The present invention relates to a fiberizer and spinner for use in the manufacture of high quality glass wool fibers, and more particularly to an improved radiation shield for insulating spinners used in the rotary fiberizing process.
Fibers of glass and other thermoplastic materials are useful in a variety of applications including acoustical and thermal insulation materials. Common prior art methods for producing fiberglass insulation products involve producing glass fibers from a rotary process. In a rotary process, glass composition is melted and forced through orifices in the outer peripheral wall of a centrifuge, commonly known as a centrifugal spinner, to produce the fibers. One commonly used spinner is generally cup-shaped that has a base wall with a central hole, a top opening and an outer peripheral sidewall that curves upward from the base wall, forming the top opening. Another commonly used spinner uses a slinger cup to propel the glass composition to the sidewall for fiberization. A drive shaft is used to rotate the spinner and is typically fixed to the spinner with a quill.
During fiberization, the spinner is subjected to high temperatures and high rotational speeds that exert substantial force on the spinner. An external burner forces a jet of hot gas onto the fibers as they are extruded through the orifices of the sidewall to heat the fibers, and an external blower is used to stretch the fibers. During fiberization, it is important to maintain the glass at a predetermined temperature to improve the quality of fiberization. While the preferred temperature varies based on equipment and manufacture, it is typically the temperature at which the molten glass has a viscosity of 1000 poise (also referred to as the log 3 viscosity).
Spinners are formed of metal alloys and typically include a base wall and a foraminous sidewall. The molten glass is dropped onto the base surface of the spinner and is propelled against the sidewall by the rotation of the spinner. The base surface of the spinner radiates and converts heat from the molten glass and spinner sidewall. The orifices at the lower edge of the sidewall cool to a temperature lower than that of the higher orifices. The cooling of the orifices cools the glass and increases viscosity of the glass and leads to thicker stiffer primary fibers. Allowing the glass to cool may allow for devitrification of the glass, which may lead to plugging of the lower orifices.
Thus, there exists a need in the art for a spinner that maintains the spinner base and peripheral sidewall as well as the molten glass, while in the spinner prior to fiberizing, at a preferred temperature and that confers improved properties to the fiberglass insulation product.
The need to control glass temperature in the spinner and improve glasswool quality is met by a spinner according to the present invention. The spinner of the present invention is adapted to control the temperature of the molten glass by including a radiation shield mounted beneath the spinner. The radiation shield is positioned beneath the spinner and typically includes a multi-layer structure. The objectives, features, and advantages of the present invention will become apparent upon consideration of the description herein and the appended claims and drawings.
The advantages of this invention will be apparent upon consideration of the following detailed disclosure of the invention, especially when taken in conjunction with the accompanying drawings wherein:
Although the present invention is herein described in terms of specific embodiments, it will be readily apparent to those skilled in this art that various modifications, rearrangements, and substitutions can be made without departing from the spirit or scope of the invention. The scope of the present invention is thus only limited by the claims appended hereto.
Referring to
The spinner 12 is supplied with a stream 78 of a molten thermoplastic material. Conventional supply equipment 82 can be used to supply stream 78 of molten glass. Such molten glass supply equipment is well known in the industry and, therefore, will not be discussed in detail herein. The glass in stream 78 drops into the chamber 42 of spinner 12 and through centripetal force is directed against the peripheral wall 18 and flows outwardly to form a build-up or head 90 of glass. The glass then flows through the orifices 20 to form primary fibers 22, which are heated and stretched by burners 24 and annular blower 28.
The rotation of the spinner 12 (as depicted by the circular arrow (a) in
A hollow quill 64 is press fit in a borehole formed through the center of hub 54 and locked in place with three circumferentially spaced locking pins 66. The upper end of the quill 64 is threaded into the lower end of a hollow drawbar 68. The quill 64 is preferably cooled further with water circulated through an annular cooling jacket 70 disposed around spindle 14 and quill 64 and above hub 54. The quill 64 and hub 54 are preferably fabricated from a low thermal expansion alloy to minimize differential thermal expansion between them.
The radiation shield may include a number of individual plates 52a, 52b, 52c. The plates may be connected to the hub 54 of quill 64. The plates inhibit convection from the base of the spinner and inhibit the infrared energy from escaping from the base of spinner 12 and decreases the thermal gradient along the height of the peripheral sidewall 18 thus inhibit devitrification within the glass head 90 and controls the temperature of the glass as it passes through the orifices 20 at the lower edge of peripheral sidewall 18. The uppermost shield 52a is preferably frustoconical to follow the base wall 16 of spinner 12. The lower shields 52b, 52c may be frustoconical or planar to allow space between the shields. The shields 52 may be formed of stainless steel or a refractory metal, such as HASTELLOY alloy a transition metal nickel based high temperature alloy. On especially suitable material for the shields is HASTELLOY X alloy, which is available from Haines International of Kokomo, Ind., USA. HASTELLOY X alloy includes 47 weight % Ni, 22 weight % Cr, 18 weight % Fe, 9 weight % Mo, 1.5 weight % W, 0.1 weight % C, 1 weight % Mn (maximum), 1 weight % Si (maximum) and 0.008 weight % B (maximum).
Similarly, the fiberizer 10 of
Spinners are manufactured in a variety of geometries depending upon the fiberization process used. Typically, major manufacturers of glass fiber have their own fiberization process, which varies from manufacturer to manufacturer; however, the principles of the present invention are equally suitable for use in any rotary fiberization process.
The invention of this application has been described above both generically and with regard to specific embodiments. Although the invention has been set forth in what is believed to be the preferred embodiments, a wide variety of alternatives known to those of skill in the art can be selected within the generic disclosure. The invention is not otherwise limited, except for the recitation of the claims set forth below.
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Number | Date | Country | |
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20080156042 A1 | Jul 2008 | US |