JPH0930821A - Glass foam granule, method for producing the same, lightweight filler and lightweight plastic using the same - Google Patents

Glass foam granule, method for producing the same, lightweight filler and lightweight plastic using the same

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Publication number
JPH0930821A
JPH0930821A JP18448995A JP18448995A JPH0930821A JP H0930821 A JPH0930821 A JP H0930821A JP 18448995 A JP18448995 A JP 18448995A JP 18448995 A JP18448995 A JP 18448995A JP H0930821 A JPH0930821 A JP H0930821A
Authority
JP
Japan
Prior art keywords
glass
foam
lightweight
granule
glass foam
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP18448995A
Other languages
Japanese (ja)
Inventor
Shinji Hamada
信二 濱田
Takuji Kajiwara
拓治 梶原
Yoshimasa Hikosaka
吉尚 彦坂
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toyota Motor Corp
Original Assignee
Toyota Motor Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toyota Motor Corp filed Critical Toyota Motor Corp
Priority to JP18448995A priority Critical patent/JPH0930821A/en
Publication of JPH0930821A publication Critical patent/JPH0930821A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C03GLASS; MINERAL OR SLAG WOOL
    • C03BMANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
    • C03B19/00Other methods of shaping glass
    • C03B19/10Forming beads
    • C03B19/108Forming porous, sintered or foamed beads
    • C03B19/1085Forming porous, sintered or foamed beads by blowing, pressing, centrifuging, rolling or dripping

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

(57)【要約】 【課題】 強度を向上したガラス発泡造粒体とその製造
方法およびそれを利用した軽量化充填材、軽量プラスチ
ックの提供。 【解決手段】 発泡粒の中に多数の独立気泡3を分散さ
せたガラス発泡造粒体1。隔壁2を有すので強度が向上
する。たとえば自動車ガラスを粉粒とし、たとえばドロ
マイトからなる発泡剤を混練して溶融、発泡させるガラ
ス発泡造粒体の製造方法。このガラス発泡造粒体は軽量
化充填材として利用でき、それを樹脂の粉粒体と混練、
成形することによって比重0.7〜0.8の軽量プラス
チックを提供できる。
(57) [PROBLEMS] To provide a glass foam granule having improved strength, a method for producing the same, a lightweight filler using the same, and a lightweight plastic. A glass foam granulated body 1 in which a large number of closed cells 3 are dispersed in foamed granules. Since the partition wall 2 is provided, the strength is improved. For example, a method for producing a glass foam granule in which automobile glass is made into powder particles and a foaming agent made of, for example, dolomite is kneaded, melted, and foamed. This glass foam granule can be used as a lightweight filler, and it is kneaded with resin powder granules,
By molding, a lightweight plastic having a specific gravity of 0.7 to 0.8 can be provided.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、ガラス発泡造粒体
とその製造方法、およびガラス発泡造粒体の性質を専ら
利用した軽量化充填材、ガラス発泡造粒体を含む軽量プ
ラスチックに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a glass foam granule, a method for producing the same, a lightweight filler exclusively utilizing the properties of the glass foam granule, and a lightweight plastic containing the glass foam granule.

【0002】[0002]

【従来の技術】従来、ガラスを主材とする中空発泡造粒
体(バルン)は、シリカ系バルン、シラス系バルン、お
よびパーライト系バルンが存在する。シリカ系バルンの
特徴は、1粒の比重が0.2程度で軽い、20μm〜1
30μmの微小粒径である、高い耐圧強度をもつ、水や
樹脂と反応せず化学安定度が高い、熱伝導が小さく断熱
性に優れる、ことである。また、シラス系、パーライト
系バルンの特徴は、シリカ系バルンより軽い、天然原料
を使用している、原料中の結晶水がガス化して発泡す
る、等である。
2. Description of the Related Art Conventionally, hollow foamed granules (baluns) mainly made of glass include silica baluns, silas baluns, and pearlite baluns. The characteristic of silica-based balun is 20μm ~ 1
It has a fine particle size of 30 μm, has high compressive strength, does not react with water or resin, has high chemical stability, has low heat conduction, and has excellent heat insulating properties. Further, the characteristics of the shirasu-based and perlite-based baluns are that they are lighter than the silica-based baluns, that they use natural raw materials, that the water of crystallization in the raw materials is gasified, and foams.

【0003】[0003]

【発明が解決しようとする課題】しかし、従来技術に
は、つぎの問題がある。 1. シリカ系バルンのコストが高い(たとえば、10
00〜1500円/kg)。 1)シリカ系バルンのバルン化工程は図9に示す通りで
あり、バルン化設備が火焔式で複雑となり、バルンのコ
ストが高くなる。 2)1,100℃の高温加熱部分を0.5〜10秒の極
短時間滞留で発泡させる。そのため、炉内が高温である
ため設備費が高く、エネルギー費もかかる。 3)高温のため炉内の温度管理が困難で回収率が悪い。
すなわち、火焔中の温度振れ幅が大きいため、粒ごとに
発泡程度が異なりやすく、品質上ばらつきが発生し、必
要とする品質のバルンの回収率が低下する。したがっ
て、高価となる。 4)発泡剤に有機系を使用している。そのため、発泡剤
が噴霧乾燥式造粒の際にかなり逃げ出しロスがでる。ま
た、ガス発生分解温度は約200℃、噴霧乾燥温度は1
80〜370℃であり、高温のため価格が高い(800
/kg程度)。 2. バルン粒径(30〜120μm)が微粒子のた
め、製造工程や取扱い使用時に飛散等しやすい。 3. シラス系、パーライト系は天然材を使用。産地に
よる鉱物成分の違いから、産地別の原料特性の調査や選
別が必要で、収率や強度が相違する。また、融解温度が
高く1,000〜1,200℃で加熱発泡させている。 本発明の目的は、従来に比べ低温で、したがって低コス
トで製造できるとともに、品質が安定し、強度も向上し
た、ガラスを主材とする発泡造粒体、その製造方法、発
泡造粒体の性質を利用した軽量化充填材、発泡造粒体を
含有する軽量プラスチックを提供することにある。
However, the prior art has the following problems. 1. The cost of silica-based balun is high (for example, 10
(00 to 1500 yen / kg). 1) The balunization process of silica-based balun is as shown in FIG. 9, and the balunization equipment becomes complicated by the flame method and the cost of balun becomes high. 2) The portion heated at a high temperature of 1,100 ° C. is foamed by staying for a very short time of 0.5 to 10 seconds. Therefore, since the temperature inside the furnace is high, the equipment cost is high and the energy cost is high. 3) Due to the high temperature, it is difficult to control the temperature inside the furnace and the recovery rate is poor.
That is, since the temperature fluctuation range during the flame is large, the degree of foaming is likely to differ for each grain, quality variations occur, and the recovery rate of the required quality balun decreases. Therefore, it becomes expensive. 4) An organic type is used as the foaming agent. Therefore, the foaming agent escapes considerably during the spray-drying granulation, resulting in loss. Further, the gas generation decomposition temperature is about 200 ° C, and the spray drying temperature is 1
The temperature is 80-370 ℃, and the price is high due to the high temperature (800
/ Kg). 2. Since the balun particle size (30 to 120 μm) is fine particles, it easily scatters during the manufacturing process, handling and use. 3. Natural materials are used for shirasu and perlite. Due to the difference in mineral composition depending on the place of origin, it is necessary to investigate and select raw material characteristics by place of origin, resulting in different yields and strengths. In addition, the melting temperature is high and the foaming is performed at 1,000 to 1,200 ° C. An object of the present invention is to produce a foamed granule mainly composed of glass, which can be manufactured at a lower temperature than conventional ones, and thus can be manufactured at low cost, has stable quality, and has improved strength, a method for manufacturing the same, and a foamed granule. An object of the present invention is to provide a lightweight plastic material containing properties and a lightweight plastic containing expanded granules.

【0004】[0004]

【課題を解決するための手段】上記目的を達成する本発
明はつぎの通りである。 (1) ガラスを主材とし、これに発泡剤を混合して発
泡させることによって、発泡粒の中に多数の独立気泡を
分散させたことを特徴とするガラス発泡造粒体。 (2) 粉砕したガラスと少なくとも発泡剤とを混合
し、これに溶媒を加えて造粒するとともに、これを乾燥
せしめ、さらに乾燥された造粒体を加熱して発泡させる
ことを特徴とするガラス発泡造粒体の製造方法。 (3) 前記ガラスに約700℃以下で軟化を開始する
ガラスを使用し、前記発泡剤にドロマイトを使用した
(2)記載のガラス発泡造粒体の製造方法。 (4) 加熱、発泡工程における加熱温度を730℃〜
900℃、加熱時間を10秒〜20分の範囲で調整し
て、所望の比重、強度とする(2)記載のガラス発泡造
粒体の製造方法。 (5) ガラスを主材とし、これに発泡剤を混合して発
泡させることによって、発泡粒の中に多数の独立気泡を
分散させたガラス発泡造粒体からなる軽量化充填材。 (6) ガラスを主材とし、これに発泡剤を混合して発
泡させることによって、発泡粒の中に多数の独立気泡を
分散させたガラス発泡造粒体からなる軽量化充填材と、
樹脂粉粒体とを、混練、加熱、成形した軽量プラスチッ
ク。
The present invention to achieve the above object is as follows. (1) A glass expanded granulated product characterized in that a large number of closed cells are dispersed in expanded beads by mixing glass with a foaming agent and foaming the glass as a main material. (2) A glass characterized by mixing crushed glass and at least a foaming agent, adding a solvent to the mixture to granulate it, drying it, and heating the dried granulated body to foam it. Method for producing expanded granules. (3) The method for producing a glass foam granule according to (2), wherein glass that starts softening at about 700 ° C. or less is used as the glass, and dolomite is used as the foaming agent. (4) The heating temperature in the heating and foaming process is 730 ° C to
The method for producing a glass foam granule according to (2), wherein the specific gravity and the strength are set to 900 ° C. and the heating time is adjusted within the range of 10 seconds to 20 minutes. (5) A lightweight filler made of a glass foam granule in which a large number of closed cells are dispersed in foam particles by mixing glass with a foaming agent to foam the glass as a main material. (6) A lightweight filler made of glass foam granules in which a large number of closed cells are dispersed in foam particles by mixing glass with a foaming agent to foam the glass as a main material,
Lightweight plastic made by kneading, heating, and molding with resin powder.

【0005】上記(1)のガラス発泡造粒体は、造粒体
内の気泡間に隔壁があり、従来のように中空なものに比
べて強度が高い。上記(2)のガラス発泡造粒体の製造
方法では、造粒体内の気泡間に隔壁をもつ強度の高いガ
ラス発泡造粒体を製造できる。上記(3)の方法ではガ
ラスに約700℃以下で軟化を開始するガラス(たとえ
ば、自動車ガラス)を使用し、発泡剤にドロマイト(約
700℃〜750℃で発泡する)を使用したので、約7
30℃〜900℃でガラスを溶融、発泡させることがで
き、従来に比べて低温でよく、炉内温度管理が安定して
品質が安定しそれによって回収効率が高くなり、かつ炉
設備も低価になり、製品コストも低減できる。上記
(4)の方法では、加熱温度、加熱時間を調整して、ガ
ラス発泡造粒体の比重、強度を調整できる。上記(5)
では、ガラス発泡造粒体を利用した軽量化充填材を提供
できる。上記(6)では、軽量化充填材を利用して軽量
プラスチックを提供できる。
The glass foam granule of the above (1) has a partition wall between the air bubbles in the granule and has a higher strength than a conventional hollow granule. According to the method (2) for producing a glass foam granule, it is possible to manufacture a high strength glass foam granule having partition walls between cells in the granule. In the method of (3) above, glass that starts softening at about 700 ° C. or lower is used as glass (for example, automobile glass), and dolomite (foaming at about 700 ° C. to 750 ° C.) is used as a foaming agent. 7
Glass can be melted and foamed at 30 ° C to 900 ° C, the temperature is lower than in the past, the temperature control in the furnace is stable, the quality is stable, and the recovery efficiency is high. Therefore, the product cost can be reduced. In the above method (4), the heating temperature and the heating time can be adjusted to adjust the specific gravity and strength of the glass foam granule. Above (5)
In, it is possible to provide a lightweight filler using a glass foam granule. In the above (6), a lightweight plastic can be provided by using the lightweight filler.

【0006】[0006]

【発明の実施の形態】まず、本発明実施例に係るガラス
発泡造粒体の製造方法を説明する。ガラス発泡造粒体の
製造における配合はつぎの通りである。ガラスを主原料
として添加剤を適量配合し、簡易製造方法により粒径5
0〜600μmのガラス発泡造粒体(軽量充填材)を製
造する。配合は、主原料のガラスと発泡剤にドロマイト
(MgCO3 ・CaCO3 )、融剤に硼砂(Na2 4
7 ・5H2 O)を表1の重量比で混合する。ドロマイ
トは約700℃〜750℃で発泡する。
BEST MODE FOR CARRYING OUT THE INVENTION First, a method for producing a glass foam granule according to an embodiment of the present invention will be described. The composition in the production of the glass foam granules is as follows. Glass is used as the main raw material with an appropriate amount of additives, and a particle size of 5
A glass foam granule (light weight filler) of 0 to 600 μm is manufactured. The composition is glass as the main raw material, dolomite (MgCO 3 · CaCO 3 ) as the foaming agent, and borax (Na 2 B 4 ) as the flux.
O 7 .5H 2 O) are mixed in the weight ratio shown in Table 1. Dolomite foams at about 700 ° C to 750 ° C.

【0007】[0007]

【表1】 [Table 1]

【0008】ガラスには約700℃以下で軟化を開始す
るもの、たとえば自動車ガラス(たとえば、廃車のガラ
ス)等が使用可能である。ドロマイトは天然の産物で安
価な材料である。また、ガラスが軟化する温度範囲にお
いて、発泡ガス(炭酸ガスCO2 )を発生する。硼砂は
ガラスの融点を調整して下げるため添加する。たとえば
図1のように、自動車ガラスの融解状態は融解開始温度
550℃〜融解温度700℃である。硼砂5%添加した
場合、自動車ガラス融解状態は、融解開始温度530℃
〜融解温度685℃となる。昇温によるドロマイト発泡
状態は、分解開始温度620℃〜終了温度730℃であ
る。ただし、硼砂は必要量以上に添加すると、加熱時に
融解ガラス粘性が低下し、融着防止用の離型剤がバルン
に付着しやすくなって比重が重くなることがある。
As the glass, it is possible to use a glass which starts to soften at about 700 ° C. or lower, for example, automobile glass (for example, a glass of a scrap car). Dolomite is a natural product and an inexpensive material. In addition, foaming gas (carbon dioxide gas CO 2 ) is generated in the temperature range in which the glass softens. Borax is added to adjust and lower the melting point of glass. For example, as shown in FIG. 1, the melting state of automobile glass is a melting start temperature of 550 ° C. to a melting temperature of 700 ° C. When 5% borax is added, the melting state of automobile glass is 530 ° C.
~ The melting temperature is 685 ° C. The foaming state of dolomite due to temperature rise is from a decomposition start temperature of 620 ° C to an end temperature of 730 ° C. However, if borax is added in an amount more than the necessary amount, the viscosity of the molten glass will decrease during heating, and the release agent for preventing fusion will tend to adhere to the balun and the specific gravity may increase.

【0009】ガラス発泡造粒体の製造における、ガラス
の粉砕、造粒、加熱、発泡の工程を、図2を参照して説
明する。製法は図2のように、各原料を配合した粉砕、
混合物を造粒、乾燥〜加熱、発泡により造粒化する。ガ
ラスの粉砕はボールミルで行い、平均粒子径3〜10μ
mにした後、配合したものを均一に混ぜて粉末状の混合
物をつくる。造粒、乾燥は転動ミキサー方式またはスプ
レードライヤー噴霧乾燥方式で行う。転動ミキサーの場
合は、混合物に水を混ぜて15〜18%水分量の造粒物
としたあと乾燥すると型崩れしなくてよい。噴霧乾燥方
式の場合は、混合物を溶媒の水と混ぜて32〜38%水
分量のスラリーとして使用する。造粒の際、一般には結
合用バインダー剤を使用するが、ガラス粉は湿気を帯び
ると凝集力があり、バインダー剤の添加を必要としな
い。加熱、発泡はロータリー炉方式または火焔方式で行
う。炉壁や粒同士の融着がある場合は、必要に応じて離
型剤を添加する。離型剤はバルン付着による比重低下を
防ぐため、なるべく比重の軽い無機系のものがよい。た
とえば水ひ粘土やアルミナがある。造粒物の加熱は温度
730〜900℃(廃車ガラスの場合は比較的低温で溶
融する)、数十秒〜20分の時間(従来に比べて長く、
加熱が安定し、品質が安定する)で行い、ガラスが溶融
すると共に発泡ガスが発生して、発泡ガスがガラス内に
取り込まれ発泡造粒化する。火焔方式の場合は、急加熱
による割れを防ぐため火焔投入前にガラスが融着しない
温度で加熱しておくと発泡効率がよい。かくして、ガラ
ス発泡造粒体が製造される。
The steps of crushing, granulating, heating and foaming glass in the production of a glass foam granule will be described with reference to FIG. As shown in Fig. 2, the manufacturing method is pulverization in which each raw material is mixed,
The mixture is granulated, dried to heat and foamed to be granulated. The glass is crushed with a ball mill, and the average particle size is 3 to 10 μm.
After adjusting to m, the blended ingredients are uniformly mixed to form a powdery mixture. Granulation and drying are performed by a tumbling mixer method or a spray dryer spray drying method. In the case of a tumbling mixer, the mixture does not lose its shape when mixed with water to form a granulated product having a water content of 15 to 18% and then dried. In the case of the spray drying method, the mixture is mixed with water as a solvent and used as a slurry having a water content of 32 to 38%. When granulating, a binder agent for binding is generally used, but the glass powder has a cohesive force when moist and does not require the addition of a binder agent. Heating and foaming are performed by a rotary furnace method or a flame method. If there is fusion between the furnace wall and the particles, a release agent is added if necessary. In order to prevent a decrease in specific gravity due to adhesion of balun, it is preferable that the release agent be an inorganic one having a low specific gravity. For example, hydrangea and alumina. The granulated material is heated at a temperature of 730 to 900 ° C. (in the case of scrap car glass, it melts at a relatively low temperature) and a time of several tens of seconds to 20 minutes (longer than conventional ones,
The heating is stable and the quality is stable), the glass is melted and the foaming gas is generated, and the foaming gas is taken into the glass and foam-granulated. In the case of the flame method, in order to prevent cracking due to rapid heating, it is preferable to heat the glass at a temperature at which the glass does not melt before charging the flame, so that the foaming efficiency is good. Thus, a glass foam granule is manufactured.

【0010】つぎに、ガラス発泡造粒体とその特性を、
図3、図5〜図7を参照して、説明する。製造したガラ
ス発泡造粒体1は図3に拡大して示すように、いくつか
の壁2で区切られた微小独立気泡3の集まりで1粒の球
になっている。この造粒体内の隔壁2が圧縮破壊強度で
有利となる(強度を増大させる)。また、もし軽量充填
材に使用して一部の気泡が壊れたとしても、まだ他の気
泡が残っており安全側にある。外径では50〜600μ
mの球状のものが製造できる。図4は従来のバルン(中
空造粒体)1´の拡大図を示す。
Next, the glass foam granules and their characteristics will be described.
This will be described with reference to FIGS. 3 and 5 to 7. As shown in FIG. 3 in an enlarged manner, the manufactured glass foam granules 1 are one sphere composed of a collection of minute closed cells 3 separated by several walls 2. The partition walls 2 in this granule are advantageous in terms of compressive fracture strength (increase in strength). Also, even if some bubbles are broken when used as a lightweight filler, other bubbles still remain, which is on the safe side. 50-600μ in outer diameter
m spherical shape can be manufactured. FIG. 4 shows an enlarged view of a conventional balun (hollow granule) 1 '.

【0011】本発明実施例のガラス発泡造粒体を自動車
ガラスを使って製造した場合の、機械的諸特性を図5〜
図7に示す。粒径は300〜600μmに製造したもの
である。これらグラフのように、加熱温度と加熱時間等
の製造条件を変えることにより、必要とする圧縮破壊強
度と比重のものがグラフ範囲内で自由に製造し選択でき
る。
Mechanical properties when the glass foam granules of the examples of the present invention were manufactured using automobile glass are shown in FIG.
As shown in FIG. The particle size is manufactured to 300 to 600 μm. As shown in these graphs, by changing the manufacturing conditions such as heating temperature and heating time, it is possible to freely manufacture and select the one having the required compressive fracture strength and specific gravity within the graph range.

【0012】つぎに、ガラス発泡造粒体の軽量という特
定の性質を専ら利用した軽量化充填材について説明す
る。ガラス発泡造粒体がそのまま軽量化充填材となり、
その利用法は、樹脂に添加して成形することにより、プ
ラスチックを軽量化できる充填材となる。樹脂は廃樹脂
であってもよい。軽量プラスチックは、図8に示すよう
な工程で製造する。ガラス発泡造粒体は、軽量プラスチ
ック製造途中で壊れることのない圧縮破壊強度のものを
選択し、かつ必要なプラスチック比重が得られるように
添加量を定めるとよい。得られた軽量プラスチックは、
強度や剛性の高いものとなる。例えば表2に示すよう
に、ポリプロピレン樹脂(比重0.91)に比重0.5
のガラス発泡造粒体を重量比7:3で混合〜成形する
と、比重0.73の軽量プラスチックができる。
Next, a description will be given of a weight-reducing filler material that exclusively utilizes the specific property of the foamed glass granules that is lightweight. Glass foam granules can be used as a lightweight filling material,
Its usage is to add it to a resin and mold it to obtain a filler that can reduce the weight of plastic. The resin may be a waste resin. The lightweight plastic is manufactured by the process shown in FIG. It is advisable to select a glass foam granule having a compressive fracture strength that does not break during the production of a lightweight plastic, and to determine the addition amount so that the required plastic specific gravity can be obtained. The resulting lightweight plastic is
It has high strength and rigidity. For example, as shown in Table 2, polypropylene resin (specific gravity 0.91) has a specific gravity of 0.5
By mixing and molding the glass foam granules of (3) at a weight ratio of 7: 3, a lightweight plastic having a specific gravity of 0.73 is produced.

【0013】[0013]

【表2】 [Table 2]

【0014】[0014]

【発明の効果】請求項1のガラス発泡造粒体によれば、
発泡粒の中に独立気泡を分散させたものからなるので気
泡間の隔壁によって強度が増大された造粒体を提供でき
る。請求項2のガラス発泡造粒体の製造方法によれば、
独立気泡を含む造粒体を製造できる。請求項3のガラス
発泡造粒体の製造方法によれば、ガラス材に700℃以
下で軟化を開始するガラス(たとえば、自動車ガラス)
を使用、発泡材にドロマイトを使用したので、従来に比
べて低温(約730℃〜900℃)で溶融、発泡させる
ことができ、品質の高い、かつ低コストのガラス発泡造
粒体を提供できる。請求項4のガラス発泡造粒体の製造
方法によれば、加熱温度を730〜900℃の範囲で、
加熱時間を20分〜10秒の範囲で変えることにより、
ガラス発泡造粒体の破壊強度を20〜300kg/cm
2 ・cmの範囲に自由に変化でき、かつ比重を0.3〜
1.0の範囲に自由に変化できる。請求項5のガラス発
泡造粒体からなる軽量化充填材によれば、樹脂等に混合
して成形されることにより、樹脂成形品等を軽量化でき
る。請求項6の軽量化プラスチックによれば、軽量化充
填材を利用して、比重がたとえば0.7〜0.8の軽量
化プラスチックを提供できる。
According to the glass foam granules of claim 1,
Since the closed cells are formed by dispersing the closed cells in the foamed particles, it is possible to provide a granulated body having an increased strength due to the partition walls between the cells. According to the method for producing a glass foam granule of claim 2,
Granules containing closed cells can be produced. According to the method for producing a glass foam granule according to claim 3, a glass which starts softening at 700 ° C. or lower (for example, automobile glass).
Since dolomite is used as the foam material, it can be melted and foamed at a lower temperature (about 730 ° C. to 900 ° C.) than conventional ones, and a high-quality and low-cost glass foam granule can be provided. . According to the method for producing a glass foam granule of claim 4, the heating temperature is in the range of 730 to 900 ° C,
By changing the heating time in the range of 20 minutes to 10 seconds,
The breaking strength of the glass foam granules is 20 to 300 kg / cm
It can be freely changed within the range of 2 cm and the specific gravity is 0.3 ~
It can be changed freely within the range of 1.0. According to the lightweight filler made of the glass foam granules according to the fifth aspect, the resin molded product and the like can be lightened by being mixed with resin or the like and molded. According to the lightweight plastic of the sixth aspect, the lightweight plastic having a specific gravity of, for example, 0.7 to 0.8 can be provided by using the lightweight filler.

【図面の簡単な説明】[Brief description of drawings]

【図1】自動車ガラスとドロマイトと硼砂の混合物にお
ける加熱温度(融解温度、融解開始温度)と硼砂添加量
との関係を示すグラフである。
FIG. 1 is a graph showing the relationship between the heating temperature (melting temperature, melting start temperature) and the amount of borax added in a mixture of automobile glass, dolomite, and borax.

【図2】本発明実施例のガラス発泡造粒体の製造方法の
工程図である。
FIG. 2 is a process drawing of a method for manufacturing a glass foam granule according to an example of the present invention.

【図3】本発明実施例のガラス発泡造粒体の1粒の拡大
断面図である。
FIG. 3 is an enlarged cross-sectional view of one grain of a glass foam granule according to an example of the present invention.

【図4】従来のガラスバルン(市販品)の1粒の拡大断
面図である。
FIG. 4 is an enlarged cross-sectional view of one grain of a conventional glass balun (commercially available product).

【図5】本発明実施例のガラス発泡造粒体の圧縮破壊強
度と1粒の比重との関係を示すグラフである。
FIG. 5 is a graph showing the relationship between the compressive fracture strength and the specific gravity of one grain of the glass foam granules of the examples of the present invention.

【図6】本発明実施例のガラス発泡造粒体の1粒の比重
と加熱温度との関係を示すグラフである。
FIG. 6 is a graph showing the relationship between the specific gravity of one particle of the glass foam granulated material of the example of the present invention and the heating temperature.

【図7】本発明実施例のガラス発泡造粒体の圧縮破壊強
度と加熱温度との関係を示すグラフである。
FIG. 7 is a graph showing the relationship between the compressive fracture strength and the heating temperature of the glass foam granules of the examples of the present invention.

【図8】本発明実施例のガラス発泡造粒体を主材とする
軽量化充填材を利用した軽量プラスチックの製造工程図
である。
FIG. 8 is a manufacturing process diagram of a lightweight plastic using a lightweight filler mainly composed of a glass foam granule according to an example of the present invention.

【図9】従来のシリカ系バルンの製造工程である。FIG. 9 is a manufacturing process of a conventional silica balun.

【符号の説明】[Explanation of symbols]

1 ガラス発泡造粒体 2 隔壁 3 気泡 1 glass foam granules 2 partition walls 3 bubbles

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 ガラスを主材とし、これに発泡剤を混合
して発泡させることによって、発泡粒の中に多数の独立
気泡を分散させたことを特徴とするガラス発泡造粒体。
1. A glass foam granule characterized in that a large number of closed cells are dispersed in foam particles by using glass as a main material and mixing a foaming agent with the glass to foam the glass.
【請求項2】 粉砕したガラスと少なくとも発泡剤とを
混合し、これに溶媒を加えて造粒するとともに、これを
乾燥せしめ、さらに乾燥された造粒体を加熱して発泡さ
せることを特徴とするガラス発泡造粒体の製造方法。
2. A method in which crushed glass and at least a foaming agent are mixed, a solvent is added to this to granulate, and this is dried, and the dried granulated body is heated to foam. A method for producing a glass foam granule.
【請求項3】 前記ガラスに約700℃以下で軟化を開
始するガラスを使用し、前記発泡剤にドロマイトを使用
した請求項2記載のガラス発泡造粒体の製造方法。
3. The method for producing a glass foam granule according to claim 2, wherein the glass used is a glass which starts softening at about 700 ° C. or lower, and dolomite is used as the foaming agent.
【請求項4】 加熱、発泡工程における加熱温度を73
0℃〜900℃、加熱時間を10秒〜20分の範囲で調
整して、所望の比重、強度とする請求項2記載のガラス
発泡造粒体の製造方法。
4. The heating temperature in the heating and foaming process is 73.
The method for producing a glass foam granule according to claim 2, wherein a desired specific gravity and strength are obtained by adjusting the heating time in the range of 0 ° C to 900 ° C for 10 seconds to 20 minutes.
【請求項5】 ガラスを主材とし、これに発泡剤を混合
して発泡させることによって、発泡粒の中に多数の独立
気泡を分散させたガラス発泡造粒体からなる軽量化充填
材。
5. A lightweight filler made of glass foam granules having glass as a main material and a large number of closed cells dispersed in the foam particles by mixing the foaming agent and foaming.
【請求項6】 ガラスを主材とし、これに発泡剤を混合
して発泡させることによって、発泡粒の中に多数の独立
気泡を分散させたガラス発泡造粒体からなる軽量化充填
材と、樹脂粉粒体とを、混練、加熱、成形した軽量プラ
スチック。
6. A lightweight filler made of a glass foam granule having glass as a main material and a large number of closed cells dispersed in the foam particles by mixing the foaming agent and foaming the mixture. Lightweight plastic made by kneading, heating, and molding with resin powder.
JP18448995A 1995-07-20 1995-07-20 Glass foam granule, method for producing the same, lightweight filler and lightweight plastic using the same Pending JPH0930821A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18448995A JPH0930821A (en) 1995-07-20 1995-07-20 Glass foam granule, method for producing the same, lightweight filler and lightweight plastic using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18448995A JPH0930821A (en) 1995-07-20 1995-07-20 Glass foam granule, method for producing the same, lightweight filler and lightweight plastic using the same

Publications (1)

Publication Number Publication Date
JPH0930821A true JPH0930821A (en) 1997-02-04

Family

ID=16154077

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18448995A Pending JPH0930821A (en) 1995-07-20 1995-07-20 Glass foam granule, method for producing the same, lightweight filler and lightweight plastic using the same

Country Status (1)

Country Link
JP (1) JPH0930821A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008189536A (en) * 2007-02-07 2008-08-21 Sk Kaken Co Ltd White glass particle, and method for producing the same
JP2011046758A (en) * 2009-08-25 2011-03-10 Japan Polypropylene Corp Thermoplastic resin composition and molded body thereof
JP2011149016A (en) * 2009-12-24 2011-08-04 Taiheiyo Materials Corp Granular material for lightweight molding resin and lightweight molding resin composition
CN103788935A (en) * 2012-11-05 2014-05-14 安东柏林石油科技(北京)有限公司 Semi-permeable packing particles for oil-gas well and preparation method of particles

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008189536A (en) * 2007-02-07 2008-08-21 Sk Kaken Co Ltd White glass particle, and method for producing the same
JP2011046758A (en) * 2009-08-25 2011-03-10 Japan Polypropylene Corp Thermoplastic resin composition and molded body thereof
JP2011149016A (en) * 2009-12-24 2011-08-04 Taiheiyo Materials Corp Granular material for lightweight molding resin and lightweight molding resin composition
CN103788935A (en) * 2012-11-05 2014-05-14 安东柏林石油科技(北京)有限公司 Semi-permeable packing particles for oil-gas well and preparation method of particles

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