embodiments of the inventions remedy the aforementioned deficiencies found in the current prior art systems . embodiments of the invention relate to the objective of providing a burner comprising a catalyst that provides improved combustion through efficient use of use . generally , flameless combustion is accomplished by preheating combustion air and fuel gas sufficiently that when the two streams are combined the temperature of the mixture exceeds the auto - ignition temperature of the mixture , but to a temperature less than that which would result in the oxidation upon mixing being limited by the rate of mixing . without a catalyst surface present , preheating of the streams to a temperature between about 1500 ° f . and about 2300 ° f . and then mixing the fuel gas into the combustion air in relatively small increments is required in order for flameless combustion to occur . according to an embodiment of the invention , a catalyst is deposited on a non - porous substrate in a manner such that the catalyst is strongly adhered to the substrate . in certain embodiments of the invention , the catalyst is deposited on a metal substrate . in other embodiments of the invention , the catalyst is deposited on a dense , non - porous substrate . examples of dense non - porous substrates include , without limitation , glass and non - porous ceramic materials . indeed , any suitable non - porous materials may be used to construct the substrate upon which the catalyst is deposited . in an embodiment of the invention , a supported catalyst is provided . in this embodiment , a catalyst is first deposited on a support . following this step , the supported catalyst is deposited on a non - porous substrate . in this embodiment , the support upon which the catalyst is deposited can be any material that exhibits a high cell density , a thin wall thickness and sufficient strength for catalytic applications , while exhibiting a sufficiently high geometric surface area for metal catalyst impregnation . examples of support materials that meet these requirements include , without limitation , zeolite and alumina . in an embodiment of the invention , the substrate containing the catalyst is contacted with a housing that contains a wick saturated with an appropriate fuel . in some embodiments , the substrate is contacted with the wick - containing housing by wrapping the catalyst - containing substrate around the housing . in this embodiment , a substantial portion of the substrate contacts the housing at one or more locations around its circumference . in another embodiment of the invention , the catalyst - containing substrate is suspended over a housing containing the wick . in this embodiment , the substrate may contact the housing at one or more points on the sides of the housing , while a substantial portion of the substrate does not contact the housing . according to certain embodiments of the invention , the housing that contains the wick is made of a substance that is an effective conductor of heat . in certain embodiments of the invention , the housing is made of one or more metals or a metal alloy . according to an embodiment of the invention , the housing is heated with a heating source , which in turn heats the catalyst - containing substrate . in certain embodiments of the invention , the heating source may be a lighter , match or resistive heater . according to an embodiment of the invention , the catalyst is ignited by an ignition source having a flame . in certain embodiments of the invention , the catalyst is ignited by a flameless ignition source . according to an embodiment of the invention , the catalyst and housing are heated and the temperature is raised to a suitable working temperature . once the appropriate working temperature is reached the catalyst begins to combust the fuel . in an embodiment of the invention , the combustion of the fuel occurs in a cyclical manner . the catalyst and housing are heated and the temperature is raised to a suitable working temperature . when the appropriate working temperature is reached , the catalyst begins to combust the fuel , thus heating the substrate upon which the catalyst is deposited . the catalyzed substrate in turn heats the housing containing the wick . the heated housing heats the fuel saturated wick contained within the housing . the heating of the wick vaporizes the fuel . the fuel vapors flow over the catalyst and are combusted by the catalyst . the excess heat generated by the combustion of the fuel heats the housing . the heated housing in turn heats the wick , thereby repeating the fuel combustion cycle . according to an embodiment of the invention , the bulk of the fuel is not consumed by the catalyst during this process , but is emitted into the surrounding atmosphere at a high rate . in certain embodiments of the invention , the fuel is emitted into the atmosphere at ˜ 9 . 0 to 12 . 0 grams / hour . the emission of the fuel into the atmosphere by an embodiment of the invention provides a suitable vehicle by which volatile substances such as fragrances , perfumes and other products that are soluble in the fuel may be emitted into the atmosphere . in an embodiment of the invention , the fuel may contain one or more chemical compounds . in such an embodiment , the fuel / chemical compound mixture comes into intimate contact with the catalyst to transform the chemical compound ( s ) in some fashion . in certain embodiments , the transformation of the chemical compound ( s ) enhances the combustion of the fuel . a catalytic burner as embodied herein is not subject to the problems and drawbacks associated with the porous ceramic catalytic burner systems . by carefully selecting the material from which the housing of the catalytic burner is constructed , the wick can be situated so that it is not in direct contact with the housing . this lack of contact between the wick and the housing greatly reduces the rate at which the wick is degraded and increases the lifetime of the burner . additionally , degradation of the wick , even if it were to occur , does not affect the overall performance to as high a degree in the claimed invention , as it does in the porous ceramic system . when loss of fuel flow occurs due to wick degradation , the degraded wick can easily be replaced with a new wick without loss of function . although the fragrance may still be partially degraded and remain on the wick , the wick continues to function . however , the claimed invention does not have pores that can become clogged , as happens with porous ceramic burners . in certain embodiments of the invention , ignition of the catalyst is achieved without a flame . since the catalyst is situated over or around the housing containing the saturated wick , and does not contact the wick there is no need to desorb the fuel from the catalyst to achieve ignition . rather , the only requirement is that the system receives enough heat to reach the working temperature of the catalyst . in certain embodiments of the invention , the catalyst and housing are heated and the temperature is raised to a suitable working temperature of around 250 ° c . additionally , unlike other systems where the catalyst is required to absorb fuel before it can be combusted , only the wick needs to absorb fuel before operation of the burner in the claimed invention . in certain embodiments of the invention , the amount of fuel that is required to sustain combustion of the catalyst is absorbed in a very short time after the wick comes into contact with the fuel . in an embodiment of the invention , the amount of time for the wick to absorb an effective amount of fuel to sustain combustion of the catalyst is less than 5 minutes . in general , the invention relates to a catalytic burner that is capable of self - sustained operation after initial start up . according to an embodiment of the invention , the catalytic burner operates on a fuel mixture that is contained in a reservoir and delivered to the burner via an absorbent wick . according to an embodiment of the invention , the catalytic burner is composed of three main parts : an absorbent wick , a housing and a catalyst that has been deposited on a suitable substrate ( fig1 and 2 ). the construction of the burner and the geometry of the supported catalyst , allow the catalytic burner to operate continuously for extended periods of time . in certain embodiments of the invention , a catalytic burner that is constructed and operated as set forth herein can operate continuously for around 184 hours . according to an embodiment of the invention , the housing can be composed of any metal or metal alloy such as ( but not limited to ): brass , brass alloy , medium leaded brass , high leaded brass , extra high leaded brass , free cutting brass , phosphor bronze , free cutting phosphor bronze , aluminum bronze , brass , bronze , brass or bronze alloy , aluminum , aluminum alloys , or stainless steels . in certain embodiments , the housing can be composed other non - porous materials such as glass and high density ceramic . the housing can be formed in any shape that is suitable for holding a wick . examples of suitable shapes for the housing include a collar - style housing ( fig1 a and 1b ) or tube - style housing ( fig2 a and 2b ). referring now to fig1 a and 1b , the drawings represent a collar - style catalytic burner ( 10 ) according to the present invention . the collar ( 10 b ) serves as the housing which holds the wicking material tightly in place . the substrate containing the supported catalyst ( 10 a ) is held in place over the wicking material . the substrate is held in place by making contact with the sides of the collar or housing ( 10 b ). in this embodiment , the catalyst ( 10 a ) is not in direct contact with the wicking material . however , the heat that is radiated from the catalyst during operation is directed towards the fuel - filled wicking material . the catalyzed substrate ( 10 a ) is held by the collar at a suitable distance from the fuel filled wick so as to maximize evaporation of the fuel and minimize degradation of the wick . the distance between the surface of the catalyst and the surface of the wick can range from 0 . 01 to 0 . 50 inches , but is preferably 0 . 20 inches . to further minimize degradation of the wick , the collar ( 10 b ) can be designed in a manner so as to control the amount of heat that reaches the wicking material . this may be accomplished by separating the wick from the catalyzed substrate with a perforated material that acts as a heat shield , but allows the passage of vapors . the configuration of the catalytic burner allows for continuous cyclical operation , wherein the fuel ( absorbed by the wick ) is vaporized by the supported catalyst . the vaporized fuel flows over the catalyst and is catalytically combusted . the catalytic combustion produces heat at a temperature of around 250 ° c . the heat produced by the catalyst radiates to the wick ( 10 c ), which causes vaporization of fuel , and the process is repeated . during this process the majority of the fuel is not consumed by the catalyst but is emitted into the surrounding atmosphere at a high rate , typically ˜ 9 . 0 to 12 . 0 grams / hour . according to an alternate embodiment of the invention , the housing can also be formed into a tubular shape . fig2 a and 2b depict a tube - style catalytic burner ( 20 ) according to the present invention . the tube shaped body ( 20 b ) can be composed of any metal or metal alloy such as ( but not limited to ): brass , brass alloy , medium leaded brass , high leaded brass , extra high leaded brass , free cutting brass , phosphor bronze , free cutting phosphor bronze , aluminum bronze , brass , bronze , brass or bronze alloy , aluminum , aluminum alloys , or stainless steels , or made from glass or a non - porous ceramic . in an embodiment of the invention , the metal used to construct the tube - style metal housing is stainless steel . in certain embodiments of the invention where a tube - style housing is employed , the housing has a wall thickness ranging from 0 . 005 to 0 . 04 inches . a preferred wall thickness for a tubular housing is 0 . 01 inches . in an embodiment of the invention , the catalyzed substrate ( 20 a ) is wrapped around and / or over the tubular housing and held in place by connectors at a distance of 0 . 01 inches to 0 . 10 inches , and more preferably 0 . 05 inches from the outer surface of the tube . the tubular housing ( 20 b ) also serves to hold the wick ( 20 c ) at the proper location to efficiently deliver fuel and / or fuel vapors to the catalyst . a support ring ( 20 e ) serves to position the catalytic burner when the burner is placed on top of a fuel reservoir . in certain embodiments of the invention , the tubular body contains perforations ( 20 d ) around the circumferential portion of the tubular housing . the perforations permit a larger volume of vaporized fuel to reach the catalyst , in embodiments where the substrate containing the catalyst surrounds the tubular housing . the perforations may cover up to 90 % of the surface of the tubular housing . in an embodiment of the invention , the perforations comprise 2 % of the surface and are located along an upper circumferential portion of the tubular housing . according to embodiments of the invention , the substrates comprising the supported catalyst ( 10 a or 20 a ) are situated at a suitable distance from the wick ( 10 c or 20 c ) to provide a limited region wherein the oxidation reaction temperature is lowered . distribution of these catalytic surfaces provide for distribution of heat release within the burner . the catalytic substrates are sized to accomplish a nearly even temperature distribution along the burner . a nearly even temperature profile within the burner results in more uniform heat distribution . a more even temperature profile will also result in the lower maximum temperatures for the same heat release . because the materials of construction of the burner dictate the maximum temperatures , even temperature profiles will increase the heat release possible for the same materials of construction . preheating of the fuel gases to obtain flameless combustion without a catalyst would result in significant generation of carbon unless a carbon formation suppressant is included in the fuel gas stream . the need to provide such a carbon formation suppressant is therefore avoided by operating the burner in the presence of a catalyst . in embodiments of the invention , initial ignition is accomplished by using a source that generates a flame or spark . according to embodiments of the invention , ignition is accomplished by injecting pyrophoric material , an electrical igniter , a spark igniter , temporally lowering an igniter into the space between the wick and the catalyst substrate , or an electrical resistance heater . the substrate is preferably rapidly brought to a temperature at which a flameless combustion is sustained to minimize the time period at which a flame exists within the burner . the rate of heating the substrate will typically be limited by the thermal gradients the burner can tolerate . in an embodiment of the invention , the catalytic burner assembly is ignited by bringing an open flame close to the burner for a short period time . the time required to ignite a burner assembly of the invention using an open flame is 20 seconds or less . the ignition of the catalytic burner according to embodiments of the invention , can be enhanced by provision of supplemental oxidants during the start - up phase , or by use of a fuel that has a lower catalyzed autoignition temperature such as hydrogen . preferred supplemental oxidants include supplemental oxygen and nitrous oxide . hydrogen can be provided along with a natural gas stream , and could be provided as shift gas , with carbon monoxide present and carbon dioxide present . the use of start - up oxidants and / or fuels is preferred only until the catalyst has been heated to a temperature sufficient to enable operation with a fuel of choice and air as the oxidant . according to embodiments of the invention , methanol , ethanol , propanol , butanol , dimethyl ketone , ethyl acetate , methane , ethane , propane , butane , propylene glycol , dimethyl formamide or any other suitable fuel known in the prior art can be used as the working fuel in embodiments of the invention . noble metals such as palladium or platinum , or semi - precious or precious metals , base metal or transition metals and their oxides can be used as catalyst in embodiments of the invention . the metals or their oxides can be deposited or coated , preferably by electroplating ( or pulsed laser deposition ( pld ), chemical vapor deposition ( cvd ), electrophoretic deposition ( epd ), washcoating , hydrothermal treatment , or microwave assisted hydrothermal treatment ) onto a surface of the catalyst support to enhance oxidation of the fuel at lower temperatures . the metal could then be oxidized as necessary to provide a catalytically effective surface . such a catalytic surface has been found to be extremely effective in promoting oxidation of fuels in air at temperatures as low as 500 ° f . this reaction rapidly occurs on the catalytic surface and in the adjacent boundary layer . an advantage of having a significant catalytic surface as part of the catalytic burner assembly of the invention , is that the temperature range within which the flameless combustor operates can be significantly increased . according to embodiments of the invention , the supported catalyst is deposited on the non - porous substrate by methods such as coating , electroplating , vapor deposition or electrohoretic deposition . according to embodiments of the invention , semi - precious metals , and transition metal oxides , for e . g ., gold , silver , chromium oxide and cobalt oxide may be used as catalysts in embodiments of the invention . indeed , metal catalysts such as palladium and platinum can be doped with other metal or metal oxide catalysts to promote chemical transformations in conjunction with the burner . in an embodiment of the invention , the catalyst is deposited on a support such as an alumina or silica microparticle or nanoparticle . the catalyzed particle can then be deposited on any suitable substrate to form the catalyzed substrate . according to an embodiment of the invention , the substrate on which the catalyst is deposited is any material to which the catalyst can be adhered and which can withstand temperatures greater than 500 ° c . in certain embodiments of the invention , the substrate is composed of a material such as ( but not limited to ), alumina , alumina fiber , fiberglass , nextel ® ceramic fiber or any other ceramic fiber , any refractory ceramic fiber , any synthetic vitreous fiber , silicon carbide fibers , silicon nitride fibers , zirconia fibers , or fiberfrax ® ceramic fibers , cordierite , mullite , porcelain , alumina , silicon nitride , zirconia , steatite , wollastonite or any non - porous ceramic . in other embodiments of the invention , the substrate is composed of a metal such as ( but not limited to ), stainless steel , stainless steel alloys , inconel , zinc alloys , titanium , or any metal or alloy . a metal substrate can be expanded , perforated , or in the form of sheets , wires , mesh , or gauze . according to embodiments of the invention , the catalyzed substrate can be formed into various geometries to improve burner functionality and external appearance . the geometry of the catalyzed substrate can be varied to optimize the performance of the catalytic burner for various types of fuel ( fig3 a to 3g ). examples of the various geometries of catalyzed substrate include , but are not limited to , circular ( fig3 a ), crimped ( fig3 b ), theta ( θ ) shape ( fig3 c ), vertical ( fig3 d ), horizontal ( fig3 e ), tent shaped ( fig3 f ), roof shaped ( fig3 g ), or any other shape that provides optimal fuel vapor flow over the catalyst . according to an embodiment of the invention , the function of the wick ( 10 c and 20 c ) is to transport fuel or permit fuel to flow from the fuel reservoir to the upper region of the catalytic burner . the wick may be any device or material which provides adequate fuel flow to support continuous operation of the catalytic burner and combustion of the catalyst . in certain embodiments of the invention , the wick is composed of a porous material . suitable examples include any wicking material such as ( but not limited to ): cotton cloth , alumina , alumina fiber , fiberglass , nomex ®, teijinconex ®, teijinconex ® ht , or any meta - aramid fiber , kevlar ®, technocrat ®, tarpon ®, or any para - aramid fiber , teflon ®, tooling ®, or any fluorocarbon fiber , raton ®, procom ®, toray pps ®, or any polyphenylene sulfide fiber , basofil ® or any melamine fiber , zylon ®, or any poly ( phenylene benzobisoxazole ) fiber , polybenzimidazole fibers , p - 84 ®, or any polyimide fibers , lastan ®, polyacrylonitrile , or any carbon fibers , glass fibers , or any formulation of glass fibers , spectra ®, dyneema ®, or any high density polyethylene fibers , nextel ® ceramic fiber , or any ceramic fiber , any refractory ceramic fiber , any synthetic vitreous fiber , silicon carbide fibers , silicon nitride fibers , zirconia fibers , or fiberfrax ® ceramic fibers . in certain embodiments of the invention , the wick may be composed of porous materials , fritted metal , or any material that is capable of transporting of fuel from the reservoir to a region near the catalyst . in other embodiments of the invention , the wick may also be any device which provides fuel transport from the fuel reservoir to the catalytic burner , such as ( but not limited to ): capillary pumps , fluid pumps , microfluidic systems , or any device or system capable of fluid transfer . a catalyzed inconel substrate was prepared by coating with a precious metal catalyst supported on alumina nanoparticles . the inconel substrate was an expanded sheet 0 . 25 ″ high by 2 . 0 ″ long by 0 . 012 ″ wide . the catalyzed substrate was connected to a brass ( brass alloy 260 ) collar which contained a fiberglass wick . the catalytic burner assembly was placed on a filled fuel reservoir . the wick was allowed to absorb fuel for ten minutes . an open flame was then held to the catalytic burner assembly for 20 seconds . after removing the open flame , the catalytic burner was allowed to continuously operate for 5 hours with an average emission rate of 9 . 0 g / hr . a non - porous ceramic catalyst support was prepared by mixing 35 . 0 grams kaolin , 25 . 0 grams talc , and 3 . 4 grams cmc gum in a ball mill for 3 hours . 30 . 0 grams di water was then added and the mixture was kneaded into a dough consistency . the dough was extruded as ¼ ″ by ¾ ″ flat pieces . the pieces were dried at room temperature for 24 hours and then heated to 1200 ° c . for 4 hours and allowed to cool naturally . one side of the dense ceramic pieces was coated with precious metal catalyst supported on alumina nanoparticles . the catalyzed ceramic was suspended over a fiberglass wick , with the catalyzed side facing the wick , using a brass ( brass alloy 260 ) collar to hold it in place . the catalytic burner assembly was then placed in a fuel reservoir , and then , once fuel had been absorbed , ignited for 20 seconds , and blown out . the catalytic burner was allowed to operate continuously for 5 hours with an average emission rate of 7 . 0 g / hr . a catalyzed inconel substrate was prepared by coating with a precious metal catalyst supported on alumina nanoparticles . the inconel substrate was an expanded sheet 0 . 25 ″ high by 2 . 0 ″ long by 0 . 012 ″ wide . the catalyzed substrate was suspended around a brass ( brass alloy 260 ) tube at a distance of 0 . 05 ″ from the outside of the tube . the metal tube was 0 . 50 ″ in diameter and 1 . 4 ″ in length and perforated with 48 holes 0 . 0625 ″ in diameter . the holes were equally spaced in four lines around the top 0 . 50 ″ of the metal tube . a cotton wick was placed inside the tube to complete the catalytic burner assembly . the catalytic burner assembly was placed on a filled fuel reservoir . the wick was allowed to absorb fuel for ten minutes . an open flame was then held to the catalytic burner assembly for 20 seconds . after removing the open flame the catalytic burner was allowed to continuously operate for 5 hours with an average emission rate of 12 . 0 g / hr . a non - porous ceramic catalyst support was prepared by mixing 35 . 0 grams kaolin , 25 . 0 grams talc , and 3 . 4 grams cmc gum in a ball mill for 3 hours . 30 . 0 grams di water was then added and the mixture was kneaded into a dough consistency . the dough was extruded as a hollow cylinder 0 . 25 ″ tall with an outside diameter of 0 . 575 ″ and an inside diameter of 0 . 50 ″. the hollow cylinder was dried at room temperature for 24 hours and then heated to 1200 ° c . for 4 hours and allowed to cool naturally . the outside of the dense ceramic hollow cylinder was coated with precious metal catalyst supported on alumina nanoparticles . the catalyzed ceramic substrate was fit around a brass ( brass alloy 260 ) tube . the metal tube was 0 . 50 ″ in diameter and 1 . 4 ″ in length and perforated with 48 holes 0 . 0625 ″ in diameter . the holes were equally spaced in four lines around the top 0 . 50 ″ of the metal tube . a cotton wick was placed inside the tube to complete the catalytic burner assembly . the catalytic burner assembly was placed on a filled fuel reservoir . the wick was allowed to absorb fuel for ten minutes . an open flame was then held to the catalytic burner assembly for 20 seconds . after removing the open flame the catalytic burner was allowed to continuously operate for 5 hours with an average emission rate of 9 . 0 to 12 . 0 g / hr .