JP2005041754A - Method for manufacturing foamed glass - Google Patents
Method for manufacturing foamed glass Download PDFInfo
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- JP2005041754A JP2005041754A JP2003280035A JP2003280035A JP2005041754A JP 2005041754 A JP2005041754 A JP 2005041754A JP 2003280035 A JP2003280035 A JP 2003280035A JP 2003280035 A JP2003280035 A JP 2003280035A JP 2005041754 A JP2005041754 A JP 2005041754A
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- dolomite
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- 239000011521 glass Substances 0.000 title claims abstract description 112
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 19
- 238000000034 method Methods 0.000 title description 5
- 239000004088 foaming agent Substances 0.000 claims abstract description 39
- 239000010459 dolomite Substances 0.000 claims abstract description 27
- 229910000514 dolomite Inorganic materials 0.000 claims abstract description 27
- 239000000843 powder Substances 0.000 claims abstract description 26
- 239000000203 mixture Substances 0.000 claims abstract description 6
- 238000002156 mixing Methods 0.000 claims abstract description 5
- 238000010438 heat treatment Methods 0.000 claims description 29
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 18
- 239000002699 waste material Substances 0.000 claims description 11
- 229910021538 borax Inorganic materials 0.000 claims description 10
- 239000004328 sodium tetraborate Substances 0.000 claims description 10
- 235000010339 sodium tetraborate Nutrition 0.000 claims description 10
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 9
- 239000011494 foam glass Substances 0.000 claims description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 229910052799 carbon Inorganic materials 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 4
- 238000010298 pulverizing process Methods 0.000 claims description 4
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 claims description 4
- 229910010271 silicon carbide Inorganic materials 0.000 claims description 4
- 238000005507 spraying Methods 0.000 claims description 2
- 238000007654 immersion Methods 0.000 claims 1
- 238000010791 quenching Methods 0.000 claims 1
- 230000000171 quenching effect Effects 0.000 claims 1
- 239000002994 raw material Substances 0.000 abstract description 8
- 239000000654 additive Substances 0.000 abstract description 6
- 238000010304 firing Methods 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 2
- 238000005187 foaming Methods 0.000 description 13
- 239000002562 thickening agent Substances 0.000 description 8
- 238000000354 decomposition reaction Methods 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 230000005484 gravity Effects 0.000 description 5
- 239000002245 particle Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000006260 foam Substances 0.000 description 3
- 230000000630 rising effect Effects 0.000 description 3
- 239000005361 soda-lime glass Substances 0.000 description 3
- 239000002689 soil Substances 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 239000004604 Blowing Agent Substances 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000009933 burial Methods 0.000 description 1
- HHSPVTKDOHQBKF-UHFFFAOYSA-J calcium;magnesium;dicarbonate Chemical compound [Mg+2].[Ca+2].[O-]C([O-])=O.[O-]C([O-])=O HHSPVTKDOHQBKF-UHFFFAOYSA-J 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000006063 cullet Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 238000003892 spreading Methods 0.000 description 1
Classifications
-
- 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
- C03C11/00—Multi-cellular glass ; Porous or hollow glass or glass particles
- C03C11/007—Foam glass, e.g. obtained by incorporating a blowing agent and heating
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Glass Compositions (AREA)
Abstract
Description
本発明は、主として廃ガラスを使用して、土壌改良、路盤埋設、屋上緑化などに使用することのできる比較的軽量の発泡ガラスを製造する技術に関する。 The present invention relates to a technique for producing a relatively lightweight foam glass that can be used for soil improvement, roadbed burying, rooftop greening, etc., mainly using waste glass.
廃ガラス、特に着色瓶ガラスは着色材料が瓶によって異なり、それらの分別が困難なことから、特定のものを除いては瓶ガラスあるいはガラスとしての再生が困難であり、多くは土中埋設されていた。最近に至り、このようなガラスを発泡化してその比重を0.2から1.2程度まで小さくするとともに、ガラス成分の溶出が生じないようにして、斜面処理、緑化、路盤処理、埋設、土壌改良あるいは屋上緑化などに使用することが提案されるようになっている。 Waste glass, especially colored bottle glass, is difficult to recycle as bottle glass or glass except for certain ones because the coloring materials differ depending on the bottle and it is difficult to separate them. It was. Recently, such glass has been foamed to reduce its specific gravity from about 0.2 to 1.2, and the glass components are not eluted, so that slope treatment, greening, roadbed treatment, burial, soil It has been proposed to use it for improvement or rooftop greening.
このような発泡ガラスとしては「ミラクルソル(商品名)」、「スーパーソル(商品名)」などと呼ばれるものが代表的であり、これを利用した工法とともに広がりつつある。これらの工法に使用する発泡ガラスは瓶ガラスなどを原料として、それを粉砕した後、発泡剤として、炭酸カルシウム、炭素、炭化珪素、硼砂などを最低でも2種類、通常は、数種類組み合わせて添加し、昇温時のガラスの軟化に合わせてこれらの発泡剤の分解、ガス発生を行わせ、それをガラス中にトラップするようにして製造されている。 As such foamed glass, those called “miracle sol (trade name)”, “super sol (trade name)” and the like are typical, and they are spreading along with a construction method using this. Foamed glass used in these methods is made from bottle glass as a raw material, pulverized, and then added as a foaming agent with at least two types of calcium carbonate, carbon, silicon carbide, borax, etc., usually a combination of several types. These foaming agents are decomposed and gas is generated in accordance with the softening of the glass when the temperature is raised, and the glass is trapped in the glass.
この場合の製造条件は、例えば、特許文献1に示されているように、ガラス粉末に、炭酸カルシウム、炭化珪素及び増粘剤としての硼砂を加え、加熱炉を用いて室温から約1000℃まで1時間程度で加熱し、ガラスが融体化した時点で、炭化珪素の分解による発泡ならびに炭酸カルシウムの分解による発泡を行わせるとともに、増粘剤である硼砂によって粘性を高めておき、これらの発泡した気泡をガラスの中に保持して発泡ガラスを形成した後、加熱炉から取り出して急冷したり、あるいは加熱炉から取り出すとともに水を噴霧するなどして急冷したりすることによって発泡ガラスを得るようにしている。 The manufacturing conditions in this case are, for example, as shown in Patent Document 1, adding calcium carbonate, silicon carbide and borax as a thickener to glass powder, and using a heating furnace from room temperature to about 1000 ° C. When the glass is melted by heating for about 1 hour, foaming by decomposition of silicon carbide and foaming by decomposition of calcium carbonate are performed, and viscosity is increased by borax as a thickener, and these foams are formed. After forming the foamed glass by holding the bubbles in the glass, it is taken out from the heating furnace and rapidly cooled, or it is taken out from the heating furnace and sprayed with water to obtain the foamed glass. I have to.
このようにして製造される発泡ガラスに内在する気泡には、良く知られるように、連続気泡と単独気泡との2種類があるが、これらのうちのどちらの気泡を形成するかについては、発泡剤の選択と加熱条件とによって選択するようにしている。このほか、発泡ガラスの製造についてはいくつかの条件が提案されているが、いずれも、炭酸カルシウムあるいは炭素を主体として数種類の発泡剤を組み合わせることが行われている。 As is well known, there are two types of bubbles in the foamed glass produced in this way: open cells and single cells. Which of these bubbles is formed is determined by foaming. The selection is made according to the selection of the agent and the heating conditions. In addition, several conditions have been proposed for the production of foamed glass, and in any case, several kinds of foaming agents are combined mainly with calcium carbonate or carbon.
主体となる発泡反応を炭酸カルシウムで行う場合には、炭酸カルシウムの分解温度が900℃であるので、それより高い温度、通常は950℃以上が必要であった。また、炭素紛を発泡剤として使用した場合、800℃程度から連続的に発泡していくが、この場合、炭素はガラス中の酸化物の酸素を一部取り入れながらCO2となって発泡剤として働く。しかしながら、この反応は必ずしも完全ではないため、炭素がガラス内部に残ってしまい黒色に着色することがあり、また、必ずしも発泡性が良いとは言えないので、他の発泡条件との組み合わせが必要である。 In the case where the main foaming reaction is performed with calcium carbonate, the decomposition temperature of calcium carbonate is 900 ° C., and therefore a higher temperature, usually 950 ° C. or higher, is necessary. In addition, when carbon powder is used as a foaming agent, it continuously foams from about 800 ° C., but in this case, carbon becomes CO 2 while partially taking in oxygen of the oxide in the glass as a foaming agent. work. However, since this reaction is not always complete, carbon may remain inside the glass and may be colored black, and it may not be said that foamability is always good, so a combination with other foaming conditions is necessary. is there.
従来の発泡ガラス製造方法においては、前述したように、最終加熱温度が一般に950℃以上と高いので、このような高温度においては、瓶ガラスなどのいわゆるソーダガラス、ソーダ石灰ガラスではどうしても粘性が低くなりすぎ、気泡の保持が困難となる。そこで、特殊な条件以外においては、一般に増粘剤を加える必要があった。この場合、通常、硼砂が増粘剤として加えられるが、硝種に依ってはこれだけでは不十分であり、これらの組み合わせでは、発泡ガラスが得られないこともあった。 In the conventional method for producing foamed glass, as described above, the final heating temperature is generally as high as 950 ° C. or higher. Therefore, at such a high temperature, so-called soda glass such as bottle glass and soda lime glass are inevitably low in viscosity. It becomes too much and it becomes difficult to hold bubbles. Therefore, it was generally necessary to add a thickener except under special conditions. In this case, borax is usually added as a thickener, but this alone is insufficient depending on the type of glass, and foam glass may not be obtained with these combinations.
即ち、主な発泡反応は炭酸カルシウムによっているが、その分解温度が900℃であるため、焼成工程における加熱温度は950℃以上とすることが必要であり、通常の硝種に対しても増粘剤が必須となる。また、他の発泡剤を加えるなど、複数の成分を加えることが必要であり、さらに、その調整にも手間取るだけでなく、高価な硼砂を加えなければならないという問題点もあった。また、焼成温度が高いということは余分なエネルギーを消費するという問題点も併せ持っていた。 That is, the main foaming reaction depends on calcium carbonate, but its decomposition temperature is 900 ° C., so the heating temperature in the firing step needs to be 950 ° C. or higher, and it is also a thickener for ordinary glass types. Is essential. In addition, it is necessary to add a plurality of components such as adding other foaming agents. Furthermore, there is a problem that not only the adjustment is required, but also expensive borax must be added. In addition, the high firing temperature also has the problem of consuming excess energy.
一方、蛍光灯などの管球ガラスの場合は瓶ガラスよりソーダ分が3%程度多いので、軟化温度が30℃程度低下するだけでなく、軟化温度以上では急激に粘性が低下するため硼砂を加えてもほとんど気泡の保持ができず、実質的に発泡ガラス、特に連続気泡を有する発泡ガラスの製造はほとんど不可能であった。また、炭素を主発泡剤として使った場合、最高温度900℃程度でも発泡が得られにくいという問題があった。 On the other hand, in the case of tube glass such as fluorescent lamps, the soda content is about 3% higher than that of bottle glass, so not only does the softening temperature decrease by about 30 ° C, but the viscosity decreases rapidly above the softening temperature, so borax is added. However, it was almost impossible to produce foamed glass, especially foamed glass having open cells. Further, when carbon is used as a main foaming agent, there is a problem that foaming is hardly obtained even at a maximum temperature of about 900 ° C.
本発明はこのような問題点を解決するためになされたものであり、添加物を簡素化するとともに焼成最高温度を低下することによって容易に発泡ガラスを製造することができ、しかもエネルギー消費量を削減できるように発泡剤とその製造条件を見出すこと、また、従来非常に困難であった管球ガラスを原料とした発泡ガラスの製造を可能とすることを課題とする。 The present invention has been made in order to solve such problems, and it is possible to easily produce foamed glass by simplifying the additive and lowering the maximum firing temperature, and reducing the energy consumption. It is an object of the present invention to find a foaming agent and its production conditions so that it can be reduced, and to make it possible to produce foamed glass from tube glass that has been very difficult in the past.
本発明の発泡ガラス製造方法は、ガラス粉末に対し、主としてドロマイト粉末から成る発泡剤を前記ガラス粉末の重量の1重量%〜5重量%混合して形成した混合物を30分〜60分かけて室温から800℃〜920℃まで加熱し、しかる後に急冷することを特徴とする。発泡剤はドロマイト粉末からなる発泡剤あるいはドロマイト単味でも良いので、添加物が非常に簡略化されるとともに、加熱温度を従来の製造方法に比較して50℃〜100℃低下させることができ、省エネルギー化を達成することができる。 The method for producing foamed glass of the present invention comprises a mixture formed by mixing 1% by weight to 5% by weight of the weight of the glass powder with a foaming agent mainly composed of dolomite powder with respect to the glass powder at room temperature over 30 to 60 minutes. To 800 ° C. to 920 ° C. and then cooled rapidly. Since the foaming agent may be a foaming agent made of dolomite powder or a simple dolomite, the additive can be greatly simplified, and the heating temperature can be reduced by 50 ° C. to 100 ° C. compared to the conventional production method, Energy saving can be achieved.
これは、ドロマイトの分解温度が初期730℃〜760℃であるとともに、一部はさらに高温である850℃で分解すること、また、瓶ガラスの場合はガラスの軟化温度である730℃より50℃〜100℃程度高い温度から液体化するが、それからさらに50℃〜100℃程度は比較的粘性が高く保持されること、また、管球ガラスの場合は軟化温度が瓶ガラスより30℃程度低いが、液状化した後の同じ粘度に対する温度は瓶ガラスより約100℃低いことを見出し、それらがドロマイトの発泡条件でカバーできることを知見して本発明をなすに至ったものである。 This is because the decomposition temperature of dolomite is 730 ° C. to 760 ° C. at the initial stage, and partly decomposes at 850 ° C., which is a higher temperature. Although it is liquefied from a temperature as high as ˜100 ° C., the viscosity is further maintained at a relatively high temperature of 50 ° C. to 100 ° C. The present inventors have found that the temperature for the same viscosity after liquefaction is about 100 ° C. lower than that of the bottle glass, and found that they can be covered with the foaming conditions of dolomite.
以下、詳細に説明する。前述したように、ドロマイト(CaMg(CO3)2)は730℃〜760℃で分解してCO2を発生する、つまり発泡するが、この分解反応の一部が850℃で起こることが判明した。このときに通常使用される発泡ガラス原料であるソーダ石灰ガラスのうちの瓶ガラスは、その軟化温度が前述したように730℃であるが、実際にガラス内部で発泡が起こるような比較的粘度の低い状態となるためには、さらに50℃〜100℃程度の高い温度が必要であることが判っている。 Details will be described below. As described above, it has been found that dolomite (CaMg (CO 3 ) 2 ) decomposes at 730 ° C. to 760 ° C. to generate CO 2 , that is, foams, but a part of this decomposition reaction occurs at 850 ° C. . The bottle glass of the soda-lime glass that is a foam glass raw material that is usually used at this time has a softening temperature of 730 ° C. as described above, but has a relatively high viscosity so that foaming actually occurs inside the glass. It has been found that a higher temperature of about 50 ° C. to 100 ° C. is necessary to achieve a low state.
また、瓶ガラスの場合は内部に発泡状態を残せる程度、つまり800℃程度から若干高い温度で発泡し、しかもそのときのガラス内部に気泡を残せる程度に粘性の高い状態はさらに50℃〜100℃程度高い温度、つまりほぼ900℃まで保持される。したがって、この温度範囲で適正に発泡が起こるような発泡剤を使用すれば発泡化ガラスを形成することができる。 Further, in the case of bottle glass, the foamed state can be left in the inside, that is, foamed at a slightly higher temperature from about 800 ° C., and the viscosity is high enough to leave bubbles in the glass at that time, further 50 ° C. to 100 ° C. The temperature is maintained at a relatively high temperature, that is, approximately 900 ° C. Therefore, if a foaming agent that causes foaming properly in this temperature range is used, foamed glass can be formed.
さらに、これに適合する単味の発泡剤が存在すれば、従来のように、いくつかの発泡剤あるいは増粘剤の組み合わせによる複雑な添加物を使わなくても、目的とする発泡化ガラスを形成することができるはずである。そこで、本発明者が、この様な条件下で発泡剤が存在する可能性を検討したところ、前述したようなドロマイトが最も合目的であることが判明した。 Furthermore, if there is a simple foaming agent that meets this requirement, the target foamed glass can be obtained without using complex additives such as a combination of several foaming agents or thickeners. Should be able to form. Then, when this inventor examined the possibility that a foaming agent exists under such conditions, it turned out that the above-mentioned dolomite is the most suitable purpose.
また、廃蛍光管などの管球ガラスの場合、同じソーダ石灰ガラスではあるがアルカリ分が約3%高いのでガラス軟化点は700℃であり、30℃程度低い。さらに、この場合は粘性の低下が急激であり、しかも低い温度で粘性の低下が生じ、瓶ガラスに比較して同じ粘性範囲を有する温度は730℃〜830℃程度である。この場合もドロマイトを使えば適正な温度範囲において気泡が起こることがわかる。 In the case of a tube glass such as a waste fluorescent tube, the soda-lime glass is the same, but the alkali content is about 3% higher, so the glass softening point is 700 ° C., which is about 30 ° C. lower. Further, in this case, the viscosity is drastically reduced, and the viscosity is lowered at a low temperature. The temperature having the same viscosity range as that of the bottle glass is about 730 ° C to 830 ° C. Also in this case, it can be seen that bubbles are generated in an appropriate temperature range if dolomite is used.
これらのことにより、廃ガラスから発泡ガラスを製造するにあたっては、その最大の供給源である、瓶ガラス、電球ガラスともにドロマイト単味を発泡剤として使用することによって、従来方法に従って発泡ガラスを製造することができることが分かる。 For these reasons, when producing foamed glass from waste glass, both the bottle glass and bulb glass, which are the largest supply sources, produce foamed glass according to conventional methods by using dolomite as a foaming agent. I can see that
発泡ガラスは、必要に応じて、連続気泡あるいは単独気泡の選択が行われるが、このために、発泡剤をドロマイト単味として、加熱並びに温度条件を選択するようにしても良いが、主発泡剤をドロマイトとするものの、わずかな量の他の発泡剤と組み合わせることができることは言うまでもない。 For foamed glass, open cells or single cells are selected as necessary. For this purpose, the foaming agent may be a simple dolomite, and heating and temperature conditions may be selected. Of course, it can be combined with a small amount of other blowing agents.
例えば、瓶ガラスの場合、破砕して、金属分などを除去した後、粒度40μm程度に粉砕する。これに、発泡剤としてドロマイト粉末を2.5重量%〜5重量%程度添加して、十分に混合する。または、ガラス粉砕の際にドロマイト粉末を加えて同時に粉砕を行っても良い。そして、加熱炉のベルトコンベア上に、十分に混合した原料を厚さ20mm程度に敷き詰め、室温から約900℃まで連続的に30分〜60分かけて温度を上昇させていき、900℃に到達した後は同じ温度で保持することなく直ちに炉外に出すか、あるいは水を噴霧して急冷する。これによって単独気泡を有する発泡ガラスを製造することができる。 For example, in the case of bottle glass, it is crushed to remove metal and the like and then pulverized to a particle size of about 40 μm. To this, about 2.5 wt% to 5 wt% of dolomite powder as a foaming agent is added and mixed well. Alternatively, dolomite powder may be added and pulverized at the same time during glass pulverization. Then, spread the fully mixed raw material on the belt conveyor of the heating furnace to a thickness of about 20 mm, and continuously increase the temperature from room temperature to about 900 ° C. over 30 to 60 minutes, reaching 900 ° C. After that, it is immediately put out of the furnace without being kept at the same temperature, or it is rapidly cooled by spraying water. This makes it possible to produce foamed glass having single cells.
この場合、前記加熱工程において、加熱温度をわずかに下げ、その温度で3分ほど保持した後急冷すれば連続気泡を有する発泡ガラスを製造することができる。また、発泡剤として2.5重量%〜5重量%のドロマイトに加え、さらに0.5重量%程度の硼砂を増粘剤として加えると、初期の条件のままでも連続気泡とすることが可能である。 In this case, in the heating step, if the heating temperature is slightly lowered, held at that temperature for about 3 minutes and then rapidly cooled, foamed glass having open cells can be produced. Moreover, in addition to 2.5% to 5% by weight of dolomite as a foaming agent, and further adding about 0.5% by weight of borax as a thickener, it is possible to form open cells even under the initial conditions. is there.
一方、廃蛍光管や廃電球などの管球ガラスを原料とする場合、前処理は瓶ガラスの場合と同様の工程で粉砕し、発泡剤としてドロマイトを混合して原料ガラスとし、これを瓶ガラスの場合と同様にして同条件で加熱を行っていく。ただし、電球ガラスの場合は粘性が低くなりやすいので、最高温度は800℃程度にする。これによってドロマイトの分解によるガスをガラス中に保持するか、あるいは気泡の通過跡をガラス中に残すことによって発泡ガラスを形成することができる。 On the other hand, when tube glass such as a waste fluorescent tube or a light bulb is used as a raw material, the pretreatment is pulverized in the same process as in the case of bottle glass, and dolomite is mixed as a foaming agent to form raw glass, which is used as bottle glass. Heating is performed under the same conditions as in. However, in the case of bulb glass, the viscosity tends to be low, so the maximum temperature is about 800 ° C. Thereby, it is possible to form the foamed glass by keeping the gas generated by the decomposition of dolomite in the glass or by leaving the passage of bubbles in the glass.
そして、発泡後は速やかにガラスを固化させる必要があるので、大気中に取り出して、そのままあるいは冷風を送って冷却する、または大気中に取り出してすぐに水を噴射するなどして急冷することによって発泡状態を保持し、発泡ガラスを製造することができる。 And since it is necessary to solidify the glass immediately after foaming, it is taken out into the atmosphere and cooled as it is or by sending cold air, or it is taken out into the atmosphere and immediately cooled by jetting water. The foamed state can be maintained and foamed glass can be produced.
なお、使用する加熱炉その他の設備に関しては特には限定されないが、連続的な加熱プロセスが重要であるので、バッチ式加熱炉を使用する場合は、昇温速度が速くしかも安定に温度保持のできるものであることが望ましい。また、連続式加熱炉の場合は最高温度が900℃〜1000℃程度まで加熱できる機能を有するものであることが望ましい。 In addition, although it does not specifically limit regarding the heating furnace and other equipment to be used, since a continuous heating process is important, when using a batch-type heating furnace, the temperature rising rate is fast and the temperature can be stably maintained. It is desirable to be a thing. Moreover, in the case of a continuous heating furnace, it is desirable that the maximum temperature has a function capable of heating up to about 900 ° C to 1000 ° C.
ここで、添加する発泡剤の量はガラス粉末の重量の1重量%〜7重量%とすることが望ましく、発泡化するガラスの硝種によっても異なるが、特に、2.5重量%〜5重量%とすることが望ましい。1重量%未満では発泡が不十分となり、6重量%以上では急激な発泡により生成ガラスの発泡状態が不均一になることがある。言うまでもないが、主発泡剤はドロマイトであり、単味でも良く、目的によっては他の発泡剤や、増粘剤としての硼砂などの添加剤を加えることができる。 Here, the amount of the foaming agent to be added is preferably 1% by weight to 7% by weight of the weight of the glass powder, and varies depending on the glass type of the glass to be foamed. Is desirable. If it is less than 1% by weight, foaming may be insufficient, and if it is 6% by weight or more, the foamed state of the resulting glass may become uneven due to rapid foaming. Needless to say, the main foaming agent is dolomite and may be simple, and other foaming agents and additives such as borax as a thickener can be added depending on the purpose.
本発明により以下の効果が認められた。 The following effects were recognized by the present invention.
(1)わずかに温度条件を変え、発泡剤としてドロマイト単味を使用することによって発泡ガラスが製造できることが分かった。 (1) It was found that foam glass can be produced by slightly changing the temperature conditions and using dolomite plain as the foaming agent.
(2)発泡剤としてドロマイトを主としてわずかに他の発泡剤を加えることにより加熱温度条件を同じにしても気泡の状態を変えることができた。 (2) By adding a little other foaming agent mainly as a foaming agent, the state of the bubbles could be changed even if the heating temperature conditions were the same.
(3)従来使用されていた炭酸カルシウムを主とする発泡剤に比較して、50℃〜100℃程度低い温度で発泡ガラスを得ることができ、省エネルギーを図ることができた。 (3) Compared with conventionally used foaming agents mainly composed of calcium carbonate, it was possible to obtain foamed glass at a temperature lower by about 50 ° C. to 100 ° C., and to save energy.
(4)従来は高耐熱性の高価なステンレススチールを一部使用した加熱炉が必要であったが、920℃以下の温度で製造可能となったので、炉材として使用する材料の低価格化を図ることができるようになった。 (4) Previously, a heating furnace using a part of high heat-resistant expensive stainless steel was required, but since it became possible to manufacture at a temperature of 920 ° C or less, the price of the material used as the furnace material was reduced. It became possible to plan.
(5)発泡剤を簡素化するとともに、安価にすることができた。 (5) The foaming agent can be simplified and made inexpensive.
(6)ドロマイトを発泡剤とし、加熱温度を下げることによって、従来は困難とされていた廃蛍光灯などの管球ガラスを用いて発泡ガラスを容易に作れるようになった。 (6) By using dolomite as a foaming agent and lowering the heating temperature, it has become possible to easily produce foamed glass using tube glass such as waste fluorescent lamp, which has been considered difficult in the past.
(7)発泡剤はドロマイトの単味で良く、この場合はガラスとの混合が容易になるとともに、わずかなその他の添加剤により、気泡の状態を制御することができるようになった。 (7) The foaming agent may be a simple dolomite. In this case, mixing with glass becomes easy, and the state of bubbles can be controlled with a few other additives.
以下、本発明の実施例について説明するが、本発明に係る発泡ガラス製造方法はこれらの実施例に制限されないことは言うまでもない。 Examples of the present invention will be described below, but it goes without saying that the method for producing foam glass according to the present invention is not limited to these examples.
[実施例1]着色瓶ガラスのカレットを、アルミナボールを入れたボールミルにより粉砕して平均粒径50μm〜60μmのガラス粉末を形成した。このガラス粉末に対し、市販されている吉沢石灰工業株式会社製のドロマイト粉末を当該ガラス粉末の重量の3.5重量%加えてさらに粉砕、混合した。30分間の粉砕、混合を行うことにより平均粒径40μmの混合微粉末が得られた。この混合微粉末をステンレス板上に厚さ約20mmとなるように平らに積み上げ、マッフル炉中に装入した。 [Example 1] Colored bottle glass cullet was pulverized by a ball mill containing alumina balls to form glass powder having an average particle size of 50 to 60 µm. To this glass powder, commercially available dolomite powder manufactured by Yoshizawa Lime Industry Co., Ltd. was added by 3.5% by weight of the glass powder, and further pulverized and mixed. By mixing and pulverizing for 30 minutes, a mixed fine powder having an average particle size of 40 μm was obtained. The mixed fine powder was flatly stacked on a stainless steel plate so as to have a thickness of about 20 mm, and charged into a muffle furnace.
そして、これをほぼ20℃/分の上昇温速度で加熱し、約45分経過後、900℃となった時点でそのまま3分間保持した後、マッフル炉中から取り出し、室温下で扇風機の風を当てながら冷却した。冷却後の発泡ガラスの見かけ厚みは4cm〜4.5cmとなっており、見かけ比重は0.7から0.8であった。この発泡ガラスを水に浸漬したところ、しばらくの間は浮いていたが、徐々に沈みはじめ、最終的には沈んでしまった。このことから発泡ガラスに内在する気泡は連続気泡であることがわかった。これにより連続気泡を有する発泡ガラスとなったことがわかった。 Then, this was heated at a rate of temperature increase of about 20 ° C./min. After about 45 minutes, when it reached 900 ° C., it was held for 3 minutes, then removed from the muffle furnace, and the fan wind was blown at room temperature. Cooled down while hitting. The apparent thickness of the foamed glass after cooling was 4 cm to 4.5 cm, and the apparent specific gravity was 0.7 to 0.8. When this foamed glass was immersed in water, it floated for a while, but began to sink gradually, and finally sank. From this, it was found that the bubbles contained in the foamed glass were open cells. It turned out that it became the foam glass which has an open cell by this.
なお、前述した加熱工程において、加熱温度を920℃まで上昇させ、920℃に到達後すぐに炉から取り出して同様にして冷却したところ、見かけ比重が0.8〜1.0の独立気泡を有する発泡ガラスが形成されていることが分かった。 In the heating step described above, the heating temperature is increased to 920 ° C., and after reaching 920 ° C., it is taken out of the furnace and cooled in the same manner, and has closed cells with an apparent specific gravity of 0.8 to 1.0. It was found that foam glass was formed.
[実施例2]実施例1と同様の発泡剤入りのガラス粉末を利用した。ただし、発泡剤は3重量%のドロマイトと、0.5重量%の硼砂との混合物とした。このような混合微粉末について、実施例1と同じ条件で加熱して520℃まで昇温させ、温度520℃に到達した後、直ちに炉から取り出し、扇風機の風を当てながら急冷した。この結果、見かけ比重が0.7〜1.0の発泡ガラスが得られた。なお、生成したガラスは独立気泡を有する発泡ガラスであった。 [Example 2] The same glass powder containing a foaming agent as in Example 1 was used. However, the foaming agent was a mixture of 3% by weight of dolomite and 0.5% by weight of borax. About such mixed fine powder, it heated on the same conditions as Example 1, heated up to 520 degreeC, and after reaching temperature 520 degreeC, it took out from the furnace immediately, and cooled rapidly, applying the wind of the electric fan. As a result, a foamed glass having an apparent specific gravity of 0.7 to 1.0 was obtained. The produced glass was foamed glass having closed cells.
「実施例3」ガラス原料として廃瓶ガラスを使用し、この廃瓶ガラスを実施例1と同様にして粉砕した後、ドロマイト粉末を加えてさらに粉砕混合を行い、平均粒径50μm〜100μmの混合微粉末を得た。この混合粉末を試験用の連続式トンネル炉のコンベア上に厚さ約20mmとなるように広げ、加熱を行った。 [Example 3] Using waste bottle glass as a glass raw material, this waste bottle glass was pulverized in the same manner as in Example 1, then dolomite powder was added and further pulverized and mixed, and mixed with an average particle size of 50 μm to 100 μm A fine powder was obtained. This mixed powder was spread on a conveyor of a test continuous tunnel furnace so as to have a thickness of about 20 mm and heated.
この加熱工程においては、最初、昇温温度25℃/分で室温から750℃まで上昇させた後、750℃で15分間保持し、しかる後に、昇温速度を30℃/分として900℃まで再加熱し、その後、炉から出して空気中で冷却した。このような工程をとることにより、見かけ比重が0.8〜1.0の連続気泡を有する発泡ガラスを得ることができた。 In this heating step, the temperature is first raised from room temperature to 750 ° C. at a temperature rising temperature of 25 ° C./min, then held at 750 ° C. for 15 minutes, and then reheated to 900 ° C. at a temperature rising rate of 30 ° C./min. Heated, then removed from the furnace and cooled in air. By taking such a process, it was possible to obtain foamed glass having open cells having an apparent specific gravity of 0.8 to 1.0.
本発明の発泡ガラス製造方法は、廃ガラスを原料として、土壌改良材、路盤埋設用資材、屋上緑化用資材などに使用する発泡ガラスを製造する技術分野において広く利用することができる。 The foamed glass production method of the present invention can be widely used in the technical field of producing foamed glass used for soil improvement materials, roadbed burying materials, rooftop greening materials, etc., using waste glass as a raw material.
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