CN108706856A

CN108706856A - A kind of lateral flame furnace production system and production method of glassware

Info

Publication number: CN108706856A
Application number: CN201810544632.2A
Authority: CN
Inventors: 杨德宁
Original assignee: Individual
Current assignee: Shenzhen Qianhai Fawei New Material Technology Co ltd Shanghai Branch
Priority date: 2017-12-27
Filing date: 2018-05-19
Publication date: 2018-10-26
Also published as: WO2019223325A1

Abstract

The invention discloses a kind of lateral flame furnace production systems and production method of glassware；It includes glass raw material transport device, and flame thermal energy dominates the lateral flame furnace Jie Ju devices of glass melting；The card neck flow passage device of glass metal；Temperature controlled clarification, exhaust bubble and anti-crystallization device are carried out to the glass metal flowed from the top to the bottom using electrode；Using electrode, temperature controlled glass metal rise channel s structure is carried out to the glass metal flowed from bottom to top；The molding machine of glassware；It is characterized in that：In the card neck flow passage device of glass metal, depth between the surface and bottom of device of glass metal, it is that flame thermal energy is dominated the lateral flame furnace Jie Ju devices of glass melting and carried out in temperature controlled clarification, exhaust bubble and anti-crystallization device to the glass metal flowed from the top to the bottom using electrode, the 10%-40% of the depth between the surface and bottom of device of glass metal.

Description

A kind of lateral flame furnace production system and production method of glassware

Technical field

The invention belongs to the process units field of glassware, it is related in the big production system of glassware, to existing The structural element of the glassware process units of technology, the innovation life that Zuo Chu Jie Ju variations, change in location, interactively change Produce apparatus system.

Background technology

Existing correlation technique 1：

The sodium calcium float glass production line of the prior art of the large-tonnage of kiloton on being related to hundreds of tons of all daily outputs In lateral flame furnace system in combination device, after the lateral flame furnace Jie Ju devices that flame thermal energy dominates glass melting, What is be coupled by card neck device is a kind of cooling end or the device of entitled work department；Its card neck device, lateral flame furnace knot In the device of Ju devices, cooling end or entitled work department, the depth of glass metal is all consistent, about 1 meter or so, so glass Liquid is totally all horizontally oriented towards molding machine and moves.Its prior art cooling end or the device of entitled work department accommodate glass Liquid it is sufficiently bulky, all reach daily pull amount of glass 3-5 times (namely if produce daily 600 tons production line cooling end Or the device of entitled work department, can be reached by accommodating glass metal by 2000-3000 tons).One of its technological principle：It is that glass metal is made to exist It is slowly cooled down in cooling end or the device of entitled work department；The two of its technological principle：Make glass metal in cooling end or entitled work Make in the device in portion slowly to complete exhaust bubble, (i.e. glass metal is slow by 3-5 days time wherein for the process of clarification process The slow process for completing exhaust bubble, clarification process).In the schematism device of the sodium calcium float glass production line of the prior art In, the device of this cooling end or entitled work department has formed apparatus structure constant in decades, formed it is so-called not The authoritative structure that can shake.

It is to lead to this cooling end or the device of entitled work department shape substantially because there is a kind of technology prejudice At reason constant in decades：

Such as：1, in the China's chemical industry publishing house float glass technologs published in 2005 and one book of equipment 1 to 2 row of page 92 of float shaping technique chapters and sections is pointed out：Glass floating process ... glass metal flows into tin kiln ... phase The viscosity answered is 10³Pa Sec.(the sodium calcium float glass life of the prior art of the large-tonnage of the upper kiloton of hundreds of tons of all daily outputs The enterprise of producing line, all so operates).

And the 10 of sodium calcium float glass²Pa Sec exhaust bubble, clarification process viscosity temperature be 1430 DEG C；Sodium calcium is floating The 10 of method glass³Pa Sec moulding process viscosity temperature be 1080 DEG C；So the large-tonnage of the upper kiloton of hundreds of tons of daily output The sodium calcium float glass production line of the prior art, 10 when in order to reach into molding tin kiln³Pa Sec moulding process it is viscous The technique purpose that temperature is 1080 DEG C is spent, all makes 1400 DEG C or more of the glass metal from melting end, enters by card neck traditional After this cooling end or the device of entitled work department, a cooling technique stage is entered, so that glass metal is cooled to 1080 DEG C and comes In accordance with so-called 10³Pa Sec moulding process required standard.For effective temperature-reducing, traditional this cooling end or entitled work Several exhausting cooling systems are arranged at the top for making the device in portion.And in being molded tin kiln, in order to make glass metal and glass tape will not Because cooling down it is too fast due to cannot complete time to put down, make thinner and edge machine draws thin technique, and added many heating devices on Xi Yaoding.

One of its existing defects：In this cooling end or the device of entitled work department, since sodium calcium float glass is not achieved 10²Pa Sec exhaust bubble, clarification process viscosity temperature be 1430 DEG C of requirement, so using one kind making glass metal Slowly the technique-of the process of completion exhaust bubble, clarification process (i.e. want by glass metal in cooling end or the device of entitled work department The time passed through 3-5 days wherein slowly completes the process of exhaust bubble, clarification process).One of its defect is low production efficiency, Waste the production time.

The two of its existing defects：Also due to the glass metal after temperature reduction technology, into tin kiln booth book process when because only There is 5-7CM thickness area again very big, in order to keep temperature to add many heating devices on being molded Xi Yaoding again, so caused by Energy waste.

The three of its existing defects：Since in this cooling end or the device of entitled work department, the depth of glass metal is all 1 Rice or so, glass metal are totally all horizontally oriented towards molding machine and move, glass metal upper surface portion, left and right part, lower bottom portion all No Have complete, accurate, unified heating and control the system and device of temperature, thus especially with shaping area close cooling end or The upper and lower layer temperature difference of glass metal in entitled work department back segment reaches 70-90 DEG C；This can cause sodium calcium float glass production exhaust The process of bubble, clarification process, it is impossible to accurately according to the distinctive clarification of soda-lime glass ingredient, row's bubble 10²(Pa Sec) glues Temperature is spent, it, can the scarce defect of the row's of causing bubble quality to complete the process of exhaust bubble, clarification process.

(2) existing correlation technique 2：In the glass fibre transverse direction flame furnace life for being related to the large-tonnage of 100-600 tons of daily output In the schematism device of the prior art of producing line, flame thermal energy is all used to dominate the lateral flame furnace knot of glass melting Ju devices (10)；Device (the 17)-i.e. main channel for the loading glass metal being directly coupled, and it is designed with 10-30 glass liquid stream Road, each of which runner are coupled the molding machine of the glass fibre production of glassware, separately flow into corresponding 2-30 and hold The dry crucible of glass metal is carried, glass metal passes through corresponding 2-30 bushing, glass fibers are formed under the action of corresponding wire drawing machine Dimension.

Existing correlation technique -- in the glass fibre transverse direction flame furnace production for being related to the large-tonnage of 100-600 tons of daily output In the schematism device of line, all unspecial uses electrode, is controlled into trip temperature the glass metal flowed from the top to the bottom Device；No have the device of the temperature of the glass metal for the big flow that can accurately control large volume, cannot ensure the big of large volume The glass metal of flow is substantially higher than recrystallization temperature before moulding process.

Its existing defects is：Because of the salic super high-strength glass fibre up to 20-25%, recrystallization temperature it is very high, Be related to daily output 100-600 tons large-tonnage glass fiber manufacturing line schematism device before moulding process Device Zhong , No have the temperature of the glass metal for the big flow that can accurately control large volume, cannot ensure the glass of the big flow of large volume Glass liquid is substantially higher than recrystallization temperature before moulding process, does not generate crystallization completely.So existing correlation technique -- it is being related to day The schematism device of the glass fiber manufacturing line of the large-tonnage of 100-600 tons of production always can not all produce salic reach The super high-strength glass fibre of 20-25%；Unlikely produce the salic super high-strength glass fibre up to 20-49%.

(3) existing correlation technique 3：There is no flame thermal energy to dominate the pure electric melting furnace systematicness of the prior art of glass melting Combination unit, although it is also included：Using electrode, temperature controlled device is carried out to the glass metal flowed from the top to the bottom (2)；Using electrode, temperature controlled glass metal rise channel s structure (3) is carried out to the glass metal flowed from bottom to top；But by Yu No have the lateral flame furnace Jie Ju devices that flame thermal energy dominates glass melting, existing defects to be：Because of traditional glass Product electric melting furnace process units knot Ju systems are limited to by Electric Melting Technology tonnage, it is impossible to be used in the daily output is up to 100 tons to upper kiloton Big production capacity glassware production line.

So compared with the daily output is up to hundreds of tons of big production capacity glassware tank furnace production lines to upper kiloton, one of defect It is：It is low to invest output ratio, low production efficiency.Defect second is that：The energy consumption of identical yield is than high.The three of defect are：It is identical Yield human resources consume it is high；The four of defect are：.Because without highly conductive in the high-aluminum alkali-free glass material of high melting-point Base material ingredient, so without flame thermal energy dominate glass melting lateral flame furnace Jie Ju devices (10) technique fill The glassware process units system of (1) is set, (i.e. pure electric melting furnace)-is unable to dissolve fully high-aluminum alkali-free glass material, exists not The defect of the high-aluminum alkali-free glass material of high melting-point can be produced.

(4) existing correlation technique 4：A kind of horseshoe kiln device for having electric boosting again that flame thermal energy is leading：

One of its existing defects are：A kind of horseshoe kiln device for having electric boosting again that flame thermal energy is leading, due to Jie Ju It is simpler than lateral flame furnace, thus it is at low cost, take up an area few；Mainly for the manufacture of to glass quality vierics of less demanding Ware product, and day production tonnage is not more than 50 tons, limits to using by tonnage, it is impossible to be used in the daily output is up to 100 tons to upper The big production capacity glassware production line of kiloton.

Its existing defects second is that：A kind of horseshoe kiln device for having electric boosting again that flame thermal energy is leading, after dissolving Glass metal is all horizontally oriented mobile；Its existing defects be horizontally oriented mobile glass metal have the phenomenon that reflux also without Method controls；And the distance of glass metal horizontal direction movement is longer, so its glass metal upper layer just has heat dissipation problem, it will It is uneven to form the temperature of glass liquid moved horizontally；Exactly apart from the longer glass metal top moved horizontally using flame or The additional thermal process of electric heating, due to the additional thermal process of flame or electric heating, the electric current heating with the electrode in glass metal is two kinds Device, temperature that cannot be between the glass metal upper layer temperature and middle lower layer of effective controlled level movement form the consistent of control Property and stability.It is uneven that the temperature of glass liquid moved horizontally will be formed.So a kind of flame thermal energy it is leading have electric boosting again Horseshoe kiln device, cannot effectively reach make glass liquid energy be accurately controlled clarification, row bubble needed for predetermined temperature 1-5 DEG C error within, it is horizontal to be unable to the exhaust bubble of effective guarantee glass metal, clarification process；It is especially this in the high lead glass of production When recrystallization temperature height and the product of crystallization speed, effective guarantee glass metal is unable to before entering into operation stage, glass Liquid temperature is consistently higher than recrystallization temperature.

The three of its existing defects are：A kind of flame thermal energy it is leading there is the horseshoe kiln device of electric boosting to dissolve again after Glass metal is all horizontally oriented mobile；Its existing defects is：It is had not on the both sides at the hole of top area and lower part The dead angle of sharp melt flow, especially when producing high this recrystallization temperature of high lead glass and the product of crystallization speed, meeting It is very easy to generate glass metal crystallization at the not runny dead angle of glass metal.

(5) existing correlation technique 5：The patent of invention that the present inventor applied in 2014 is a kind of for the cold of glass technology But the anti-crystallization device in portion region, it is characterised in that：In the space on the metal level of cooling end, by pool wall fire resisting In the distance range of the inside 10-80mm of brick, there are 2 to 80 electric heater units and 2 to 80 measuring temperature devices. It proposes to dispose electrode system in the glass metal in cooling end region to control temperature of glass liquid.

One of its existing defects are：[1]A kind of cooling end region for glass technology anti-crystallization device device or In all existing cooling ends or the device of entitled work department, the lateral flame furnace knot of glass melting is dominated in flame thermal energy After Ju devices, what is be coupled by card neck device is a kind of anti-crystallization device device in cooling end region；Its card neck device, Lateral flame furnace Jie Ju devices, cooling end region anti-crystallization device device in, the depth of glass metal is all consistent, about 1 Rice or so.It is moved so glass metal is totally all horizontally oriented towards molding machine.Although there are also installed electrodes, it is desirable to solve glass The temperature of glass liquid controls, but the glass metal of horizontal direction movement has the phenomenon that reflux, also can not effectively control the temperature of glass metal Degree；[2]And added the external heating device of electric heating on the refractory brick of glass metal side, glass metal top layers Mian No just control temperature The device (cooling end generally have 8-15 meters wide, 10-20 meters long, top center level heat dissipation problem is serious) of degree.

So a kind of anti-crystallization device in cooling end region for glass technology can not effective controlled level shifting Temperature between dynamic glass metal upper layer temperature and middle lower layer forms the consistency and stability of control.Horizontal shifting will be formed Dynamic temperature of glass liquid is uneven.

So a kind of anti-crystallization device in cooling end region for glass technology, cannot effectively reach makes glass liquid energy It is accurately controlled within 1-5 DEG C of the error of predetermined temperature needed for clarification, row's bubble, is unable to the exhaust of effective guarantee glass metal Bubble, clarification process are horizontal；It, cannot especially when producing high this recrystallization temperature of high lead glass and the product of crystallization speed Effective guarantee glass metal is consistently higher than recrystallization temperature before entering into operation stage.

Its existing defects second is that：A kind of anti-crystallization device device or existing in the cooling end region for glass technology All cooling ends or entitled work department device in, the glass metal moved horizontally is designed to make glass metal from cooling end The glass metal flashboard hole of top area of tail portion enter shaping area.Cooling end generally has 8-15 meters wide, and glass metal Flashboard hole is only less than 2M wide, so the both sides and lower part in the cooling end domain at the glass metal flashboard hole moved horizontally, meeting There is the dead angle of unfavorable melt flow, especially in the product for producing the high crystallization speed again of this recrystallization temperature of high lead glass When, it can be very easy to generate glass metal crystallization at the not runny dead angle of glass metal.

(6) existing correlation technique 6：

In the existing skill for the lateral flame furnace production line for being related to high alumina and superelevation aluminium float flat glass and electronic glass In the schematism device of art, join after the lateral flame furnace Jie Ju devices (10) that flame thermal energy dominates glass melting Knot is a kind of cooling end or the device of the entitled Ministry of worker, and the lateral flame furnace Jie Ju dresses of glass melting are dominated in flame thermal energy After setting, what is be coupled by card neck device is a kind of cooling end or the device of entitled work department；Its card neck device, laterally fire In the device of flame tank furnace Jie Ju devices, cooling end or entitled work department, the depth of glass metal is all consistent, about 1 meter or so, It is moved so glass metal is totally all horizontally oriented towards molding machine.The body of its cooling end or the receiving glass metal of the entitled Ministry of worker Product is very big, all reaches 3-5 times of pull amount of glass daily.(namely if the high alumina of 200 tons of daily output and superelevation aluminium float glass process are flat The device of the cooling end or entitled work department of glass sheet and electronic glass production line, 600-1000 can be reached by accommodating glass metal Ton).One of its technological principle：It is that glass metal is made slowly to be cooled down in cooling end or the device of entitled work department；Its technique is former Then two：Make glass metal in cooling end or the device of entitled work department slowly complete exhaust bubble, clarification process process-(i.e. The time that glass metal will pass through 3-5 days wherein slowly completes the process of exhaust bubble, clarification process).In the high alumina of the prior art In the schematism device of the prior art of superelevation aluminium float flat glass and electronic glass production line, this cooling end Or the device of entitled work department has formed apparatus structure constant in decades, has formed so-called unshakable authority Property structure.Its technological principle is that glass metal is made slowly to cool down wherein；Glass metal is set slowly to complete exhaust bubble, clarification wherein The process of technique.This is constant in decades apparatus structure, has formed so-called unshakable authoritarian structure, substantially It is a kind of technology prejudice.

Such as：1, in the China's chemical industry publishing house float glass technologs published in 2005 and one book of equipment 1 to 2 row of page 92 of float shaping technique chapters and sections is pointed out：Glass floating process ... glass metal flows into tin kiln ... phase The viscosity answered is 10³Pa Sec.(enterprise of related to high alumina and superelevation aluminium float flat glass and electronic glass production line, All so make).

And the 10 of high alumina and superelevation aluminium float flat glass and electronic glass^2.0Pa Sec exhaust bubble, clarification process Viscosity temperature is 1540-1580 DEG C；10³Pa Sec moulding process viscosity temperature be 1480-1520 DEG C；So all, from 1450 DEG C or more of glass metal of melting end will also passed into after the device of traditional this cooling end or entitled work department The front upper part of this cooling end of system or the device of entitled work department, adds flame system to heat.

One of its existing defects：The cooling end or entitled of this high alumina and superelevation aluminium float flat glass and electronic glass In the device of work department, due to be not achieved 10²Pa Sec exhaust bubble, clarification process viscosity temperature be 1480-1520 DEG C Requirement；Again since in this cooling end or the device of entitled work department, the depth of glass metal is all 1 meter or so, and glass metal is total Body is all horizontally oriented towards molding machine and moves, and glass metal upper surface portion, left and right part, lower bottom portion No have complete, accurate, system One heating and the system and device for controlling temperature, so especially close cooling end or entitled work department back segment with shaping area The middle upper and lower layer temperature difference of glass metal reaches 70-90 DEG C；And the glass metal of horizontal direction movement has the phenomenon that reflux also can not Control；So this can cause the process of glass production exhaust bubble, clarification process, it is impossible to accurately according to high alumina and superelevation aluminium Float flat glass and the distinctive clarification of electronic glass ingredient, row's bubble 10²The viscosity temperature of (Pa Sec), come complete exhaust bubble, The process of clarification process；The serious bubble of existing high alumina and superelevation aluminium float flat glass and electronic glass can be caused Quality defect, or because glass metal clarifies the glass muscle of bad generation or the quality defect of layering.It especially will also be traditional this The front upper part of cooling end or the device of entitled work department, adds flame system to heat, and can be directed at serious 2 bubbles.

The two of its existing defects：The cross of existing correlation technique -- high alumina and superelevation aluminium float flat glass and electronic glass Into the schematism device of flame furnace production line, and horizontal direction movement glass metal have the phenomenon that reflux also without Method controls；Also all unspecial use electrode and electrical heating, to the glass metal flowed from the top to the bottom, from upper surface portion, left and right Portion, lower bottom portion carry out complete, accurate, unified heating and control the system and device of temperature, all No have can accurately control it is big The device of the temperature of the glass metal of the big flow of volume, cannot ensure the glass metal of the big flow of large volume moulding process it Before be substantially higher than recrystallization temperature.

So existing correlation technique -- the lateral flame furnace of high alumina and superelevation aluminium float flat glass and electronic glass is given birth to In the schematism device of producing line, the salic super high-strength glass up to 20-49% always can not be all produced.

(7) existing correlation technique 7：First there are the molten kiln technology of electricity and flame kiln technology, the main aluminium oxide that produces to contain The high aluminum that middle aluminum products, the alumina content that low aluminum products, the alumina content that amount is 1-4% are 5-9% are 10-16% Product.

First there are the molten kiln technology of electricity and flame kiln technology, several technologies without present invention process method to want Su Jie Ju features, so, prior art, without the process conditions for overcoming its technological difficulties.

First there are the molten kiln technology of electricity and flame kiln technology, mainly considers and dissolve glass and exhaust bubble and homogenizing Glass metal, it is desirable to form the electricity Chang &#91 between electrode;Wen Duchang ]It is uniformly basic goal to be.It plays and asks without the present invention, The specific region position of the glass metal in the region of bottom refractory material 5-30CM in multiple regions, is designed with 3-20 The requirement of a electrode assembly, and without the present invention play ask in multiple regions, away from refractory material bottom 5-30CM distances Region glass metal in, the work technological temperature in the section of a minimum of 100 cubes of CM volumes will be maintained at 1320 DEG C -1450 DEG C, the technique for being higher than 20-80 DEG C of the technological temperature of work of the region glass metal apart from bottom refractory material 30-60CM distances Method.

Invention content

A kind of lateral flame furnace production system of glassware comprising：Glass raw material transport device (19), flame Thermal energy dominates the lateral flame furnace Jie Ju devices (10) of glass melting；The card neck flow passage device (60) of glass metal；Using electrode Temperature controlled clarification, exhaust bubble and anti-crystallization device (30) are carried out to the glass metal flowed from the top to the bottom；It is right using electrode The glass metal flowed from bottom to top carries out temperature controlled glass metal rise channel s structure (40)；The molding machine of glassware (50)：

It is characterized in that：

In the card neck flow passage device (60) of glass metal, the depth between the surface and bottom of device of glass metal is flame heat The lateral flame furnace Jie Ju devices (10) of glass melting can be dominated and the glass metal flowed from the top to the bottom is carried out using electrode Temperature controlled clarification is vented in bubble and anti-crystallization device (30), the depth between the surface and bottom of device of glass metal 10%-40%；

Temperature controlled clarification, exhaust bubble and anti-crystallization device are carried out to the glass metal flowed from the top to the bottom using electrode (30) surrounding is designed with the electrode of 4-50 control temperature of glass liquid；

Temperature controlled clarification, exhaust bubble and anti-crystallization device are carried out to the glass metal flowed from the top to the bottom using electrode (30) lower part is designed with the hole (6) of glass metal outflow, and the hole (6) of the glass metal outflow of design is coupled a use Electrode carries out temperature controlled glass metal rise channel s structure (40), rise channel s structure to the glass metal flowed from bottom to top In, it is designed with the electrode of control temperature of glass liquid；

Temperature controlled glass metal rise channel s structure (40) is carried out to the glass metal flowed from bottom to top using electrode Top exit is coupled the device (17) of a loading glass metal, is designed with the electrode of control temperature of glass liquid.

A kind of lateral flame furnace production system of glassware according to claim 1, it is characterised in that：

In the card neck flow passage device (60) of its glass metal, the depth between the surface and bottom of device of glass metal, is flame Thermal energy dominate glass melting lateral flame furnace Jie Ju devices (10) and using electrode to the glass metal that flows from the top to the bottom into The clarification of trip temperature control is vented in bubble and anti-crystallization device (30), the depth between the surface and bottom of device of glass metal 10%-40%；The card neck flow passage device (60) of glass metal in the glass metal in the region of bottom refractory material 5-30CM, It is designed with 3-20 electrode assembly；

It uses electrode to carry out temperature controlled clarification, exhaust bubble and anti-crystallization to the glass metal flowed from the top to the bottom and fills The surrounding for setting (30) is designed with the electrode of 4-50 control temperature of glass liquid, using electrode to the glass metal that flows from the top to the bottom Carry out temperature controlled clarification, exhaust is steeped and the glass in the region of bottom refractory material 5-30CM of anti-crystallization device (30) In glass liquid, it is designed with 3-20 electrode assembly；

It is additionally provided with bottom flow liquid channel (20), in the glass metal in the region of bottom refractory material 5-30CM, if In respect of 3-20 electrode assembly；

It uses electrode to carry out temperature controlled glass metal rise channel s structure to the glass metal flowed from bottom to top -- (40) surrounding is designed with the electrode of 4-50 control temperature of glass liquid；Rise channel s structure (40) apart from bottom refractory material In glass metal in the region of 5-30CM, it is designed with 3-20 electrode assembly；

The lateral flame furnace production system of a kind of glassware according to claim 1, which is characterized in that adopt The glass metal that temperature controlled clarification is carried out to the glass metal flowed from the top to the bottom with electrode, is vented bubble and anti-crystallization device, it is deep Degree is within 90-150CM；Temperature controlled clarification is carried out to the glass metal flowed from the top to the bottom using electrode, exhaust is steeped and anti- The top design of crystallization device (30) has heating device.

The lateral flame furnace production system of a kind of glassware according to claim 1, which is characterized in that adopt The top exit of temperature controlled glass metal rise channel s structure (40) is carried out to the glass metal flowed from bottom to top with electrode, The top of the device (17) for the loading glass metal being coupled, is designed with heating device；The device for the loading glass metal being coupled (17) bottom, the electrode design for being also configured with control temperature of glass liquid have heating device.

A kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that its The daily output that flame thermal energy dominates the lateral flame furnace Jie Ju devices (10) of glass melting reaches 100 tons -1500 tons；Its fire Flame nozzle is mounted in two survey faces of lateral flame furnace, and the direction of flame injection direction and lateral flame furnace length is place In the directions Guang；In the glass metal of its lateral flame furnace Jie Ju device, it is designed with the electrode of electric boosting control temperature of glass liquid.

A kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that its The glass metal flowed from bottom to top at the top of temperature controlled glass metal rise channel s structure (40) go out using electrode Mouthful, the top of the device (17) for the loading glass metal being coupled is designed with heating device；The dress for the loading glass metal being coupled The bottom for setting (17) is also configured with the electrode of control temperature of glass liquid；The region for leading to molding machine is designed with glass metal lock Door；

The molding machine (50) of its glassware is the tin kiln structure of float flat glass technique comprising：Tin kiln bottom Layer has tin metal；Tin kiln both sides have 10-40 to edge machine；There is electric heater unit at the top of tin kiln；

After the tin kiln structure of float flat glass technique, also glass annealing device and glass plate cut material device.

A kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that its The glass metal flowed from bottom to top at the top of temperature controlled glass metal rise channel s structure (40) go out using electrode Mouthful, the top of the device (17) for the loading glass metal being coupled is designed with heating device；The dress for the loading glass metal being coupled The bottom for setting (17) is also configured with the electrode of control temperature of glass liquid, is coupled the sprue of glass metal, being coupled has 2- The molding machine (50) of 30 glass metal runners, each glass metal runner, the glassware being coupled is glass fibre The molding machine of production；Its glass fibre production molding machine include：2-30 dry crucibles of bearing glass liquid, 2-30 drawing Filament plate, wire drawing machine.

A kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that its The glass metal flowed from bottom to top at the top of temperature controlled glass metal rise channel s structure (40) go out using electrode Mouthful, the top of the device (17) for the loading glass metal being coupled is designed with heating device；The dress for the loading glass metal being coupled The bottom for setting (17) is also configured with the electrode of control temperature of glass liquid, is coupled the sprue of glass metal, being coupled has 2- 30 glass metal runners, each glass metal runner are coupled the molding machine (50) of glassware；Glassware Molding machine (50) is the blow molding device of industry and utility glass ware；In industry and 2-30 of daily glass product After blow molding device (50), the also annealing device of glassware.

A kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that its The glass metal flowed from bottom to top at the top of temperature controlled glass metal rise channel s structure (40) go out using electrode Mouthful, the top of the device (17) for the loading glass metal being coupled is designed with heating device；The dress for the loading glass metal being coupled The bottom for setting (17) is also configured with the electrode of control temperature of glass liquid, is coupled the sprue of glass metal, being coupled has 2- 30 glass metal runners, each glass metal runner are coupled the molding machine (50) of glassware；Glassware Molding machine (50) is the compression molding device of industry and utility glass ware；In industry and 2-30 of utility glass ware After compression molding device (50), the also annealing device of glassware.

A kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that its The glass metal flowed from bottom to top at the top of temperature controlled glass metal rise channel s structure (40) go out using electrode Mouthful, the top of the device (17) for the loading glass metal being coupled is designed with heating device；The dress for the loading glass metal being coupled The bottom for setting (17) is also configured with the electrode of control temperature of glass liquid, is coupled the sprue of glass metal, being coupled has 2- 30 glass metal runners, each glass metal runner are coupled the molding machine (50) of glassware；Glassware Molding machine (50) is the drawing molding device of industry and utility glass ware；In industry and 2-30 of utility glass ware After the molding machine (50) of drawing, the also annealing device of glassware.

A kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that its Using electrode, the glass metal flowed from bottom to top at the top of temperature controlled glass metal rise channel s structure (50) go out Mouthful, the top of the device (17) for the loading glass metal being coupled is designed with heating device；The dress for the loading glass metal being coupled The bottom for setting (17) is also configured with the electrode of control temperature of glass liquid, is coupled 2-30 glass metal runner, runner is coupled The molding machine (50) of glassware；The molding machine (50) of glassware is the blow molding device of bathroom glassware； After 2-30 blow molding device of bathroom glassware, the also annealing device of bathroom glassware.

A kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that its The composition of the glass material used is：By weight percentage, alumina content 0.01%--39%, content of magnesia For 5%--20%, silica content is 2.51-5.8 times of calcium oxide content, and calcium oxide content is the 0.7 of content of magnesia - 2.3 times again.

A kind of production method of glassware：

Get required device ready：Flame thermal energy dominates the lateral flame furnace Jie Ju devices (10) of glass melting, glass metal Card neck flow passage device (60), using electrode to the glass metal that flows from the top to the bottom carry out temperature controlled clarification, exhaust bubble and Anti- crystallization device (30) carries out temperature controlled glass metal rising passway knot using electrode to the glass metal flowed from bottom to top Structure (40), the molding machine (50) of glassware；Electrode energy in these devices can be filled in the molding of glassware When setting (50) and being stopped, so that the glass metal in respective device is maintained at 1300 DEG C or more , And and be maintained at higher than devitrification of glass temperature On degree；

Step 1. is scheduled glass raw material, and by glass raw material transport device, glass melting is dominated into flame thermal energy Lateral flame furnace Jie Ju devices (10) in, carry out dissolving to form glass metal, glass metal passes through the card neck runner of glass metal again Device (60), enters from upper lateral part using electrode, and temperature controlled clarification, exhaust are carried out to the glass metal flowed from the top to the bottom In bubble and anti-crystallization device (30)；And make card neck flow passage device (60) and using electrode to the glass metal that flows from the top to the bottom into The clarification of trip temperature control, the temperature of exhaust bubble and the glass metal in anti-crystallization device (30), control is higher than clarification, row's bubble 10²Pa Sec viscosity temperature on section and higher than the section on devitrification of glass temperature；

Process characteristic is：By the card neck flow passage device (60) of glass metal apart from the area of bottom refractory material 5-30CM In glass metal in domain, 3-20 electrode assembly of design makes card neck flow passage device (60) region, away from refractory material bottom In the glass metal in the region of 10-30CM distances, the work technological temperature in the section of a minimum of 100 cubes of CM volumes will be maintained at 1320 DEG C -1450 DEG C, it is higher than the work technological temperature 20- of the region glass metal apart from bottom refractory material 30-60CM distances 80℃；

Process characteristic is：Temperature controlled clarification, exhaust bubble and anti-analysis are carried out by the glass metal flowed from the top to the bottom The design of brilliant device (30) in the glass metal in the region of bottom refractory material 5-30CM, respective 3-20 electrode assembly, The glass metal flowed from the top to the bottom is set to carry out temperature controlled clarification, exhaust bubble and anti-crystallization device (30) region, away from fire resisting In the glass metal in the region of material bottom 5-30CM distances, the work technological temperature in the section of a minimum of 100 cubes of CM volumes, 1320 DEG C -1450 DEG C are maintained at, the work work of the region glass metal apart from bottom refractory material 30-60CM distances is higher than 20-80 DEG C of skill temperature；

Step 2. makes glass metal from using electrode, and temperature controlled clarification, row are carried out to the glass metal flowed from the top to the bottom Bubble and anti-crystallization device (30) lower part, the bottom flow liquid channel (20) of entrance enter back into one be coupled and use electrode pair The glass metal flowed from bottom to top carries out temperature controlled glass metal rise channel s structure (40)；

Process characteristic is：By what is designed in bottom flow liquid channel (20), apart from the region of bottom refractory material 5-30CM In glass metal in, 3-20 electrode assembly of design makes bottom flow liquid channel (20) region, away from refractory material bottom 5- In the glass metal in the region of 30CM distances, the work technological temperature in the section of a minimum of 100 cubes of CM volumes will be maintained at 1320 DEG C -1450 DEG C, it is higher than the work technological temperature 20- of the region glass metal apart from bottom refractory material 30-60CM distances 80℃；

Process characteristic is：Temperature controlled glass metal is carried out to the glass metal flowed from bottom to top by using electrode It is designed in rise channel s structure (40), in the glass metal in the region of bottom refractory material 5-30CM, 3-20 of design Electrode assembly makes bottom flow liquid channel (20) region, in the glass metal in the region away from refractory material bottom 5-30CM distances, The work technological temperature in the section of a minimum of 100 cubes of CM volumes, will be maintained at 1320 DEG C -1450 DEG C, be higher than apart from bottom 20-80 DEG C of the work technological temperature of the region glass metal of refractory material 30-60CM distances；

Process characteristic is：By it in the glass metal in the region of bottom refractory material 5-30CM, the 3-20 of design A electrode assembly makes bottom flow liquid channel (20) region, the glass metal in the region away from refractory material bottom 5-30CM distances In, the work technological temperature in the section of a minimum of 100 cubes of CM volumes will be maintained at 1320 DEG C -1450 DEG C, be higher than distance 20-80 DEG C of the work technological temperature of the region glass metal of bottom refractory material 30-60CM distances；

Step 3. glass metal again by bottom flow liquid channel (20), into electrode to the glass metal that flows from bottom to top into The glass metal rise channel s structure (40) of trip temperature control；

Process characteristic is：By it in the glass metal in the region of bottom refractory material 5-30CM, the 3-20 of design A electrode assembly carries out temperature controlled glass metal rise channel s structure using electrode to the glass metal flowed from bottom to top (40) region, in the glass metal in the region away from refractory material bottom 5-30CM distances, the areas of a minimum of 100 cubes of CM volumes Between work technological temperature, to be maintained at 1320 DEG C -1450 DEG C, be higher than apart from the area of bottom refractory material 30-60CM distances 20-80 DEG C of the work technological temperature of domain glass metal；

Step 4. moulding process：

Selection 1, the first glassware moulding process, the top exit above-mentioned by rise channel s structure (40) Glass metal, into the device (17) for the loading glass metal being coupled, using glass metal gate (8), into glassware at Type device (50)；The molding machine (50) of its glassware is the tin kiln structure of float flat glass technique；Glass metal enters tin The smooth plane for being furnished with the tin metal dissolved of kiln structure carries out glass metal time and divides thin and polishing；Again by the 10- on both sides 40 pairs of edge machines pull into required thickness to the glass tape of formation；Using annealing, material process is cut, forms float flat glass system Product；Or

Selection 2, second of glassware moulding process, the top exit above-mentioned by rise channel s structure (40) Glass metal, into the device (17) for the loading glass metal being coupled；The device (17) for loading glass metal is exactly the mainstream of glass metal Road, glass metal, which enters to be coupled, 2-30 glass metal runner；Glass metal enters the glassware that each runner is coupled Glass fibre production molding machine；The dry crucible of corresponding 2-30 bearing glass liquid is separately flowed into, glass metal is by corresponding to 2-30 bushing, form glass fibre under the action of corresponding wire drawing machine；Or

Selection 3, the third glassware moulding process, the top exit above-mentioned by rise channel s structure (40) Glass metal, into the device (17) for the loading glass metal being coupled；The device (17) for loading glass metal is exactly the mainstream of glass metal Road, glass metal, which enters to be coupled, 2-30 glass metal runner；Glass metal enters the glassware that each runner is coupled 2-30 industry and the blow molding device of utility glass ware；It is blow molded into the product of industry and domestic glass respectively；It passes through again The blow molding product of industry and domestic glass is made in the processing for crossing the annealing device of glassware；Or

Selection 4, the 4th kind of glassware moulding process, the top exit above-mentioned by rise channel s structure (40) Glass metal, into the device (17) for the loading glass metal being coupled；The device (17) for loading glass metal is exactly the mainstream of glass metal Road, glass metal, which enters to be coupled, 2-30 glass metal runner；Glass metal enters the glassware that each runner is coupled 2-30 industry and the compression molding device of utility glass ware；It is pressed into the product of industry and domestic glass respectively；It passes through again The compression moulding product of industry and domestic glass is made in the processing for crossing the annealing device of glassware；Or

Selection 5, the 5th kind of glassware moulding process, the top exit above-mentioned by rise channel s structure (40) Glass metal, into the device (17) for the loading glass metal being coupled；The device (17) for loading glass metal is exactly the mainstream of glass metal Road, glass metal, which enters to be coupled, 2-30 glass metal runner；Glass metal enters the glassware that each runner is coupled 2-30 industry and the drawing molding device of domestic glass, be drawn into the product of industry and domestic glass respectively；Using glass The drawing moulded products of industry and domestic glass are made in the processing of the annealing device of glass product；Or

Selection 6, the 6th kind of glassware moulding process, the top exit above-mentioned by rise channel s structure (40) Glass metal, into the device (17) for the loading glass metal being coupled；The device (17) for loading glass metal is exactly the mainstream of glass metal Road, glass metal, which enters to be coupled, 2-30 glass metal runner；Glass metal enters the glassware that each runner is coupled 2-30 bathroom glassware blow molding device, bathroom glassware is respectively prepared；Using the annealing of glassware Bathroom glassware is made in the processing of device.

Description of the drawings

Fig. 1 and Figure of abstract are the present invention a kind of lateral flame furnace production systems and producer of glassware Method, equipment composition side diagrammatic cross-section.

Fig. 2 is the present invention a kind of lateral flame furnace production system and production method of glassware, float glass The flow diagram of preparation process.

Fig. 3 is a kind of lateral flame furnace production system of glassware of the present invention and the glass fibre of production method The flow diagram of preparation process.

Symbol description

Fig. 1 and Figure of abstract are the present invention a kind of lateral flame furnace production systems and producer of glassware Method, equipment composition side diagrammatic cross-section in：

Symbol 10 indicates that flame thermal energy dominates the lateral flame furnace Jie Ju devices of glass melting；

Symbol 19 indicates glass raw material transport device；

Symbol 50 indicates that flame thermal energy dominates the lateral flame furnace Jie Ju devices of glass melting；

The expression of symbol 60, the card neck flow passage device of glass metal；

Symbol 30 indicates to carry out temperature controlled device to the glass metal flowed from the top to the bottom using electrode；

Symbol 40 indicates to use electrode, rise to the temperature controlled glass metal of glass metal progress flowed from bottom to top logical Road structure；

Symbol 20 indicates bottom flow liquid channel；

Symbol 17 indicates to load the device of glass metal；

Symbol 50 indicates the molding machine of glassware；

Symbol 8 indicates the electrode (8) in glass metal；

Symbol 9 indicates the electric heater unit (9) of glass metal upper layer space of planes；

Fig. 2 is a kind of lateral flame furnace production system of glassware of invention and floating for production method The flow diagram of method glass preparation technique：

20 symbolic indication bottom flow liquid channel of symbol；The expression of symbol 50, the molding machine of glassware.

Fig. 3 is a kind of lateral flame furnace production system of glassware of invention and the glass of production method The flow diagram of glass fiber preparation process：

Symbol 40 indicates to use electrode, rise to the temperature controlled glass metal of glass metal progress flowed from bottom to top logical The glass metal of road structure；

20 symbolic indication bottom flow liquid channel of symbol；

The expression of symbol 50, the molding machine of fiberglass products.

Specific implementation mode

Illustrate embodiments of the present invention referring to schema, it is noted that following figures system is the schematic diagram of simplification Formula, and only illustrate the basic conception of the present invention in a schematic way, only illustrate the structure related with the present invention in schema then rather than press Component count, shape when according to actual implementation and size are drawn, when actual implementation each component kenel, quantity and ratio simultaneously It is non-to be limited with diagram, it can need to make to change according to actual design, conjunction is first chatted bright.

Specific implementation mode

Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete Site preparation describes.

Embodiment 1：

A kind of (600 tons of original design pull amount) float glass process sodium calcium tablet of the lateral flame furnace production system of glassware Glass production apparatus structure system embodiment：

Get a kind of (600 tons of original design pull amount) float glass process sodium calcium of the lateral flame furnace production system of glassware ready Production structural system device needed for plate glass：

Get glass raw material transport device (19) ready first；Flame thermal energy dominates the lateral flame furnace Jie Ju of glass melting Device (10)；The card neck flow passage device (60) of glass metal, using electrode, to the glass metal that flows from the top to the bottom into trip temperature control The device (30) of system；Using electrode, temperature controlled glass metal rise channel s structure is carried out to the glass metal flowed from bottom to top (40)；Molding machine (50) needed for float glass process sodium calcium plate glass；

It is right since glass metal conducts thermal energy in 1450 DEG C of 1300 DEG C or more and thermal radiation, and due to using electrode The glass metal flowed from the top to the bottom carries out top, surrounding, the bottom of temperature controlled device (3), the control glass metal temperature of design The control of the heating device of degree, so in the glass metal of movement from top to down, using electrode, to what is flowed from the top to the bottom Glass metal carries out in temperature controlled device (3), can be accurately controlled 1-5 DEG C of mistake of the predetermined temperature needed for clarification, row's bubble Within difference, so only needing 3-6 hours time, so that it may to ensure -- soda-lime glass liquid exhaust bubble, clarification process stage, energy Reach high level and completes exhaust bubble, clear process goal.

For the present invention in soda-lime glass liquid exhaust bubble, in the clarification process stage, the technology for having broken traditional handicraft and device is inclined See-broken that traditional handicraft glass metal will be in cooling end or the device of entitled work department, it is necessary to by 3-5 days when Between, slowly complete the process of exhaust bubble, clarification process.The present invention can overcome its low production efficiency, waste lacking for production time It falls into；The present invention can overcome it, it is impossible to accurately according to the distinctive clarification of soda-lime glass ingredient, row's bubble 10²(Pa Sec) glues Temperature is spent, to complete the process of exhaust bubble, clarification process, quality can be caused to lack defect.Because of advanced technologies, glass can be made Liquid is in the stable clarification being higher than, row's bubble 10²When on the viscosity temperature of (Pa Sec), only passes through 3-6 hours, can reach The technique purpose that high-quality clarification, row steep.

Step 4. float glass process sodium calcium formed from plate glass technique：

The soda-lime glass liquid of top exit above-mentioned by rise channel s structure (40), into the loading glass being coupled The device (17) of glass liquid, using glass metal gate (8),

Glass metal is higher than 1080 DEG C 103 Pa Secs of the so-called soda-lime glass of traditional technology prejudice with 1230-1300 DEG C The requirement of molding technological temperature carry out glass tape into the smooth plane for being furnished with the tin metal dissolved of tin kiln structure Time divide thin and polishing process；It is 6-7mm that traditional soda-lime glass liquid, which enters the thickness plowed when dividing thin operation stage,；But this The technique of the Zhuan Zhi Jie Ju systems of invention, into when time dividing thin operation stage：A. due to 1230-1300 DEG C of soda-lime glass liquid Than 1080 DEG C viscosity are much lower, soda-lime glass liquid enter time divide thin operation stage its thickness can be thinner than traditional 6-7mm thickness, Reach 3-4mm, thus glass metal from 1230-1300 DEG C of downward cooling rate quickly；B. again since part original design can be turned off Tin kiln top glass band a large amount of heating and heat-insulating devices time divided in thin and polishing process, greatly reduce tin kiln structure The electrical heating energy at top, so can more greatly promote glass metal from 1230-1300 DEG C of downward cooling rate；C. again due to tin The lower part of the glass metal of kiln structure is furnished with the smooth tin metal dissolved, can be rapidly 1230- because of its extremely strong thermal conductivity 1300 DEG C of glass metal thermal energy are transmitted to entire tin kiln space.

The technique effect of technique one of of the device of the invention Jie Ju systems in formative stage：Because above-mentioned A.B.C.'s Process acts, so the process equipment change system of the present invention, it can be the temperature reduction technology of traditional cooling end or entitled work department Function, the thin and polishing process stage of time dividing for being arranged into moulding process are rapidly completed, make the glass tape after cooling, entering Required viscosity temperature requirement can be reached when edge machine.

The device of the invention Jie Ju systems the technique of formative stage technique effect two：Because turning off part original to set The a large amount of heating and heat-insulating devices of the tin kiln top glass band of meter time divided in thin and polishing process, the present invention is according to having in tin kiln In operation stage, break traditional handicraft and the technology prejudice of device, the technique effect for saving energy consumption can be generated.

The device of the invention Jie Ju systems the technique of formative stage technique effect three：Again due to tin kiln structure The lower part of glass metal is furnished with the smooth tin metal dissolved, can be rapidly 1230-1300 DEG C of glass because of its extremely strong thermal conductivity Glass liquid thermal energy is transmitted to entire tin kiln space, so it is not only advantageous to the polishing quality of polishing process, and industry glass tape is entering drawing When machine draws the glass tape of formation, the operation stage of required thickness, higher space temperature are more advantageous to intrinsic tin kiln Top glass band plows a large amount of heating and heat-insulating devices and its cooperation appropriate divided in thin and polishing process, makes glass tape more Be conducive to reach the suitable viscosity temperature needed for technique, can more be conducive to promotion 10-40 and institute is pulled into glass tape to edge machine It needs the efficiency of the thin technique of drawing of thickness and draws the quality of thin technique.

Due to using electrode, temperature controlled device (3) is carried out to the glass metal flowed from the top to the bottom and uses electrode, Temperature controlled glass metal rise channel s structure (40) is carried out to the glass metal that flows from bottom to top, top, surrounding, bottom, All design control temperature of glass liquid heating device, so movement from top to down glass metal and flow from bottom to top Glass metal, can control at 1300 DEG C or more；Again because 1300 DEG C with glass fluid be with thermal radiation conduction thermal energy, so Chu Yu &#91 can be accurately controlled;Using electrode, temperature controlled Zhuan Zhi &#93 is carried out to the glass metal flowed from the top to the bottom;(3) and [It adopts With electrode, temperature controlled glass metal rise channel s structure is carried out to the glass metal flowed from bottom to top;(4) the sodium calcium within Glass metal is completely in higher than 10 needed for soda-lime glass clarification, row's bubble²Pa Sec -- 20 DEG C on 1430 DEG C of temperature Stable state , [Zhi Nei &#93 of the error at 1-5 DEG C;.In this high-caliber glass metal exhaust bubble, clarification Advanced Manufacturing Technology In, glass metal can be completed within 3-6 hour reaches the clarification of high-quality, the soaked flat target of row.

So can overcome in the prior art 1, the sufficiently bulky of glass metal is accommodated, all reaches the 3-5 of pull amount of glass daily The time that the device of prior art cooling end again or entitled work department, i.e. glass metal will pass through 3-5 days wherein slowly complete The defect of the low production efficiency of the process of exhaust bubble, clarification process；

In the production of conventional float sodium calcium plate glass, everybody is desirable on the basis of existing equipment, in product product On the basis of matter qualification, production capacity is promoted by improving the pull amount of plate glass, improves device efficiency.This is conventional float In sodium calcium plate glass field, people thirst for solving always but fail the technical barrier to succeed always.

And in numerous large-scale float glass process Na Gai plate glass enterprises, thirst on the basis of existing equipment, is closed in product quality On the basis of lattice, production capacity is promoted by improving the pull amount of plate glass, in the effort to improve device efficiency, is encountered Problem is exactly：If in device of the glass metal without traditional cooling end or entitled work department, 3-5 days time is slowly complete The in a row process of bubble, clarification process, but increase pull amount 30-40% (namely glass metal warps in the moulding process stage It crosses in traditional cooling end or the device of entitled work department, 2 days time has only been used to complete the process for being vented bubble, clarification process) Afterwards, in float glass process sodium calcium flat glass product be not in the quarrel point occurred because dissolving operation stage reason, the product matter of calculus It measures unqualified problem and (illustrates fusion process production technology, under same energy consumption equally equipment, increasing production capacity 30-40% No has quarrel The unqualified problem of product quality of point, calculus)；But the production of float glass process sodium calcium plate glass adds under same energy consumption equally equipment The serious air bubble problems of big production capacity 30-40%, Hui Chu Qiu, the unqualified problem of product quality.Illustrate in the same energy of equivalent devices In the state of consumption, it is not problem to increase the 30-40% fusings of pull production capacity, and bubble quality is only problem.

The device of the invention knot Ju systems are generated in the change of technique device knot Ju elements and the change of interactively Give having technical effect that unexpectedly：Because can solve in several hours shorter Shi Jian [Rather than several days Shi Jian ], just complete Clarification, the soaked flat target of row for reaching high-quality at glass metal, so can add in the state of equivalent devices same energy consumption Big sodium calcium float glass pull-can be in the state of equivalent devices same energy consumption, and the production capacity of high-quality sodium calcium float glass can To rise 30-40%.

Float glass process sodium calcium plate glass belt of the step 5. Jing Guo moulding process cuts material process using annealing operation, is formed The float glass process sodium calcium final sheet of predetermined size.

Embodiment 2：

A kind of 500 tons of superelevation aluminium of the lateral flame furnace production system of glassware【Aluminium oxide 16-25%】Alkali-free Glass fiber producing device structural system embodiment：

Get a kind of production structural system device of the lateral flame furnace production system of glassware ready：

The present invention steeps, in glass metal exhaust in the clarification process stage, has broken traditional handicraft and the technology prejudice-of device Having broken traditional handicraft glass metal will be in cooling end or the device of entitled work department, it is necessary to pass through 3-5 days time, Slowly complete the process of exhaust bubble, clarification process.The present invention can overcome its low production efficiency, waste the defect of production time； The present invention can overcome it, it is impossible to accurately according to the distinctive clarification of soda-lime glass ingredient, row's bubble 10²The viscosity of (Pa Sec) Temperature can cause quality to lack defect to complete the process of exhaust bubble, clarification process.Because of advanced technologies, glass metal can be made In the stable clarification being higher than, row's bubble 10²When on the viscosity temperature of (Pa Sec), only pass through 3-6 hours, can reach high The technique purpose that quality clarification, row steep.

The above-mentioned technology essential factor of the present invention and the goal of the invention of technique are：

And the present invention is because use above-mentioned completely new technique：In the molten Yao Jie Ju devices of multiple regions, bottom refractory material In glass metal in the region of 5-30CM distances, 3-20 electrode assembly is all devised, uses completely new technique：Make more In the glass metal in the region of the bottom refractory material 10-30CM distances in a molten kiln knot Ju devices region in region, minimum each own 1 The work technological temperature in a section is maintained at 1320 DEG C -1450 DEG C, higher than apart from the area of bottom refractory material 30-60CM distances 20-80 DEG C of the work technological temperature of domain glass metal.So these regions can be formed, apart from bottom refractory material 5-30- The glass metal of 60CM distances is small-scale to flow up and down homogenizing, makes " rich aluminium deposition phenomenon -- i.e. high-alumina component content Glass metal part, the phenomenon that deposition is in bottom due to than great ", be homogenized, be resolved.It can fundamentally solve Glass finished-product formative stage is certainly in turn resulted in because composition is seriously uneven, glass muscle, striped, oxygen-enriched piece of White-opalescent and item occurs Products underproof difficult point at all is waited, so that the glassware of the alumina content of the production 15--35% of high qualification rate is become can Energy.

And the present invention can also overcome in prior art, attempt to reach using traditional stirring technique by prior art Traditional stirring technique is used to purpose, overcomes and the difficult point that " rich aluminium deposition phenomenon " generates occurs in glass metal bottom.

One of the stirring technique difficult point for overcoming its traditional：It is close to glass shaping area using traditional stirring technique Electric melting furnace bottom or rising passway top position, stirring technique are easy to generate secondary bubble, and a large amount of bubbles is made to occur directly in production In product；

The two of the stirring technique difficult point for overcoming its traditional：Using traditional stirring technique, if in the ring more than 1300 DEG C In border, using the stainless steel mixer for adding cooling water circulation to cool down, serious blender side wall glass metal nearby can be caused, because Long-term water-cooled cooling conduction, and a large amount of crystallizations of glass metal are generated, the electric melting furnace bottom in close glass shaping area or rising passway Top position, crystallization directly can largely occur in the product；

The three of the stirring technique difficult point for overcoming its traditional：Using platinum blender, can there is that cost is too high and platinum is in height There is new bubble in lower reacted with glass of temperature, the electric melting furnace bottom in close glass shaping area or rising passway top position, production Raw secondary bubble, also can be such that a large amount of bubbles occur directly in product.This is that the production that existing technology all can not be qualified contains The major reason of the glassware of 20% or more superelevation aluminium content.

Again because these elements are set, electrode is all used, the temperature of superelevation aluminium alkali-free glass fibre glass metal, control Make the section on 1310 DEG C of degree of recrystallization temperature of the superelevation aluminium alkali-free glass fibre raw material higher than salic 15-35%； Since glass metal conducts thermal energy in 1430 DEG C of 1300 DEG C or more and thermal radiation；Again due to using electrode, to glass metal into Top, surrounding, the bottom of the device of trip temperature control are designed with the control of the heating device of control temperature of glass liquid；So energy It is accurately controlled within 1-5 DEG C of error of required predetermined temperature, so (salic to reach 15-35%) can effectively be controlled The strong glass product of superelevation large volume big flow glass metal, before reaching process for forming glass, completely control In the target higher than recrystallization temperature.

The goal of the invention of the present invention also resides in：

When producing superelevation lead glass, since the flame thermal energy in production system dominates the lateral flame pond of glass melting Yao Jie Ju devices (10)；Using electrode, temperature controlled device (3) is carried out to the glass metal flowed from the top to the bottom；Using electricity Pole carries out temperature controlled glass metal rise channel s structure (40) to the glass metal flowed from bottom to top；It can be in glassware Molding machine (50) (faulty in such as moulding process, safety gate is closed, the life before making entirely to be molded when being stopped Production system glass liquid be within respective device, when not pressing process and flowing), it sets in this 3 element devices of the invention The rational position and electrode energy of the electrode of meter can be maintained at glass metal within respective device higher than superelevation lead glass 1290 DEG C of recrystallization temperature or more, reaches 1300-1400 DEG C, so that glass is in the state of thermal radiation conduction thermal energy, so as to ensure Temperature of glass liquid control in these three element devices scheduled requirement+ranges of -1-5 DEG C of difference.So can overcome In the state of the flowing glass metal thermal energy that the glass melting process that No have flame thermal energy leading generates, ensure that glass metal is not analysed It is brilliant.

And the glass producing system device of the prior art, due to wanting white, quiet clothes to set the electricity for having with No and wherein designing without this 3 The rational position and electrode energy of pole, thus at all cannot in day glass producing system device of the production capacity hundreds of to upper kiloton, Produce the salic superelevation lead glass product up to 15--35%.

This is also the relationship change of the position relationship variation and interaction of 3 element devices described in present invention power one, And the specific electrode factor change in 3 element devices and skill unexpected caused by the relationship change of interaction Art effect.

And in the glass producing system device of the prior art：A. Bu Zhi No have the position relationship of 3 above-mentioned element devices Variation innovation and the relationship change innovation to interact；B. Ye No have specific electrode factor change in 3 element devices and The relationship change of interaction is innovated；C. Ye No have and expect not caused by the relationship change innovation that these elements interact The technique effect arrived.

Step 4. superelevation aluminium alkali-free glass fibre moulding process：

The superelevation aluminium alkali-free glass fibre of top exit above-mentioned by rise channel s structure (40), glass metal enter The glass metal of device (17) top exit above-mentioned by rise channel s structure (40) for the loading glass metal being coupled, into Enter the device (17) for the loading glass metal being coupled；The device (17) for loading glass metal is exactly the sprue of glass metal, glass metal There is 2-30 glass metal runner into being coupled；Glass metal enters the glass fibers for the glassware that each runner is coupled Tie up the molding machine of production；The dry crucible of corresponding 2-30 bearing glass liquid is separately flowed into, glass metal is by corresponding 2-30 Bushing.There is heating in the top of the sprue of (1) glass metal and glass metal and controls the device of temperature, and this rank Section glass metal only control the superelevation aluminium alkali-free glass fibre raw material higher than salic 30% 1310 DEG C of recrystallization temperature it On 1330 DEG C of sections；It is also that thermal radiation conducts thermal energy；The mistake that temperature of glass liquid reaches 1-5 DEG C can be made using thermal radiation conduction Within difference.(2) glass metal, which enters, is coupled the top for having 2-30 glass metal runner and has heating and control in glass metal The device of temperature, and this staged glass liquid is only controlled in the superelevation aluminium alkali-free glass fibre raw material higher than salic 30% 1310 DEG C of recrystallization temperature on 1330 DEG C of sections；It is also that thermal radiation conducts thermal energy；Glass metal can be made using thermal radiation conduction Temperature reaches within 1-5 DEG C of error.(3) top and the glass of the dry crucible of corresponding 2-30 bearing glass liquid are separately flowed into There is heating in liquid and control the device of temperature, and this staged glass liquid is only controlled in the superelevation higher than salic 30% 1330 DEG C of sections on 1310 DEG C of the recrystallization temperature of aluminium alkali-free glass fibre raw material；It is also that thermal radiation conducts thermal energy；Using heat Width is penetrated within the error conducted and temperature of glass liquid can be made to reach 1-5 DEG C.(4) this glass metal passes through corresponding 2-30 bushing On be also configured with heating with control temperature device；Importantly, salic the 30% of the present embodiment super high-aluminum alkali-free glass The molding viscosity temperature of 10 2.5 (Pa Secs) of glass fibrous raw material is 1330 DEG C；So wire drawing plate temperature control higher than 1330 DEG C of progress wire drawings on 1310 DEG C of recrystallization temperature, form under the action of corresponding wire drawing machine -- and the present embodiment contains The superelevation aluminium alkali-free glass fibre product of aluminium oxide 30%.

The critically important technique effect that the device of the invention Jie Ju systems generate：The prior art produces salic 20- 25% high-aluminum alkali-free S level fiberglass is all complete in producing tens to hundreds of kilograms of the device of glass fiber manufacturing line daily At.Everybody is intended to the dress of the glass fiber manufacturing line using the large-tonnage (producing ten thousand tons of 7-20 per year) for producing 100-600 tons daily It sets, to produce the high-aluminum alkali-free S level fiberglass of salic 15-25-35%, on the basis of reaching product quality qualification, High-aluminum alkali-free S level fiberglass production efficiencys are greatly improved, to adapt to high-caliber wind-powered electricity generation leaf, new-energy automobile, aerospace The requirement in market.This is in high-aluminum alkali-free S level fiberglass field, and people thirst for solving always but fail to succeed always Technical barrier.But the present invention solves this technical barrier.

The schematism device , No of existing correlation technique have the glass metal for the big flow that can accurately control large volume Temperature cannot ensure that the glass metal of the big flow of large volume is substantially higher than recrystallization temperature before moulding process, not generate completely Crystallization.So existing correlation technique -- in the schematism device for the prior art for being related to glassware class production line, always The salic strong glassware of the superelevation up to 20-49% can not all be produced.

Existing correlation technique：Traditional glassware electric melting furnace process units Jie Ju systems, although it is also included：It adopts With electrode, temperature controlled device (3) is carried out to the glass metal flowed from the top to the bottom；Using electrode, to what is flowed from bottom to top Glass metal carries out temperature controlled glass metal rise channel s structure (40)；But You Yu No have flame thermal energy to dominate glass melting Lateral flame furnace Jie Ju devices, existing defects are：Because of traditional glassware electric melting furnace process units Jie Ju systems, There can only be the production line of tens tons of daily output by tonnage limitation, it is impossible to be used in the daily output is given birth to up to hundreds of tons of big production capacity glassware Producing line.

So compared with the daily output is up to hundreds of tons of big production capacity glassware production line, one of defect is：Invest output Ratio is low, low production efficiency.Defect second is that：The energy consumption of identical yield is than high.The three of defect are：The people of identical yield Power resource consumes high.

Embodiment 3：

A kind of (800 tons of original design pull amount) float glass process superelevation aluminium of the lateral flame furnace production system of glassware【Oxygen Change aluminium 15-35%】Plate glass process units structural system embodiment；

For the present invention in soda-lime glass liquid exhaust bubble, in the clarification process stage, the technology for having broken traditional handicraft and device is inclined See-broken that traditional handicraft glass metal will be in cooling end or the device of entitled work department, it is necessary to by 3-5 days when Between, slowly complete the process of exhaust bubble, clarification process.The present invention can overcome its low production efficiency, waste lacking for production time It falls into；The present invention can overcome it, it is impossible to accurately according to the distinctive clarification of glass ingredient, row's bubble 10²The viscosity temperature of (Pa Sec) Degree can cause quality to lack defect to complete the process of exhaust bubble, clarification process.Because of advanced technologies, glass metal can be made to exist The stable clarification being higher than, row's bubble 10²When on the viscosity temperature of (Pa Sec), only passes through 3-6 hours, Gao Pin can be reached The technique purpose that matter clarification, row steep.

Again because several elements are set, electrode is all used, the temperature of superelevation lead glass liquid, is controlled higher than containing oxidation Section on 1310 DEG C of degree of recrystallization temperature of the superelevation aluminium alkali-free glass fibre raw material of aluminium 15-30%；Since glass metal exists 1430 DEG C of 1300 DEG C or more and thermal radiation conduction thermal energy；Again due to using electrode, glass metal is carried out temperature controlled Top, surrounding, the bottom of device are designed with the control of the heating device of control temperature of glass liquid；So can be accurately controlled Within 1-5 DEG C of error of required predetermined temperature, so the super high-strength glass of (salic to reach 15-30%) can be controlled effectively The glass metal of the big flow of the large volume of product, before reaching glass moulding processes, control is higher than recrystallization temperature completely Target.

The goal of the invention of the present invention also resides in：

And the glass producing system device of the prior art, due to wanting white, quiet clothes to set the electricity for having with No and wherein designing without this 3 The rational position and electrode energy of pole, thus at all cannot in day glass producing system device of the production capacity hundreds of to upper kiloton, Produce the salic superelevation lead glass product up to 20-30%.

Step 4. float glass process superelevation lead glass moulding process：

The superelevation lead glass liquid of top exit above-mentioned by rise channel s structure (40), into the loading being coupled The device (17) of glass metal, using glass metal gate (8), superelevation lead glass liquid is with 1300 DEG C, into the smooth of tin kiln structure The plane for being furnished with the tin metal dissolved, carry out glass tape time divides thin and polishing process；Traditional soda-lime glass liquid, which enters, to be plowed Thickness when dividing thin operation stage is 6-7mm；But the technique of the device of the invention Jie Ju systems, due to enter time divide it is thin When operation stage：A. due to 1300 DEG C of superelevation lead glass liquid, than superelevation lead glass 10³The molding viscosity temperature of (Pa Sec) 1200 DEG C of viscosity are much lower, glass metal enter time divide thin operation stage its thickness can be thinner than traditional 6-7mm thickness, reach 4- 5mm；So glass metal from 1300 DEG C of downward cooling rates quickly；B. again since part intrinsic tin kiln top can be turned off Glass tape plows a large amount of heating and heat-insulating devices divided in thin and polishing process, and the electricity for greatly reducing tin kiln structural top adds Thermal energy, so can more greatly promote glass metal from 1300 DEG C of downward cooling rates；C. again due to tin kiln structure glass metal it Lower part is furnished with the smooth tin metal dissolved, because of its extremely strong thermal conductivity, 1300 DEG C of glass metal thermal energy can be transmitted to rapidly Entire tin kiln space.

The device of the invention Jie Ju systems the technique of formative stage technique effect three：Again due to tin kiln structure The lower part of glass metal is furnished with the smooth tin metal dissolved, can be rapidly 1300 DEG C of glass metals because of its extremely strong thermal conductivity Thermal energy is transmitted to entire tin kiln space, so be not only advantageous to the polishing quality of polishing process, and glass tape is into edge machine The operation stage of side required thickness, higher space temperature is drawn the glass tape of formation to be more advantageous to intrinsic tin kiln top Glass tape plows a large amount of heating and heat-insulating devices and its cooperation appropriate divided in thin and polishing process, keeps glass tape more advantageous In reaching the suitable viscosity temperature needed for technique, it can more be conducive to promotion 10-40 and required thickness is pulled into glass tape to edge machine The efficiency of the thin technique of drawing of degree and the quality for drawing thin technique.

Due to the present invention a kind of lateral flame furnace production system and production method of glassware；In, it devises and adopts With electrode, temperature controlled device (3) carried out to the glass metal flowed from the top to the bottom, the perfect superelevation lead glass that solves Clarification, row's bubble 10²The quality of the operation stage of (Pa Sec)；So in the equipment of existing 800 tons of float glass process superelevation aluminium plate glass On the basis of, on the basis of product quality qualification, production capacity is promoted by improving the pull amount of plate glass, is set to improve Pull amount, is increased 30% or more, reached by the equipment that standby efficiency can make former design pull 1000 tons of float glass process superelevation aluminium plate glass of amount To 1000 tons or more, it also can guarantee that the serious air bubble problems of float glass process superelevation aluminium plate glass Bu Hui Chu Qiu, product quality are unqualified Problem.Because of advanced technologies, glass metal can be made in the stable clarification being higher than, row's bubble 10²The viscosity temperature of (Pa Sec) it When upper, only passed through 3-4 hours, and high-quality clarification can be reached, the technique purpose that row steeps)

Float glass process superelevation aluminium plate glass belt of the step 5. Jing Guo moulding process cuts material process, shape using annealing operation At the float glass process superelevation aluminium final sheet of predetermined size.

Right of the present invention play ask 1 novelty

(1) present invention is a kind of element relationship change invention,【A kind of lateral flame furnace production system of glassware System】The right of patent, which is played, asks 1, mainly there is 6 technique device Jie Ju elements and 4 subdivision technique device Jie Ju elements：

It mainly has 6 technique device Jie Ju elements to be：It includes glass raw material transport device (19), flame thermal energy master Lead the lateral flame furnace Jie Ju devices (10) of glass melting；The card neck flow passage device (60) of glass metal；Using electrode to from upper The glass metal to flow downward carries out temperature controlled clarification, exhaust bubble and anti-crystallization device (30)；Using electrode, to from it is lower to The glass metal of upper flowing carries out temperature controlled glass metal rise channel s structure (40)；The molding machine (50) of glassware.And And claim 1 has further statement to the substantive characteristics of this six technique device Jie Ju elements.

(2) 4 subdivision technique device Jie Ju elements be：

(3) with the immediate prior art of the present invention, there are 6 classes：

1. the cross of the sodium calcium float glass production line of the prior art of the large-tonnage of kiloton is gone up in all hundreds of tons of daily outputs- To flame furnace schematism device.

【1】Qi No has the main technique device Jie Ju elements of the present invention-to be：Using electrode to flowing from the top to the bottom Glass metal carries out temperature controlled clarification, exhaust bubble and anti-crystallization device (30)；Using electrode, to the glass flowed from bottom to top Glass liquid carries out temperature controlled glass metal rise channel s structure (40)；Bottom flow liquid channel (20)；The master of these three present invention- The technique device Jie Ju elements wanted.

【2】Qi No has 4 subdivision technique device Jie Ju elements of the present invention-.

2. be related to the prior art of high alumina and superelevation aluminium float flat glass and electronic glass production line-tank furnace system System property combination unit.

3. the system of the prior art of the glass fibre transverse direction flame furnace production line of the large-tonnage of 100-600 tons of daily output Property combination unit.

4. tens tons of the All Electric Melting Furnace schematism device of tens tons of the daily output of the prior art and the daily output of the prior art Horseshoe kiln system combination unit.

【1】Qi No has the main technique device Jie Ju elements of the present invention-to be：Flame thermal energy dominates the cross of glass melting To flame furnace Jie Ju devices (10)；The card neck flow passage device (60) of glass metal.

5. the present invention：A kind of lateral flame furnace production system and production method of glassware；People was Shen in 2014 A kind of anti-crystallization device in cooling end region for glass technology of patent of invention please.

The above-mentioned 5 class prior art, with the present invention【A kind of lateral flame furnace production system of glassware】So this hair Bright claim 1 has novelty.

Right of the present invention play ask 1 creativeness

Invention ... the element relationship changed according to Guidelines for Patent Examination second part chapter 4 4.6.1 element relationships Change, such as the change of position, the change ... of interactively

(2) if element relationship change causes invention to produce unexpected technique effect, invention has outstanding Substantive distinguishing features and significant progress, it is creative.

In the claims in the present invention 1, technique device Jie Ju elements, compare 5 kinds of prior arts：

A. invention have been described on technique device Jie Ju factor contents and position, compare kind of a prior art and have to change first Become；

B. of the invention：A kind of lateral flame furnace production system and production method of glassware；Also it describes, On the interactively of technique device Jie Ju elements, comparing kind of a prior art has change；

C. moreover, being described in description of the invention, these element relationships of generation change, and lead to unexpected skill Art effect.So the claims in the present invention 1 have substantive distinguishing features outstanding and significant progress, it is creative.

Compare the prior art 1：

The transverse direction of the sodium calcium float glass production line of the prior art of the large-tonnage of kiloton is gone up in all hundreds of tons of daily outputs- In flame furnace schematism device, lateral flame furnace Jie Ju devices, what is be coupled by card neck device is a kind of cooling The device of portion or entitled work department；In the device of its card neck device, cooling end or entitled work department, the depth of glass metal is all 1 Rice or so, glass metal are totally all horizontally oriented towards molding machine and move.

The present invention due to the depth of the glass metal of the card neck flow passage device (60) of glass metal position, with flame thermal energy master Lead the lateral flame furnace knot Ju devices (10) of glass melting and using electrode to the glass metal that flows from the top to the bottom into trip temperature Clarification, the exhaust of control are steeped and the position of the depth of metal of anti-crystallization device (30) is changed, by existing tank furnace technology Depth of metal is consistent in above three technique device element in device, changes into the card neck flow passage device of glass metal (60) depth of glass metal is only only that flame thermal energy is dominated the lateral flame furnace Jie Ju devices (10) of glass melting and adopted Temperature controlled clarification is carried out to the glass metal flowed from the top to the bottom with electrode, exhaust is steeped and the glass of anti-crystallization device (30) The 10%-40% of liquid depth.(see Figure of description 3)

The change that the position of card neck flow passage device (60) depth of metal of this glass metal occurs, can just make glass metal Card neck flow passage device (60) glass metal, the glass metal bottom horizontal flow sheet from prior art tank furnace Jie Ju becomes the card for making glass metal Neck flow passage device (60) glass metal carries out temperature controlled clarification, exhaust from using electrode to the glass metal flowed from the top to the bottom The upper lateral part of bubble and anti-crystallization device (30) flows into (see Figure of description 3)；The variation of melt flow position could be formed, It forms glass metal and temperature controlled clarification, exhaust bubble and anti-crystallization is being carried out to the glass metal flowed from the top to the bottom using electrode In device (30), the variation that flows from the top to the bottom.

The present invention, also the technique device Jie Ju elements of the prior art【A kind of device of cooling end or entitled work department】, It is changed to【Temperature controlled clarification, exhaust bubble and anti-crystallization device are carried out to the glass metal flowed from the top to the bottom using electrode】 (3)；【Using electrode, temperature controlled glass metal rise channel s structure is carried out to the glass metal flowed from bottom to top】(4).

C. it due to the change of change and interactively in technique device knot Ju elements, is stated in description of the invention , these element relationships of generation change, and lead to unexpected technique effect：

Due to using electrode, temperature controlled device (3) is carried out to the glass metal flowed from the top to the bottom and uses electrode, The top of temperature controlled this 2 devices of glass metal rise channel s structure (40), four are carried out to the glass metal flowed from bottom to top Week, bottom, the heating device of the control temperature of glass liquid all designed, so the glass metal of movement wherein from top to down and from Under the glass metal that flows up, can control at 1300 DEG C or more；Again because with glass fluid being conducted with thermal radiation at 1300 DEG C Thermal energy, so Chu Yu &#91 can be accurately controlled;Using electrode, temperature controlled Zhuan Zhi &#93 is carried out to the glass metal flowed from the top to the bottom; (3) and [Using electrode, temperature controlled glass metal Shang Shengtongdaojiegou &#93 is carried out to the glass metal flowed from bottom to top;(4) it Interior soda-lime glass liquid is completely in higher than 10 needed for soda-lime glass clarification, row's bubble²Pa Sec -- 1430 DEG C of temperature it On 20 DEG C of stable state , [Zhi Nei &#93 of the error at 1-5 DEG C;.In this high-caliber glass metal exhaust bubble, the first system of clarification It makes in technique, glass metal can be completed within 3-6 hour and reaches the clarification of high-quality, the soaked flat target of row.

So can overcome in the prior art 1, the sufficiently bulky of glass metal is accommodated, all reaches the 3-5 of pull amount of glass daily The time that the device of prior art cooling end again or entitled work department, i.e. glass metal will pass through 3-5 days wherein slowly complete The defect of the low production efficiency of the process of exhaust bubble, clarification process.

And in numerous large-scale float glass process Na Gai plate glass enterprises, the problem encountered is exactly：If glass metal is without tradition Cooling end or entitled work department device in, 3-5 days time slowly completed the process of exhaust bubble, clarification process, but The moulding process stage increases pull amount 30-40%, and (namely glass metal passes through the dress of traditional cooling end or entitled work department In setting, 2 days time is only used to complete the process for being vented bubble, clarification process).

Its consequence 1 is：Be not in the quarrel occurred because dissolving operation stage reason in float glass process sodium calcium flat glass product Point, calculus the unqualified problem of product quality (illustrate fusion process production technology, same energy consumption equally equipment under, increase production Energy 30-40% No have the point that is cut, the unqualified problem of product quality of calculus)；

Its consequence 2 is：The production of float glass process sodium calcium plate glass increases production capacity 30-40% under same energy consumption equally equipment, The serious air bubble problems of Hui Chu Qiu, the unqualified problem of product quality.

Illustrate in the state of equivalent devices same energy consumption, it is not problem to increase the 30-40% fusings of pull production capacity, and gas Bubble quality is only problem.

In the production of conventional float sodium calcium plate glass, everybody is desirable on the basis of existing equipment, in product product On the basis of matter qualification, production capacity is promoted by improving the pull amount of plate glass, improves device efficiency.This is conventional float In sodium calcium plate glass field, people thirst for solving always but fail the technical barrier to succeed always；

The invention of the change of this technology Zhuan Zhi Jie Ju elements solves this people and thirsts for always solving but always failing The technical barrier to succeed, so the invention of the change of this technology Zhuan Zhi Jie Ju elements, have substantive distinguishing features outstanding and Significant progress, it is creative.

The present invention is on technique device Jie Ju factor contents and position, on the interactively of technique device Jie Ju elements, Comparing the prior art has essential change；Moreover, because on technique device Jie Ju factor contents and position, in technique device knot On the interactively of Ju elements, the essence for comparing prior art generation changes, and leads to unexpected technique effect.So this Invention claim 1 has substantive distinguishing features outstanding and significant progress, creative.

Compare the prior art 2：

In the prior art of the glass fibre transverse direction flame furnace production line for the large-tonnage for being related to 100-600 tons of daily output In schematism device, flame thermal energy is all used to dominate the lateral flame furnace Jie Ju devices (10) of glass melting；Directly join Device (the 17)-i.e. main channel for the loading glass metal being knotted, and it is designed with 10-30 glass metal runner, each of which runner, connection It is knotted the molding machine of the glass fibre production of glassware, separately flows into the dry crucible of corresponding 2-30 bearing glass liquid, glass Glass liquid passes through corresponding 2-30 bushing, and glass fibre is formed under the action of corresponding wire drawing machine.Existing correlation technique -- In the schematism device for being related to the glass fibre transverse direction flame furnace production line of large-tonnage of 100-600 tons of daily output, fire Flame thermal energy dominates the lateral flame furnace Jie Ju devices (10) of glass melting；The device for the loading glass metal being directly coupled (17)-i.e. glass metal main channel and 10-30 glass metal runner.The lateral flame pond of glass melting is dominated in flame thermal energy Glass metal in Yao Jie Ju devices (10), be horizontally oriented it is mobile, the top of flame interaction with lower layer's glass metal temperature difference too Greatly, the large volume in the lateral flame furnace Jie Ju devices (10) of the leading glass melting of flame thermal energy cannot be accurately controlled completely The temperature of glass metal of big flow be substantially higher than analysis before entering glass metal main channel and 10-30 glass metal runner Brilliant temperature.Again due to high alumina and superelevation lead glass fiber, salic to reach 20-25-35%, recrystallization temperature is all very high, and many is all Reach 1300 DEG C or more.If there is the glass metal of crystallization enters sprue and each runner, sprue and each runner are It can not be the crystal re-melting of crystallization.This will make the crystal of crystallization enter the dry crucible of glass dimension molding and bushing, cause to block up Wire drawing hole and Queues are produced.

So existing correlation technique -- in the tank furnace glass fiber manufacturing line for the large-tonnage for being related to 100-600 tons of daily output Schematism device, can only produce at present it is salic up to 15% glass fibre；It always can not all produce salic reach The super high-strength glass fibre of 20-25%；Unlikely produce the salic super high-strength glass fibre up to 20-49%.

A. lateral flame of the present invention the leading glass melting of technique device Jie Ju element flame thermal energy in the prior art Tank furnace Jie Ju devices (10)；Later, 3 new technique device Jie Ju elements are increased：The card neck flow passage device of glass metal (60)；Temperature controlled clarification, exhaust bubble and anti-crystallization device are carried out to the glass metal flowed from the top to the bottom using electrode (30)；Using electrode, temperature controlled glass metal rise channel s structure (40) is carried out to the glass metal flowed from bottom to top；By In the change of change and interactively in technique device knot Ju elements：

B. the present invention generate due to these element relationships change, caused unexpected technique effect：

The change that the position of card neck flow passage device (60) depth of metal of this glass metal occurs, can just make glass metal Card neck flow passage device (60) glass metal, the glass metal bottom horizontal flow sheet from prior art tank furnace Jie Ju becomes the card for making glass metal Neck flow passage device (60) glass metal carries out temperature controlled clarification, exhaust from using electrode to the glass metal flowed from the top to the bottom The upper lateral part of bubble and anti-crystallization device (30) flows into (see Figure of description 3), could form the variation of melt flow position, It forms glass metal and temperature controlled clarification, exhaust bubble and anti-crystallization is being carried out to the glass metal flowed from the top to the bottom using electrode The variation flowed from the top to the bottom in device (30).

The present invention carries out temperature controlled device (3) to the glass metal flowed from the top to the bottom and uses due to using electrode Electrode, to the glass metal that flows from bottom to top carry out the top of temperature controlled glass metal rise channel s structure (40), surrounding, Bottom, the heating device of the control temperature of glass liquid all designed, so in the glass metal and from bottom to top of movement from top to down The glass metal of flowing can be controlled at 1300 DEG C or more；Again because 1300 DEG C with glass fluid be with thermal radiation conduction thermal energy, institute Chu Yu &#91 can be accurately controlled;Using electrode, temperature controlled Zhuan Zhi &#93 is carried out to the glass metal flowed from the top to the bottom;(3) and [Using electrode, temperature controlled glass metal Shang Shengtongdaojiegou &#93 is carried out to the glass metal flowed from bottom to top;(4) containing within Aluminium oxide is completely in up to the glass metal of the super high-strength glass fibre of 20-49% higher than 20 DEG C steady on devitrification of glass temperature Determine state , [Zhi Nei &#93 of the error at 1-5 DEG C;.

So the present invention：A kind of lateral flame furnace production system and production method of glassware；These elements Relationship changes, and can be overcome the deficiencies of existing technologies on the basis of general cost, and reaching makes salic surpassing up to 20-49% The glass metal of high-strength glass fibre, before entering moulding process, the technology being maintained on higher than recrystallization temperature that can stablize Purpose.The technical barrier generated because of these technology essential factor devices missing for overcoming the prior art, makes 100 ton -600 of daily output On the high efficiency tank furnace glass fiber manufacturing line of ton, the strong glass of superelevation of high alumina and superelevation aluminium (salic 20-49%) can be produced Glass fiber generates unexpected technique effect.

The goal of the invention of the present invention also resides in：

When producing the super high-strength glass fibre of high alumina and superelevation aluminium (salic 20-49%), there is glassware (faulty in such as moulding process, safety gate is closed, before making entirely to be molded when the state that molding machine (50) is stopped Production system glass metal be within respective device, press process flowing state).

At this moment, the flame thermal energy in production system dominates the lateral flame furnace Jie Ju devices (10) of glass melting；Using Electrode carries out temperature controlled device (3) to the glass metal flowed from the top to the bottom；Using electrode, to the glass flowed from bottom to top Glass liquid carries out temperature controlled glass metal rise channel s structure (40)；In this 3 this element device of the invention, the electricity of design Glass metal within respective device can be maintained at the crystallization higher than superelevation lead glass by the rational position and electrode energy of pole 1300-1480 DEG C or more of temperature makes glass metal be in the state of thermal radiation conduction thermal energy, so as to ensure these three elements Temperature of glass liquid control in device scheduled requirement+ranges of -1-5 DEG C of difference.

Conversely, when producing the super high-strength glass fibre of high alumina and superelevation aluminium (salic 20-49%), there is glass When the state that the molding machine (50) of product is stopped (it is faulty in such as moulding process, safety gate close, make entirely at Production system glass metal before type is within respective device, does not press the state of process flowing).Ru Guo No have this The relationship change innovation that Fa Ming No have the position relationship variation innovation of 3 above-mentioned element devices and interact, just differs Surely it will appear glass metal before entering moulding process, a wide range of crystallization.

And the big production system device of glass fibre tank furnace of the prior art, there is it with No due to there is no this 3 white, quiet clothes is wanted to set The rational position and electrode energy of the electrode of middle design, thus at all cannot day production capacity 100-500 tons of big production capacity, efficiently In rate, inexpensive glass fiber production system device, the salic super high-strength glass fibre system up to 20-49% is produced Product.

In the production of the big production system device of glass fibre tank furnace of the prior art, everybody is intended to using daily output The device of the glass fiber manufacturing line of 100-600 tons of large-tonnage (producing ten thousand tons of 7-20 per year), to produce salic 20-25- 35% high-aluminum alkali-free S level fiberglass greatly improves S grades of glass of high-aluminum alkali-free on the basis of reaching product quality qualification Fibre production efficiency, to adapt to the requirement of high-caliber wind-powered electricity generation leaf, new-energy automobile, aerospace market.This is high-aluminum alkali-free In S level fiberglass field, people thirst for solving always but fail the technical barrier to succeed always.But the present invention solves This technical barrier.

The invention of the change of this technology Zhuan Zhi Jie Ju elements,.It solves this people to thirst for always solving but always failing The technical barrier to succeed, so the invention of the change of this technology Zhuan Zhi Jie Ju elements, have substantive distinguishing features outstanding and Significant progress, it is creative.

The present invention is on technique device Jie Ju factor contents and position, on the interactively of technique device Jie Ju elements, Comparing the prior art has change；Moreover, because on technique device Jie Ju factor contents and position, wanted in technique device Jie Ju On the interactively of element, compares the change of prior art generation, lead to unexpected technique effect.So right of the present invention It is required that 1 has substantive distinguishing features outstanding and significant progress, it is creative.

Compare the prior art 3：

The electric melting furnace schematism device of the prior art --【There is no flame thermal energy to dominate glass melting】

For in the schematism device for the prior art for being related to glassware class production line, all using only tens tons Electric melting furnace Jie Ju devices；Device (the 17)-i.e. main channel for the loading glass metal being directly coupled, and it is coupled 2-30 glass Glass liquid runner, each of which runner are coupled the molding machine of glassware.

Compare hundreds of tons of production capacities of lateral flame furnace production line, electric melting furnace schematism device：

One of defect is：It is low to invest output ratio, low production efficiency.

Defect second is that：The energy consumption of identical yield is than high.

The three of defect are：The human resources of identical yield consume high；The four of defect are：Because the high alumina of high melting-point without The base material ingredient of high conductivity is free of in alkali glass material, so dominating the lateral flame of glass melting without flame thermal energy The glassware process units system (i.e. pure electric melting furnace)-of the process unit (1) of tank furnace Jie Ju devices (10) cannot be filled and be dissolved High-aluminum alkali-free glass material.

The four of defect are：By having the lateral flame furnace knot Ju devices that flame thermal energy dominates glass melting, Bu Nengda in No To 100-1000 tons of production capacities of the daily output.

The king of defect is：So electric melting furnace schematism device, with the daily output up to hundreds of tons of big production capacities to upper kiloton Glassware tank furnace production line compares, and 1. its investment output ratio are low；2. low production efficiency；3. the energy consumption ratio of identical yield It is high；4. the human resources of identical yield consume high；In the presence of the defect for the high-aluminum alkali-free glass material that cannot produce high melting-point.

The device of the invention Jie Ju systems, can overcome defect existing for electric melting furnace schematism device.

Compare the prior art 4：

A kind of horseshoe kiln device for having electric boosting again that flame thermal energy is leading

Due to the horseshoe kiln device Jie Ju for having electric boosting again that a kind of flame thermal energy is dominated, than the letter of lateral flame furnace It is single, thus it is at low cost, take up an area few；Since its flame is that U-shaped horse-hof shape is presented, flame is short, and the small day production tonnage in kiln pond is not more than 50 tons, limit to using by tonnage, it is impossible to be used in the daily output up to 100 tons of big production capacity glassware production lines to upper kiloton, Mainly for the manufacture of to glass quality glassware product of less demanding.

One of its existing defects are：It is coupled the horseshoe kiln device that a kind of flame thermal energy is leading and has electric boosting, it is molten Glass metal after change, is all horizontally oriented mobile, and defect is：Horizontal direction movement glass metal have the phenomenon that reflux without Method controls；And the distance of glass metal horizontal direction movement is longer, so its glass metal upper layer just has heat dissipation problem, it will It is uneven to form the temperature of glass liquid moved horizontally；Exactly apart from the longer glass metal top moved horizontally using flame or The additional thermal process of electric heating, due to the additional thermal process of flame or electric heating, the electric current heating with the electrode in glass metal is two kinds Device, temperature that cannot be between the glass metal upper layer temperature and middle lower layer of effective controlled level movement form the consistent of control Property and stability.It is uneven that the temperature of glass liquid moved horizontally will be formed.So a kind of flame thermal energy it is leading have electric boosting again Horseshoe kiln device, cannot effectively reach make glass liquid energy be accurately controlled clarification, row bubble needed for predetermined temperature 1-5 DEG C error within, it is horizontal to be unable to the exhaust bubble of effective guarantee glass metal, clarification process；It is especially this in the high lead glass of production When recrystallization temperature height and the product of crystallization speed, effective guarantee glass metal is unable to before entering into operation stage, glass Liquid temperature is consistently higher than recrystallization temperature.

Its existing defects second is that：Horseshoe kiln device dissolve after glass metal, be all horizontally oriented mobile；Its Existing defects are：The dead angle of unfavorable melt flow is had on the both sides at the hole of top area and lower part, it is especially high in production When this recrystallization temperature height of lead glass and the product of crystallization speed, it can be very easy to produce at the not runny dead angle of glass metal Raw glass metal crystallization.

The three of its existing defects are：Compare the prior art -- in the 1980s, German Industrial circle-" tentative " one kind Depth of metal reaches the horseshoe kiln device of the clarification zone device of 3M, and glass metal flows into settling section from melting end horizontal direction Device forms the settling section of a 1.3-3M depth at depth of metal about 1.3M.

[1]Although a kind of depth of metal is reached up to the horseshoe kiln device of the clarification zone device of 3M in depth of metal In the settling section of 1.4--3M, there are also installed electrodes, it is also desirable to solve glass metal and be horizontally oriented mobile and cause glass metal The problem of having the phenomenon that reflux, being unfavorable for controlling temperature of glass liquid.But it is in the top depth of 1.3-1.5M, and glass metal is still It deposits and moves in the horizontal direction defect, this glass metal that there is horizontal direction movement can cause glass metal to have the phenomenon that reflux Problem is unfavorable for controlling temperature of glass liquid.The depth of 1.5-3M is only arrived, glass metal just starts to flow from the top to the bottom.

[2]Although a kind of depth of metal is devised up to the horseshoe kiln device of the clarification zone device of 3M in metal depth Degree reaches in the settling section of 1.4--3M, makes glass metal in movement from the top down, ites is desirable to control temperature of glass liquid by telegram； But its existing defects is：Production alumina content reach 15-25-39% high alumina or superelevation lead glass liquid, a part occur Separation settles downwards [Oxygen enrichment aluminium Fen Cengxianxiang ]When：--[Alumina composition in dissolving is significantly high because proportion is up to 3.8 In the proportion of glass 2.5, generates aluminium oxide and gather and be layered Xian Xiang ]；

There is separation sedimentation Xian Xiang &#91 downwards in a part for this high alumina glass metal;Oxygen enrichment aluminium Fen Cengxianxiang ]In 0.8- In the glass metal of 1.2M depths, it can also be allowed to overcome with agitating device.But reach the clarification zone device of 2-3M in depth of metal When middle：One is installation agitating device is very difficult；The second is since alumina ratio weighs 3.8, it is easier to down than glass 2.5 Depth is sunk to up to the bottom of the clarification zone device of 3M, at this moment to be flowed up by glass metal part appearance separation is downward The high alumina Bo Liye &#91 of sedimentation;Oxygen enrichment aluminium Fen Cengxianxiang ], then flow to the glass shaping area of the height of 2-3M or more upward and be It is impossible.It is just bound in production, depth of metal makes this downward sedimentation up to the bottom of the clarification zone device of 2-3M High alumina Bo Liye [Oxygen enrichment aluminium Fen Cengxianxiang ]It is a large amount of to heap, and the glass ingredient in intensive alumina content region, not It is the glass ingredient of design, will produce crystallization more higher than predetermined recrystallization temperature, generates this and detach the height settled downwards Lead glass Ye [Oxygen enrichment aluminium Fen Cengxianxiang ]Region, generate large-scale crystallization.

This is also this in the 1980s, German Industrial circle-" tentative ", the settling section of depth of metal up to 3M fill It sets, due to there is no industrial applicibility, the main reason for recent decades are not used by horseshoe kiln device glass enterprise.

Card neck flow passage device (60) of the present invention due in technique device element, increasing glass metal, and use electrode Temperature controlled clarification, exhaust bubble and anti-crystallization device (30) are carried out to the glass metal flowed from the top to the bottom；Change again this 2 The bottom of pond depth location of the control depth of metal of a technique device element produces the different interactivelies to glass metal, Produce the technique effect given unexpectedly：

【A】The present invention to the position of the depth of the glass metal of the card neck flow passage device (60) of glass metal carried out with it is existing The entirely different element of technology changes.It changes into：The depth of metal of the card neck flow passage device (60) of glass metal is flame heat Can dominate the flame furnace knot Ju devices (2) of glass melting and using electrode to the glass metal that flows from the top to the bottom into trip temperature Clarification, the exhaust of control are steeped and the 10%-40% of the depth of metal of the depth of metal of anti-crystallization device (30).(see explanation Book attached drawing 3)

【B】The present invention in prior art horseshoe kiln device, " tentative ", a kind of depth of metal reaches the clarification of 3M Zone device --- it uses electrode to carry out temperature controlled clarification, exhaust bubble and anti-crystallization to the glass metal flowed from the top to the bottom and fills The position for setting the depth of the glass metal of (30) change with the entirely different element of the prior art.It is changed by depth 3M Depth described in the claims in the present invention is within 90-150CM；(see Figure of description 3)

Due to the change of the depth of metal position of this 2 technique device elements, the card neck stream by glass metal is formd The outlet port of road device (60) rises significantly, forms clarification zone device -- and use electrode to the glass that flows from the top to the bottom Glass liquid carries out temperature controlled clarification, the big rising in the entry position into glass metal of exhaust bubble and anti-crystallization device (30), makes glass Glass liquid flows into (see Figure of description 3) from upper lateral part, and changing Xian has the state of glass metal bottom horizontal flow sheet in Ji Shu Jie Ju.(see Figure of description 3)

The present invention due to the relationship of above-mentioned multiple technique device elements, position, effect variation, compare the prior art Horseshoe kiln device, including " tentative "-depth of metal up to 3M clarification zone device horseshoe kiln device, generation Give having the technical effect that unexpectedly：

A. the present invention produces the schematism dress of the glass transverse direction flame furnace production line of 100-1000 tons of large-tonnage daily Set, can overcome prior-art devices, including " tentative "-horseshoe kiln depth of metal up to the clarification zone device of 3M production capacity It is confined to 50 tons of defect；

B. the present invention produces the schematism dress of the glass transverse direction flame furnace production line of 100-1000 tons of large-tonnage daily Set, can overcome the prior art-" tentative "-horseshoe kiln depth of metal up to 3M clarification zone device meeting in production, glass Glass liquid depth makes this high alumina glass metal settled downwards up to the bottom of the clarification zone device of 3M;Oxygen enrichment aluminium Fen Cengxianxiang ] It is a large amount of to heap, and the glass ingredient in intensive alumina content area, it has not been the glass ingredient of design, has will produce than predetermined The higher recrystallization temperature of recrystallization temperature generates this and detaches the high alumina Bo Liye &#91 settled downwards;Oxygen enrichment aluminium Fen Cengxianxiang ]Area Domain generates large-scale devitrification defects.

Compare the prior art 5：

The patent of invention that the present inventor applied in 2014, a kind of anti-crystallization in cooling end region for glass technology Device, it is characterised in that：In the space on the metal level of cooling end, the inside 10-80mm's by pool wall refractory brick In distance range, there are 2 to 80 electric heater units and 2 to 80 measuring temperature devices.It is also proposed that in cooling end region Electrode system is disposed to control temperature of glass liquid in glass metal.

One of its existing defects are：

[1]In a kind of anti-crystallization device device in the cooling end region for glass technology, glass metal is all horizontal shifting Dynamic；Although there are also installed electrodes, it is desirable to solve the temperature control of glass metal, the glass metal of horizontal direction movement has reflux The phenomenon that, it also can not effectively control the temperature of glass metal；

[2]And the additional thermal process of the electric heating on the refractory brick on the side above glass metal and the electrode in glass metal Electric current heating is two kinds of devices, in addition the upper top Ceng Mian No of its glass metal central region just control the device (cooling end of temperature It is general have it is 8-15 meters wide, it is 10-20 meters long), so roof deck heat dissipation problem is serious.

So a kind of anti-crystallization device in cooling end region for glass technology, it can not effective controlled level shifting Temperature between dynamic glass metal upper layer temperature and middle lower layer forms the consistency and stability of control.So will be formed The temperature of glass liquid moved horizontally is uneven.

So a kind of anti-crystallization device in cooling end region for glass technology, cannot effectively reach makes glass liquid energy It is accurately controlled within 1-5 DEG C of the error of predetermined temperature needed for clarification, row's bubble, is unable to the exhaust of effective guarantee glass metal Bubble, clarification process are horizontal；It, cannot especially when producing high this recrystallization temperature of high lead glass and the product of crystallization speed Effective guarantee glass metal is consistently higher than recrystallization temperature before entering into operation stage.(the technology of the present invention element device, formation The glass metal of perpendicular flow and the electrode at four sides can overcome this defect)

Its existing defects second is that：

The anti-crystallization device device or all existing cooling ends or entitled in a kind of cooling end region for glass technology In the device of work department, the glass metal moved horizontally is designed to the top area for the tail portion for making glass metal from cooling end Glass metal flashboard hole enters shaping area.Cooling end generally has 8-15 meters wide, and glass metal flashboard hole is only less than 2M Width, so the both sides and lower part in the cooling end domain at the glass metal flashboard hole moved horizontally, have unfavorable melt flow Dead angle can be very easy to especially when producing high this recrystallization temperature of high lead glass and the product of crystallization speed in glass metal Not runny dead angle generates glass metal crystallization.(the technology of the present invention element device, the glass metal of the perpendicular flow of formation and four The electrode in face can overcome this defect)

A. the present invention is in technique device Jie Ju elements【Card neck device】In content and position, compare a kind of use of the prior art It is in the change of the anti-crystallization device in the cooling end region of glass technology, in the card neck flow passage device (60) of glass metal, glass Depth between the surface and bottom of device of liquid, change into be flame thermal energy dominate glass melting lateral flame furnace Jie Ju It device (10) and temperature controlled clarification, exhaust bubble and anti-crystallization is carried out to the glass metal that flows from the top to the bottom using electrode fills It sets in (30), the 10%-40% of the depth between the surface and bottom of device of glass metal；(see specification Fig. 3)

B. of the invention：A kind of lateral flame furnace production system and production method of glassware；The prior art Technique device Jie Ju elements【A kind of anti-crystallization device in the cooling end region for glass technology】, it is changed to【Using electrode pair The glass metal flowed from the top to the bottom carries out temperature controlled clarification, exhaust bubble and anti-crystallization device】(3) and【It is right using electrode The glass metal flowed from bottom to top carries out temperature controlled glass metal rise channel s structure】(4).(see specification Fig. 3)

C. due to the change of change and interactively in technique device knot Ju elements：

It is described in description of the invention, these element relationships of generation change, and lead to unexpected technique effect：

The present invention due to the depth of the glass metal of the card neck flow passage device (60) of glass metal position, with flame thermal energy master Lead the lateral flame furnace knot Ju devices (10) of glass melting and using electrode to the glass metal that flows from the top to the bottom into trip temperature Clarification, the exhaust of control are steeped and the position of the depth of metal of anti-crystallization device (30) is changed, by existing tank furnace technology Depth of metal is consistent in above three technique device element in device, changes into the card neck flow passage device of glass metal (60) depth of glass metal is only only that flame thermal energy is dominated the lateral flame furnace Jie Ju devices (10) of glass melting and adopted Temperature controlled clarification is carried out to the glass metal flowed from the top to the bottom with electrode, exhaust is steeped and the glass of anti-crystallization device (30) The 10%-40% of liquid depth.(see specification Fig. 3)

The change that the position of card neck flow passage device (60) depth of metal of this glass metal occurs, can just make glass metal Card neck flow passage device (60) glass metal, the glass metal bottom horizontal flow sheet from prior art tank furnace Jie Ju becomes the card for making glass metal Neck flow passage device (60) glass metal carries out temperature controlled clarification, exhaust from using electrode to the glass metal flowed from the top to the bottom The upper lateral part of bubble and anti-crystallization device (30) flows into [See Figure of description 3], the variation of melt flow position could be formed, It forms glass metal and temperature controlled clarification, exhaust bubble and anti-crystallization is being carried out to the glass metal flowed from the top to the bottom using electrode The variation flowed from the top to the bottom in device (30).(see specification Fig. 3)

Using electrode, temperature controlled device (3) is carried out to the glass metal flowed from the top to the bottom and uses electrode, to from Under the glass metal that flows up carry out temperature controlled glass metal rise channel s structure (40), top, surrounding, bottom, all set The heating device of the control temperature of glass liquid of meter, so the glass metal in movement from top to down and the glass that flows from bottom to top Glass liquid can be controlled at 1300 DEG C or more；Again because with glass fluid being to conduct thermal energy with thermal radiation at 1300 DEG C, so can be smart True control is in [Using electrode, temperature controlled Zhuan Zhi &#93 is carried out to the glass metal flowed from the top to the bottom;(3) and [Using electricity Pole carries out temperature controlled glass metal Shang Shengtongdaojiegou &#93 to the glass metal flowed from bottom to top;(4) high alumina within and super The glass metal of high alumina float flat glass and electronic glass is completely in higher than 10 needed for glass clarifying, row's bubble²Pa Sec 1300-1480 DEG C of temperature on 20 DEG C of stable state , [Zhi Nei &#93 of the error at 1-5 DEG C;.In this high-caliber glass In liquid exhaust bubble, clarification Advanced Manufacturing Technology, glass metal can be completed within 3-6 hour and reaches the clarification of high-quality, row's bubble Horizontal target.So the present invention：A kind of lateral flame furnace production system and production method of glassware；These are wanted Plain relationship changes, and can make the production of high alumina and superelevation aluminium float flat glass and electronic glass on the basis of general cost In, overcome the deficiencies of existing technologies, reach the glass metal for making high alumina and superelevation aluminium float flat glass and electronic glass, into Before entering moulding process, the technical purpose being maintained on higher than recrystallization temperature that can stablize.

Compare the prior art 6：

In the lateral flame furnace production line for being related to prior art high alumina and superelevation aluminium float flat glass and electronic glass Schematism device in, flame thermal energy dominate glass melting lateral flame furnace knot Ju devices (10) after join Knot is a kind of cooling end or the device of the entitled Ministry of worker, and the lateral flame furnace Jie Ju dresses of glass melting are dominated in flame thermal energy After setting, what is be coupled by card neck device is a kind of cooling end or the device of entitled work department；Its card neck device, laterally fire In the device of flame tank furnace Jie Ju devices, cooling end or entitled work department, the depth of glass metal is all 1 meter or so, and glass metal is overall It is all horizontally oriented towards molding machine and moves.

The device existing defects 1 of this cooling end or entitled work department：Due to this cooling end or the dress of entitled work department In setting, the depth of glass metal is all 1 meter or so, and glass metal is totally all horizontally oriented towards molding machine and moves, above glass metal Portion, left and right part, lower bottom portion No have complete, accurate, unified heating and control the system and device of temperature, so especially With shaping area in close cooling end or entitled work department back segment, the upper and lower layer temperature difference of glass metal reaches 70-90 DEG C.

This can cause exhaust bubble, clarification process in the production of high alumina and superelevation aluminium float flat glass and electronic glass Process, it is impossible to accurately according to glass ingredient it is distinctive clarification, row bubble 10²The viscosity temperature of (Pa Sec), come the row of completion The process of bubble, clarification process, bubble and glass muscle quality during product can be caused to produce lack defect；This is the cooling of the prior art Portion or entitled work part device produce difficult point (but the Corning Incorporated of high alumina and superelevation aluminium float flat glass and electronic glass Platinum channel technique device patent and the vacuum extractor patent of Asahi Glass company can overcome this defect, but cost is too high).

The device existing defects 2 of this cooling end or entitled work department：Due to this cooling end or the dress of entitled work department In setting, the depth of glass metal is all 1 meter or so, and glass metal is totally all horizontally oriented towards molding machine and moves, above glass metal Portion, left and right part, lower bottom portion No have complete, accurate, unified heating and control the system and device of temperature, so especially With shaping area in close cooling end or entitled work department back segment, the upper and lower layer temperature difference of glass metal reaches 70-90 DEG C.

High alumina and superelevation aluminium float flat glass and electronic glass reach 20-25-35%, recrystallization temperature due to salic All very high, many all reaches 1300--1480 DEG C or more.So in production, the device of this cooling end or entitled work department, The glass metal that can't resolve high alumina and superelevation aluminium float flat glass and electronic glass can be stablized before entering moulding process The technical barrier being maintained on higher than recrystallization temperature.

A. the present invention is in technique device Jie Ju elements【Card neck device】In content and position, compare the change of the prior art, It is in the card neck flow passage device (60) glass metal, the depth between the surface and bottom of device of glass metal is flame thermal energy master Lead the lateral flame furnace knot Ju devices (10) of glass melting and using electrode to the glass metal that flows from the top to the bottom into trip temperature The clarification of control is vented in bubble and anti-crystallization device (30), the 10%- of the depth between the surface and bottom of device of glass metal 40%.(see Figure of description 3)

B. of the invention：A kind of lateral flame furnace production system and production method of glassware；The prior art Technique device Jie Ju elements【A kind of device of cooling end or entitled work department】, it is changed to【Using electrode to flowing from the top to the bottom Glass metal carry out it is temperature controlled clarification, exhaust bubble and anti-crystallization device】(3) and【Using electrode, to flowing from bottom to top Glass metal carry out temperature controlled glass metal rise channel s structure】 (4).(see Figure of description 3)

C. due to the change of change and interactively in technique device knot Ju elements, the present invention：A kind of glassware Lateral flame furnace production system and production method；It is described in specification, these element relationships of generation change, and lead Cause unexpected technique effect：

The change that the position of card neck flow passage device (60) depth of metal of this glass metal occurs, can just make glass metal Card neck flow passage device (60) glass metal, the glass metal bottom horizontal flow sheet from prior art tank furnace Jie Ju becomes the card for making glass metal Neck flow passage device (60) glass metal carries out temperature controlled clarification, exhaust from using electrode to the glass metal flowed from the top to the bottom The upper lateral part of bubble and anti-crystallization device (30) flows into [See Figure of description 3], the variation of melt flow position could be formed, It forms glass metal and temperature controlled clarification, exhaust bubble and anti-crystallization is being carried out to the glass metal flowed from the top to the bottom using electrode The variation flowed from the top to the bottom in device (30).

Compare prior art 1-6：

First there are the molten kiln technology of electricity and flame firer's skill technical glass product, the main alumina content that produces is 1-4% Low aluminum products, alumina content be 5-9% middle aluminum products, alumina content be 10-16% high alumina products.

First there are the molten kiln technology of electricity and flame kiln technology, several technologies without present invention process method to want Su Jie Ju features, so, first there is the molten kiln technology of electricity, without the process conditions for overcoming its technological difficulties.It is played without the present invention It asks, the specific region position of the glass metal in the region of bottom refractory material 5-30CM in multiple regions is designed with The requirement of 3-20 electrode assembly, and without the present invention play ask in multiple regions, away from refractory material bottom 5-30CM In the glass metal in the region of distance, the work technological temperature in the section of a minimum of 100 cubes of CM volumes, to be maintained at 1320 DEG C- 1450 DEG C, it is higher than 20-80 DEG C of the technological temperature of work of the region glass metal apart from bottom refractory material 30-60CM distances Process.

【The difference of the present invention and prior art (1)-(6)】

(1) first, the preparation method of process characteristic of the present invention, with first have invention (1)-(6) technical solution and Any prior art proposal is also all different.Preparation method characteristic of the present invention could generate and first have similar products complete Different,【Wan full No have the feature that milky rich aluminum strip line or richness aluminium block , No have glass layering, aluminium oxide in glass Content reaches the glassware of 15--35%】.

And if not using preparation method characteristic of the present invention, alumina content reaches the glassware of 15--35% In, the opaque significant deficiency there are milky rich aluminum strip line or milky rich aluminium block is will be easy to, or glass occur The significant deficiency problem of glass layering.

(2) and the present invention because use completely new technique：In the molten Yao Jie Ju devices of multiple regions, bottom refractory material In glass metal in the region of 5-30CM distances, 3-20 electrode assembly is all devised, uses completely new technique：Make more In the glass metal in the region of the bottom refractory material 10-30CM distances in a molten kiln knot Ju devices region in region, minimum each own 1 The work technological temperature in a section is maintained at 1320 DEG C -1450 DEG C, higher than apart from the area of bottom refractory material 30-60CM distances 20-80 DEG C of the work technological temperature of domain glass metal.So these regions can be formed, apart from bottom refractory material 5-30- The glass metal of 60CM distances is small-scale to flow up and down homogenizing, makes " rich aluminium deposition phenomenon -- i.e. high-alumina component content Glass metal part, the phenomenon that deposition is in bottom due to than great ", be homogenized, be resolved.It can fundamentally solve Glass finished-product formative stage is certainly in turn resulted in because composition is seriously uneven, glass muscle, striped, oxygen-enriched piece of White-opalescent and item occurs Products underproof difficult point at all is waited, so that the glassware of the alumina content of the production 15--35% of high qualification rate is become can Energy.

So can accomplish, the glassware of the alumina content of 15--35% is produced, not only will be during normal production, energy Make in respective device, the glass metal of especially bottom section is maintained at 1300 DEG C or more；And it can be in the molding machine of glassware (5) when being stopped, i.e., Ye No have from the glass metal dissolved when Yao Jie Ju devices flow over the high-temperature glass liquid come, also can shape At these regions, the minimum each work for having 1 section by oneself of glass metal apart from bottom refractory material 5-30-60CM distances Technological temperature is maintained at 1320 DEG C -1450 DEG C, and minimum each work technological temperature for having 1 section by oneself is maintained at 1320 DEG C -1450 DEG C, higher than 20-80 DEG C of the work technological temperature of the region glass metal apart from bottom refractory material 30-60CM distances；And small range Flow up and down homogenizing, make " rich aluminium deposition phenomenon -- the i.e. glass metal part of high-alumina component content, because than great And deposition is the bottom the phenomenon that ", it is homogenized, is resolved.

Completely new art inventions conception plans are one kind in specific environment, to the technology side in specific region The invention of the glass product of case production, produces the technique effect given unexpectedly.

The goal of the invention of the present invention also resides in：

When producing high alumina and superelevation aluminium (salic 20-49%) float flat glass and electronic glass, there is glass When the state that the molding machine (50) of product is stopped (it is faulty in such as moulding process, safety gate close, make entirely at Production system glass metal before type is within respective device, does not press the state of process flowing).

Conversely, when producing high alumina and superelevation aluminium (salic 20-49%) float flat glass and electronic glass, go out (faulty in such as moulding process, safety gate is closed, and is made when the state that the molding machine (50) of existing glassware is stopped Production system glass metal before entire molding is within respective device, does not press the state of process flowing).If No has the relationship change innovation that the No of Ben Faming has the position relationship variation innovation of 3 above-mentioned element devices and interacts, It just not necessarily will appear glass metal before entering moulding process, a wide range of crystallization.

And high alumina and superelevation aluminium (salic 20-49%) float flat glass and electronic glass tank furnace of the prior art Production system device, due to wanting white, quiet clothes to set the rational position and electrode energy that have the electrode wherein designed with No without this 3, So at all 100-1000 tons of big production capacity, high efficiency, the float flat glass of low cost and electronics glass cannot be reached in day production capacity In glass fiber production system device, it is floating to produce salic high alumina and superelevation aluminium (salic 20-49%) up to 20-49% Method plate glass and electronic glass product.

In the prior art, everybody be desirable in day production capacity 100-1000 tons of big production capacity, high efficiency, low cost In float flat glass production system device, produce salic high alumina and superelevation aluminium float flat glass up to 20-49% with Electronic glass product.On the basis of reaching product quality qualification, high alumina glass fibre production efficiency is greatly improved, to adapt to The requirement of high-caliber building glass, engineering glass, special glass, aerospace glass market.This is people in glass art Always thirst for solve but fail the technical barrier to succeed always.

The above, merely to illustrate the preferable preferred embodiment of the present invention, however it is to the present invention that it, which is not, Limitation, anyone familiar with this technology is changed or is modified to possibly also with the technology contents of the disclosure above equivalent The equivalent embodiment of variation can be implemented by different requirements and performance -- a kind of lateral flame pond of glassware of the present invention Kiln production system and production method.As it can be seen that every content without departing from technical solution of the present invention, especially entitlement requests item Content, according to the technical essence of the invention to any simple modification made by above example, equivalent variations and modification, In the range of still belonging to technical solution of the present invention.

Claims

1. a kind of lateral flame furnace production system of glassware comprising：

Glass raw material transport device (19), flame thermal energy dominate the lateral flame furnace Jie Ju devices (10) of glass melting；Glass The card neck flow passage device (60) of liquid；Temperature controlled clarification is carried out to the glass metal flowed from the top to the bottom using electrode, exhaust is steeped With anti-crystallization device (30)；Using electrode, temperature controlled glass metal rising passway is carried out to the glass metal flowed from bottom to top Structure (40)；The molding machine (50) of glassware：It is characterized in that：

In the card neck flow passage device (60) of glass metal, the depth between the surface and bottom of device of glass metal is flame thermal energy master Lead the lateral flame furnace knot Ju devices (10) of glass melting and using electrode to the glass metal that flows from the top to the bottom into trip temperature The clarification of control is vented in bubble and anti-crystallization device (30), the 10%- of the depth between the surface and bottom of device of glass metal 40%；

Temperature controlled clarification, exhaust bubble and anti-crystallization device (30) are carried out to the glass metal flowed from the top to the bottom using electrode Surrounding is designed with the electrode of 4-50 control temperature of glass liquid；

Temperature controlled clarification, exhaust bubble and anti-crystallization device (30) are carried out to the glass metal flowed from the top to the bottom using electrode Lower part be designed with glass metal outflow hole (6), design glass metal outflow hole (6) be coupled one using electrode to from Under the glass metal that flows up carry out temperature controlled glass metal rise channel s structure (40), in rise channel s structure, be designed with Control the electrode of temperature of glass liquid；

The top of temperature controlled glass metal rise channel s structure (40) is carried out to the glass metal flowed from bottom to top using electrode Outlet is coupled the device (17) of a loading glass metal, is designed with the electrode of control temperature of glass liquid.

2. a kind of lateral flame furnace production system of glassware according to claim 1, it is characterised in that：

In the card neck flow passage device (60) of its glass metal, the depth between the surface and bottom of device of glass metal is flame thermal energy It dominates the lateral flame furnace Jie Ju devices (10) of glass melting and temperature is carried out to the glass metal flowed from the top to the bottom using electrode It spends in clarification, exhaust bubble and the anti-crystallization device (30) of control, the 10%- of the depth between the surface and bottom of device of glass metal 40%；The card neck flow passage device (60) of glass metal in the glass metal in the region of bottom refractory material 5-30CM, be designed with 3-20 electrode assembly；

It uses electrode to carry out temperature controlled clarification, exhaust bubble and anti-crystallization device (30) to the glass metal flowed from the top to the bottom Surrounding be designed with the electrode of 4-50 control temperature of glass liquid, using electrode to the glass metal that flows from the top to the bottom into trip temperature The clarification of control, exhaust bubble and anti-crystallization device (30) in the glass metal in the region of bottom refractory material 5-30CM, if In respect of 3-20 electrode assembly；

It is additionally provided with bottom flow liquid channel (20), in the glass metal in the region of bottom refractory material 5-30CM, is designed with 3-20 electrode assembly；

It uses electrode to carry out temperature controlled glass metal rise channel s structure to the glass metal flowed from bottom to top -- (40) Surrounding is designed with the electrode of 4-50 control temperature of glass liquid；Rise channel s structure (40) apart from bottom refractory material 5-30CM's In glass metal in region, it is designed with 3-20 electrode assembly；

3. a kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that using electricity Temperature controlled clarification extremely is carried out to the glass metal flowed from the top to the bottom, exhaust is steeped and the glass metal of anti-crystallization device, depth exist Within 90-150CM；Temperature controlled clarification, exhaust bubble and anti-crystallization are carried out to the glass metal flowed from the top to the bottom using electrode The top design of device (30) has heating device.

4. a kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that using electricity The top exit that temperature controlled glass metal rise channel s structure (40) is extremely carried out to the glass metal flowed from bottom to top, is coupled Loading glass metal device (17) top, be designed with heating device；The bottom of the device (17) for the loading glass metal being coupled Portion, the electrode design for being also configured with control temperature of glass liquid have heating device.

5. a kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that its flame The daily output that thermal energy dominates the lateral flame furnace Jie Ju devices (10) of glass melting reaches 100 tons -1500 tons；Its flame-thrower nozzle It is mounted in two survey faces of lateral flame furnace, the direction of flame injection direction and lateral flame furnace length is to be in the side Guang To；In the glass metal of its lateral flame furnace Jie Ju device, it is designed with the electrode of electric boosting control temperature of glass liquid.

6. a kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that it is used Electrode carries out the glass metal flowed from bottom to top the top exit of temperature controlled glass metal rise channel s structure (40), is coupled The top of the device (17) for the loading glass metal, is designed with heating device；The device (17) for the loading glass metal being coupled Bottom is also configured with the electrode of control temperature of glass liquid；The region for leading to molding machine is designed with glass metal gate；

7. a kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that it is used Electrode carries out the glass metal flowed from bottom to top the top exit of temperature controlled glass metal rise channel s structure (40), is coupled The top of the device (17) for the loading glass metal, is designed with heating device；The device (17) for the loading glass metal being coupled Bottom is also configured with the electrode of control temperature of glass liquid, is coupled the sprue of glass metal, being coupled has 2-30 glass metal Runner, each glass metal runner, the molding machine (50) for the glassware being coupled are the moldings of glass fibre production Device；Its glass fibre production molding machine include：2-30 dry crucibles, 2-30 bushing, wire drawing machinees of bearing glass liquid.

8. a kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that it is used Electrode carries out the glass metal flowed from bottom to top the top exit of temperature controlled glass metal rise channel s structure (40), is coupled The top of the device (17) for the loading glass metal, is designed with heating device；The device (17) for the loading glass metal being coupled Bottom is also configured with the electrode of control temperature of glass liquid, is coupled the sprue of glass metal, being coupled has 2-30 glass metal Runner, each glass metal runner are coupled the molding machine (50) of glassware；The molding machine (50) of glassware It is the blow molding device of industry and utility glass ware；In 2-30 blow molding device of industry and daily glass product (50) after, the also annealing device of glassware.

9. a kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that it is used Electrode carries out the glass metal flowed from bottom to top the top exit of temperature controlled glass metal rise channel s structure (40), is coupled The top of the device (17) for the loading glass metal, is designed with heating device；The device (17) for the loading glass metal being coupled Bottom is also configured with the electrode of control temperature of glass liquid, is coupled the sprue of glass metal, being coupled has 2-30 glass metal Runner, each glass metal runner are coupled the molding machine (50) of glassware；The molding machine (50) of glassware It is the compression molding device of industry and utility glass ware；In 2-30 compression molding device of industry and utility glass ware (50) after, the also annealing device of glassware.

10. a kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that it is adopted The top exit of temperature controlled glass metal rise channel s structure (40) is carried out to the glass metal flowed from bottom to top with electrode, is joined The top of the device (17) for the loading glass metal being knotted, is designed with heating device；The device (17) for the loading glass metal being coupled Bottom, be also configured with control temperature of glass liquid electrode, be coupled the sprue of glass metal, being coupled has 2-30 glass Liquid runner, each glass metal runner are coupled the molding machine (50) of glassware；The molding machine of glassware (50) it is the industrial drawing molding device with utility glass ware；In the molding of industry and 2-30 drawing of utility glass ware After device (50), the also annealing device of glassware.

11. a kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that it is adopted With electrode, the top exit of temperature controlled glass metal rise channel s structure (50) is carried out to the glass metal flowed from bottom to top, The top of the device (17) for the loading glass metal being coupled, is designed with heating device；The device for the loading glass metal being coupled (17) bottom is also configured with the electrode of control temperature of glass liquid, is coupled 2-30 glass metal runner, runner is coupled glass The molding machine (50) of product；The molding machine (50) of glassware is the blow molding device of bathroom glassware；In bathroom After 2-30 blow molding device of glassware, the also annealing device of bathroom glassware.

12. a kind of lateral flame furnace production system of glassware according to claim 1, which is characterized in that it makes The composition of glass material is：By weight percentage, alumina content 0.01%--39%, content of magnesia are 5%--20%, silica content are 2.51-5.8 times of calcium oxide content, calcium oxide content is 0.7 times of content of magnesia- 2.3 again.

13. a kind of preparation process of the lateral flame furnace production system of glassware：

Get required device ready：Flame thermal energy dominates the lateral flame furnace Jie Ju devices (10) of glass melting, the card of glass metal Neck flow passage device (60) carries out temperature controlled clarification, exhaust bubble and anti-analysis using electrode to the glass metal flowed from the top to the bottom Brilliant device (30) carries out temperature controlled glass metal rise channel s structure using electrode to the glass metal flowed from bottom to top (40), the molding machine (50) of glassware；Electrode energy in these devices, can be in the molding machine of glassware (50) when being stopped, so that the glass metal in respective device is maintained at 1300 DEG C or more , And and be maintained at higher than devitrification of glass temperature On；

Scheduled glass raw material is dominated the cross of glass melting into flame thermal energy by step 1. by glass raw material transport device It into flame furnace Jie Ju devices (10), carries out dissolving to form glass metal, glass metal passes through the card neck flow passage device of glass metal again (60), enter from upper lateral part using electrode, temperature controlled clarification is carried out to the glass metal flowed from the top to the bottom, exhaust is steeped and anti- In crystallization device (30)；And make card neck flow passage device (60) and using electrode to the glass metal that flows from the top to the bottom into trip temperature control The clarification of system, the temperature of exhaust bubble and the glass metal in anti-crystallization device (30), control is higher than clarification, row's bubble 10²Pa Sec Viscosity temperature on section and higher than the section on devitrification of glass temperature；

Process characteristic is：By the card neck flow passage device (60) of glass metal in the region of bottom refractory material 5-30CM In glass metal, 3-20 electrode assembly of design makes card neck flow passage device (60) region, away from refractory material bottom 10-30CM In the glass metal in the region of distance, the work technological temperature in the section of a minimum of 100 cubes of CM volumes, to be maintained at 1320 DEG C- 1450 DEG C, it is higher than 20-80 DEG C of the work technological temperature of the region glass metal apart from bottom refractory material 30-60CM distances；

Process characteristic is：Temperature controlled clarification, exhaust bubble and anti-crystallization dress are carried out by the glass metal flowed from the top to the bottom Set (30) design in the glass metal in the region of bottom refractory material 5-30CM, respective 3-20 electrode assembly, make from On the glass metal that flows downward carry out temperature controlled clarification, exhaust bubble and anti-crystallization device (30) region, away from refractory material In the glass metal in the region of bottom 5-30CM distances, the work technological temperature in the section of a minimum of 100 cubes of CM volumes will be kept At 1320 DEG C -1450 DEG C, it is higher than the work technological temperature of the region glass metal apart from bottom refractory material 30-60CM distances 20-80℃；

Step 2. makes glass metal from using electrode, carries out temperature controlled clarification to the glass metal flowed from the top to the bottom, exhaust is steeped With anti-crystallization device (30) lower part, the bottom flow liquid channel (20) of entrance enters back into one be coupled using electrode under The glass metal flowed up carries out temperature controlled glass metal rise channel s structure (40)；

Process characteristic is：By what is designed in bottom flow liquid channel (20), in the region of bottom refractory material 5-30CM In glass metal, 3-20 electrode assembly of design makes bottom flow liquid channel (20) region, away from refractory material bottom 5-30CM away from From region glass metal in, the work technological temperature in the section of a minimum of 100 cubes of CM volumes, to be maintained at 1320 DEG C- 1450 DEG C, it is higher than 20-80 DEG C of the work technological temperature of the region glass metal apart from bottom refractory material 30-60CM distances；

Process characteristic is：It is logical that temperature controlled glass metal rising is carried out to the glass metal flowed from bottom to top by using electrode It is designed in road structure (40), in the glass metal in the region of bottom refractory material 5-30CM, 3-20 electrode of design fills It sets, makes bottom flow liquid channel (20) region, it is a minimum of in the glass metal in the region away from refractory material bottom 5-30CM distances The work technological temperature in the section of 100 cubes of CM volumes, will be maintained at 1320 DEG C -1450 DEG C, be higher than apart from bottom refractory material Expect 20-80 DEG C of the work technological temperature of the region glass metal of 30-60CM distances；

Process characteristic is：By it in the glass metal in the region of bottom refractory material 5-30CM, 3-20 electricity of design Pole device makes bottom flow liquid channel (20) region, in the glass metal in the region away from refractory material bottom 5-30CM distances, at least The work technological temperature for having the section of 100 cubes of CM volumes, will be maintained at 1320 DEG C -1450 DEG C, be higher than apart from bottom refractory 20-80 DEG C of the work technological temperature of the region glass metal of material 30-60CM distances；

Step 3. glass metal again by bottom flow liquid channel (20), into electrode to the glass metal that flows from bottom to top into trip temperature The glass metal rise channel s structure (40) of control；

Process characteristic is：By it in the glass metal in the region of bottom refractory material 5-30CM, 3-20 electricity of design Pole device carries out temperature controlled glass metal rise channel s structure (40) region using electrode to the glass metal flowed from bottom to top , in the glass metal in the region away from refractory material bottom 5-30CM distances, the work work in the section of a minimum of 100 cubes of CM volumes Skill temperature will be maintained at 1320 DEG C -1450 DEG C, be higher than the region glass metal apart from bottom refractory material 30-60CM distances Work 20-80 DEG C of technological temperature；

Step 4. moulding process：

Selection 1, the first glassware moulding process, the glass of the top exit above-mentioned by rise channel s structure (40) Liquid, into the device (17) for the loading glass metal being coupled, using glass metal gate (8), the molding into glassware fills It sets (50)；The molding machine (50) of its glassware is the tin kiln structure of float flat glass technique；Glass metal enters tin kiln knot The smooth plane for being furnished with the tin metal dissolved of structure carries out glass metal time and divides thin and polishing；Again by the 10-40 on both sides to drawing Side machine pulls into required thickness to the glass tape of formation；Using annealing, material process is cut, forms float flat glass product；Or

Selection 2, second of glassware moulding process, the glass of the top exit above-mentioned by rise channel s structure (40) Liquid, into the device (17) for the loading glass metal being coupled；The device (17) for loading glass metal is exactly the sprue of glass metal, glass Glass liquid, which enters to be coupled, 2-30 glass metal runner；Glass metal enters the glass for the glassware that each runner is coupled The molding machine of fiber production；The dry crucible of corresponding 2-30 bearing glass liquid is separately flowed into, glass metal passes through corresponding 2-30 A bushing forms glass fibre under the action of corresponding wire drawing machine；Or

Selection 3, the third glassware moulding process, the glass of the top exit above-mentioned by rise channel s structure (40) Liquid, into the device (17) for the loading glass metal being coupled；The device (17) for loading glass metal is exactly the sprue of glass metal, glass Glass liquid, which enters to be coupled, 2-30 glass metal runner；Glass metal enters the 2-30 for the glassware that each runner is coupled The blow molding device of a industry and utility glass ware；It is blow molded into the product of industry and domestic glass respectively；Using glass The blow molding product of industry and domestic glass is made in the processing of the annealing device of product；Or

Selection 4, the 4th kind of glassware moulding process, the glass of the top exit above-mentioned by rise channel s structure (40) Liquid, into the device (17) for the loading glass metal being coupled；The device (17) for loading glass metal is exactly the sprue of glass metal, glass Glass liquid, which enters to be coupled, 2-30 glass metal runner；Glass metal enters the 2-30 for the glassware that each runner is coupled The compression molding device of a industry and utility glass ware；It is pressed into the product of industry and domestic glass respectively；Using glass The compression moulding product of industry and domestic glass is made in the processing of the annealing device of product；Or

Selection 5, the 5th kind of glassware moulding process, the glass of the top exit above-mentioned by rise channel s structure (40) Liquid, into the device (17) for the loading glass metal being coupled；The device (17) for loading glass metal is exactly the sprue of glass metal, glass Glass liquid, which enters to be coupled, 2-30 glass metal runner；Glass metal enters the 2-30 for the glassware that each runner is coupled The drawing molding device of a industry and domestic glass, is drawn into the product of industry and domestic glass respectively；Using glassware Annealing device processing, industry and the drawing moulded products of domestic glass are made；Or

Selection 6, the 6th kind of glassware moulding process, the glass of the top exit above-mentioned by rise channel s structure (40) Liquid, into the device (17) for the loading glass metal being coupled；The device (17) for loading glass metal is exactly the sprue of glass metal, glass Glass liquid, which enters to be coupled, 2-30 glass metal runner；Glass metal enters the 2-30 for the glassware that each runner is coupled The blow molding device of a bathroom glassware, is respectively prepared bathroom glassware；Using the annealing device of glassware Processing, is made bathroom glassware.