专利摘要:
A flow block and bushing assembly employing an orifice plate having a perforated drawing area with a planar undersurface against which bulk gas flow is directed for cooling and fiber attenuation purposes. The flow block is comprised of an interior layer of highly glass corrosion resistant material, such as zircon, and an exterior layer of highly thermal shock-resistant material. A flow passage extends through both of said layers and is lined with platinum foil. The bushing assembly is removably secured beneath the flow block and comprises a body of refractory material having a flow chamber extending therethrough in alignment with the flow passage. The flow chamber is lined with a platinum foil lining and the orifice plate is joined to the lining and extends over the lower end of the chamber. The orifice plate is reinforced by ribs integrally joined to and extending across the upper surface of its perforated drawing area and a perforated reinforcing plate is integrally joined to the ribs in spaced parallel relationship to the orifice plate. Electrodes are joined to the orifice plate to either side of the drawing area whereby electrical current may be passed through the orifice and reinforcing plates and flow chamber walls to effect the resistance heating thereof. Bulk gas flow is provided by a nozzle having a plurality of individual inlet conduits communicating with a common elongate discharge passage. An adjustable manifold communicates with the inlet conduits of the nozzle to provide for the selective supply of gas thereto and the nozzle is adjustably mounted so that its angular orientation relative to the undersurface of the drawing area may be varied.
公开号:SU1072798A3
申请号:SU802942257
申请日:1980-07-01
公开日:1984-02-07
发明作者:Гали Коггин Чарльз (Младший)
申请人:Нитто Босеки Ко.,Лтд (Фирма);
IPC主号:
专利说明:


Yu
00 The invention relates to the building materials industry, in particular to the equipment of glass fiber factories. The closest to the proposed technical essence and the achieved result is a device for drawing fiberglass, including refractory bars with a channel and a working chamber with a flat perforated plate. The disadvantage of the device is low productivity, since the perforated plate is not. caused by heat and pressure of the feeder glass melt, which causes deformation of the perforated plate. The purpose of the invention is to increase productivity. This goal is achieved by the fact that the device for drawing Glass Fiber, including refractory bars with a channel and a working chamber with a flat perforated plate, is provided with a reflective sheet installed with a gap above the perforated plate having a perforation in the center, and the channel and chamber made with a coating connected to a perforated plate. In this case, the working chamber is made expanding to the perforated plate. FIG. 1 shows a device, an overall view, a longitudinal section; in fig. 2 the same, a cross-section ;, in FIG. 3, refractory bars and a working chamber, a longitudinal section; 4, the same cross section; on fig.Z the same, top view; in fig. 6 - refractory bars and a working chamber, embodiment, longitudinal incision. . The device consists of refractory bars, the inner layer 1, made of heat resistant and glass resistant material, such as zirconium, and the outer layer 2, made of a material that has high resistance to thermal shock, such as mullite. Channel 3 for the passage of glass melt is lined with tin foil 4. The foil lining completely covers channel 3 and forms horizontal sections on the refractory bars x, upper section 5 and lower section b (FIG. 3). The platinum dressing protects the channel from erosion and cracking resulting from the passage of hot glass through it, and is practical from an economic point of view due to the relatively small size of the channel. The presence of a lining allows the use of a material having a high resistance to thermal shock, such as a multiplier, so this layer is completely protected from direct contact with pacn iaaen glass. The small size of the channel 3 provides a rapid flow of liquid glass. Faster flow eliminates the possibility of stagnation or slow movement of glass at which growth may occur to the points. In addition, the glass is thermally more uniform in comparison with the glass flowing through a relatively large hole. FIG. 3 shows a variant of the proposed device. The inner layer 1 of the refractory bars forms a larger channel for entering the glass mass than the outer layer 2 of the refractory bars, and only the Channel formed by the outer layer of the 2. refractory bars is covered with platinum foil. The term platinum is understood to mean all alloys of platinum. The production chamber 7 is removably attached to the lower surface of the outer layer 2 of the refractory bars. Fastening is performed using a frame containing the angles 8, which are engaged in adhesion with the sides and the bottom surface of the processing chamber in order to maintain the chamber in the centered position relative to channel 3. The inner surface of the working chamber 7 is lined with aluminum foil coating 9 and the flange 10 attached to the top end of the cover and secured around the open top end of the chamber. When the working chamber is in place, the flange 10 is hermetic; superimposed on the outer part of the lower portion 6 of the cladding of platinum foil. The production chamber 7 is made with a flat perforated plastid 11 with spinnerets that do not protrude from it. The perforated plate 11 has a perforation in the center and is made with non-perforated settling zones 12 on both sides of the drawing area. . The perforated plate is reinforced by the use of a 13 pack-type design. | Vacuum pads for eggs. In addition, the working chamber is provided with a baffle plate 14 mounted across the entrance of the chamber at a distance from the lower end of the channel 3. The reflective plate is held in place by attaching it to the sides of the cover 9 of the working chamber 7 and has a pointed perforated structure. By virtue of the sharp construction, the reflective plate tends to deflect liquid glass entering the growth chamber. In this way, the reflective plate reduces the force, with the liquid glass entering the chamber falling onto the ground-breaking structure 13, and deflects the particles, for example, fragments of refractory materials or crystals into the collection zones. The extraction is terminated by means of a heat exchange pipe 15. This pipeline is of conventional construction and is used to prevent the steel from penetrating the flange and bottom of the lining of the refractory bars. The glass (and 2) is thinned in the fiber by | <1 pulling it through a perforated plate. The steel fibers 16 are drawn through the device 17 for applying an appraising composition, from where they enter the collecting roller 18 and then onto the winding mechanism 19. During the drawing process, the bulk gas flow is directed upwards onto the flat surface of the perforated plate with the spinneremes scrap 2p. The gas is used for cooling and. matine fiber. The gas is supplied to the nozzle 20 through the means of the pipeline 21. The proposed construction facilitates the removal of the working chamber during the service. Removing the camera does not present any problem, since the area of glass to be destroyed is relatively small and not one of the parts of the chamber is included in the channel. The parameters of the various elements used in the invention may differ significantly. Examples of a working chamber giving both working and physical characteristics are given below. / Construction / chambers with 795 holes with dies A 90% platinum-10% Alloy type rhodium. Perforated plate with dies Dkametr dies, see the distance between the centers, tM Plate thickness, cm Location Five sections, 11 p dies, with the number of dies in rows alternating from 14 to 15, and the total number of dies per section is em 159. The dimensions of the area of the archway, cm 2.61. 8.89 size of the plate, cm 3.81 -15.24 sturdy 1130 holes of dilite, 0.0119 cm and thickness O, 381 cm 0.787 cm and distance of 0.102 cm between the centers 3.81 1.78 cm characteristics of the temperature behind. stewing, L:. 1210-1 60 rpm capacity .5-23.4 capacity, kg / h. Chamber construction with spinneret, 98 holes 80% platinum 20% ro Hyp alloy di 90% platinum 10% Rhodium Perforated plate with dies Diameter of the nozzle, see Center distance, cm Plate thickness, cm Location Six sections of the nozzles (15-9 ), 12 corners, square arrangement. Dimensions of the area of drawing, S1.2,84 10,79 Plate size, cm 3.81 -16.51 Strengthening 1200 holes plate with a diameter of 0.119 cm and thickness 0.0381 cm The distance between the center and Ø 0.102. HO, 635. cm by 3.81 iil.80 tM Temperature Ш2-12б6 solidification, Throughput, kg / h 20-25.8 Construction of cambra with spinnerers With 810 holes 80% platinum-20% Alloy type rhodium-90% platinum-0% rhodium Perforated plate with dies Dieter dies, see Distance. between centers, mi, cm
0.152
Six sections (159), square arrangement, 1200 spinnerets with a diameter of 0.119
3, 05 11.43 3.81 - 16.51
1200 holes with a diameter of 0.119 with a thickness of 0.381 cm Distance between centers 0.102 x
"0.65 cm by 3.81" 1.90 cm
1221-1293
12,2-22,2
In each of the examples, the thickness of the side walls of the cam shown in cross section in FIG. 2 is 0.0508 cm, and the thickness of the end walls of the chamber shown in cross section in FIG. 1 is 0.1016 cm. The thickness of the electrode connector This is 0.318 cm and the flange thickness is 24-0.0381 cm.
The proposed device is characterized by improved performance.
Fig
/ ril
/eight
V
Hl.
Fzg.5
- ,,,, -:.:, - ::,
X /
/ /
I ///.- l
///// X
/ /
/ jf // N N NN N N: N
x-f N 4 A AN;
权利要求:
Claims (2)
[1]
1. DEVICE FOR EXTRACTING A GLASS FIBER, including refractory bars with a channel and a production chamber with a flat perforated plate, characterized in that, in order to increase · productivity, it is provided with a / reflective plate installed with a gap above the perforated plate having a perforation in the center / a the channel and the chamber are made with a coating connected to a perforated plate.
[2]
2. The device pop. 1, characterized in that the development chamber is made expandable to the perforated plate.
ho Μ yu os
类似技术:
公开号 | 公开日 | 专利标题
SU1072798A3|1984-02-07|Apparatus for drawing glass fiber
JP4248798B2|2009-04-02|In-line degasser
JP3905146B2|2007-04-18|Low profile molding furnace for fiber production
US7220292B2|2007-05-22|Metallic fiber nonwoven fabric manufacturing apparatus, its manufacturing method and laminated aluminum material manufacturing method
US4330311A|1982-05-18|High pressure forming bushing and fin cooler
HU201143B|1990-09-28|Method for cooling rotary furnace with coolant
JP2003347198A5|2003-12-05|
WO1998035774A1|1998-08-20|Feeder of molten metal for moulds of continuous casting machines
US5439047A|1995-08-08|Heated nozzle for continuous caster
US3151200A|1964-09-29|Ladle lining apparatus
SK286801B6|2009-05-07|Method and installation for dip coating of a metal strip, in particular a steel strip
US4230474A|1980-10-28|Apparatus and process for simultaneous thermic glass sheet hardening
US6249538B1|2001-06-19|Cooling device with panels for electric arc furnace
CN1851370B|2011-02-02|Open type double-layer magnesium alloy melting furnace
US6041854A|2000-03-28|Water cooled panel
CN108588397B|2019-05-07|A kind of residual water remove device of Strip roll-type hardened face and method
CN210237737U|2020-04-03|Light heat preservation protective cover plate and aluminum liquid purification device
RU2265782C1|2005-12-10|Heat-exchanger with honeycomb members
CN212042585U|2020-12-01|Novel continuous casting secondary cooling chamber water-cooling wall
CN210044957U|2020-02-11|Hot gas filter
CN207775282U|2018-08-28|Steel smelting equipment with auxiliary material conveying mechanism
CN206433680U|2017-08-25|A kind of multiple-grooved pot of continuous tea enzyme deactivating and strip sorting machine
CN215328281U|2021-12-28|Spring steel wire heat treatment lead bath quenching device
CN209879194U|2019-12-31|Filter equipment, cooling system and toast equipment
CN211552281U|2020-09-22|Evaporation gold drying equipment
同族专利:
公开号 | 公开日
DE2634281B2|1979-05-10|
AU1629276A|1978-02-02|
FR2335459B1|1983-08-26|
NL7608130A|1977-02-01|
FR2335460A1|1977-07-15|
GB1550903A|1979-08-22|
FR2335459A1|1977-07-15|
SE8103103L|1981-05-18|
DE2634281A1|1977-02-03|
BR7604033A|1977-06-28|
SE7608163L|1977-01-29|
DE2634281C3|1980-01-10|
CA1087856A|1980-10-21|
JPS5215631A|1977-02-05|
ZA764196B|1977-07-27|
NZ181569A|1981-05-15|
BE844554A|1976-11-16|
IN148692B|1981-05-16|
IN146959B|1979-10-20|
FR2327968B1|1983-02-04|
SE8103102L|1981-05-18|
US3988135A|1976-10-26|
JPS5514072B2|1980-04-14|
FR2327968A1|1977-05-13|
SE423532B|1982-05-10|
FR2335460B1|1985-05-17|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题

DE580502C|1930-04-28|1933-07-17|Oscar Gossler Fa|Method and device for melting glass, in particular for processing on spun glass|
US2947028A|1954-11-19|1960-08-02|Owens Corning Fiberglass Corp|Apparatus for manufacture of fibrous glass|
US3283055A|1963-08-15|1966-11-01|Owens Corning Fiberglass Corp|Temperature control system for high temperature melters or the like|
US3539318A|1967-11-24|1970-11-10|Owens Corning Fiberglass Corp|Apparatus for producing fibers|
US3516478A|1967-12-05|1970-06-23|Monsanto Co|Apparatus for separation of impurities from metal melts in a filament spinning device|
US3574581A|1968-09-13|1971-04-13|Ppg Industries Inc|Bushing for use in extruding fibers|
US3867119A|1970-07-20|1975-02-18|Paramount Glass Mfg Co Ltd|Apparatus for manufacturing glass fibers|
US3726655A|1970-11-27|1973-04-10|Owens Corning Fiberglass Corp|Apparatus and method for attenuating mineral fibers|
US3920430A|1973-10-09|1975-11-18|Owens Corning Fiberglass Corp|Support for bushing for containing molten mineral material|
US3837823A|1973-12-13|1974-09-24|Ppg Industries Inc|Bushing block assembly and screen|
JPS5146859B2|1974-01-14|1976-12-11|
DE2420650A1|1974-01-14|1975-07-24|Edward Thomas Strickland|METHOD AND DEVICE FOR MANUFACTURING FIBER GLASS FIBER|US4164401A|1976-06-30|1979-08-14|Nitto Boseki Co., Ltd.|Curved orifice plate for forming glass fibers|
US4178162A|1976-07-07|1979-12-11|Nitto Boseki Co., Ltd.|Bushing for apparatus for spinning glass fibers|
JPS6113386Y2|1977-09-26|1986-04-25|
US4149865A|1977-12-30|1979-04-17|Nitto Boseki Co., Ltd.|Apparatus and method for the drawing of glass fiber|
US4155731A|1978-01-11|1979-05-22|The Greickor Company|Fiber forming bushing construction|
US4161396A|1978-03-17|1979-07-17|Owens-Corning Fiberglas Corporation|Method and apparatus for processing heat-softened fiber-forming material|
US4194895A|1978-08-03|1980-03-25|Owens-Corning Fiberglas Corporation|Fluid flow method and apparatus used in manufacture of glass fibers|
US4202680A|1978-10-16|1980-05-13|Owens-Corning Fiberglas Corporation|Fluid flow apparatus in combination with glass fiber forming apparatus|
US4469499A|1979-11-20|1984-09-04|Societe Vetrotex Saint-Gobain|Method and apparatus for the manufacture of fibers|
JPS56159628U|1980-04-28|1981-11-28|
DE3111484C2|1981-03-24|1983-12-22|Diether 6203 Hochheim Böttger|Method and device for the production of glass fibers|
US4525188A|1983-02-07|1985-06-25|Ppg Industries, Inc.|Fiber forming bushing and method for using same|
JPH0141872Y2|1983-02-22|1989-12-08|
US4488891A|1983-04-11|1984-12-18|Owens-Corning Fiberglas Corporation|Method for forming glass fibers|
US4553994A|1984-04-09|1985-11-19|Owens-Corning Fiberglas Corporation|Method for forming glass fibers|
AU4996597A|1996-10-25|1998-05-22|Owens Corning|Continous in-line system for producing high-temperature glass fiber materials|
US5925164A|1997-03-07|1999-07-20|Owens Corning Fiberglas Technology, Inc.|Finshield assemblies for fiber-forming apparatus|
US5928402A|1997-08-04|1999-07-27|Owens Corning Fiberglas Technology, Inc.|Multi-screen system for mixing glass flow in a glass bushing|
US7434421B2|1997-09-15|2008-10-14|Johns Manville|Fiberizing apparatus|
US5935291A|1997-10-29|1999-08-10|Ppg Industries Ohio, Inc.|Bushings and fiber forming assemblies|
US6543258B1|1997-12-02|2003-04-08|Nitto Boseki Co., Ltd.|Glass fiber nonwoven fabric and printed wiring board|
US5948135A|1998-05-12|1999-09-07|Ppg Industries Ohio, Inc.|Bushing insulation and frame arrangement for making fiber glass|
US6044666A|1998-05-12|2000-04-04|Ppg Industries Ohio, Inc.|Insulating flow and bushing blocks, bushing assemblies, fiber forming apparatus and method for forming fibers|
US6065310A|1998-07-01|2000-05-23|Owens Corning Fiberglas Technology, Inc.|High throughput glass fiberizing system and process|
US6453702B1|2000-09-29|2002-09-24|Johns Manville International, Inc.|Fiberizing apparatus and method|
US6779366B2|2001-11-09|2004-08-24|Owens Corning Fiberglas Technology, Inc.|Bushing assembly/support structure arrangement|
DE10203418C1|2002-01-28|2003-02-27|Heraeus Gmbh W C|Bath used for drawing glass fibers has side walls and a base plate with openings which open into dies on the side of the plate facing away from the inner chamber|
FR2870232B1|2004-05-14|2007-02-16|Saint Gobain Vetrotex|DIE FOR THE MANUFACTURE OF FILAMENTS, IN PARTICULAR GLASS AND ITS FIBRAGE INSTALLATION|
US8001807B2|2006-12-14|2011-08-23|Ocv Intellectual Capital, Llc|Palladium screens for bushing assembly and method of using|
US20080141727A1|2006-12-14|2008-06-19|Sullivan Timothy A|Refractory system for bushing assembly|
US7980099B2|2007-03-15|2011-07-19|Ocv Intellectual Capital, Llc|Multiple alloy bushing assembly|
US8024946B2|2008-09-18|2011-09-27|Johns Manville|Transverse row bushing support|
US8776551B2|2011-05-23|2014-07-15|Johns Manville|Transverse row bushings having ceramic supports|
US8402793B2|2011-05-23|2013-03-26|Johns Manville|Transverse row bushings and methods with freedom of movement|
CN103524033A|2012-07-06|2014-01-22|苏州宏久航空防热材料科技有限公司|High-temperature alloy bushing plate plated by platinum and alloy thereof, and preparation method of high-temperature alloy bushing plate|
CN105271709B|2015-10-22|2019-03-15|南京航空航天大学|A method of two-component ultra-fine fibre glass cotton is prepared by two-stage bushing kiln|
法律状态:
优先权:
申请号 | 申请日 | 专利标题
US05/599,720|US3988135A|1975-07-28|1975-07-28|Assembly for the drawing of glass fibers|
[返回顶部]