CN111875234A - Heating device for molten glass - Google Patents
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- CN111875234A CN111875234A CN202010915656.1A CN202010915656A CN111875234A CN 111875234 A CN111875234 A CN 111875234A CN 202010915656 A CN202010915656 A CN 202010915656A CN 111875234 A CN111875234 A CN 111875234A
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- 239000006060 molten glass Substances 0.000 title claims abstract description 41
- 238000010438 heat treatment Methods 0.000 title claims abstract description 36
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims abstract description 210
- 229910052697 platinum Inorganic materials 0.000 claims abstract description 105
- 238000001816 cooling Methods 0.000 claims description 15
- 230000003014 reinforcing effect Effects 0.000 claims description 11
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 8
- 239000000463 material Substances 0.000 claims description 7
- 229910052759 nickel Inorganic materials 0.000 claims description 4
- 230000005499 meniscus Effects 0.000 claims description 3
- 239000010970 precious metal Substances 0.000 claims description 3
- 229910000923 precious metal alloy Inorganic materials 0.000 claims description 3
- 239000002826 coolant Substances 0.000 claims description 2
- 239000011521 glass Substances 0.000 abstract description 19
- 239000007788 liquid Substances 0.000 abstract description 18
- 238000003756 stirring Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 5
- 230000003068 static effect Effects 0.000 abstract description 5
- 238000002791 soaking Methods 0.000 abstract 1
- 239000004020 conductor Substances 0.000 description 13
- 238000005485 electric heating Methods 0.000 description 7
- 238000005352 clarification Methods 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000012530 fluid Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 239000005388 borosilicate glass Substances 0.000 description 2
- 238000013021 overheating Methods 0.000 description 2
- PXXKQOPKNFECSZ-UHFFFAOYSA-N platinum rhodium Chemical compound [Rh].[Pt] PXXKQOPKNFECSZ-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 239000005361 soda-lime glass Substances 0.000 description 1
- 239000003351 stiffener Substances 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000000844 transformation Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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Classifications
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- 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
- 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
- C03B5/183—Stirring devices; Homogenisation using thermal means, e.g. for creating convection currents
- C03B5/185—Electric means
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Glass Melting And Manufacturing (AREA)
Abstract
Description
技术领域technical field
本发明涉及玻璃制造领域,特别涉及一种熔融玻璃的加热装置。The invention relates to the field of glass manufacturing, in particular to a heating device for molten glass.
背景技术Background technique
硼硅玻璃与普通的钠钙硅玻璃相比,其机械性能、热稳定性能、抗水性能、抗碱性能、抗酸性能等均大幅度提高,因此,其广泛用于航天、军事、化工、医药、消防、家电等多个行业,具有良好的应用价值和社会效益。Compared with ordinary soda-lime-silica glass, borosilicate glass has greatly improved mechanical properties, thermal stability, water resistance, alkali resistance, acid resistance, etc. Therefore, it is widely used in aerospace, military, chemical, It has good application value and social benefits in many industries such as medicine, fire protection, and home appliances.
其中,中性药用硼硅玻璃在生产过程中,通过包含各种工艺区段的铂金通道将熔融玻璃传送至成型装置中。为了确保熔融玻璃在工艺需求的温度曲线下运行,铂金通道的每个区段可通过在这些区段中施加电流来对铂金通道进行直接或间接加热,进而对其中的熔融玻璃进行加热,铂金通道的工艺区段包括但不限于澄清段、搅拌段及冷却段等。Among them, in the production process of neutral medicinal borosilicate glass, the molten glass is conveyed to the forming device through a platinum channel including various process sections. To ensure that the molten glass operates under the temperature profile required by the process, each section of the platinum channel can heat the molten glass within the platinum channel by applying an electrical current in these sections, directly or indirectly, to heat the molten glass within the platinum channel. The process section includes but is not limited to clarification section, stirring section and cooling section.
然而,铂金通道内的玻璃液由于重力的影响,在上下方向上成分不均一。同时,在现有的熔融玻璃加热装置中,电流更易流经铂金通道的上壁部分,流经铂金通道上壁部分的电流要大于流经铂金通道下壁部分的电流,在其他条件相同的情况下,铂金通道上壁产生的热量大于铂金通道下壁产生的热量。如此造成玻璃液在上下方向上受热不均一,进一步导致玻璃液在上下方向上的成分不均一。However, the glass liquid in the platinum channel is not uniform in composition in the up-down direction due to the influence of gravity. At the same time, in the existing molten glass heating device, the current is easier to flow through the upper wall of the platinum channel, and the current flowing through the upper wall of the platinum channel is larger than the current flowing through the lower wall of the platinum channel. Other conditions are the same. The heat generated by the upper wall of the platinum channel is greater than the heat generated by the lower wall of the platinum channel. In this way, the heating of the molten glass in the vertical direction is not uniform, which further leads to the non-uniform composition of the molten glass in the vertical direction.
发明内容SUMMARY OF THE INVENTION
本发明的主要目的是提供一种熔融玻璃的加热装置,旨在使铂金通道内的玻璃液达到均温均质的效果。The main purpose of the present invention is to provide a heating device for molten glass, which aims to make the glass liquid in the platinum channel achieve the effect of uniform temperature and homogeneity.
为实现上述目的,本发明提出了一种熔融玻璃的加热装置,具有沿竖直方向的对称线,包括:To achieve the above object, the present invention proposes a heating device for molten glass, with a line of symmetry along the vertical direction, comprising:
铂金通道,其壁厚在周向上发生变化;所述铂金通道的径向截面包括位于上方的第一圆弧以及位于下方的第二圆弧,所述第一圆弧和第二圆弧围合形成所述铂金通道的径向截面,所述第二圆弧的径向厚度大于所述第一圆弧的径向厚度,且所述第一圆弧和第二圆弧均沿所述对称线呈对称设置;The platinum channel, the wall thickness of which varies in the circumferential direction; the radial section of the platinum channel includes a first circular arc located above and a second circular arc located below, the first circular arc and the second circular arc enclosing A radial section of the platinum channel is formed, the radial thickness of the second circular arc is greater than the radial thickness of the first circular arc, and both the first circular arc and the second circular arc are along the symmetry line Symmetrical setup;
法兰,套设于所述铂金通道的外壁面并与所述铂金通道电接触,所述法兰包括内环及与所述内环周接的外环;所述内环包括位于上方的第一弧段和位于下方的第二弧段,所述第一弧段和第二弧段围合形成所述内环,所述第一弧段和第二弧段均沿所述对称线呈对称设置;所述第一弧段的轴向厚度小于所述第二弧段的轴向厚度;所述内环与所述铂金通道同心设置,所述外环在竖直方向上相对于所述铂金通道向上偏心设置。A flange is sleeved on the outer wall surface of the platinum channel and is in electrical contact with the platinum channel, the flange includes an inner ring and an outer ring peripherally connected to the inner ring; the inner ring includes a first ring located above an arc segment and a second arc segment located below, the first arc segment and the second arc segment enclose the inner ring, and the first arc segment and the second arc segment are symmetrical along the symmetry line The axial thickness of the first arc segment is smaller than the axial thickness of the second arc segment; the inner ring is arranged concentrically with the platinum channel, and the outer ring is vertically opposite to the platinum channel Channel up eccentric setting.
可选地,所述第二圆弧的径向截面面积为所述铂金通道的径向截面面积的30%~60%。Optionally, the radial cross-sectional area of the second arc is 30% to 60% of the radial cross-sectional area of the platinum channel.
可选地,所述第二弧段的轴向厚度为所述第一弧段的轴向厚度的1.2~3倍。Optionally, the axial thickness of the second arc segment is 1.2 to 3 times the axial thickness of the first arc segment.
可选地,所述外环的圆心相对于所述铂金通道的圆心向上的偏移量为所述铂金通道直径的10%~60%。Optionally, the upward offset of the center of the outer ring relative to the center of the platinum channel is 10% to 60% of the diameter of the platinum channel.
可选地,所述外环上开设有扼流孔,所述扼流孔沿所述对称线呈对称设置,所述扼流孔位于所述内环的上方。Optionally, the outer ring is provided with choke holes, the choke holes are symmetrically arranged along the symmetry line, and the choke holes are located above the inner ring.
可选地,所述扼流孔在径向截面上的形状为长条形、弯月形或者燕尾形。Optionally, the shape of the choke hole in the radial section is a long strip, a meniscus or a dovetail.
可选地,所述熔融玻璃的加热装置还包括冷却管,所述冷却管环绕设于所述外环上,且所述冷却管内通有冷却介质。Optionally, the heating device for molten glass further includes a cooling pipe, the cooling pipe is arranged around the outer ring, and a cooling medium passes through the cooling pipe.
可选地,所述熔融玻璃的加热装置还包括多个加强件,多个所述加强件沿所述铂金通道的长度方向间隔设于所述铂金通道顶部的内侧壁面上。Optionally, the heating device for molten glass further includes a plurality of reinforcing members, and the plurality of reinforcing members are arranged on the inner sidewall surface of the top of the platinum channel at intervals along the length direction of the platinum channel.
可选地,所述铂金通道的径向截面的形状为圆形、矩形、三角形、梯形、平行四边形、椭圆形或跑道形。Optionally, the shape of the radial section of the platinum channel is a circle, a rectangle, a triangle, a trapezoid, a parallelogram, an ellipse or a racetrack shape.
可选地,所述内环的材质为铂系贵金属或铂系贵金属合金;所述外环的材质为纯度至少为99wt%的镍。Optionally, the material of the inner ring is platinum-series precious metal or platinum-series precious metal alloy; the material of the outer ring is nickel with a purity of at least 99wt%.
本发明通过特殊设计,铂金通道的底部通过更多的电流,产生更多的热量,铂金通道底部的玻璃液被强烈加热后,产生了向上的玻璃液流,该玻璃液流到达铂金通道顶部后分别向左、向下及向右、向下流动,实现了“静态搅拌”的功能,玻璃液温度和成分的均匀性得以改善,从而使玻璃液达到均质均热的效果。Through the special design of the present invention, more current is passed through the bottom of the platinum channel to generate more heat. After the glass liquid at the bottom of the platinum channel is strongly heated, an upward glass liquid flow is generated. After the glass liquid flow reaches the top of the platinum channel Flowing to the left, down, right, and down, respectively, realizes the function of "static stirring", and the uniformity of the temperature and composition of the glass liquid is improved, so that the glass liquid can achieve the effect of homogeneous heating.
附图说明Description of drawings
为了更清楚地说明本发明实施例或示例性中的技术方案,下面将对实施例或示例性描述中所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图示出的获得其他的附图。In order to illustrate the technical solutions in the embodiments or exemplary embodiments of the present invention more clearly, the following briefly introduces the accompanying drawings used in the embodiments or exemplary descriptions. Obviously, the drawings in the following description are only the For some embodiments of the invention, for those of ordinary skill in the art, other drawings can also be obtained from those shown in these drawings without any creative effort.
图1为本发明实施例铂金通道的径向截面为圆形时熔融玻璃的加热装置的主视示意图;1 is a schematic front view of a heating device for molten glass when the radial cross section of the platinum channel according to the embodiment of the present invention is circular;
图2为图1的沿轴向的剖面结构示意图;Fig. 2 is the cross-sectional structure schematic diagram along the axial direction of Fig. 1;
图3~5为本发明铂金通道的径向截面为圆形时第二圆弧的三种实施方式示意图;3 to 5 are schematic diagrams of three embodiments of the second arc when the radial cross section of the platinum channel of the present invention is circular;
图6为本发明实施例铂金通道的径向截面为跑道形时熔融玻璃的加热装置的主视示意图;6 is a schematic front view of a heating device for molten glass when the radial section of the platinum channel according to the embodiment of the present invention is a racetrack shape;
图7~9为本发明铂金通道的径向截面为跑道形时第二圆弧的三种实施方式示意图;7 to 9 are schematic diagrams of three embodiments of the second arc when the radial section of the platinum channel of the present invention is a racetrack shape;
图10为本发明实施例铂金通道加强筋的安装示意图;FIG. 10 is a schematic diagram of the installation of a platinum channel stiffener according to an embodiment of the present invention;
图11为本发明实施例相邻两个电加热法兰与供电件的连接示意图。11 is a schematic diagram of the connection between two adjacent electric heating flanges and a power supply member according to an embodiment of the present invention.
附图标记说明:Description of reference numbers:
本发明目的的实现、功能特点及优点将结合实施例,参照附图做进一步说明。The realization, functional characteristics and advantages of the present invention will be further described with reference to the accompanying drawings in conjunction with the embodiments.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明的一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
需要说明,本发明实施例中所有方向性指示(诸如上、下、左、右、前、后……)仅用于解释在某一特定姿态(如附图所示)下各部件之间的相对位置关系、运动情况等,如果该特定姿态发生改变时,则该方向性指示也相应地随之改变。It should be noted that all directional indications (such as up, down, left, right, front, back, etc.) in the embodiments of the present invention are only used to explain the relationship between various components under a certain posture (as shown in the accompanying drawings). The relative positional relationship, the movement situation, etc., if the specific posture changes, the directional indication also changes accordingly.
另外,各个实施例之间的技术方案可以相互结合,但是必须是以本领域普通技术人员能够实现为基础,当技术方案的结合出现相互矛盾或无法实现时应当认为这种技术方案的结合不存在,也不在本发明要求的保护范围之内。In addition, the technical solutions between the various embodiments can be combined with each other, but must be based on the realization by those of ordinary skill in the art. When the combination of technical solutions is contradictory or cannot be realized, it should be considered that the combination of such technical solutions does not exist. , is not within the scope of protection required by the present invention.
如本文所用,术语“径向截面”是指当铂金通道被垂直于该铂金通道的纵轴的平面切割时形成的截面,除非另有规定。As used herein, the term "radial section" refers to the section formed when a platinum channel is cut by a plane perpendicular to the longitudinal axis of the platinum channel, unless otherwise specified.
本发明提供了一种熔融玻璃的加热装置。The present invention provides a heating device for molten glass.
在一实施例中,如图1~5所示,所述熔融玻璃的加热装置包括铂金通道10以及法兰20,其中,所述加热装置具有沿竖直方向的对称线Y,所述铂金通道10的壁厚在周向上发生变化,所述法兰20套设于所述铂金通道10的外壁面并与所述铂金通道10电接触。将交流电连接至所述法兰20,所述法兰20将电流传导给所述铂金通道10,所述铂金通道10作为电加热负载,进行电加热。所述法兰20包括内环21及与所述内环21周接的外环22,所述内环21与所述铂金通道10的外壁面电接触。所述外环22起到分配电流的作用,所述内环21起到将电流导入所述铂金通道10的作用。In one embodiment, as shown in FIGS. 1 to 5 , the heating device for molten glass includes a
其中,所述铂金通道10的径向截面包括位于上方的第一圆弧11以及位于下方的第二圆弧12,所述第一圆弧11和第二圆弧12围合形成所述铂金通道10的径向截面,所述第二圆弧12的径向厚度大于所述第一圆弧11的径向厚度,且所述第一圆弧11和第二圆弧12均沿所述对称线Y呈对称设置;所述内环21包括位于上方的第一弧段211和位于下方的第二弧段212,所述第一弧段211和第二弧段212围合形成所述内环21,所述第一弧段211和第二弧段212均沿所述对称线Y呈对称设置;所述第一弧段211的轴向厚度小于所述第二弧段212的轴向厚度;所述内环21与所述铂金通道10同心设置,所述外环22在竖直方向上相对于所述内环21向上偏心设置。Wherein, the radial section of the
根据导体电阻的计算公式:According to the calculation formula of conductor resistance:
R=ρ×L/S;R=ρ×L/S;
其中,ρ为导体的电阻率,L为导体的长度,S为导体的截面面积。Among them, ρ is the resistivity of the conductor, L is the length of the conductor, and S is the cross-sectional area of the conductor.
所述第二圆弧12的径向厚度大于所述第一圆弧11的径向厚度,即所述第二圆弧12的导电截面积比所述第一圆弧11的导电截面积大。根据导体电阻的计算公式,在其他条件相同的情况下,使得所述第二圆弧12的电阻小于所述第一圆弧11的电阻,即更厚的第二圆弧12相比于所述第一圆弧11具有更小的电阻。而由于所述第一圆弧11与所述第二圆弧12为并联设置,若施加一定的电压,根据欧姆定律,在电压一定的前提下,电阻越小,则电流越大,因此,流经所述第二圆弧12的电流大于流经所述第一圆弧11的电流。而根据W=UI,在电压一定的情况下,所述第二圆弧12产生的电加热功率大于所述第一圆弧11产生的的电加热功率,即所述铂金通道10底部的电加热功率要大于所述铂金通道10顶部的电加热功率。The radial thickness of the second
同理,所述第一弧段211的轴向厚度W1小于所述第二弧段212的轴向厚度W2,即所述第一弧段211的导电截面积比所述第二弧段212的导电截面积小。根据导体电阻的计算公式,在其他条件相同的情况下,所述第一弧段211的电阻大于所述第二弧段212的电阻。由于所述第一弧段211与所述第二弧段212为并联设置,若施加一定的电压,根据欧姆定律,在电压一定的前提下,电阻越小,则电流越大,因此,流经所述第二弧段212的电流大于流经所述第一弧段211的电流,而所述第二弧段212与所述第二圆弧12是电接触的,所述第二弧段212将较大的电流导入所述第二圆弧12,进一步增加了所述铂金通道10底部的电加热功率。Similarly, the axial thickness W1 of the
由于所述外环22在竖直方向上相对于所述铂金通道10向上偏心设置。所述外环22上部分的径向宽度H1大于所述外环22下部分的径向宽度H2。所述外环22的上部分具有和所述外环22的下部分相同的电阻率ρ及导电截面积S,根据导体电阻计算公式,由于所述外环22的上部分的径向宽度H1大于所述外环22的下部分的径向宽度H2,导致所述外环22的上部分通电导体长度L较大,因而所述外环22的上部分具有较大的电阻R。根据欧姆定理,所述外环22的上部分具有较大的电阻R,在同样的电压U下,将较小的电流通入所述铂金通道10顶部,将较大的电流通入所述铂金通道10底部,进一步增大所述铂金通道10底部的电加热功率。Because the
本发明通过特殊设计,所述铂金通道10的底部通过更多的电流,产生更多的热量,所述铂金通道10底部的玻璃液被强烈加热后,产生了向上的玻璃液流,该玻璃液流到达所述铂金通道10顶部后分别向左、向下及向右、向下流动(如图5所示,其中,图示中的箭头表示玻璃液的流动方向),实现了“静态搅拌”的功能,玻璃液温度和成分的均匀性得以改善,从而使玻璃液达到均质均热的效果。Through the special design of the present invention, more current passes through the bottom of the
同时,本发明在保证所述铂金通道10寿命的前提下,大大地提升了所述铂金通道10内流过的玻璃液温度和成分的均匀性。对于澄清段的所述铂金通道10,本发明有效地提升了在澄清段靠近底部中心位置处玻璃液的温度,同时加速了该处玻璃液中所含气态物质上浮及从玻璃液中排出的速度,极大地提升了澄清段对其内玻璃液的澄清效果。玻璃液在所述铂金通道10出口中心的温度,与玻璃液在所述铂金通道10出口液面处的温度温差小于或等于5℃。At the same time, the present invention greatly improves the uniformity of the temperature and composition of the glass liquid flowing in the
所谓“静态搅拌”,指的是在没有运动部件作用下流体在所述铂金通道10内部的运动。区别于传统的依靠运动部件进行搅拌,“静态搅拌”产生的原因是流体中存在不均温、不均质现象,致使流体的密度产生差异,不同密度间的流体在受热产生对流。The so-called "static stirring" refers to the movement of the fluid inside the
在本发明的一实施例中,所述第二圆弧12的径向截面面积为所述铂金通道10的径向截面面积的30%~60%,以使所述第二圆弧12处提供足够的热量。在所述第二圆弧12的径向截面面积占比过小时,所述第二圆弧12加厚不明显,所述第二圆弧12的电流增大不够明显;在所述第二圆弧12的径向截面面积占比过大时,比如,超过所述铂金通道10的径向截面面积的60%,会增加造成成本。In an embodiment of the present invention, the radial cross-sectional area of the
所述第二圆弧12的具体形式不做限制,只要满足所述第二圆弧12的径向厚度大于所述第一圆弧11的径向厚度,且所述第二圆弧12沿所述对称线呈对称设置。The specific form of the
具体地,在本发明的一实施例中,所述第二圆弧12可以均匀加厚,如图3和4和7所示,均匀加厚的制造工艺简单。在其他实施例中,所述第二圆弧可以不均匀加厚。如图5和8所示,所述第二圆弧12包括连续的第一壁部分121以及第二壁部分122,所述第一壁部分121位于所述第二圆弧12的中心,所述第二壁部分122包括两个,两个所述第二壁部分122分别位于所述第一壁部分121的两侧,且所述第一壁部分121的径向厚度大于所述第二壁部分122的径向厚度,所述第二壁部分122的径向厚度大于所述第一圆弧11的径向厚度。Specifically, in an embodiment of the present invention, the
作为一个可选的实施例,如图9所示,所述第二圆弧12还包括第三壁部分123,所述第三壁部分123设于所述第一壁部分121与所述第二壁部分122之间,且所述第三壁部分123的径向厚度小于所述第一壁部分121的径向厚度,所述第三壁部分123的径向厚度大于所述第二壁部分122的径向厚度。即所述第三壁部分123为所述第一壁部分121与所述第二壁部分122之间的过渡段,其径向厚度处于所述第一壁部分121的径向厚度与所述第二壁部分122的径向厚度之间,以避免从较厚的所述第一壁部分121直接减小到较薄的所述第二壁部分122,防止所述第二圆弧12温度向两侧骤减。As an optional embodiment, as shown in FIG. 9 , the
在本发明的一实施例中,如图1-5所示,所述铂金通道的径向截面的形状为圆形;在本发明的另一实施例中所述铂金通道的径向截面的形状为跑道形,如图6-9所示,该跑道形由两条平行直线和两个半圆形拼接形成。圆形和跑道形因其侧壁是连续的弧形,方便玻璃液流动。在其他实施例中,所述铂金通道的径向截面形状还可以为其他形状,比如:矩形、三角形、梯形、平行四边形或椭圆形等,在此并不限定。In an embodiment of the present invention, as shown in FIGS. 1-5 , the shape of the radial section of the platinum channel is a circle; in another embodiment of the present invention, the shape of the radial section of the platinum channel is It is a racetrack shape, as shown in Figure 6-9, the racetrack shape is formed by splicing two parallel straight lines and two semicircles. The circular and racetrack shapes facilitate the flow of glass liquid due to the continuous arc of the side walls. In other embodiments, the radial cross-sectional shape of the platinum channel may also be other shapes, such as a rectangle, a triangle, a trapezoid, a parallelogram, or an ellipse, which is not limited herein.
可选地,所述内环21的材质为铂系贵金属(如纯铂)或铂系贵金属合金(如铂铑10wt%或铂铑20wt%);所述外环22为纯度至少为99wt%的镍。当然,在其他实施例中,所述内环21和所述外环22还可以采用其他材质进行制备,在此并不限定。Optionally, the material of the
在本发明的一实施例中,如图2所示,所述第二弧段212的轴向厚度W2为所述第一弧段211的轴向厚度W1的1.2~3倍,以使所述第二弧段212能够分得足够大的电流,然后导入所述第二圆弧12,即所述铂金通道10的底部。在所述第二弧段212的轴向厚度W2小于所述第一弧段211的轴向厚度W1的1.2倍,则可能造成所述铂金通道10底部(即第二圆弧12)加热不明显的后果;在所述第二弧段212的轴向厚度W2大于所述第一弧段211的轴向厚度W1的3倍,则可能造成所述铂金通道10底部(即第二圆弧12)过热的后果,同时也会造成制造成本的增加。In an embodiment of the present invention, as shown in FIG. 2 , the axial thickness W2 of the
在本发明的一实施例中,如图1和6所示,所述外环22的圆心相对于所述铂金通道10的圆心向上的偏移量为所述铂金通道10直径的10%~60%,以使所述外环22的下方获得更多的电流。在所述外环22的圆心相对于所述铂金通道10的圆心向上的偏移量超过所述铂金通道10直径的60%,则可能造成所述铂金通道10底部(即第二圆弧12)过热的后果,而在所述外环22的圆心相对于所述铂金通道10的圆心向上的偏移量不足所述铂金通道10直径的10%,则可能造成所述铂金通道10底部(即第二圆弧12)加热不明显的后果。In an embodiment of the present invention, as shown in FIGS. 1 and 6 , the upward offset of the center of the
在本发明的一实施例中,如图1和6所示,所述外环22上开设有扼流孔23,所述扼流孔23沿所述对称线Y呈对称设置,所述扼流孔23位于所述内环21的上方。在所述外环22上方设置的扼流孔23,用于阻断了沿所述外环22上方中心位置直接传递至所述第一弧段211的电流。即本实施例中通过设置扼流孔23,使得所述外环22上方传递至所述第一弧段211的交流电绕行,即增加了电流的流通路线,以间接增加导体的长度,即根据导体电阻计算公式(如上描述),从所述扼流孔23的左、右侧绕行的所述外环22上方的导体电阻R,具有比未加装所述扼流孔23时更大的通电导体的长度,使得所述外环22上方的电阻值加大。根据欧姆定理,所述外环22上部的电阻大于所述外环22下部的电阻,使得所述第二弧段212分配得到的电流大于所述第一弧段211分配得到的电流,并由所述第二弧段212将更多的电流通入至所述第二圆弧12处,使所述第二圆弧12处获得更多的电加热功率,从而增加所述第二圆弧12处的温度。In an embodiment of the present invention, as shown in FIGS. 1 and 6 , the
可选地,所述扼流孔23的形状为在径向截面上的形状为长条形、弯月形或者燕尾形。当然,在其他实施例中,所述扼流孔23还可以设置为其他形状,在此并不对此进行限定。Optionally, the shape of the
进一步地,继续参照图1和6所示,所述法兰20还包括与法兰20电接触的电极24,并起到通过线缆、汇流条(buss bar)或其它电导体将法兰20连接至电源的作用。Further, with continued reference to FIGS. 1 and 6 , the
进一步地,如图1和2所示,所述熔融玻璃的加热装置还包括冷却管30,所述冷却管3环绕设置在所述外环22的外侧,以对所述法兰20进行冷却,防止所述法兰20温度较高而导致所述法兰20损耗。所述冷却管30中通有冷却水或压缩空气。或者,所述冷却管30内通有其他冷却物质,在此并不限定。Further, as shown in FIGS. 1 and 2 , the heating device for molten glass further includes a cooling
可选地,所述冷却管30由铜或者镍制成。或者,所述冷却管30还可以为其他材料制成,在此并不限定。Optionally, the cooling
进一步地,如图10所示,所述熔融玻璃的加热装置还包括多个加强件40,多个所述加强件40沿所述铂金通道10的长度方向间隔设于所述铂金通道10顶部的内侧壁面上,用于防止所述铂金通道10的管壁塌陷。Further, as shown in FIG. 10 , the heating device for molten glass further includes a plurality of reinforcing
可选地,所述加强件40为加强筋,加强筋的宽度为5mm~20mm,加强筋的厚度为0.5mm~1.5mm,且加强筋的间隔距离为200mm~500mm。Optionally, the reinforcing
具体地,如图11所示,所述法兰20包括多个,所述熔融玻璃的加热装置还包括供电件50,所述供电件50的两端分别连接于相邻两个所述法兰20的电流接入引出端24上,以对相邻两个所述法兰20之间的所述铂金通道10(比如澄清段的容器)进行加热。即所述供电件50、相邻两个所述法兰20、所述铂金通道10形成加热回路。Specifically, as shown in FIG. 11 , the
以上所述仅为本发明的可选实施例,并非因此限制本发明的专利范围,凡是在本发明的构思下,利用本发明说明书及附图内容所作的等效变换,或直接/间接运用在其他相关的技术领域均包括在本发明的专利保护范围内。The above descriptions are only optional embodiments of the present invention, and are not intended to limit the scope of the present invention. All under the concept of the present invention, the equivalent transformations made by the contents of the description and drawings of the present invention, or directly/indirectly applied in Other related technical fields are included within the scope of patent protection of the present invention.
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