a chamber c is provided having a bottom , a top , and an intermediate wall 1 &# 39 ;. both the top , the bottom , and the intermediate wall are provided with openings or apertures 2 to provide for ventilation within the chamber . lateral doors may be fitted in the chamber , and both the top as well as the bottom may be made removable or pivotably secured to provide ready access to the inside of the chamber . hinges and the like have been omitted from the drawing for clarity , and can be applied in any suitable and desired manner . dental prosthesis parts 3 are located within the chamber c . the dental prostheses 3 are secured to holders , for example clamps 4 , which are fitted in a holding spider or wheel 5 and secured in the spider or wheel 5 by clamping screws 6 . the holders 4 may also be made of flexible material in order to improve fine adjustment of positioning of the dental prosthesis parts -- which are not necessarily always identical -- with respect to a flame hydrolysis burner 11 . the spider or wheel , in short a turntable , 5 is held by a shaft 7 , coupled to a motor 8 , and rotated as schematically indicated by the arrow 9 . the turntable 5 , as schematically indicated by the double arrow 12 , is vertically adjustably positioned on shaft 7 in order to properly locate the respective dental prosthesis parts 3 in optimal position with respect to the flame or flame cone 10 emanating from the flame hydrolysis burner 11 . a clamping screw 13 positions the shaft in a selected vertical level . the axis of rotation of the shaft 7 could also be located essentially parallel to the flame hydrolysis burner . the flame hydrolysis burner , as best seen in fig1 is separated from the region of the chamber within the housing 1 by a separating wall 15 formed with an opening 14 . the flame hydrolysis burner can be retracted into the burner chamber 16 within the structure 1 when the apparatus is out of operation . in that case , preferably , a cover plate 17 is applied over the opening 14 , moved , as desired , in accordance with the direction of the double arrow 18 , by being upwardly and downwardly slidable . the flame hydrolysis burner 11 is supplied with air over a supply connection 19 , and further is supplied with combustion gas over a supply connection 20 . a suitable and preferred combustion gas is propane . a silicon compound is supplied , in gaseous form , in which , preferably , an oxidizable gaseous silicon compound is added to the air supply . the flame hydrolysis burner 11 is linked by a settable connecting link 21 , which can be clamped in position by suitable clamping screws , not specifically shown , to a holder 22 . holder 22 , as indicated by arrow 23 , can be rotated by hand and , as illustrated by arrow 24 , can be moved back - and - forth . the optimum operating position is then fixed by tightening a set screw 25 . an optimum operating condition is so selected that , in the apparatus shown , the flame cone 10 is essentially horizontal . the maximum distance between the forward edge of the burner and the most remote part of the prosthesis 3 should be , at the most , about 15 cm . this distance is shown in fig1 as d . the length l of the flame cone 10 -- dimension shown only in fig2 for clarity -- is , at least , about 15 cm , and at the most 20 cm . a cooling device 26 is located within chamber 1 , offset by 90 ° with respect to the direction of the flame cone 10 . the closing shield 17 is lowered to the position shown in fig1 and the flame hydrolysis burner is passed through the opening 14 and placed in position . the position of the flame hydrolysis burner is so adjusted that the flame cone will be directed towards oppositely positioned dental prosthesis parts 3 , by level positioning the axis of rotation of the shaft 7 of the turntable 5 and / or by height positioning and / or rotation of the holders 4 within the reception openings therefor in the turntable 5 ; and / or by rotation and back - and - forth adjustment of clamp 22a and holder 22 , in accordance with arrows 23 , 24 . after optimizing the position of the burner 14 with respect to all of the dental prostheses parts 3 located on the turntable 5 , motor 8 is started and the turntable is slowly rotated , for example at a speed of about 30 rpm . air and fuel are then supplied to the connections 19 , 20 , respectivley , and oxidizable silicon compounds to the flame hydrolysis burner are opened , and the flame hydrolysis burner is ignited . the rotating dental prosthesis parts 3 are sequentially exposed to the flame cone 10 of the flame hydrolysis burner 11 , and the silicon oxide - containing adhesion - promoting layer will precipitate or deposit on the dental prosthesis parts 3 . the speed of rotation of the turntable 5 is so adjusted or controlled that , during one rotation of the turntable 5 , the coated dental prosthesis 3 will cool sufficiently until they are again exposed to the flame cone 10 for deposition of a further , thin silicon oxide - containing coating or layer . cooling can be enhanced by the cooling apparatus 26 which supplies cooling for the dental prostheses 3 , by projecting cooling air or an air - water mixture on the prostheses . the cooling device 26 is , preferably , formed as a slit nozzle with a vertically extending nozzle slit 27 . after several revolutions , and when the dental prosthesis parts 3 have received a sufficiently thick coating of the silicon oxide adhesion - promoting layer , air and fuel supply as well as silicon supply to the burner is turned off , and the burner retracted into the burner chamber 16 , for example by loosening set screws connecting the links 21 . the closing shield 17 is then closed . the dental prosthesis parts or frames 3 can then be removed from the coating chamber c , and may be further treated , for example as described in the referenced u . s . pat . no . 4 , 364 , 731 , that is , by coating with a commercial dental plastic material , using , for example , a silane - containing coating . preferably , and in advance of placing the prostheses in the holders 4 , they are thoroughly cleaned and sandblasted as schematically shown by the box &# 34 ; sandblasting &# 34 ;. this step , as such , is conventional . fig2 and 3 illustrate , in highly schematic form , other embodiments of flame hydrolysis burners which may be substituted for the burner 11 of fig1 and which can be connected by attachment tabs 32 to the linkage 21 . the burner 11 &# 39 ; of fig2 differs from the burner 11 of fig1 in that a double burner is provided , having two burner heads 28 , 28 &# 39 ;, located one above each other . it is , of course , equally possible to locate the burners adjacent each other . fig3 illustrates a flame hydrolysis burner 11 &# 34 ; which differs from the burner 11 of fig1 in providing a single burner opening 29 which leads to a manifold having a plurality of exit openings 30 . the number or pass - through diameter of the exit openings 30 can be changed , for example by sliding or rotating an aperture control member 31 within the manifold 29 . the apparatus has the advantage that it is readily possible to move the dental prosthesis part or the base frame , made of metal , during the coating with respect to the cone of the flame of the flame hydrolysis burner so that , sequentially , different surface portions of the prosthesis can be exposed to the flame cone . locating all the prosthesis elements on a turntable has the advantage that the dental prosthesis parts 3 , during a rotation of the turntable , can cool sufficiently before a further silicon oxide - containing adhesion - promoting layer is being applied . the cooling device 26 preferably is located at an angular offset of from between 20 ° to 120 °, preferably about 90 °, with respect to the flame hydrolysis burner 11 . it may be located , and preferably is located , next to the turntable . the turntable is relatively movable upwardly and downwardly with respect to the flame cone 10 of the flame hydrolysis burner to insure optimum adjustment of the position of the dental prosthesis with respect to the coating effect obtained by the flame cone . optimal adjustment is further obtained by locating the burner 11 in accordance with the adjustment provided , as schematically shown by arrows 23 , 24 . the linkage 21 may be provided with preset adjustment markers so that an adjustment by the linkage 21 which is once made is reproducible . linkage 21 is used to withdraw the burner 11 into the chamber 16 . by setting the various adjustments -- clamping screw 13 , clamp 22a , set screw 25 and the clamping screw 6 -- optimum placement of the respective prosthesis elements 3 with respect to the burner cone 10 is insured . various other arrangements of adjusting the burner , so that the flame cone 10 will have the appropriate characteristic with respect to the prostheses 3 , may be used . fine adjustment of the burner flame can be easily obtained by changing the size and throughput of flame gases , as well as the size of the burner itself -- see fig3 . if the burner has a slit - type nozzle , a controller plate , for example a knife edge , partially obstructing the slit nozzle , can be used . burners having nozzle openings of circular cross section can be adjusted , as is well known , by placing a positioning needle or positioning cone more , or less , within the circular nozzle opening . the flame hydrolysis burner is preferably operated with a combustion gas - air mixture . a preferred combustion gas or fuel gas is propane gas . an inorganic compound such as sih 4 may be used as the oxidizing silicon compound ; organic silicon compounds , likewise , may be used such as organosilane , organooxylsilane , organosiloxane , or a mixture of respective inorganic and organic , or only organic silicon compounds . if the oxidizable silicon compound is not available in gaseous form , it may be applied to the flame hydrolysis burner in vaporized form . in a preferred arrangement , the oxidizable silicon compound is supplied in gaseous form to the flame hydrolysis burner over the same connecting stub as the air being supplied for the fuel gas - air mixture , mixed in the burner in accordance with well known arrangements . to obtain reproducible coating , and to be able to adjust the flame cone of the flame hydrolysis burner properly for optimum coating , the flame is preferably colored by addition of a coloring substance , for example volatile sodium or boron compounds . the coloring or tinting element is preferably supplied over the same supply stub as the oxidizable silicon compound , with metered supply of air , silicon compound , and tinting or coloring material . metered supply is shown only in fig2 in which , in the respective lines 40 supplying air , 41 supplying silicon compound , and 42 supplying tinting substance , valves 50 , 51 , 52 are located . a similar illustration has been omitted from the other drawings for simplicity . overall , the arrangement has the substantial advantage that it can be operated under normal , atmospheric conditions , that is , in ambient atmosphere , without vacuum or the like . in a preferred structure , the dental prostheses and their holder are located within the chamber c which is ventilated by ventilation slits 2 , which permit circulation of ambient air through the chamber c . in this arrangement , the flame hydrolysis burner can be positioned in the same chamber as the articles to be coated . the additional chamber 16 is , however , preferred since additional protection against possible danger of fire is afforded , particularly if the linkage 21 is so arranged that it can be rapidly retracted from a preset position , with an externally accessible closure of the shield 17 , thus shutting off the generation of flame from the burner , even if a control valve 53 in the fuel line 43 to stub 20 should not be immediately operable . the arrangement permits deposition of intermediate layers , particularly suitable for enhancing adhesion of plastic on a metal substrate which includes silicon dioxide . use of such an intermediate adhesion - promoting layer is described in the referenced u . s . pat . no . 4 , 364 , 731 . the arrangement also permits deposition of carbon - containing sio x layers on dental prostheses . the carbon is then present , preferably , in form of remanent hydrocarbons , joined to the silicon . adhesion - promoting layers with hydrocarbons have the particular advantage with respect to mere silicon dioxide layers that they have even better adhesion - promoting qualities between the dental plastic and the metal alloys used for prostheses . further , they are more durable with respect to resistance to formation of fissures within the environment of a user &# 39 ; s mouth , that is , under influence of moisture , changes in temperatures , and mechanical stresses applied thereto . optimal results can be obtained with deposited silicon oxide - containing adhesion - promoting layers , having a carbon content of between 5 % to 40 % ( by weight ) of the adhesion - promoting layer . obtaining such layers with the carbon content , in accordance with the present invention , is achieved by carrying the prosthesis part 3 to the forward third portion of the flame cone of the flame hydrolysis burner , and operating the flame hydrolysis burner with a carbon - containing fuel gas - air mixture , to which the above - referenced oxidizable silicon compound is admixed in metered or dosed amounts . to promote the best possible adhesion , it is preferred to expose the dental prosthesis parts 3 to sandblasting in advance of application of the adhesion - promoting layer . for sandblasting , corundum , with an average particle size of 0 . 25 mm , or more , has been found suitable .
to apply a silicon oxide adhesion - promoting layer to a metal prosthesis part or frame , for subsequent application of a dental plastic thereon , the prosthesis is subjected to flame hydrolysis derived from a flame hydrolysis burner which has a silicon compound in vapor or gas form applied thereto in addition to a carbon - containing combustion gas , such as propane and air , the prosthesis part or frame being passed through the flame from the burner in the forward third thereof , the burner flame cone having , in operation , a length of between 15 to 20 cm , a gas stream speed of about 1 m / sec ., and wherein the length of the cone exceeds the spacing distance of the farthest part of the prosthesis from the mouth of the burner by only up to about 25 %. for fine adjustment of the cone , a tinting substance can be added to the flame .