Patent Application
20090151565
The present invention pertains to the art of glass-wool fiber insulation production and, more particularly, to a method and scrubbing apparatus for removing particulate pollutants from stack gases generated during the production of glass fiber wool-type insulation products.
During the manufacture of glass fiber wool-type insulation products, molten glass from a refining tank flows into equipment which physically forms the molten glass into fibers which are sprayed with a curable organic resin binder. The binder coated glass fibers are then formed into a pack or mat via deposition onto a foraminous belt. The foraminous belt conveys the glass fiber/resin mixture through a curing oven during which time the resin hardens to create a wool-like insulation product.
Located beneath the foraminous belt is an air intake. The air intake receives a gas flow that penetrates through the formed pack of fibers and the foraminous belt. The gas flow is composed of natural gas combustion products, along with compressed and induced air exhausted from the fiber forming equipment, evaporated water, compressed and induced air that is used to distribute the glass fibers onto the foraminous belt and inducted factory air that serves to contain the falling resin/fiber mixture within the glass fiber pack/mat forming apparatus. The gas flow ultimately passes through a vertical exhaust stack and is discharged into ambient atmosphere. Prior to being discharged, the air flow passes through a scrubber system that removes foreign particles developed during the glass wool fiber and pack/mat forming process.
In general, most known scrubber systems employ water droplet impaction, gravity settling, cyclonic separation or barrier impaction to sequentially cause larger, and then smaller, particles to be removed from the air flow. Another known system constitutes a wet electrostatic precipitator or WEP that can be used to capture particles which have Is passed through a preceding device. In a WEP, the particulate is ionized via an electrode created corona discharge. The ionized particulate is then collected on a positively charged wall located within the WEP. While considered effective, the WEP is a very high capital and operating cost component that consumes additional energy during operation.
Certainly, other emission reducing systems exist in other product manufacturing fields. One such known arrangement is constituted by a cloud chamber system that employs a pre-conditioning chamber (PCC) and a set of cloud generating vessels (CGV's) to remove particles from an air flow. While in the PCC, coarse particles are removed and many ultra fine particles are grown to larger particles. The PCC also allows the air stream to cool to the saturation point. From the PCC, the air stream passes through a demister and then into the CGV's. In the first CGV, the air stream mixes with a cloud of positively or negatively charged water droplets and, in the second CGV, the air stream mixes with a cloud of water droplets which are charged oppositely than those in the first CGV. Neutrally charged particles contained within the air stream are attracted to the positively and negatively charged water droplets and captured. After treatment in the cloud chamber system, the air flow is passed to a demister which removes remaining moisture.
In connection with the present invention, a need has been recognized for an enhanced apparatus and method for removing fine particulate pollutants from stack gases generated during the production of glass-wool fiber insulation. More specifically, a need has been recognized for an energy efficient, cost effective, particulate removal system having multiple stages that synergistically operate to reduce line emissions in the field of fiberglass wool insulation production.
The present invention is directed to a scrubbing apparatus for removing particulate from an air stream generated during a glass-wool insulation fiber and pack/mat forming process. The apparatus includes an air duct that guides an air stream containing glass-wool particulate away from a glass-wool insulation fiber and pack/mat forming apparatus, a first separator system, established by a series of chambers and separators, for removing a first portion of the particulate from the air stream and for providing cooling, humidification and residence time to promote the growth and agglomeration of smaller particles into larger particles, a second separator system in the form of a single cloud generating vessel (CGV) employed to remove a second portion of the particulate, and a third separator system for both removing moisture and a third portion of the particulate from the air stream.
In accordance with the invention, the first separator system effectively provides ample time for the air stream to cool to saturation temperatures, become humidified and be stripped of larger particulates, while also affording a high residence or pre-treatment time that enables fine particles to grow into larger particles. In accordance with the invention, the first separator system can take various forms, including:
In any case, the air stream emanating from the first separator system is directed to the single CGV for further particulate separation. By providing sufficient time for the fine particles to grow into larger particles in the first separator system, the overall efficacy and efficiency of the single CGV cloud generating chamber is significantly improved. Downstream of the CGV is the third separator system which functions to remove both moisture and another portion of the particulate prior to exhausting of the air stream. The use of the first separator system in combination with the single CGV and the third or downstream separator system has been found to have a synergistic effect in reducing fiberglass wool insulation production line emissions such that an extremely effective and efficient overall production control arrangement is established.
Additional objects, features and advantages of the present invention will become more readily apparent from the following detailed description of preferred embodiments when taken in conjunction with the drawings wherein like reference numerals refer to corresponding parts in the several views.
With initial reference to
As will become more fully evident below, the present invention can take various forms and employ certain variations in construction without departing from the invention. In the embodiment depicted in
In accordance with this first embodiment of the invention, scrubbing apparatus 33 includes an air duct 40 having a first end portion 42 which is fluidly connected to collection hopper 25 through fan 30 and extends to a second end portion 43. Second end portion 43 is connected to a first separator 47 which, in accordance with the first embodiment of the present invention, is constituted by a venturi scrubber forming part of a first separator system. Venturi scrubber 47 includes an inlet portion 49 for receiving the particulate laden air stream and an outlet portion 50. In addition, venturi scrubber 47 includes a water inlet 56 which receives a pressurized water flow that mixes with the air stream to moisten any particulate contained therein. While in venturi scrubber 47, a first portion or larger particles are trapped and collected, while finer particles collide and grow into larger particles. In any case, venturi scrubber 47 is also shown to include a drain 58 which leads back to recycled water reservoir 24. After being treated in venturi scrubber 47, the air stream laden with moist particulate, enters into an air duct 60 and passes into a second separator 64 of the first separator system.
In further accordance with the embodiment shown, second separator 64 is constituted by a cyclone separator, of a type known in the art, having an inlet portion 67 that receives the air stream laden with moistened particulate and an outlet portion 68. Cyclone separator 64 is further shown to include in some cases a water inlet conduit 71 which is connected to a nozzle ring 72 that is positioned adjacent outlet portion 68 or inlet portion 67. Nozzle ring 72 preferably includes ten to twelve water nozzles (not shown) that provide a water spray within cyclone separator 64 that facilitates the capture of another portion of the particulate. More specifically, whether water sprays systems depicted by 71 and 72 are included or not included, the cyclonic environment forces larger particles to fall along inner wall portions of cyclone separator 64, while allowing smaller particulates to exit through outlet portion 68. In addition, while in cyclone separator 64, fine particles adhere to one another and grow into even larger particles. Cyclone separator 64 is also shown to include a drain 74 that allows water flowing from second separator 64 to pass through a drain conduit 75 into recycled water reservoir 24. Water 23 typically only includes larger particles which can be readily removed through a simple filtering process. With this arrangement, a high percentage of water utilized in the overall glass-wool forming process can be readily re-used. In any case, by passing the particulate laden air stream through first and second separators 47 and 64, not only does the air stream cool to saturation temperatures, but the particles are provided a high residence time prior to entering a duct 80 for passage to a third separator 83 which captures yet another portion of the particulate. As noted above, the higher residence time enables an extremely large portion of the ultra fine particles, in the order of the size of a few hundredths of a micron, to grow in size, such as to a few tenths of a micron, thereby facilitating their removal from the air stream.
As noted above, the air stream passes from second separator 64 through duct 80 into third separator 83 which, in accordance with the present embodiment, is part of a second separator system and constituted by a single cloud generating vessel having an inlet portion 86, an outlet portion 87 and an interior chamber 88. The overall operation of cloud generating vessel 83 is known in other fields as discussed above and therefore will not be described in detail herein. However, in broad terms, while in interior chamber 88, particles are attracted to droplets of water and captured through monopole induced dipole charging effects. In accordance with the invention, either positive or negative charges are associated with the operation of cloud generating vessel 83. The cloud generating vessel defining third separator 83 can take various forms, such as a cloud generating vessel produced by the TRI-MER Corporation. After the particulate is captured within cloud generating vessel 83, the air stream passes through outlet portion 87. Residual moisture containing captured particles remaining within interior chamber 8 is directed through a drain 92 which leads to a drain conduit 93 that empties into a gray water reservoir 96. More specifically, the portion of the particulate separated out by cloud generating vessel 83 contains high percentages of cured or advanced binding material or resin. Towards that end, any moisture accumulated within interior chamber 88 and discharged through drain 92 likewise contains a high percentage of cured or advanced resin and thus is preferably not recycled back through the glass-wool fiber forming process. Any water contained within gray water reservoir 96 can be readily treated and discharged or, treated, retained and stored to address local environmental regulations. The air stream passes from outlet portion 87 into a duct 100 to a fourth separator 104 of a third separator system which removes entrained moisture and yet another portion of the particulate.
In accordance with the embodiment shown, separator 104 is constituted by a cyclone separator/demister having an inlet portion 107 for receiving the moisture laden air flow having a very low particulate content, and an outlet or stack portion 108 which leads to ambient atmosphere. Cyclone separator/demister 104 removes a majority of any remaining particulate from the air stream along with a majority of the moisture. Moisture is directed to a drain 112 through a discharge conduit 113 into gray water reservoir 96. As noted above, moisture removed from the air stream at this point in scrubbing system 33 contains relatively high levels of resin and therefore is not preferably re-used in the fiberglass insulation process. However, the air stream, now substantially free from particulate, is passed from cyclone separator/demister 104 to ambient atmosphere.
Reference will now be made to
However, in accordance with this embodiment, first separator 47′ is constituted by a drop-out box having an inlet portion 49′ and an outlet portion 50′. In addition, the drop-out box or first separator 47′ is provided with a water inlet 56′ and a drain 58′. More specifically, water 23 from reservoir 24 is directed, under pressure from a pump (not shown), through water inlet 56′ and sprayed into drop-out box 47′ to trap and collect a first portion of the particulate from the air stream. From drop-out box 47′, the air stream passes through an air duct 60′ to a second separator 64′ where another portion of the particulate is removed.
Second separator 64′ is constituted by a cyclonic vortex or chevron baffle separator having an inlet portion 67′ for receiving the air stream from first separator 47′ and an outlet portion 68′. More specifically, particulate laden water from first separator 47′ is removed from the airstream that enters second separator 64′. At this point, residual water returns, via a drain conduit 75, to reservoir 24 and the air stream is passed through an air duct 80′ to the third separator which is defined by cloud generating vessel 83. After entering cloud generating vessel 83, the process directly corresponds to that described above with respect to scrubbing system 33 of the first embodiment and will not be described in further detail.
As indicated above, the overall scrubber system can take various forms, particularly in connection with the structure and operation of the one or more separators arranged upstream of the cloud generating vessel.
It is important to note that the pre-cloud generating vessel separator(s), e.g., first and second separators 47′ and 67′, as with first and second separators 47 and 67, not only provide ample time for the air stream to cool to saturation temperatures but also provide a high residence time that facilitates the growth of ultra-fine particles into larger particles before the air stream enters the cloud generating vessel. By providing a high residence time to facilitate particle growth, the scrubbing system of the present invention surprisingly raises the overall efficiency and efficacy of cloud generating vessel 83 thereby ensuring that any air stream exiting to ambient atmosphere exceeds local and Federal environmental regulations. That is, the multiple separators operate synergistically to not only ensure compliance with present regulations but also looks to the future for compliance with potential newer, more strict regulations.
Incorporating a cloud generating vessel into the overall scrubbing apparatus of the present invention not only reduces capital costs, e.g., the single cloud generating vessel is considerably less expensive than a wet electrostatic precipitator (WEP), but also enables the scrubbing apparatus to operate in a more energy and operationally efficient manner. That is, the overall scrubbing apparatus of the present invention has been found to significantly reduce energy consumption, i.e., by as much as 60%, over presently employed systems. Furthermore, by directing process water from the first and second separators into a recycled water reservoir, and the process water from the third and fourth separators into a separate gray water reservoir, a higher percentage of process water can be efficiently re-used in the overall glass-wool forming process.
Although described with reference to preferred embodiments of the invention, it should be readily understood that various changes and/or modifications can be made to the invention without departing from the spirit thereof. In general, the invention is only intended to be limited by the scope of the following claims.
