Abstract:
An apparatus and method for ultraviolet irradiation of air for the purpose of removing contaminants from that air is disclosed. A U-shaped ultraviolet bulb enshrouded within a quartz tube provides enhanced contaminant destruction characteristics. By combining a plurality of those bulbs in a chamber that is of polished aluminum, and further combining aluminum filters therewith, added irradiation enhancement is achieved. Further provided are baffles or baffling proximate the ultraviolet bulbs that cause the air to go turbulent thus drawing the air closer to the ultraviolet bulb and further enhancing the contaminant destruction characteristics. Moreover disclosed is treatment of substrates with a chemical agent that facilitates the arrest of contaminants from the air onto the substrate for further irradiation of the contaminants from the bulbs. This further irradiation breaks down the arrested contaminants thus providing the substrate with a self-cleansing effect.

Description:
FIELD OF THE INVENTION 
     This invention relates generally to air cleansing devices. More particularly, this invention relates to ultraviolet (UV) irradiation and filtration devices. In particular, the invention deals with the use of ultraviolet radiation to decompose organic molecules that have a tendency to colonize filters and evaporation coils that are utilized to condition the air in enclosed surroundings. Also, the invention deals with the placement of ultraviolet lamps placed within a chamber that has a means for passing air therethrough. The chamber&#39;s walls are polished and as such the UV radiation emitting from the UV lamps is reflected off the chamber walls which results in the decay of organic particles adjacent and within the surround and contained therein. Further, baffles adjacent the UV lamps in the chamber cause turbulence within the air passing therethrough which results in an increase in decay of the organic molecules. 
     BACKGROUND OF THE INVENTION 
     Ultraviolet (UV) light in the form of germicidal lamps has been used since the early 1900&#39;s to kill the same types of microorganisms that typically cause the same types of problems today. Since then, UV radiation in the short wave or C band range (UVC) has been used in a wide range of germicidal applications to destroy bacteria, mold, yeast and viruses. After World War II, the use of WVC rapidly increased. UVC is generally understood to exist in the 180 nm to 280 nm wave length area. Typical examples included hospitals, beverage production, meat storage and processing plants, bakeries, breweries, pharmaceutical production and animal laboratories; virtually anywhere microbial contamination was of concern. Early UVC strategies primarily consisted of an upper air approach. This method directed a beam across the ceiling of a room. 
     During the 1950&#39;s when tuberculoses infections were on the rise, the use of UVC became a major component in the control and irradiation of TB. It was discovered that by placing UVC lamps in the air handling equipment, they could initially be more effective. 
     However, certain conditions found within the air handling systems drastically reduced UVC performance. Moving air, especially below 77° F., over the tubes decreased the output and service life of conventional UVC products and thus their ability to destroy viable organisms. The use of UVC with airflow systems virtually disappeared over the next decade due to the introduction of new drugs, sterilizing cleaners and control procedures combined with the performance problems of UVC lamps and air handling systems (reduced output, short tube life, and high maintenance). In order for UVC to be effective in the “hostile” environment of indoor central air circulating systems (or HVAC systems), a new method of producing effective UV had to be developed. 
     The ability of ultraviolet light to decompose organic molecules has been known for a long time, but it is only recently that UV cleaning of surfaces has been explored. In 1972, it was discovered that ultraviolet light could clean contaminated surfaces. Plus, it was learned that there is a predictable nanometer location of absorption of ozone and organic molecules. It was then learned that the combination of ozone and UV could clean surfaces up to two thousand times quicker than one or the other alone. However, from testing it can be seen that the destructive potential of a combination of UVC and ozone for system components is detrimental. The negative side effects of ozone are now known. 
     In 1972, tests were conducted using a quartz tube filled with oxygen. A medium pressure mercury (Hg) UV source which generated ozone was placed within centimeters of the tube. A several thousand angstrom thick polymer was exposed to this and was depolymerized in less than one hour. The major products of this reaction were water (H 2 O) and carbon dioxide (CO 2 ). It was discovered that UV (300 nm and below) and oxygen played a major role in depolymerization. In 1974, research concluded that during such cleaning, the partial pressure of O 2  decreased and that of CO 2  and H 2 O increased, suggesting breakdown. 
     It was also discovered that the absorption coefficient of O 2  increases rapidly below 200 nm with decreasing wave lengths. A 184.9 nm wave length (optimal spectral line for ozone generation) is readily absorbed by oxygen, thus leading to the generation of ozone (O 3 ). Ozone may be generated at undetectable levels at other wave lengths below 200 nm. Therefore, radiation emission below 200 nm was found undesirable. 
     Similarly, most organic molecules have a strong absorption band between 200 nm and 300 nm. A wave length of 253.7 nm is useful for exciting and disassociating contaminant molecules. 265 nm was thought to be the optimal spectral line for germicidal effectiveness. The 253.7 nm wave length is not absorbed by O 2 ; therefore, it does not contribute to ozone generation, but it is absorbed by most organic molecules and by ozone (O 3 ). Thus, when both wave lengths are present, ozone is continually being formed and destroyed. Unfortunately, previously existing lamps operated between 250 nm and 258 nm, peaking at 254 nm, missing out on the optimal 265 nm goal. 
     As indicated above, the effective killing power of UV seemed to be greatest at 265 nm. However, conventional UV has its maximum intensity at 254 nm. Furthermore, the intensity degrades as a function of temperature and distance. This was due to the conventional tubes being designed as long, straight lamps. 
     With regard to HVAC systems, biological contaminants are difficult to control because they grow in our moist, indoor environment. The most common strategy is to try to use an effective air system filter to rid indoor air of biological contaminants. While this is an important element of cleaning air, this has its problems. Most filters are inadequate because of the many organisms that pass right on through the filter. Also, any organisms that collect on the filter can form germ colonies that may soon contaminate passing air. Further, if the filter should be too efficient, it blocks the passage of air and creates back pressure, causing the blower to struggle to move air through the system. Furthermore, when the system is turned off, natural temperature differences between the system and indoor air spaces cause convection or back draft flow into the supply ducts (bypassing the filter). This causes contaminants to be pulled back into the duct work, implanting microbes in the air flow duct cavity. These new cultures become added sources of contaminant. 
     In the past, to try to eliminate the biological contaminants in ducts, a common strategy was to clean the ducts followed by a biocide treatment. But this has its draw backs also. Most biological contaminants return and are active in the treated area within three months. Further, if the system is being treated for severe contamination such as legionela, an acid wash of the coil is common. This is not only expensive, but can shorten the life of the equipment. Furthermore, all biocide used in the ducts are chemical based, leaving potential toxic vapors and chemical pollutants circulating in the system as well. For obvious health reasons, the preferred way to control biological contaminants is through natural, non-polluting strategies. 
     The term “air-conditioning” (A/C) normally refers to cooling the air of a building. An A/C system operates like this: the outdoor portion of the A/C unit compresses a gas to a liquid. During this compression, heat energy is driven out of the liquid. This colder liquid then travels through tubing to the evaporative coil located inside the building proximate the central/furnace fan. 
     The evaporation coil has numerous rows of fins. The fins are all made of an aluminum alloy that is extremely tough due to an impervious film of oxide on the metal. The fins act as heat exchangers with the circulating air within the system. When this compressed liquid reaches the evaporative coil, the liquid expands and evaporates, converting back to a gas. As it does, it recovers the amount of heat energy lost in the compression cycle. This conversion absorbs heat through the coil fins from the surrounding air that is moving across the fins. 
     With the blower operating, air moves across the coil fins and is cooled by losing its heat to the evaporation process inside the coil. 
     If for some reason the central air system becomes less efficient during its operational life, the energy consumption and costs will rise. Since so much energy is involved just in normal use, any change in efficiency will mean a sharp increase in costs. 
     The evaporative coil is made of tiny, closely fitting fins for cooling the air. These fins are so close, the coil essentially becomes a filter, screening out and collecting dust particles from the air. Indoor airborne organic particles and microorganisms are primarily byproducts of human, animal, insect and microbial output (dead skin, hair, paint flakes, insect feces, carpet fibers, etc.) within the indoor environment. As these particles build up, the space between the fins becomes blocked, thus reducing airflow and restricting cooling efficiency of the coil. 
     The coil not only collects these particles, but also becomes a bio-nursery for mold and bacteria. When the A/C operates, water condenses onto the evaporative coil fins. This water drains off into a drip pan. Depending on the amount of moisture within the air, the amount of water collected and drained can be typically six gallons per day. 
     The evaporative coil is mounted in line to the furnace fan housing. Because of its location, the coil housing is very dark and moist. Thusly, it becomes an ideal nursery for the growth of bacteria and mold. Those skilled in the art consider the coil as the number one source of mold in homes. 
     At the coil, volumes of organic contaminates collect in two ways: (a) mold and bacteria growth in the damp coil produces sticky enzyme materials for trapping airborne organic material for food (this forms an activated crusty surface on the fins), and (b) the close fitting coil fins collect airborne particles much like a filter. 
     When the mold colonies grow on the coil, they produce a sticky substance called enzyme mycelium. Enzymes break down proteins and organic compounds. The enzyme mycelium performs two essential functions for molds: (a) the stickiness traps dust particles from the air, and (b) enzymes break the trapped particles into food. 
     With the dust and enzyme material collecting on the coil, an insulation film covers the fins. This installation prevents an efficient heat exchange between the air and fins and efficiency drops. With such restrictions, the cost of operating a coil can increase by 60%. 
     Thus, as can be seen, the coil then becomes a major source of airborne contamination (mold spores, enzymes, toxins and bacteria) due to the growth of mold, bacteria at the coil. 
     The following prior art reflects the state of the art of which applicant is aware and is included herewith to discharge applicant&#39;s acknowledged duty to disclose relevant prior art. It is stipulated, however, that none of these references teach singly nor render obvious when considered in any conceivable combination the nexus of the instant invention as disclosed in greater detail hereinafter and as particularly claimed. 
     
       
         
               
             
               
               
               
             
               
             
               
               
               
               
             
           
               
                   
               
             
             
               
                 U.S. PAT. NO. DOCUMENTS 
               
             
          
           
               
                 U.S. PAT. NO. 
                 ISSUE DATE 
                 INVENTOR 
               
               
                   
               
               
                 1,674,764 
                 June 26, 1928 
                 Dauphinee 
               
               
                 2,279,810 
                 April 14, 1942 
                 Arnott 
               
               
                 2,495,034 
                 January 17, 1950 
                 Sullivan 
               
               
                 2,732,501 
                 January 24, 1956 
                 Blaeker 
               
               
                 3,094,400 
                 June 18, 1963 
                 Blanton 
               
               
                 3,576,593 
                 April 27, 1971 
                 Cicirello 
               
               
                 3,674,421 
                 July 4, 1972 
                 Decupper 
               
               
                 3,744,216 
                 July 10, 1973 
                 Halloran 
               
               
                 3,745,750 
                 July 17, 1973 
                 Arff 
               
               
                 3,750,370 
                 August 7, 1973 
                 Brauss, et al. 
               
               
                 3,757,495 
                 September 11, 1973 
                 Sievers 
               
               
                 3,768,970 
                 October 30, 1973 
                 Malmin 
               
               
                 3,798,879 
                 March 26, 1974 
                 Schmidt-Burbach, et al. 
               
               
                 3,844,741 
                 October 29, 1974 
                 Dimitrik 
               
               
                 4,102,654 
                 July 25, 1978 
                 Pellin 
               
               
                 4,210,429 
                 July 1, 1980 
                 Golstein 
               
               
                 4,255,663 
                 March 10, 1981 
                 Lewis 
               
               
                 4,750,917 
                 June 14, 1988 
                 Fujii 
               
               
                 4,788,007 
                 November 29, 1988 
                 Baron 
               
               
                 4,931,654 
                 June 5, 1990 
                 Horng 
               
               
                 4,981,651 
                 January 1, 1991 
                 Horng 
               
               
                 5,185,015 
                 February 9, 1993 
                 Searle 
               
               
                 5,200,156 
                 April 6, 1993 
                 Wedekamp 
               
               
                 5,225,167 
                 July 6, 1993 
                 Wetzel 
               
               
                 5,288,461 
                 February 22, 1994 
                 Gray 
               
               
                 5,334,347 
                 August 2, 1994 
                 Hollander 
               
               
                 5,382,805 
                 January 17, 1995 
                 Fannon, et al. 
               
               
                 5,439,642 
                 August 8, 1995 
                 Hagmann, et al. 
               
               
                 5,466,425 
                 November 14, 1995 
                 Adams 
               
               
                 5,492,557 
                 February 20, 1996 
                 Vanella 
               
               
                 5,523,057 
                 June 4, 1996 
                 Mazzilli 
               
               
                 5,558,158 
                 September 24, 1996 
                 Elmore 
               
               
                 5,656,242 
                 August 12, 1997 
                 Morrow, et al. 
               
               
                 5,730,770 
                 March 24, 1998 
                 Greisz 
               
               
                 5,817,276 
                 October 6, 1998 
                 Fencl, et al. 
               
               
                 5,853,676 
                 December 29, 1998 
                 Morgan, Jr. 
               
               
                   
               
             
          
           
               
                 FOREIGN PATENT DOCUMENTS 
               
             
          
           
               
                 PATENT NO. 
                 COUNTRY 
                 PUBLICATION DATE 
                 APPLICANT 
               
               
                   
               
               
                 2,461,290 
                 Germany 
                 July 1, 1976 
                 Bohnensieker 
               
               
                 2,618,127 
                 Germany 
                 November 10, 1977 
                 Bohnensieker 
               
               
                 2,732,859 
                 Germany 
                 February 1, 1979 
                 Wagner 
               
               
                 2,817,772 
                 Germany 
                 October 31, 1979 
                 Metallw 
               
               
                 3,637,702 
                 Germany 
                 May 19, 1988 
                 Fuchs 
               
               
                   
               
             
          
         
       
     
     OTHER PRIOR ART (Including Author, Title, Date, Pertinent Pages, Etc.) 
     Nagy, et al., “Disinfecting Air with Sterilizing Lamps”,  Heating, Piping  &amp;  Air Conditioning , Vol. 26., Nos. 1-12, April 1954, pp. 82-87. 
     Steril-Air, Inc., “Steril-Air UVC Emitters Product Brochure”, date unknown, entire brochure. 
     Sterile-Air, Inc., “Guide to UVC Emitters”, date unknown, entire brochure. 
     Philips Lighting, “Disinfection by UV-radiation”, August, 1992, entire paper. 
     Westinghouse, “Sterilamp® Germicidal Ultraviolet Tubes Product Brochure”, March, 1982, entire brochure. 
     Vig, “UV/Ozone Cleaning of Surfaces,  Treatise on Clean Surface Technology , Vol. 1, 1987, pp. 1-26. 
     Jensen, “HVAC Technology is Weapon in Fight Against Tuberculosis”,  ASHRAE Journal , August, 1997, p. 12. 
     Georgia Tech Research Corporation, “Emissions from Mold and Fungus May Cause Indoor Air Problems”, 1996, entire article. 
     Ward, “Is Your Child Allergic to School—Literally?”, www.townonline.com, January, 1997, entire article. 
     Layton, “Allergy &amp; Attention Deficit Hyperactivity Disorder (ADHD)”, www.allergyconnection.com, 1996, entire article. 
     Krajick, “The Floating Zoo”,  Discover , February, 1997, pp. 66-73. Sacramento Municipal Utililty District, “Water Water Everywhere, But . . . ”, On Center , Second Quarter, 1997, p. 1. 
     Bayer, et al., “Study Suggests Some VOCs Caused by Molds and Fungi”, ASHRAE Journal , October, 1996, p. 12. 
     SUMMARY OF THE INVENTION 
     An air cleaning apparatus is disclosed including UV lamps, aluminum filters, and a polished aluminum housing. The UV lamps include a U-bend crystal of quartz, ruby, or sapphire contained within a quartz sleeve. Useful substances for containment within the U-bend bulb are mercury, argon, gallium, iron, xenon or krypton. Between the sleeve and lamp, certain gases (nitrogen or atmospheric gases) are contained therein or the area is possibly evacuated. There are advantages and disadvantages to each. By using a mixture of above gases and/or by varying the electrical charge, one can increase the bandwidth to about 240 nm to about 280 nm, including the 265 nm optimum wave length. Further, increased electrical charge can increase bandwidth and spectral line output from 240 nm to 360 nm for more germicidal effect (UVC/UVB). 
     Polished aluminum filters and chamber walls are also included in this invention. The treated, polished aluminum alloy provides enhanced reflectivity for the UV rays to enhance the irradiation of particulate flowing through the filters and by the lamps. The aluminum filters have an additional special feature in that one side of the filter is of a coarse mesh whereas the other side of the filter is of a fine mesh. Air flow is from the coarse side to the fine side of one filter, past the UV bulbs, through the fine side, and out the coarse side of another aluminum filter and then back into the duct work of an HVAC system. By providing treated, polished aluminum surfaces surrounding the UV lamps, irradiation is enhanced significantly. 
     An alternate embodiment in the form of a portable air cleaning device is also described herein. The purpose of the portable device is to clean a single room with a similar system as described hereinabove, but also including a fan built into the portable unit to move through the system. 
     Another embodiment is described wherein a UV lamp array is mounted exterior to a compressor coil of an HVAC system thereby allowing for cleansing of contaminants contained on the coil and fin structure of the compressor. It has been known that this is a breeding ground for microorganisms and cleansing of this breeding ground will enhance cleansing of the entire HVAC system. 
     By inserting an UVC lamp into the coil region and adding a chemical catalyst, a process of organic “dusting” and microbial cleaning takes place at the coil. The process is further enhanced because the aluminum fins are excellent reflectors of the ultraviolet within the coil chamber resulting in UV amplification, with little or no deterioration on the metal itself. 
     As the air passes the WVC lamp, electrons of a dust, toxins, and microorganism molecules are ejected. Electrons are negative. When the electrons are ejected a positive particle or ion is left behind. 
     As the circulating air pass through the coil fins, the aluminum oxide fins pick up the charged organic and biological materials coming from the UV light area. The organic material adheres to the aluminum fins for several reasons. 
     The oxide film in the aluminum has a high propensity to collect electrons that generates an electrostatic polarity. This produces an affinity for either negative or positive ions (depending upon the pH) to the coil fins. Aluminum oxide has the highest advantage over all solid material because it is very stable over a wide range of pH. Normally the pH on the fin surface will be relatively high from the decay of organic materials on the fins, thus attracting positive ions to the coil. 
     The process on the aluminum oxide mesh is called electronegativity, which forms the basis of electrostatic energy on the filter surface. Electronegativity is based upon the principle of the power of an atom in a molecule to attract elections to itself. The electronegativity of an element depends upon its valence state. Aluminum has an average electronegativity value of 1.61 (near the middle compared to the other element values in the group); oxygen has the second highest value of all elements to attract electrons to itself at 3.44. All coil fins are made of aluminum oxide metal, thus having a very high attraction ability of free electrons to the fins, primarily due to the strength of the oxide (oxygen) to attract elections. 
     The aluminum oxide fins have an enormous capacity to attract an abundance of free electrons stripped by the UV from the incoming organic and biological particles before getting to the coil. As the aluminum oxide collects more and more electrons, the coil loads up on electrons, becoming primarily negative. 
     And as the positively charged organic ion material (coming from the UV light area) nears the negatively charged coil, the organic molecules begin adhering to the fins based upon the principle of positive/negative polarity (the electrostatic principle). In other words, the incoming airborne positively charged organic materials are attracted to the negatively charged coil and adhere to the coil fins. 
     With the dust adhering to the coil fins, the UVC can then begin the breakdown process. The invention then has two methods of breaking apart the hydrocarbon contaminates. 
     The damaging effects of x-ray and gamma ray radiation are recognized but not fully understood. X-ray, gamma, ultraviolet, infrared and visible light energy fit in a category called electromagnetic energy. They all have the same characteristic of an oscillating energy wave that travels at the speed of light. The difference in each type of wave energy is the wavelength or the distance across the wave. The shorter the distance across the wave body, the shorter the wavelength and the stronger the energy. It is this wavelength difference that results in short-wave x-ray passing through walls, while longer wave lengths of visible light cannot. Short-wave ultraviolet and x-ray can destroy DNA in living microorganisms and break down organic material while visible light cannot. 
     The science of ultraviolet radiation usage is essentially the science of photochemistry. Photochemistry is defined as a chemical reaction or change in a material induced by the radiation of light energy. 
     The photochemical process takes place when electrons of a molecule are ejected or changed by the irradiation of light energy, leaving an incomplete and decaying molecule. With the absence of an electron, organic compounds become unstable and fall apart. 
     All organic particles and microorganisms have a strong reaction to light energy between 180-320 nm. Such molecules are vulnerable to short-wave UV irradiation. The reason: molecular structures depend upon the continued maintenance of a molecular weight. But this weight is altered when UV irradiation reduces the number of electrons orbiting an organic molecule. This causes decay of the material. 
     Ultraviolet radiation in the C-band (WVC) has properties that alter the cells of living tissue, particularly microbes due to size. WVC radiation ejects electrons and alters the bonds between amino acids in the microbe&#39;s DNA molecules. This renders bacteria, viruses and molds sterile. The cell structure of microbes will continue to degrade in the presence of short-wave UV and will break down into free state ions and/or separate carbon or hydrogen molecules. 
     One of the reactions is the formation of hydrogen peroxide (H 2 O 2 ) from the photochemical change of the dust, toxins and microorganism collecting at the coil. When the UV changes molecular electrons of the organic material often hydrogen is ejected from the molecules of the material. These hydrogen radicals then react with ordinary atmospheric oxygen (O 2 ), forming hydrogen peroxide H 2 O 2 . The hydrogen peroxide process activates a chain reaction, oxidizing organic material and helping to clean coil surfaces. 
     Further, the hydrogen peroxide is also converted to hydroxide (OH—), which is a very powerful oxidizing agent. 
     At the factory or before the coil is installed, the evaporative coil fins are sprayed with a liquid mixture of water and sodium persulfate (Na 2 S 2 O 8 ), or potassium persulfate (K 2 S 2 O 8 ) or sodium hydroxide (NaOH). These liquid mixtures dry at room temperature on the surface of the coil fins, leaving a residue of the persulfates or sodium hydroxide. 
     The persulfates, when exposed to UV at wavelengths 100 nm to 320 nm, forms hydrogen peroxide (H 2 O 2 ). Hydrogen peroxide, however, quickly breaks down into hydroxide (OH) and water (H 2 O) when exposed to these UV wavelengths. 
     Under the alternative, the sodium hydroxide, when exposed to short wave ultraviolet, breaks down into sodium (Na) and hydroxide (OH). 
     The dried crystals of persulfates within the coil fins, when exposed to UV form by products including hydrogen sulfate and hydrogen peroxide (S 2 O 8   −2 +2H 2 O+UV=2HSO 4   − +H 2 O 2 ). The hydrogen peroxide (H 2 O 2 ) both hydroxide (OH) and water in the presence of UV (H 2 O 2 +UV=H 2 O+OH). 
     The hydroxide formation is from the UV and persulfates (persulfates to hydrogen peroxides converting to hydroxide in the presence of short wave to medium wave UV) or the sodium hydroxide that have been sprayed on the coil fins. In either case hydroxide is formed in the presence of UV. 
     Hydroxide is a stable but a very potent one-electron oxidant. The reason hydroxyl ions are so destructive to organic molecules (house dust, toxins and microorganism) is the hydroxide ions “capture” hydrogen molecules from the organic materials, leaving decayed carbon ions. The removal of hydrogen from organic molecules by hydroxide forms even stronger reactive OH bonds as the result of the water at the coil. The process turns into a chain reaction, resulting in continual decay of the organic material by hydroxide formation and converting back to water. 
     Hydroxide primarily targets organic materials for oxidation. This oxidizing agent thrives by absorbing hydrogen from organic compounds. Hydroxide is perhaps the ideal oxidizer for cleaning organic growth in the evaporation coil without the corrosive effects of ozone. A damp coil is the best environment to experience the full effects of UV. It is in this promising condition that UV energy breaks down the collected organic material, setting off a chain reaction of hydroxide and hydroperoxide formation, which further destroys organic materials. 
     This means the invention effectively cleans the evaporation coil of organic particle collection and destroys any growth of germs and mold accumulating at the coil. Once clean, the coil remains clean in the presence of the invention. 
     OBJECTS OF THE INVENTION 
     Accordingly, it is a primary object of the present invention to provide an ultraviolet ray actinism chamber for destroying contaminants thereby. 
     Another object of the present invention is to avoid the production of ozone in such a system. 
     Another object of the present invention is to provide increased UV bandwidth to so increase the “killing” power of the UV system. 
     Another object of the present invention is to maintain a substantially constant temperature around the UV bulb. 
     Another object of the present invention is to increase UV reflectivity in and around the UV bulbs to enhance the UV irradiation. 
     Another object of the present invention is to provide self cleaning filters for a UV system. 
     Another object of the present invention is to provide better, yet shorter lamp lengths to fit in conventional HVAC systems. 
     Yet another object of the present invention is to enhance the bulb life of a UV bulb for such a system. 
     Viewed from a first vantage point, it is an object of the present invention to provide an apparatus for purging impurities from ambient air conditions, comprising: a source of radiation in operative communication with the ambient air conditions; and a coating upon which radiation emitted from said source impinges thereon facilitating a chemical reaction. 
     Viewed from a second vantage point, it is an object of the present invention to provide an a method for purging impurities from ambient air conditions, comprising the steps of: creating turbulent air around an ultraviolet light source; passing the turbulent air adjacent to the ultraviolet light source to create a photochemical reaction. 
     Viewed from a third vantage point, it is an object of the present invention to provide a self-cleansing filter or evaporative coil prepared by a process comprising the steps of: coating a substrate with a mixture of water and sodium hydroxide or a persulfate; drying the mixture coated in the substrate at room temperature leaving a residue of the persulfate or sodium hydroxide 
     Viewed from a fourth vantage point, it is an object of the present invention to provide a chamber for cleansing ambient air, comprising, in combination: an air inlet; an air outlet; said chamber interposed and communicating between said inlet and outlet; a source of radiation in said chamber, said chamber imperforate to the radiation; said chamber having an interior surface with means for reflecting substantially all the radiation; and a coating means to enhance the effect of the radiation. 
     Viewed from a fifth vantage point, it is an object of the present invention to provide a method for coating a filter mesh or an evaporative coil for providing either negative or positive ions depending upon the pH or pOH, the steps comprising: forming a filter mesh or evaporation coil out of aluminum; dipping or spraying the filter mesh or evaporation coil with a liquid mixture to form a film; wherein the liquid mixture is selected from the group consisting of water and sodium persulfate, potassium persulfate and sodium hydroxide. 
     Viewed from a sixth vantage point, it is an object of the present invention to provide an method of photochemically treating ambient air to purge impurities, the steps comprising: filtering the air; exposing the air to a source of radiation; further filtering the air after exposure to radiation to arrest irradiated particles within the air after irradiation; and further exposing the arrested, irradiated particles to further radiation causing a break down of the molecular structure of said irradiated particles that yields a self-cleansing effect to a structure to which the arrested, irradiated particles were arrested by. 
     Viewed from a seventh vantage point, it is an object of the present invention to provide a method of treating air with a chemical disposed on an aluminum substrate, the steps comprising: passing air through the aluminum substrate in order to arrest particles or organic molecules; exposing the particles or organic molecules to radiation to cause breakdown of the molecular structure in order to remove particles or organic molecules from the aluminum substrate thus providing a self-cleansing effect. 
    
    
     These and other objects will be made manifest when considering the following detailed specification when taken in conjunction with the appended drawing figures. 
     BRIEF DESCRIPTION OF THE DRAWINGS 
     FIG. 1 is a perspective view of the UV lamp of the invention. 
     FIG. 2 is a top view of an embodiment of the invention. 
     FIG. 2A is a top view of an alternative embodiment of the invention 
     FIG. 3 is a cross-sectional front view taken along lines  3 — 3  of FIG.  2 . 
     FIG. 3A is a cross-sectional front view taken along lines  3 A— 3 A of FIG. 2A 
     FIG. 4 is a cross-sectional side view taken along lines  4 - 4  of FIG.  2 . 
     FIG. 5 is an exploded parts perspective view of the invention. 
     FIG. 6 is a perspective view of a portable alternate embodiment of the invention with a side panel off and the two alternative reflective plates projected. 
     FIG. 7 is a perspective view of an external alternate embodiment of the invention. 
     FIG. 8 is a perspective view of the electrode connection of the invention. 
     FIG. 9 is a cutaway view of the chamber of the invention showing rays bouncing off the V-shaped reflective baffles within the chamber of the invention. 
     FIG. 9A is a cutaway view of the chamber of the invention showing rays bouncing off the somewhat U-shaped channeled baffles with the bight perpendicular to the airstream and the legs diverging outwardly down stream. 
     FIG. 10 is a top cutaway view of the coarse filter weave. 
     FIG. 11 is a top cutaway view of the fine filter weave. 
     FIG. 12 is a top view of the baffle showing the venturi effect created by its insertion into the airstream. 
     FIG. 12A is a top view of the alternative baffle showing the venturi effect created by its insertion into the airstream. 
     FIG. 13 is an alternative embodiment of the filter of the invention. 
     FIG. 14A is view showing the removal of a side panel. 
     FIG. 14B shows a view of the light bulbs being inserted. 
     FIGS. 15A, B, and C show an alternative bulb and coil positioning of the invention. 
     FIGS. 16A, B, and C show another alternative bulb and coil positioning of the invention. 
    
    
     DESCRIPTION OF PREFERRED EMBODIMENTS 
     Considering the drawings, wherein like reference numerals denote like parts throughout the various drawing figures, reference numeral  10  is directed to the air actinism chamber according to the present invention. 
     The invention relies on four main components: UV lamp  50 , photon chamber  34 , baffles  26  or  26 A and filters  20 . Each component will be described more particularly below. 
     As seen in FIGS. 1 and 8, UV lamp  50  consists of a U-shaped UV quartz, ruby, or sapphire crystal  12  (with quartz being preferred), a quartz sheath  14 , lamp coupling overlay  16 , lamp base  32 , U-shaped bulb gases  41 , and lamp gas  44 . U-shaped bulb  12  is preferably a quartz glass tube up to fifty inches long that is bent at the center to form a U-shaped bulb filled with one or more of the following: mercury, argon, iron, gallium, xenon or krypton. Aluminum metal or ceramic material is machined for the base  32  of the lamp for holding both the lamp tube  12  and electrode igniters  18 . An aluminum coupling  16  allows for good heat transference resulting from the heating of electrodes  18  inside the aluminum coupling  16 . That convection heat will be used to maintain its own stabilizing environment around the U-shaped bulb  12  and within the quartz sheath  14  regardless of ambient temperatures. 
     Once the U-shaped bulb  12  is mounted onto the aluminum coupling  16  at the point where electrodes  18  extend from within the coupling  16 , a gas or gas mixture is sealed within quartz sheath  14 . That gas or gas mixture is preferably comprised of nitrogen, ordinary air, or evacuated space. By using just air, an approximately 3% loss of intensity of UV is suffered, but certain other costs are lessened. The 3% loss could be eliminated by evacuating the space, however, heat convection does not work as well without gases. Nitrogen gas hermetically sealed under the quartz sheath  14  seems to be best, but manufacturing is more complicated. 
     By sealing the U-shaped quartz bulb  12  within quartz sheath  14 , a constant temperature around bulb  12  is maintained at approximately 80° F. to 90° F. This has been found to be the case even when ambient air temperatures are as low as 45° F. The entire lamp  50  coupled to a proper power supply, as seen in FIGS. 1 and 5, then, for all normal intents and purposes, has the ability to maintain the highest level of intensity regardless of surrounding air temperature or air speed. 
     UV lamp  50  provides a broader bandwidth compared to conventional UV lamps. As described above, conventional UV lamps emit a bandwidth of about 250 nm to 258 nm. UV lamp  50  provides a bandwidth of about 240 nm to 280 nm, including the optimal 265 nm wavelength and provides approximately six times the UV intensity of conventional lamps at colder temperatures. Furthermore, this is achieved while ambient air temperature around UV lamp  50  is 45° F. to 90° F. Although more power may be required, it has also been discovered that operation at “medium-pressure” will achieve a bandwidth of 230 nm to 380 nm, with an excellent spike at 264 nm. Another optimum point has also been discovered between 310 nm and 340 nm. So, although greater power, and therefore cost, may be required, greater particulate destruction is possible. 
     The chamber is shown in FIGS. 2 through 5. Lamps  50  are then mounted into housing  28  that includes the electronics and power supply to drive the lamps  50 . The power supply is preferably either a matched 110 or 220 volt AC input power supply having a power cord  64 . To start the lamp, the power supply sparks the UV gas core  44  and ignites it from a cold start with a temporary voltage spike of about 3,000 volts passing through electrodes  18  and wires  19  (see FIG. 8) to the substances contained within bulb  12 . Once the substances are ignited by this starting voltage, the power supply output voltage adjusts down to an operating voltage of about 200 volts to 240 volts AC. By inserting lamps  50  into a chamber of an HVAC unit, UV irradiation of air flowing over and by the lamps  50  is achieved. However, the actinism in the chamber can be enhanced by using special aluminum filters  20  and reflective surfaces within chamber  34 . 
     UV ray reflection can be accomplished by several surface types. Magnesium Oxide, for instance, has been found to achieve the greatest reflectivity (75% to 90%), but is not suited for normal use due to its negative properties. Polished aluminum alloy (treated with Alzak), on the other hand, can achieve up to 95% reflectivity and is well suited to production and manufacture. Typical duct liner reflects 0% to 1% of UV rays which is a draw back of the prior art. Even stainless steel only achieves 25% to 30% reflectivity. Therefore, treated aluminum alloy is preferred. 
     First, with regard to the filters, a two layered filter constructed of buffed aluminum is preferred. A first coarse layer  22  on an outside of the filter  20  and a second fine mesh layer  24  on the inside of the filter is preferred, wherein the mesh is a wavy aluminum strand weave  21  (FIGS.  10  and  11 ). That weave may also consist of ribbons of aluminum strands  21 A,  21 B,  21 C interwoven with other such ribbons  21 D,  21 E,  21 F, as shown in FIG.  10 . As air flows through the coarse mesh  22  large particulate can be captured and irradiated within the filter before exiting through fine mesh  24 . Additionally, because of the reflective nature of the inside of the housing and baffles  26  or  26 A the UV rays are thereby enhanced. Particles trapped within the filter will be bombarded with UV until destroyed, thereby causing the filters to be self-cleaning within the effective irradiation range. The filter housing is made of aluminum that is polished in order to get maximum UV reflectivity within the filter chamber. Further, the media filter on the output side of the filter chamber is made of fine aluminum mesh with a surface oxide for two important reason: (a) The ionization process within the chamber is assisted by the aluminum mesh, and (b) the media webbing of the filter catches (by ionization, electrostatic and barrier methods) and holds the particles/organic molecules so the UV irradiation breaks down the organic molecules, cleaning the filter surface of particulate collection. 
     The filter mesh is dipped/sprayed with a liquid mixture of water and sodium persulfate (Na 2 S 2 O 8 ), or potassium persulfate (K 2 S 2 O 8 ) or sodium hydroxide (NaOH). These liquid mixtures dry at room temperature on the surface of the mesh, leaving a residue of the persulfates or sodium hydroxide. The persulfates, when exposed to UV at wavelengths 100 nm to 320 um, form hydrogen peroxide (H 2 O 2 ). Hydrogen peroxide, however, quickly breaks down into hydroxide ions (OH—) and water (H 2 O) when exposed to these wavelengths. Under the alternative, the sodium hydroxide, when exposed to short wave ultraviolet, breaks down into sodium ions (Na+) and hydroxide ions (OH—). 
     Furthermore, by providing reflective baffles  26  and  26 A that are polished aluminum positioned on the incoming air side wall, reflection is additionally enhanced. The geometries of the baffles  26  and  26 A tend to reflect UV rays back toward the central portion of the chamber  34 . The polishing of the aluminum baffles  26  and  26 A reflect up to 90% of the UV striking the baffle surfaces and facilitate focusing the reflected UV on to the aluminum filter mesh for higher UV intensity on the fine mesh filter surface  24 . The geometry of baffle  26  is a V-shaped channel with the vertex edge facing the incoming airstream while the legs are diverging outwardly downstream. The geometry of baffle  26 A is a somewhat U-shaped channeled with the bight perpendicular to the incoming airstream and the legs diverging outwardly down stream. Also, the baffles  26  and  26 A prevent direct UV light traveling back out the coarse mesh  22 . As the air passes through the incoming opening, the baffles  26  and  26 A angle the air toward the outer edges of the baffles, creating the venturi-effect and causing turbulence. This pulls the circulating air back over the edges of the baffles, next to the UV lamps (sitting in the partial vacuum). By also providing wall  42  and bottom wall  40  of a polished aluminum material, maximum reflective irradiation is achieved. The UV rays will either strike particulates directly or will be reflected about the chamber enhancing the irradiation bombardment. Certainly, by sizing the chamber  34  appropriately, it could be retrofitted within existing certain HVAC filter housings without modification to the existing housings. However, where an HVAC unit is of an unusual size, minor modifications may be rendered to so fit chamber  34 . 
     In use and operation, as viewed in FIG. 4, air A traveling through the duct work of a HVAC system will travel through a first aluminum filter  20  by way of its first coarse mesh  22  and then its first fine mesh  24 . Thereafter, the air enters chamber  34  and as the air passes through the incoming opening, the baffles  26  and  26 A angle the air toward the outer edges of the baffles, creating the venturi-effect. This pulls the circulating air back over the edges of the baffles, next to the UV lamps (sitting in the partial vacuum) and flows by UV lamps  50  thus increasing the amount of irradiation the passing air receives. The air then exits the actinism chamber  34  through another fine mesh  24  of second aluminum filter  23  and out through a second course mesh  22 . Thereafter, having been irradiated and filtered, the air is returned to the HVAC ducts. Any particulate remaining in the second aluminum filter  23  will continue to be irradiated until destroyed by UV lamps  50  as seen in FIGS. 9 and 9A. 
     Installation of UV filter will be in the traditional location of current building central air filters: in the system return air ducts, cavity or plenum. The air is pulled through the return air ducts, cavity or plenum. The air is pulled through the return air ducts by the fan located in the furnace housing. 
     Incoming air passes through the incoming opening into the UV chamber of the filter housing. Mounted on the incoming side are several angled/curved polished aluminum baffles  26  or  26 A running from top to bottom. 
     As the air rushes (indoor air in a system return duct moves about 200-300 fpm through the duct) through the incoming filter opening, the baffles  26  and  26 A mounted inside this perforated wall, creates the venturi-effect. This results in the circulating air being pulled against each of the UV lamps mounted within the cavity of the angular baffles for maximum irradiation of passing air. See FIGS. 12 and 12A. 
     Each lamp  50  runs parallel to the baffle  26  or  26 A and within the angular cavity of the baffle. See FIGS. 9 and 9A. The UV irradiation from the backside of the lamp projected toward the baffle  26  or  26 A is reflected back out to the lamp area, increasing the UV intensity on the airborne particles that have been pulled by partial vacuum next to the lamp. Within inches of the lamps, all airborne microorganisms are irradiated with high intensity UVC (ultraviolet radiation in the short wave or C band range), leaving most airborne organisms killed. In addition, this high intensity UVC region strips electrons from the dead and dying organisms and other airborne organic particles. 
     Further, the highly polished aluminum baffles  26  or  26 A reflect up to 90% of the UV irradiation to the opposite filter mesh wall  22 . This bathes the mesh with up to 90% more UV irradiation than would be present directly from the lamps. The higher intensity at the filter mesh helps to break down the dust and biological materials collecting on the filter mesh at a faster rate. 
     Ultraviolet photons emitting from the lamps  50  with the short/medium wavelength ultraviolet light starts the electron stripping and ionization process of air passing through the actinism chamber  34  because the incoming air is populated with airborne biological and organic dust. 
     Airborne organic molecules (compounds made of carbon, hydrogen, oxygen and nitrogen) have high absorption (decay) rate when exposed to short/medium wavelength UV in the order of 230 nm-320 nm . The process of organic decay starts when UV irradiates the airborne organic or biological particles, stripping the material of electrons. The particles become positively charged or ionized. 
     The process of electron stripping, within the present invention&#39;s UV filter, has a direct effect upon circulating airborne organic and biological materials circulating and growing within the central air system. It begins when the circulating air (populated with organic and biological materials) is pulled though the filter  20  and immediately to each individual UV lamp  50  as the result of the baffles  26  and  26 A causing an eddy current of turbulence which creates a partial vacuum. The intensity in the immediate area of the lamp is elevated by the baffle reflectivity of secondary UV. As airborne organic molecules are exposed to the UV lamp  50 , electrons are stripped from the materials and the decay begins, leaving most of the airborne particles positively charged. 
     The airborne charged particles continue to be pulled to the opposite wall of the actinism chamber  34  by the system fan (e.g.  46  in FIG. 6) further downstream from the filter  23 . The filter  23  contains two porous aluminum mesh filters, the coarse mesh  22  and fine mesh  24  so the air to can continue unabated through the filter and on to the blower assembly. The filter mesh has been previously sprayed with or dipped into a liquid sodium persulfate, potassium persulfate or sodium hydroxide mixture. The mixture, once dried will form crystals on the mesh material. 
     As the air continues through the filter mesh  23 , the aluminum oxide fibers pick up the charged organic and biological materials coming from the UV light and baffle area. The organic material adheres to the aluminum mesh for several reasons. 
     The filter mesh material is an aluminum alloy that is extremely tough due to an impervious film of oxide on the metal. But any material can be used that is combined with an oxide. The aluminum oxide mesh is preferred because of two reasons: (a) The aluminum is excellent for reflecting the ultraviolet within the filter chamber resulting in UV amplification, with little or no deterioration on the metal itself. (b) The oxide film in the metal has a high propensity to collect electrons that generates an electrostatic polarity. This produces an affinity for either negative or positive ions (depending upon the pH) to the filter mesh. Aluminum oxide has the highest advantage over all solid material because it is very stable over the wide range of pH. Normally the pH on the filter surface will be relatively high from the decay of organic materials on the filter, thus attracting positive ions to the mesh. 
     The process on the aluminum oxide mesh is called electronegativity, which forms the basis electrostatic energy on the filter surface. Electronegativity is based upon the principle of the power of an atom in a molecule to attract electrons to itself. The electronegativity of an element depends upon its valence state. Aluminum has an average electronegativity value of 1.61 (near the middle compared to the other element values in the group); oxygen has the second highest value of all elements to attract electrons to itself at 3.44. The filter, made of fibrous aluminum/oxide metal, has a very high attraction ability of free electrons to the webbing, primarily due to the strength of the oxide (oxygen) to attract elections. 
     The aluminum oxide filter has an enormous capacity to attract an abundance of free electrons that the UV stripped from the incoming organic and biological particles near the baffles. As the aluminum oxide collects more and more electrons, the filter mesh loads up on electrons, becoming primarily negative. 
     And as the positively charged organic ion material (coming from the UV light area) nears the negatively charged filter, the organic molecules begin adhering to the mesh&#39;s webbing based upon the principle of positive/negative polarity (the electrostatic principle). In other words, the incoming airborne positively charged organic materials are attracted to the negatively charged webbing and adhere to the filter mesh. 
     But the electron stripping at the lamp and collection at the filter mesh is just the primer to start a very dynamic process. The process becomes a chain reaction with the formation of Hydroxide(OH—)/Hydroxyl(OH) on the filter mesh in two ways: (a) when organic compounds break down in the presence of UV, one of the byproducts is water (H 2 O). Water is exposed to short wave UV can form Hydroxyl (OH). (b) The dried crystals of persulfates within the filter mesh, when exposed to UV form hydrogen sulfate and hydrogen peroxide (S 2 O 8   −2 +2H 2 O+UV=2HSO 4   − +H 2 O 2 ). The hydrogen peroxide (H 2 O 2 ) both hydroxide (OH—) and water in the presence of UV (H 2 O 2 +UV=H 2 O+OH). 
     The UV intensity on the filter mesh  23  is extremely high due to the direct ultraviolet of the UV lamps and baffle UV reflectivity focused on the filter. With the organic material collecting the filter webbing  21 , see FIG. 10, the UV irradiation has plenty of dwell time to complete the break down process on the larger collected particles. The primary purpose of the filter mesh is to collect the organic material so the UV can decay the organic material, resulting primarily -in airborne carbon, oxygen, hydrogen and nitrogen. There will be also be traces of H 2 O (water) and CO 2  (carbon dioxide) formed as the result of the breakdown process of the organic materials. Thus cleaning the mesh surface  21 , as well as decaying airborne toxins and germs. 
     An operating actinism chamber  34  is a very dynamic environment with many physical and chemical processes going on simultaneously, all started by high intensity short/medium UV radiation. The filter baffles  26  or  26 A create eddies that pull the incoming air up against the UV lamps located within the baffle&#39;s cavity. The high intensity ultraviolet strips electrons from the airborne organic and biological materials. By losing electrons, the organic material becomes positively charged material. An abundance of free electrons collect within the filter chamber on accelerated bases as more material is exposed to UV radiation. In the meantime, the aluminum oxide filter mesh  23  has high propensity to absorb free electrons. As the aluminum oxide filter webbing  21  collect more and more electrons, the mesh gains a negative charge. The negative charge on the filter surface then gains polarity with the positive airborne organic particles, collecting the particles on the filter surface. 
     The formation of hydroxide ions from either the persulfates reaction (persulfates to hydroperoxides converting to hydroxide in the presence of short wave to medium wave UV) presents a stable but a very potent one-election oxidant. The reason is that hydroxide is destructive to organic molecules because it “steals” hydrogen molecules from the organic materials, leaving decayed carbon ions. 
     The “theft” of hydrogen from organic molecules by hydroxyl radicals forms even stronger OH bonds, with even higher oxidation, as the result of water and hydroperoxide on filter mesh. The hydroxyl oxidation process turns into a chain reaction on the filter mesh the breakdown and formation of new radicals results in continual decay of the organic material on the filter. 
     The above-described configuration is ideal for insertion into the return of an HVAC system. FIG. 6 depicts a similar, but alternative embodiment for portable use within a room. Fan  46  provides for the air flow A of this portable device through similar but smaller aluminum filters  20 . Between the filters  20 , again are maintained one or more UV lamps  50 . To transport this item, handle  48  is also provided. Reflective enhancement of the radiation is likewise caused by a plurality of polished aluminum surfaces throughout the inside of the chamber. This is an ideal apparatus for cleaning the air in a single room. 
     FIG. 7 depicts another alternate embodiment for use with an external HVAC device. An evaporative coil  54  having fins  56  is coupled to a typical compressor  52  thereby is depicted in FIG.  7 . To prevent contamination build-up and to destroy contamination build-up on or about coil  54  UV lamp or lamps  50  are mounted near coil  54 . By continuing the lamps  50  in an “on” setting, and additionally using the reflective properties of the aluminum fins  56 , any contamination on or near the coils is eliminated. The fins  56  are preferably wetted with sodium persulfate, potassium persulfate or sodium hydroxide and then dried forming a crystalline skin. By maintaining this area in a clean manner, air flow over the area and into the duct work of an HVAC system will be less likely to carry such contamination. In the alternative to this embodiment, baffles  26  and  26 A could be placed in such a configuration whereby the UV lamps  50  are contained within the cavity formed by the baffling such that the air is diverted around the UV lamps  50 . This geometry would yield similar results to the geometry for the embodiments described supra and shown in FIGS. 2 through 6 and  12  and  12 A. 
     FIG. 13 shows an alternative embodiment  200  of the invention. A filter cassette  210  includes an air outlet plate  220  and an air inlet plate  230 . The air outlet plate  220  is mainly constructed of the filter mesh  240 . The air inlet plate  230  is formed from a piece of planar material. During the manufacturing of the air inlet plate  230 , the planar material is incised at particular positions within the material. The incisions produced during the manufacturing process permit portions of the material to be bent in a manner to form the baffling  260 . This baffling is analogous to the shapes shown in FIGS. 12 and 12A for baffling  26  and  26 A. The bulbs  50  (not shown) are behind the baffling  260  and in this configuration generates analogous results as the baffling  26  and  26 A described supra. The air inlet plate  230  is hinged at  231  to permit access to the interior of the cassette. Below the removable side panel  250  is a standard  115  vac outlet  270  for supply power to the bulbs  50 . 
     FIGS. 14A and 14B show the removable side panel  250  have been remove and exposing holes  251  for the bulbs  50  to be inserted therein such that the bulbs  50  would be proximate the baffling  260  and within the filter cassette  210 . This arrangement permits ease of bulb replacement and filter cassette cleaning. 
     FIGS. 15A and 15B show the arrangement of bulbs  50  relative to a coil installation where the coils  56  are positioned in a “V” configuration. While in FIG. 15C, the figure shows the arrangement of the housing  28  with bulbs  50  relative to a coil installation where the coil  56  is at a slant within the chamber the coil  56  is installed within. The interrelation between the bulbs  50  and coils  56  is that the bulbs are positioned on the upstream side of the coils. However, alternatively the bulbs  50  could be positioned on the downstream side of the coils  56 . For the best exposure to the coil  56  the bulbs  50  should be at least six inches away from the coil or coils  56 . 
     Likewise FIGS. 16A and 16B show the arrangement of bulb  50  relative to a coil installation where the coils are positioned in a “V” configuration. While in FIG. 15C, the figure shows the arrangement of the housing  28  with bulb  50  relative to a coil installation where the coil  56  is at a slant within the chamber the coil  56  is installed within. The interrelation between the bulb  50  and coils  56  is that the bulb  50  is positioned on the upstream side of coil  56 . For the best exposure to the coil  56  the bulb  50  should be at least six inches away from the coil or coils  56 . 
     For the installations shown in FIG. 15A through 16C, viewpoint  501  should be drilled anywhere in a direct line of sight of the hole or holes  502  for the bulbs  50 . 
     Moreover, having thus described the invention, it should be apparent that numerous structural modifications and adaptations may be resorted to without departing from the scope and fair meaning of the instant invention as set forth hereinabove and as described hereinbelow by the claims.