter . this catalyst dust , holding absorbed hydrogen atoms , in an extremely active state , readily combine with oxygen or other oxidizing materials at atmospheric temperatures . thus , in order to avoid this possibility we have devised the device and system shown in fig1 . essentially , the principle is the same in that the transfer hose 4 feeds the pyrophoric material from its source to the drum 40 through the dip pipe 11 of hood 6 . however , there has been added an additional member in the form of a conical member 60 containing an outer wall 61 and a depending flange 62 . the inlet pipe 17 , is welded through weldments 63 to the outer wall portion 61 and at 63 to the inner wall portion 8 so as to space the conical member 60 in spaced relation to the inner wall 8 of the original hood 6 . in the same manner , outlet tube 19 is welded both to the inner wall 8 and the outer wall 61 by weldments 64 . other suitable spacers may be utilized . the conical top piece 60 terminates into a neck portion 65 which is connected to an annular disc 66 which closes the conical piece hermetically around the neck of the original hood 6 . the neck portion contains an outlet pipe 67 which allows air to run from the annular space or plenum 68 between the inner wall 8 and the outer wall 61 . thus , the plenum 68 is in communication with the atmosphere surrounding the drum 40 and with the neck portion and with the outlet pipe 67 of the conical piece 60 . the outlet line 69 goes to a second filter 70 which is connected in series with fan 71 which is then exhausted through line 72 to the atmosphere . the inert gases , recirculated through line 22 and through line 30 to the inlet 14 of the hood 6 passes through plenum 23 through outlet 19 back through the outlet line 22 to the filter 25 . the fan 26 connected in series pulls the nitrogen through the recirculating line 30 and make up nitrogen is added at point 33 . a positive pressure of nitrogen is maintained through the system so that when the hood 6 is lifted from the top of the drum 40 , any residual dust around the rim 41 is drawn into the annular space 68 of the conical top piece 60 . therefore , any residual pyrophoric dust is picked up through the plenum 68 afforded by the conical top piece 60 and is pulled with the surrounding air through a outlet pipe 67 and through the outlet line 69 to the filter system 70 . this dust will oxidize . however , due to the small amount of the dust and the high volume flow of air through the plenum , the heat will be sufficiently absorbed so that fire is not a problem in the filter system 70 . it will be appreciated of course , that the majority of the pyrophoric dust is collected in the filter 25 which is constantly blanketed with an inert gas nitrogen so as to prevent any oxidation or any fear of conflagration . in the event that a vacuuming technique is utilized to unload the container rather than a gravity feed system , it is still possible to utilize the dust control apparatus as is shown in the illustration in fig1 . in this instance , the dust containing solids 28 are fed through inlet 51 into a cyclone 50 , whereby the solid particles 28 for the most part are separated from the pulverant dust containing materials . the dust , entrained in the low pressure gases , is fed through outlet 52 back to the vacuum truck for collection in the bag filter located therein whereas the solid materials 28 are fed through a vacuum break 55 , in the form of a rotary air lock or gate valve and into the normally limp transfer hose 4 to the dust control hood 6 . this operation illustrates again the outlet line 22 leading to the dust collector apparatus and the fan not shown so that any dust not separated in the cyclone is eliminated from evolution at the point of transfer . it will be apparent , that many modifications will occur to those skilled in the art from the detailed description herein given . as previously mentioned , the use of this apparatus and method is not limited to unloading spent catalysts from catalytic reactors , but may find wide use in foundry operations , chemical plant operations , coal processing plants , feed and grain operations , and other industries in which the transfer of dust laden solids from one point to another offers safety , health and aesthetic problems . for these reasons , the detailed description , herein given , should be construed as being exemplary in nature and nonlimiting except so as to be commensurate in scope with the appended claims .