WO2023039991A1 - 玻璃生产设备及玻璃生产方法 - Google Patents

玻璃生产设备及玻璃生产方法 Download PDF

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WO2023039991A1
WO2023039991A1 PCT/CN2021/125588 CN2021125588W WO2023039991A1 WO 2023039991 A1 WO2023039991 A1 WO 2023039991A1 CN 2021125588 W CN2021125588 W CN 2021125588W WO 2023039991 A1 WO2023039991 A1 WO 2023039991A1
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Prior art keywords
glass
line
production
branch
melting furnace
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PCT/CN2021/125588
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English (en)
French (fr)
Inventor
平文亮
林文城
刘红刚
王明忠
肖子凡
王琰
赵仁民
Original Assignee
清远南玻节能新材料有限公司
咸宁南玻光电玻璃有限公司
中国南玻集团股份有限公司
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Publication of WO2023039991A1 publication Critical patent/WO2023039991A1/zh

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    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C4/00—Compositions for glass with special properties
    • C03C4/02—Compositions for glass with special properties for coloured glass
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B11/00—Pressing molten glass or performed glass reheated to equivalent low viscosity without blowing
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B13/00—Rolling molten glass, i.e. where the molten glass is shaped by rolling
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B15/00—Drawing glass upwardly from the melt
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B17/00—Forming molten glass by flowing-out, pushing-out, extruding or drawing downwardly or laterally from forming slits or by overflowing over lips
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B18/00—Shaping glass in contact with the surface of a liquid
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
    • C03B5/18—Stirring devices; Homogenisation
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B5/00—Melting in furnaces; Furnaces so far as specially adapted for glass manufacture
    • C03B5/16—Special features of the melting process; Auxiliary means specially adapted for glass-melting furnaces
    • C03B5/225—Refining
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B7/00—Distributors for the molten glass; Means for taking-off charges of molten glass; Producing the gob, e.g. controlling the gob shape, weight or delivery tact
    • C03B7/02—Forehearths, i.e. feeder channels
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C3/00—Glass compositions
    • C03C3/04—Glass compositions containing silica
    • C03C3/076—Glass compositions containing silica with 40% to 90% silica, by weight
    • C03C3/083—Glass compositions containing silica with 40% to 90% silica, by weight containing aluminium oxide or an iron compound
    • C03C3/085—Glass compositions containing silica with 40% to 90% silica, by weight containing aluminium oxide or an iron compound containing an oxide of a divalent metal
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C3/00—Glass compositions
    • C03C3/04—Glass compositions containing silica
    • C03C3/076—Glass compositions containing silica with 40% to 90% silica, by weight
    • C03C3/083—Glass compositions containing silica with 40% to 90% silica, by weight containing aluminium oxide or an iron compound
    • C03C3/085—Glass compositions containing silica with 40% to 90% silica, by weight containing aluminium oxide or an iron compound containing an oxide of a divalent metal
    • C03C3/087—Glass compositions containing silica with 40% to 90% silica, by weight containing aluminium oxide or an iron compound containing an oxide of a divalent metal containing calcium oxide, e.g. common sheet or container glass
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C3/00—Glass compositions
    • C03C3/04—Glass compositions containing silica
    • C03C3/076—Glass compositions containing silica with 40% to 90% silica, by weight
    • C03C3/089—Glass compositions containing silica with 40% to 90% silica, by weight containing boron
    • C03C3/091—Glass compositions containing silica with 40% to 90% silica, by weight containing boron containing aluminium
    • C03C3/093—Glass compositions containing silica with 40% to 90% silica, by weight containing boron containing aluminium containing zinc or zirconium
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C3/00—Glass compositions
    • C03C3/04—Glass compositions containing silica
    • C03C3/076—Glass compositions containing silica with 40% to 90% silica, by weight
    • C03C3/097—Glass compositions containing silica with 40% to 90% silica, by weight containing phosphorus, niobium or tantalum
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C3/00—Glass compositions
    • C03C3/04—Glass compositions containing silica
    • C03C3/076—Glass compositions containing silica with 40% to 90% silica, by weight
    • C03C3/11—Glass compositions containing silica with 40% to 90% silica, by weight containing halogen or nitrogen
    • C03C3/112—Glass compositions containing silica with 40% to 90% silica, by weight containing halogen or nitrogen containing fluorine
    • C—CHEMISTRY; METALLURGY
    • C03—GLASS; MINERAL OR SLAG WOOL
    • C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
    • C03C3/00—Glass compositions
    • C03C3/04—Glass compositions containing silica
    • C03C3/076—Glass compositions containing silica with 40% to 90% silica, by weight
    • C03C3/11—Glass compositions containing silica with 40% to 90% silica, by weight containing halogen or nitrogen
    • C03C3/112—Glass compositions containing silica with 40% to 90% silica, by weight containing halogen or nitrogen containing fluorine
    • C03C3/115—Glass compositions containing silica with 40% to 90% silica, by weight containing halogen or nitrogen containing fluorine containing boron
    • C03C3/118—Glass compositions containing silica with 40% to 90% silica, by weight containing halogen or nitrogen containing fluorine containing boron containing aluminium
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00—Technologies relating to the processing of minerals
    • Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
    • Y02P40/57—Improving the yield, e-g- reduction of reject rates

Definitions

  • the invention relates to the technical field of glass production, in particular to a glass production equipment and a glass production method.
  • the method of producing colored glass is mainly to add colorants such as metal oxides or sulfur-selenide compounds to the batch materials, and melt them into uniform colored glass through the melting pool, and then go through the float method, overflow method, up-drawing method, and calendering method. , flat drawing method, molding method, etc. to make colored glass products.
  • colorants such as metal oxides or sulfur-selenide compounds
  • One object of the present invention is to provide a kind of glass production equipment, the scheme is as follows:
  • a glass production equipment including a melting furnace, a main production line, a first branch production line and a distribution channel;
  • the main line production line includes a main line working part and a main line forming device, the main line working part communicates with the melting furnace, the main line forming device communicates with the main line working part, and the main line working part is used to make Clarification and homogenization of molten glass input from the kiln;
  • the diverging channel is connected to the melting furnace
  • the first branch line production line includes a confluence device, an auxiliary melting furnace and a first branch line forming device
  • the converging device is in communication with the diverging channel
  • the auxiliary melting furnace is connected to the converging device connected
  • the first branch line forming device communicates with the confluence device
  • the auxiliary melting furnace is used to melt the glass colorant containing the colorant and/or the glass auxiliary material containing the functional auxiliary agent
  • the confluence device is used to convert the
  • the molten glass input from the distribution channel is mixed with the molten glass input from the auxiliary melting furnace, clarified and homogenized.
  • a first flow control mechanism is provided on the channel connecting the main line forming device and the main line working part.
  • a second flow control mechanism is provided on the channel connecting the confluence device and the diverging channel.
  • a third flow control mechanism is provided on the channel connecting the auxiliary furnace and the confluence device.
  • a fourth flow control mechanism is provided on the channel connecting the confluence device and the first branch line forming device.
  • the glass production equipment further includes a neck, and the working part of the main line communicates with the melting furnace through the neck.
  • first branch production lines there are multiple first branch production lines, and the multiple first branch production lines are respectively communicated with the distribution channel.
  • the confluence device is provided with a stirring mechanism and a heating mechanism.
  • the glass production equipment further includes a second branch line production line
  • the second branch line production line includes a branch line working part and a second branch line forming device
  • the branch line working part communicates with the distribution channel
  • the The second branch line forming device communicates with the branch line working part
  • the branch line working part is provided with a feeding port, and the feeding port is used to add colorants, functional additives, and glass color containing colorants to the branch line working part. materials and/or glass accessories containing functional additives.
  • a fifth flow control mechanism is provided on the channel connecting the branch line working part and the branching channel.
  • a sixth flow control mechanism is provided on the channel connecting the second branch line forming device and the branch line working part.
  • the main line forming device includes a float glass forming mechanism, an overflow glass forming mechanism, an up-draw glass forming mechanism, a calendering glass forming mechanism, a flat-drawing glass forming mechanism and a molded glass forming mechanism. one or more of the institutions.
  • the first branch line forming device includes a float glass forming mechanism, an overflow glass forming mechanism, an up-draw glass forming mechanism, a calendering glass forming mechanism, a flat-drawing glass forming mechanism, and a molding method One or more of the glass forming mechanisms.
  • the second branch line forming device includes a float glass forming mechanism, an overflow glass forming mechanism, an up-draw glass forming mechanism, a calendering glass forming mechanism, a flat-draw glass forming mechanism, and a molding method One or more of the glass forming mechanisms.
  • Another object of the present invention is to provide a kind of glass production method, scheme is as follows:
  • a glass production method using the glass production equipment described in any one of the above embodiments, the glass production method includes the following steps:
  • Part of the molten glass is input into the confluence device of the first branch production line through the split channel, and the glass colorant containing the colorant and/or the glass auxiliary material containing the functional additive are added in the auxiliary melting furnace and melted into molten glass,
  • the molten glass in the auxiliary melting furnace is input into the confluence device, mixed with the molten glass input from the split channel, clarified and homogenized, and then input into the first branch line forming device for molding.
  • the glass batch added in the melting furnace includes: 54-78 parts by weight of SiO 2 , 0.5-28 parts by weight of Al 2 O 3 , 0-13.5 parts by weight of B 2 O 3 , 0-13.5 parts by weight of P 2 O 5 0-10 parts by weight, Li 2 O 0-9 parts by weight, Na 2 O 4-14 parts by weight, K 2 O 0-6 parts by weight, MgO 0-7 parts by weight, CaO 0-9.5 parts by weight, SrO 0-4 parts by weight, ZnO 0-4 parts by weight, ZrO 2 0-4 parts by weight, F 0-2 parts by weight; and/or the coloring agent is selected from Fe, Cr, Co, Cu, Ni, Ti, Mn , one or more of Ce, Nd, Pr, Er, V, W oxides, and Se powder.
  • the above-mentioned glass production equipment and glass production method produce different glass products through the main line production line and the first branch line production line respectively connected with the melting furnace.
  • the main line production line can produce white glass with a large market demand
  • the first branch line production line can produce market demand.
  • the main production line and the first branch production line share a melting furnace.
  • glass batch materials are added in the melting furnace to form molten glass; part of the molten glass is input into the main line working part of the main line production line for molding; Add glass colorants containing colorants and/or glass auxiliary materials containing functional additives to the melting furnace and melt them into molten glass, so that the molten glass in the auxiliary melting furnace is input into the confluence device, mixed with the molten glass input from the split channel, and clarified After homogenization, it is input into the first branch line molding device for molding.
  • the designed production capacity of the melting furnace is not limited to the output of colored glass or functional glass.
  • the production capacity of colored glass or the output of functional glass is increased, thereby increasing the production capacity of the glass production line, thereby reducing the production cost of colored glass or functional glass.
  • the glass liquid formed from the auxiliary furnace to form glass colorant and/or glass auxiliary material is input into the confluence device for mixing, which can avoid defects such as difficult melting, uneven color, and generation of bubbles caused by direct addition of colorants or additives. The problem.
  • Fig. 1 is a schematic structural diagram of a glass production equipment of an embodiment.
  • first and second are used for description purposes only, and cannot be interpreted as indicating or implying relative importance or implicitly indicating the quantity of indicated technical features.
  • the features defined as “first” and “second” may explicitly or implicitly include at least one of these features.
  • a glass production equipment 100 includes a melting furnace 110 , a main production line 120 , a first branch production line 130 and a distribution channel 140 .
  • the main production line 120 and the first branch production line 130 can produce different glass products.
  • the main line production line 120 includes a main line working part 121 and a main line forming device 122 .
  • the main line working part 121 communicates with the melting furnace 110
  • the main line forming device 122 communicates with the main line working part 121 .
  • the melting furnace 110 is used to melt the glass batch material to form molten glass, and may be a heat storage type or heat exchange type pool furnace.
  • the mainline working part 121 is used to clarify and homogenize the molten glass input from the melting furnace 110 . After the molten glass is clarified and homogenized, the temperature is lowered to a temperature suitable for forming, and then it is input to the main line forming device 122 for forming process to manufacture glass products of specific shapes.
  • the output ratio of the main line production line 120 can be set relatively large, for example, accounting for more than 60% of the total output, and can produce white glass with a large market demand.
  • the distributing channel 140 communicates with the melting furnace 110 and is used to divert part of the molten glass from the melting furnace 110 .
  • the first branch line production line 130 includes a confluence device 131 , an auxiliary furnace 132 and a first branch line forming device 133 .
  • the merging device 131 communicates with the diverging channel 140
  • the auxiliary furnace 132 communicates with the merging device 131
  • the first branch forming device 133 communicates with the merging device 131 .
  • the auxiliary melting furnace 132 is used for melting glass colorants containing colorants and/or glass auxiliary materials containing functional additives.
  • the merging device 131 is used for mixing and clarifying the molten glass input from the distribution channel 140 with the molten glass input from the auxiliary melting furnace 132 . After the mixed glass liquid is clarified and homogenized, the temperature is lowered to a temperature suitable for forming, and then it is input to the first branch line forming device 133 for forming process to manufacture glass products of specific shapes.
  • the first branch line production line 130 can produce colored glass or functional glass with small market demand, and the main line production line 120 and the first branch line production line 130 share a melting furnace 110 .
  • glass batch materials are added in the melting furnace 110 to melt to form molten glass; part of the molten glass is input into the main line working part 121 of the main line production line 120 for molding;
  • the auxiliary melting furnace 132 the glass color material containing the coloring agent and/or the glass auxiliary material containing the functional auxiliary agent are added and melted into molten glass, so that the glass liquid in the auxiliary melting furnace 132 is input into the confluence device 131, and is connected with the flow from the branch
  • the molten glass input from the channel 140 is mixed, clarified and homogenized, and then input into the first branch line forming device 133 for forming.
  • the designed production capacity of the melting furnace 110 in the above-mentioned glass production equipment 100 is not limited to the output of colored glass or functional glass, but on the basis of the existing white glass production line. Glass production capacity or output of functional glass, thereby increasing the production capacity of the glass production line, thereby reducing the production cost of colored glass or functional glass.
  • the glass liquid formed from the auxiliary melting furnace 132 to form the glass colorant and/or glass auxiliary material is input into the confluence device 131 for mixing, which can avoid melting difficulty, uneven color, and generation of bubbles caused by directly adding colorants or auxiliary agents. and other defects.
  • the glass production equipment 100 further includes a neck 150 , through which the working part 121 of the main line communicates with the melting furnace 110 .
  • the neck 150 is a narrow channel for molten glass.
  • the narrow neck 150 can reduce the transmission of dust and alkali vapor in the melting furnace 110 to the main line working part 121, and reduce the impact of dust and alkali vapor on the glass liquid in the main line working part 121. Influence.
  • a first flow control mechanism 123 is provided on the channel connecting the main line forming device 122 and the main line working part 121 .
  • the first flow control mechanism 123 can control parameters such as the flow rate and flow velocity of molten glass input from the melting furnace 110 to the main line working part 121 .
  • the main line forming device 122 includes a float glass forming mechanism, an overflow glass forming mechanism, an up-draw glass forming mechanism, a calendering glass forming mechanism, a flat-drawing glass forming mechanism, and a compression molding glass forming mechanism. one or more of .
  • the confluence device 131 includes a stirring mechanism and a heating mechanism.
  • the stirring mechanism is used to stir and mix the molten glass input from the distribution channel 140 and the molten glass input from the auxiliary melting furnace 132
  • the heating mechanism is used to control the temperature of the molten glass.
  • a second flow control mechanism 134 is provided on the channel connecting the confluence device 131 and the diverging channel 140 .
  • a third flow control mechanism 135 is provided on the passage connecting the auxiliary furnace 132 and the confluence device 131 .
  • a fourth flow control mechanism 136 is provided on the passage connecting the confluence device 131 and the first branch line forming device 132 .
  • first branch production lines 130 there are multiple first branch production lines 130 , and the multiple first branch production lines 130 are respectively communicated with the distribution channels 140 .
  • first branch production lines 130 are set up to produce different colored glass or functional glass, and the product size, shape, and molding method can be set according to requirements.
  • a single colored glass production line if it needs to be converted into other colored glass, the residual colored glass in the glass melting furnace 110 will cause color difference to the new glass. Therefore, it is preferable to set up multiple first branch production lines 130 for producing different colors, so that there will be no color difference , and there is no need to replace the auxiliary furnace 132.
  • first branch production lines 130 there are two first branch production lines 130 .
  • the first branch line forming device 133 includes a float glass forming mechanism, an overflow glass forming mechanism, an up-draw glass forming mechanism, a calendering glass forming mechanism, a flat-drawing glass forming mechanism, and a molded glass forming mechanism. one or more of the institutions.
  • the glass production facility 100 further includes a second branch production line 160 .
  • the second branch line production line 160 includes a branch line working part 161 and a second branch line forming device 162 , and the branch line working part 161 communicates with the distribution channel 140 .
  • the branch line working part 161 is provided with a feeding port for adding colorants, functional additives, glass pigments containing colorants and/or glass auxiliary materials containing functional additives into the branch line working part 161 .
  • the branch working part 161 is provided with a stirring mechanism.
  • a fifth flow control mechanism 163 is provided on the channel connecting the branch line working part 161 and the branching channel 140 .
  • a sixth flow control mechanism 164 is provided on the channel connecting the second branch forming device 162 and the branch working part 161 .
  • the second branch line forming device 162 includes a float glass forming mechanism, an overflow glass forming mechanism, an up-draw glass forming mechanism, a rolling glass forming mechanism, a flat-draw glass forming mechanism, and a press-molded glass forming mechanism. one or more of the institutions.
  • second branch production lines 160 there are multiple second branch production lines 160 , and the plurality of second branch production lines 160 are respectively communicated with the distribution channel 140 .
  • a plurality of second branch line production lines 160 can produce different colored glass or functional glass respectively, and its product size, shape and molding method etc. can all be set separately according to demand.
  • the present invention also provides a glass production method, using the glass production equipment 100 of any of the above examples, the glass production method includes the following steps:
  • Part of the molten glass is input into the main line working part 121 of the main line production line 120, and after the glass liquid is clarified and homogenized in the main line working part 121, it is input into the main line forming device 122 for molding;
  • Part of the molten glass is input into the confluence device 131 of the first branch line production line 130 through the distribution channel 140, and glass pigments containing colorants and/or glass auxiliary materials containing functional additives are added in the auxiliary melting furnace 132 and melted into molten glass.
  • the molten glass in the auxiliary melting furnace 132 is input into the confluence device 131 , mixed with the molten glass input from the distribution channel 140 , clarified and homogenized, and then input into the first branch line forming device 133 for molding.
  • the glass batch materials added in the furnace include: 54-78 parts by weight of SiO 2 , 0.5-28 parts by weight of Al 2 O 3 , 0-13.5 parts by weight of B 2 O 3 , 0-13.5 parts by weight of P 2 O 5 0 ⁇ 10 parts by weight, Li 2 O 0 ⁇ 9 parts by weight, Na 2 O 4 ⁇ 14 parts by weight, K 2 O 0 ⁇ 6 parts by weight, MgO 0 ⁇ 7 parts by weight, CaO 0 ⁇ 9.5 parts by weight, SrO 0 ⁇ 4 parts by weight Parts by weight, ZnO 0-4 parts by weight, ZrO 2 0-4 parts by weight, F 0-2 parts by weight.
  • the colorant is selected from one or more of oxides of Fe, Cr, Co, Cu, Ni, Ti, Mn, Ce, Nd, Pr, Er, V, W, and Se powder.
  • glass production equipment 100 shown in FIG. 1 is a one-kiln five-line equipment, including a main production line 120 , two first branch production lines 130 , and two second branch production lines 160 .
  • the glass production apparatus 100 can simultaneously produce glasses of different thicknesses, colors or functions. The types of glass produced are listed in Table 1.
  • the thickness T is the thickness of the glass products on the main production line 120
  • the thickness X refers to other thicknesses different from the thickness T.
  • the above-mentioned glass production equipment 100 and glass production method compared with building a colored glass or functional glass production line, share a melting furnace 110, and in addition set the confluence device 131 and auxiliary melting furnace 132 in the first branch production line 130.
  • the melting furnace 110 The designed production capacity is not limited to the output of colored glass or functional glass, but on the basis of the existing white glass production line, the capacity of colored glass or the output of functional glass is increased, thereby increasing the production capacity of the glass production line and reducing the production capacity of colored glass. Or the production cost of functional glass.
  • the glass liquid formed from the auxiliary melting furnace 132 to form the glass colorant and/or glass auxiliary material is input into the confluence device 131 for mixing, which can avoid melting difficulty, uneven color, and generation of bubbles caused by directly adding colorants or auxiliary agents. and other defects.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Manufacturing & Machinery (AREA)
  • Ceramic Engineering (AREA)
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Abstract

一种玻璃生产设备(100)及玻璃生产方法。玻璃生产设备(100)包括熔窑(110)、主线生产线(120)、第一支线生产线(130)以及分流通道(140)。主线生产线(120)包括主线工作部(121)以及主线成型装置(122)，分流通道(140)与熔窑(110)连通，第一支线生产线(130)包括合流装置(131)、辅助熔炉(132)以及第一支线成型装置(133)。熔窑(110)的设计生产量不局限于彩色玻璃或者功能玻璃的产量，在现有白玻的生产线基础上，增加了彩色玻璃产能或者功能玻璃的产出，从而提高玻璃生产线的生产量，从而降低彩色玻璃或者功能玻璃的生产成本。此外，采用由辅助熔炉(132)形成玻璃色料和/或玻璃辅料的玻璃液，输入合流装置(131)中混合的方式，可以避免直接添加着色剂或者助剂所导致的熔化困难、颜色不均、产生气泡等缺陷的问题。

Description

玻璃生产设备及玻璃生产方法 技术领域
本发明涉及玻璃生产技术领域，特别是涉及一种玻璃生产设备及玻璃生产方法。
背景技术
目前生产彩色玻璃的方法主要为再配合料中加入金属氧化物或硫硒化合物等着色剂，通过熔化池熔制成均匀的彩色玻璃，再经过浮法、溢流法、上拉法、压延法、平拉法、模压法等制成彩色玻璃制品。
传统的彩色玻璃或者功能玻璃的生产方法，缺点是一条玻璃生产线只能生产单一种类的玻璃。由于彩色玻璃、功能玻璃的市场需求量有限，一般此类窑炉产生量较小，导致生产成本居高不下。
发明内容
基于此，有必要提供一种玻璃生产设备及玻璃生产方法，以解决传统的彩色玻璃或者功能玻璃的生产方法成本较高的问题。
本发明的一个目的在于提供一种玻璃生产设备，方案如下：
一种玻璃生产设备，包括熔窑、主线生产线、第一支线生产线以及分流通道；
所述主线生产线包括主线工作部以及主线成型装置，所述主线工作部与所述熔窑连通，所述主线成型装置与所述主线工作部连通，所述主线工作部用于使从所述熔窑输入的玻璃液澄清均化；
所述分流通道与所述熔窑连通，所述第一支线生产线包括合流装置、辅助熔炉以及第一支线成型装置，所述合流装置与所述分流通道连通，所述辅助熔炉与所述合流装置连通，所述第一支线成型装置与所述合流装置连通，所述辅助熔炉用于熔化含有着色剂的玻璃色料和/或含有功能性助剂的玻璃辅料，所述合流装置用于将从所述分流通道输入的玻璃液与从所述辅助熔炉输入的玻璃液进行混合并澄清均化。
在其中一个实施例中，连通所述主线成型装置与所述主线工作部的通道上设置有第一流量控制机构。
在其中一个实施例中，连通所述合流装置与所述分流通道的通道上设置有第二流量控制机构。
在其中一个实施例中，连通所述辅助熔炉与所述合流装置的通道上设置有第三流量控制机构。
在其中一个实施例中，连通所述合流装置与所述第一支线成型装置的通道上设置有第四流量控制机构。
在其中一个实施例中，所述玻璃生产设备还包括卡脖，所述主线工作部通过所述卡脖与所述熔窑连通。
在其中一个实施例中，所述第一支线生产线的数量有多条，多条所述第一支线生产线分别与所述分流通道连通。
在其中一个实施例中，所述合流设置中设置有搅拌机构以及加热机构。
在其中一个实施例中，所述玻璃生产设备还包括第二支线生产线，所述第二支线生产线包括支线工作部以及第二支线成型装置，所述支线工作部与所述分流通道连通，所述第二支线成型装置与所述支线工作部连通，所述支线工作部设有加料口，所述加料口用于向所述支线工作部内添加着色剂、功能性助剂、 含有着色剂的玻璃色料和/或含有功能性助剂的玻璃辅料。
在其中一个实施例中，连通所述支线工作部与所述分流通道的通道上设置有第五流量控制机构。
在其中一个实施例中，连通所述第二支线成型装置与所述支线工作部的通道上设置有第六流量控制机构。
在其中一个实施例中，所述第二支线生产线的数量有多条，多条所述第二支线生产线分别与所述分流通道连通。
在其中一个实施例中，所述主线成型装置包括浮法玻璃成型机构、溢流法玻璃成型机构、上拉法玻璃成型机构、压延法玻璃成型机构、平拉法玻璃成型机构以及模压法玻璃成型机构中的一种或多种。
在其中一个实施例中，所述第一支线成型装置包括浮法玻璃成型机构、溢流法玻璃成型机构、上拉法玻璃成型机构、压延法玻璃成型机构、平拉法玻璃成型机构以及模压法玻璃成型机构中的一种或多种。
在其中一个实施例中，所述第二支线成型装置包括浮法玻璃成型机构、溢流法玻璃成型机构、上拉法玻璃成型机构、压延法玻璃成型机构、平拉法玻璃成型机构以及模压法玻璃成型机构中的一种或多种。
本发明的另一目的在于提供一种玻璃生产方法，方案如下：
一种玻璃生产方法，使用上述任一实施例所述的玻璃生产设备，所述玻璃生产方法包括以下步骤：
在所述熔窑加入玻璃配合料，熔融形成玻璃液；
使部分玻璃液输入所述主线生产线的主线工作部中，玻璃液在所述主线工作部中澄清均化后，输入所述主线成型装置，进行成型；
使部分玻璃液通过分流通道输入所述第一支线生产线的合流装置中，在所 述辅助熔炉中添加含有着色剂的玻璃色料和/或含有功能性助剂的玻璃辅料并熔化成玻璃液，使所述辅助熔炉中的玻璃液输入所述合流装置，与从所述分流通道输入的玻璃液进行混合，澄清均化后，输入所述第一支线成型装置，进行成型。
在其中一个实施例中，在所述熔窑中加入的玻璃配合料包括：SiO 2 54～78重量份、Al 2O 3 0.5～28重量份、B 2O 3 0～13.5重量份、P 2O 5 0～10重量份、Li 2O 0～9重量份、Na 2O 4～14重量份、K 2O 0～6重量份、MgO 0～7重量份、CaO 0～9.5重量份、SrO 0～4重量份、ZnO 0～4重量份、ZrO 2 0～4重量份、F 0～2重量份；和/或所述着色剂选自Fe、Cr、Co、Cu、Ni、Ti、Mn、Ce、Nd、Pr、Er、V、W的氧化物、Se粉中的一种或多种。
与现有方案相比，上述玻璃生产设备及玻璃生产方法具有以下有益效果：
上述玻璃生产设备及玻璃生产方法，通过分别与熔窑连通的主线生产线和第一支线生产线生产不同的玻璃制品，其中，主线生产线可生产市场需求量大的白玻，第一支线生产线可生产市场需求量小的彩色玻璃或者功能玻璃，主线生产线和第一支线生产线共用一个熔窑。
生产时，在熔窑加入玻璃配合料，熔融形成玻璃液；使部分玻璃液输入主线生产线的主线工作部中进行成型；使部分玻璃液通过分流通道输入第一支线生产线的合流装置中，在辅助熔炉中添加含有着色剂的玻璃色料和/或含有功能性助剂的玻璃辅料并熔化成玻璃液，使辅助熔炉中的玻璃液输入合流装置，与从分流通道输入的玻璃液进行混合，澄清均化后，输入第一支线成型装置，进行成型。
相比建造一条彩色玻璃或者功能玻璃的生产线，共用一个熔窑、另外在第一支线生产线中设置合流装置、辅助熔炉的方式，熔窑的设计生产量不局限于 彩色玻璃或者功能玻璃的产量，反倒在现有白玻的生产线基础上，增加了彩色玻璃产能或者功能玻璃的产出，从而提高玻璃生产线的生产量，从而降低彩色玻璃或者功能玻璃的生产成本。
此外，采用由辅助熔炉形成玻璃色料和/或玻璃辅料的玻璃液，输入合流装置中混合的方式，可以避免直接添加着色剂或者助剂所导致的熔化困难、颜色不均、产生气泡等缺陷的问题。
附图说明
图1为一实施例的玻璃生产设备的结构示意图。
附图标记说明：
100、玻璃生产设备；110、熔窑；120、主线生产线；121、主线工作部；122、主线成型装置；123、第一流量控制机构；130、第一支线生产线；131、合流装置；132、辅助熔炉；133、第一支线成型装置；134、第二流量控制机构；135、第三流量控制机构；136、第四流量控制机构；140、分流通道；150、卡脖；160、第二支线生产线；161、支线工作部；162、第二支线成型装置；163、第五流量控制机构；164、第六流量控制机构。
具体实施方式
为了便于理解本发明，下面将参照相关附图对本发明进行更全面的描述。附图中给出了本发明的较佳实施例。但是，本发明可以以许多不同的形式来实现，并不限于本文所描述的实施例。相反地，提供这些实施例的目的是使对本发明的公开内容的理解更加透彻全面。
需要说明的是，当元件被称为“设置”另一个元件，它可以直接在另一个元件 上或者也可以存在居中的元件。当一个元件被认为是“连通”另一个元件，它可以是直接连通到另一个元件或者可能同时存在居中元件。本文所使用的术语“垂直的”、“水平的”、“左”、“右”以及类似的表述只是为了说明的目的，并不表示是唯一的实施方式。
在本发明的描述中，需要理解的是，术语“第一”、“第二”仅用于描述目的，而不能理解为指示或暗示相对重要性或者隐含指明所指示的技术特征的数量。由此，限定有“第一”、“第二”的特征可以明示或者隐含地包括至少一个该特征。
除非另有定义，本文所使用的所有的技术和科学术语与属于本发明的技术领域的技术人员通常理解的含义相同。本文中在本发明的说明书中所使用的术语只是为了描述具体的实施例的目的，不是旨在于限制本发明。本文所使用的术语“和/或”包括一个或多个相关的所列项目的任意的和所有的组合。
请参考图1所示，本发明一实施例的玻璃生产设备100，包括熔窑110、主线生产线120、第一支线生产线130以及分流通道140。主线生产线120和第一支线生产线130可以生产不同的玻璃制品。
主线生产线120包括主线工作部121以及主线成型装置122。主线工作部121与熔窑110连通，主线成型装置122与主线工作部121连通。其中，熔窑110用于将玻璃配合料熔融形成玻璃液，可以为蓄热式或换热式的池窑。
主线工作部121用于使从熔窑110输入的玻璃液澄清均化。玻璃液澄清均化后，降温至适合成型的温度，输入至主线成型装置122中进行成型工艺，制造成特定形状的玻璃制品。
主线生产线120的产量比例可设置较大，例如占总产量的60％以上，可生产市场需求量大的白玻。
分流通道140与熔窑110连通，用于从熔窑110中分流出部分玻璃液。
第一支线生产线130包括合流装置131、辅助熔炉132以及第一支线成型装置133。合流装置131与分流通道140连通，辅助熔炉132与合流装置131连通，第一支线成型装置133与合流装置131连通。
其中，辅助熔炉132用于熔化含有着色剂的玻璃色料和/或含有功能性助剂的玻璃辅料。合流装置131用于将从分流通道140输入的玻璃液与从辅助熔炉132输入的玻璃液进行混合并澄清均化。混合玻璃液澄清均化后，降温至适合成型的温度，输入至第一支线成型装置133中进行成型工艺，制造成特定形状的玻璃制品。
第一支线生产线130可生产市场需求量小的彩色玻璃或者功能玻璃，主线生产线120和第一支线生产线130共用一个熔窑110。
生产时，在熔窑110加入玻璃配合料，熔融形成玻璃液；使部分玻璃液输入主线生产线120的主线工作部121中进行成型；使部分玻璃液通过分流通道140输入第一支线生产线130的合流装置131中，在辅助熔炉132中添加含有着色剂的玻璃色料和/或含有功能性助剂的玻璃辅料并熔化成玻璃液，使辅助熔炉132中的玻璃液输入合流装置131，与从分流通道140输入的玻璃液进行混合，澄清均化后，输入第一支线成型装置133，进行成型。
相比建造一条彩色玻璃或者功能玻璃的生产线，上述玻璃生产设备100中熔窑110的设计生产量不局限于彩色玻璃或者功能玻璃的产量，反倒在现有白玻的生产线基础上，增加了彩色玻璃产能或者功能玻璃的产出，从而提高玻璃生产线的生产量，从而降低彩色玻璃或者功能玻璃的生产成本。此外，采用由辅助熔炉132形成玻璃色料和/或玻璃辅料的玻璃液，输入合流装置131中混合的方式，可以避免直接添加着色剂或者助剂所导致的熔化困难、颜色不均、产生气泡等缺陷的问题。
在其中一个示例中，玻璃生产设备100还包括卡脖150，主线工作部121通过卡脖150与熔窑110连通。卡脖150为窄小玻璃液通道，窄小的卡脖150可以减少熔窑110内的粉尘、碱蒸汽等传输至主线工作部121，降低粉尘、碱蒸汽等对主线工作部121的玻璃液的影响。
在其中一个示例中，连通主线成型装置122与主线工作部121的通道上设置有第一流量控制机构123。第一流量控制机构123可以控制熔窑110向主线工作部121中输入玻璃液的流量、流速等参数。
在其中一个示例中，主线成型装置122包括浮法玻璃成型机构、溢流法玻璃成型机构、上拉法玻璃成型机构、压延法玻璃成型机构、平拉法玻璃成型机构以及模压法玻璃成型机构中的一种或多种。
在其中一个示例中，合流装置131包括搅拌机构以及加热机构。搅拌机构用于将从分流通道140输入的玻璃液与从辅助熔炉132输入的玻璃液进行搅拌混合，加热机构用于控制玻璃液的温度。
在其中一个示例中，连通合流装置131与分流通道140的通道上设置有第二流量控制机构134。
在其中一个示例中，连通辅助熔炉132与合流装置131的通道上设置有第三流量控制机构135。
在其中一个示例中，连通合流装置131与所述第一支线成型装置132的通道上设置有第四流量控制机构136。
在其中一个示例中，第一支线生产线130的数量有多条，多条第一支线生产线130分别与分流通道140连通。
设置多条第一支线生产线130，可分别生产不同的彩色玻璃或者功能性玻璃，其产品尺寸、形状以及成型方法等均可按需求各自进行设置。单一的彩色 玻璃生产线，如果需要转成其他彩色玻璃，玻璃熔窑110的残余彩色玻璃会新玻璃产生色差，因此，优选设置多条用于生产不同颜色的第一支线生产线130，不会产生色差，也无需更换辅助熔炉132。
在图示的具体示例中，第一支线生产线130的数量有两条。
在其中一个示例中，第一支线成型装置133包括浮法玻璃成型机构、溢流法玻璃成型机构、上拉法玻璃成型机构、压延法玻璃成型机构、平拉法玻璃成型机构以及模压法玻璃成型机构中的一种或多种。
在其中一个示例中，玻璃生产设备100还包括第二支线生产线160。第二支线生产线160包括支线工作部161以及第二支线成型装置162，支线工作部161与分流通道140连通。
支线工作部161设有加料口，加料口用于向支线工作部161内添加着色剂、功能性助剂、含有着色剂的玻璃色料和/或含有功能性助剂的玻璃辅料。
在其中一个示例中，支线工作部161设置有搅拌机构。
在其中一个示例中，连通支线工作部161与分流通道140的通道上设置有第五流量控制机构163。
在其中一个示例中，连通第二支线成型装置162与支线工作部161的通道上设置有第六流量控制机构164。
在其中一个示例中，第二支线成型装置162包括浮法玻璃成型机构、溢流法玻璃成型机构、上拉法玻璃成型机构、压延法玻璃成型机构、平拉法玻璃成型机构以及模压法玻璃成型机构中的一种或多种。
在其中一个示例中，第二支线生产线160的数量有多条，多条第二支线生产线160分别与分流通道140连通。多条第二支线生产线160可分别生产不同的彩色玻璃或者功能性玻璃，其产品尺寸、形状以及成型方法等均可按需求各 自进行设置。
在图示的具体示例中，第二支线生产线160的数量有两条。
进一步地，本发明还提供一种玻璃生产方法，使用上述任一示例的玻璃生产设备100，该玻璃生产方法包括以下步骤：
在熔窑110加入玻璃配合料，熔融形成玻璃液；
使部分玻璃液输入主线生产线120的主线工作部121中，玻璃液在主线工作部121中澄清均化后，输入主线成型装置122，进行成型；
使部分玻璃液通过分流通道140输入第一支线生产线130的合流装置131中，在辅助熔炉132中添加含有着色剂的玻璃色料和/或含有功能性助剂的玻璃辅料并熔化成玻璃液，使辅助熔炉132中的玻璃液输入合流装置131，与从分流通道140输入的玻璃液进行混合，澄清均化后，输入第一支线成型装置133，进行成型。
在其中一个示例中，在熔窑中加入的玻璃配合料包括：SiO 2 54～78重量份、Al 2O 3 0.5～28重量份、B 2O 3 0～13.5重量份、P 2O 5 0～10重量份、Li 2O 0～9重量份、Na 2O 4～14重量份、K 2O 0～6重量份、MgO 0～7重量份、CaO 0～9.5重量份、SrO 0～4重量份、ZnO 0～4重量份、ZrO 2 0～4重量份、F 0～2重量份。
在其中一个示例中，着色剂选自Fe、Cr、Co、Cu、Ni、Ti、Mn、Ce、Nd、Pr、Er、V、W的氧化物、Se粉中的一种或多种。
以图1所示具体示例的玻璃生产设备100为例，其为一窑五线设备，包括主线生产线120，两条第一支线生产线130，以及两条第二支线生产线160。该玻璃生产设备100能够同时生产不同厚度、不同颜色或功能的玻璃。生产玻璃类型如表1所例举。
表1
Figure PCTCN2021125588-appb-000001
其中，厚度T为主线生产线120上的玻璃制品的厚度，厚度X是指区别于厚度T的其他厚度。
以其中的第二支线生产线2的生产为例，其生产玻璃的实施例如表2所例举。
表2
Figure PCTCN2021125588-appb-000002
Figure PCTCN2021125588-appb-000003
以其中的第一支线生产线1的生产为例，其生产玻璃的实施例如表3所例举。
表3
Figure PCTCN2021125588-appb-000004
Figure PCTCN2021125588-appb-000005
上述玻璃生产设备100及玻璃生产方法，相比建造一条彩色玻璃或者功能玻璃的生产线，共用一个熔窑110、另外在第一支线生产线130中设置合流装置131、辅助熔炉132的方式，熔窑110的设计生产量不局限于彩色玻璃或者功能玻璃的产量，反倒在现有白玻的生产线基础上，增加了彩色玻璃产能或者功能玻璃的产出，从而提高玻璃生产线的生产量，从而降低彩色玻璃或者功能玻璃的生产成本。此外，采用由辅助熔炉132形成玻璃色料和/或玻璃辅料的玻璃液，输入合流装置131中混合的方式，可以避免直接添加着色剂或者助剂所导致的熔化困难、颜色不均、产生气泡等缺陷的问题。
以上所述实施例的各技术特征可以进行任意的组合，为使描述简洁，未对上述实施例中的各个技术特征所有可能的组合都进行描述，然而，只要这些技术特征的组合不存在矛盾，都应当认为是本说明书记载的范围。
以上所述实施例仅表达了本发明的几种实施方式，其描述较为具体和详细，但并不能因此而理解为对发明专利范围的限制。应当指出的是，对于本领域的普通技术人员来说，在不脱离本发明构思的前提下，还可以做出若干变形和改 进，这些都属于本发明的保护范围。因此，本发明专利的保护范围应以所附权利要求为准。

Claims (11)

  1. 一种玻璃生产设备，其特征在于，包括熔窑、主线生产线、第一支线生产线以及分流通道；
    所述主线生产线包括主线工作部以及主线成型装置，所述主线工作部与所述熔窑连通，所述主线成型装置与所述主线工作部连通，所述主线工作部用于使从所述熔窑输入的玻璃液澄清均化；
    所述分流通道与所述熔窑连通，所述第一支线生产线包括合流装置、辅助熔炉以及第一支线成型装置，所述合流装置与所述分流通道连通，所述辅助熔炉与所述合流装置连通，所述第一支线成型装置与所述合流装置连通，所述辅助熔炉用于熔化含有着色剂的玻璃色料和/或含有功能性助剂的玻璃辅料，所述合流装置用于将从所述分流通道输入的玻璃液与从所述辅助熔炉输入的玻璃液进行混合并澄清均化。
  2. 如权利要求1所述的玻璃生产设备，其特征在于，连通所述主线成型装置与所述主线工作部的通道上设置有第一流量控制机构；和/或，
    连通所述合流装置与所述分流通道的通道上设置有第二流量控制机构；和/或，
    连通所述辅助熔炉与所述合流装置的通道上设置有第三流量控制机构；和/或，
    连通所述合流装置与所述第一支线成型装置的通道上设置有第四流量控制机构。
  3. 如权利要求1所述的玻璃生产设备，其特征在于，所述玻璃生产设备还包括卡脖，所述主线工作部通过所述卡脖与所述熔窑连通。
  4. 如权利要求1所述的玻璃生产设备，其特征在于，所述第一支线生产线的 数量有多条，多条所述第一支线生产线分别与所述分流通道连通。
  5. 如权利要求1～4中任一项所述的玻璃生产设备，其特征在于，所述合流设置中设置有搅拌机构以及加热机构。
  6. 如权利要求1所述的玻璃生产设备，其特征在于，所述玻璃生产设备还包括第二支线生产线，所述第二支线生产线包括支线工作部以及第二支线成型装置，所述支线工作部与所述分流通道连通，所述第二支线成型装置与所述支线工作部连通，所述支线工作部设有加料口，所述加料口用于向所述支线工作部内添加着色剂、功能性助剂、含有着色剂的玻璃色料和/或含有功能性助剂的玻璃辅料。
  7. 如权利要求6所述的玻璃生产设备，其特征在于，连通所述支线工作部与所述分流通道的通道上设置有第五流量控制机构；和/或，
    连通所述第二支线成型装置与所述支线工作部的通道上设置有第六流量控制机构。
  8. 如权利要求6所述的玻璃生产设备，其特征在于，所述第二支线生产线的数量有多条，多条所述第二支线生产线分别与所述分流通道连通。
  9. 如权利要求6～8中任一项所述的玻璃生产设备，其特征在于，所述主线成型装置包括浮法玻璃成型机构、溢流法玻璃成型机构、上拉法玻璃成型机构、压延法玻璃成型机构、平拉法玻璃成型机构以及模压法玻璃成型机构中的一种或多种；和/或，
    所述第一支线成型装置包括浮法玻璃成型机构、溢流法玻璃成型机构、上拉法玻璃成型机构、压延法玻璃成型机构、平拉法玻璃成型机构以及模压法玻璃成型机构中的一种或多种；和/或，
    所述第二支线成型装置包括浮法玻璃成型机构、溢流法玻璃成型机构、上 拉法玻璃成型机构、压延法玻璃成型机构、平拉法玻璃成型机构以及模压法玻璃成型机构中的一种或多种。
  10. 一种玻璃生产方法，其特征在于，使用如权利要求1～9中任一项所述的玻璃生产设备，所述玻璃生产方法包括以下步骤：
    在所述熔窑加入玻璃配合料，熔融形成玻璃液；
    使部分玻璃液输入所述主线生产线的主线工作部中，玻璃液在所述主线工作部中澄清均化后，输入所述主线成型装置，进行成型；
    使部分玻璃液通过分流通道输入所述第一支线生产线的合流装置中，在所述辅助熔炉中添加含有着色剂的玻璃色料和/或含有功能性助剂的玻璃辅料并熔化成玻璃液，使所述辅助熔炉中的玻璃液输入所述合流装置，与从所述分流通道输入的玻璃液进行混合，澄清均化后，输入所述第一支线成型装置，进行成型。
  11. 如权利要求10所述的玻璃生产方法，其特征在于，在所述熔窑中加入的玻璃配合料包括：SiO 254～78重量份、Al 2O 30.5～28重量份、B 2O 30～13.5重量份、P 2O 50～10重量份、Li 2O 0～9重量份、Na 2O 4～14重量份、K 2O 0～6重量份、MgO 0～7重量份、CaO 0～9.5重量份、SrO 0～4重量份、ZnO 0～4重量份、ZrO 20～4重量份、F 0～2重量份；和/或所述着色剂选自Fe、Cr、Co、Cu、Ni、Ti、Mn、Ce、Nd、Pr、Er、V、W的氧化物、Se粉中的一种或多种。
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