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JPH0130076B2 - - Google Patents
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JPH0130076B2 - - Google Patents

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Publication number
JPH0130076B2
JPH0130076B2 JP56126895A JP12689581A JPH0130076B2 JP H0130076 B2 JPH0130076 B2 JP H0130076B2 JP 56126895 A JP56126895 A JP 56126895A JP 12689581 A JP12689581 A JP 12689581A JP H0130076 B2 JPH0130076 B2 JP H0130076B2
Authority
JP
Japan
Prior art keywords
drying
blower
radiation
infrared
tube
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.)
Expired
Application number
JP56126895A
Other languages
Japanese (ja)
Other versions
JPS5828974A (en
Inventor
Masao Myashiro
Ryuzo Takai
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.)
SHIGAKEN
Original Assignee
SHIGAKEN
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 SHIGAKEN filed Critical SHIGAKEN
Priority to JP12689581A priority Critical patent/JPS5828974A/en
Publication of JPS5828974A publication Critical patent/JPS5828974A/en
Publication of JPH0130076B2 publication Critical patent/JPH0130076B2/ja
Granted legal-status Critical Current

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  • Resistance Heating (AREA)
  • Drying Of Solid Materials (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は赤外線乾燥装置に関し、特に陶磁器な
らびにその石膏型乾燥に使用する赤外線乾燥装置
に関する。 陶磁器製品ならびに石膏型の乾操法は一般的に
は伝導対流による温風乾燥であるが、近年マイク
ロ波乾燥、真空乾燥、赤外線乾燥等の方法が開発
され注目を浴びている。通常の温風乾燥では被加
熱体を加熱し、その結果、表面から水蒸気が逸散
されて乾燥される。物質を加熱するには伝導、対
流輻射の三要素があり、何れかの一要素又は組合
せによつて加熱される。温風乾燥では伝導対流に
よる加熱乾燥であり、空気水蒸気等を媒体とする
ため、媒体の無効分の加熱によるエネルギー損失
が大きい。輻射による加熱は直接被乾燥体に吸収
されるため効率が良い。 輻射を使用する加熱方法では放射効率の良い材
質の検討が必要である。一般的には石英管が使用
されるが、5μm以上の長波長域、即ち遠赤外線
波長域での放射効率が悪いため他の適切な遠赤外
線放射材料を選択使用することが望ましい。 従来の赤外線加熱素子及び反射板の形状は直管
としたシーズ管及び抛物面鏡であり、塗料乾燥等
の全面加熱用として開発されたものであるため、
陶磁器等の丸型、円形、深物、加熱用としては均
一な照射は困難であり、切れ、歪み等を生じ易い
欠点がある。 尚、乾燥効率を高めるためには輻射と局部的送
風とを並用することが望ましい場合があるが、一
般的な排気装置以外にはほとんど使用されていな
い。 本発明の目的は上述の欠点を生じない放射素子
を使用した陶磁器等の遠赤外線乾燥装置を提供す
るにある。 本発明装置における放射素子はジルコン系、ジ
ルコン−フエライト系、コーデイエライト系、ペ
タライト系等の耐熱衝撃性高密材料で成形し断面
中空として円環状等の閉曲線形とし中空内部に発
熱体を挿入する。 比較計測の結果、上述の材料は遠赤外線領域で
の放射特性が石英ガラス管に比して優れ近赤外線
域では著しく特性が低い。陶磁器等は遠赤外域で
の吸収特性が良いことを確認しこのため、乾燥用
放射素子として優れている。 更に、円環状等の閉曲線形とすることによつ
て、不均等加熱は生ぜず、不良の発生は著しく減
少する。 本発明による乾燥装置は、上述の放射素子に組
合せて一方向放射を行なわせるアルミニウム反射
板と、反射板中央の送風筒と、送風筒に組合せた
送風機とを有する。 反射板材料の反射特性はアルミニウム板がステ
ンレス板よりも優れ、市販のアルミホイルが安価
有効な反射材料である。 乾燥実験の結果、上述の放射素子からの放射
と、微風程度の送風とを組合せるのが最もエネル
ギー的に有効であることを知つた。 本発明を例示とした実施例並びに図面について
説明する。 第1に各種セラミツクス材質の分光放射特性を
試験した。ジルコン系としてジルコン素地
(ZrSiO460%、粘土40%)、ペタライト系として
ペタライト60%、蛙目粘土40%、コーデイエライ
ト系としてコーデイエライトシヤモツト50%、粘
土40%、マグネサイト10%、ジルコン−フエライ
ト系としてジルコン素地70%、フエライト30%の
ものを径5mm、長さ25mmのチユーブ状として1200
〜1250℃で焼成し、600〜800℃に加熱して放射特
性を記録し、対称として、石英管、ガラス管の放
射特性と比較した。 この結果、石英管、ガラス管は波長5μm以下
の近赤外域について放射特性が強い傾向がある。 これに対して、試料は何れも5μm以上の遠赤
外域について放射特性が強く、近赤外域での放射
特性が弱い。 従つて、遠赤外線輻射による加熱の場合は石英
管、ガラス管に比較して、試料としたジルコン
系、ジルコン−フエライト系、ペタライト系、コ
ーデイエライト系材料が好適であることが明らか
になつた。 尚、上述のセラミツクス材料を石英ガラス管に
被覆した場合は、5μm以上の遠赤外域について
はほゞ同様な放射特性を有し、石英ガラス管の放
射特性よりも優れており、近赤外域については材
料単体の管に比較して強い放射特性を有し、単体
の管と石英ガラス管の中間程度の値となる。従つ
て、近赤外域の放射をも利用できる場合には石英
ガラス管外面にセラミツクス材料を被覆したもの
を有効に使用できる。 第2に、鏡面材料による反射特性を試験した。 放射を有効に利用するためには全波長域につい
て反射率の高い材料が必要である。試験した材料
は、アルミニウム蒸着の標準ミラー、市販のクツ
キング用アルミホイル、アルミニウム板、ステン
レス板、アルマイト加工アルミ板、建材用アルミ
ニウム板であつた。 反射率測定試料中、クツキング用アルミホイル
が全波長域についてほとんど標準ミラーと変らな
い著しく良い反射特性を示した。一般に良く使用
されているステンレス鋼板は近赤外域で特にアル
ミニウムに劣る。アルマイト加工及び建材用アル
ミニウム板は表面の樹脂加工の影響が極端に大き
く、そのまゝ反射板として使用することはできな
い。 第3に、粘土及び石膏の吸収、反射特性を試験
した。吸収特性はKBr錠剤法により、反射特性
は反射法によつて実験した。 両材料共に傾向は類似しており、長波長5〜
6μm以上側に吸収率が存在する。従つて長波長
加熱が有効である。反射特性は両材料共全波長に
ついてほゞ均等であるが、石膏は9μm附近で突
出した反射のピークが存在する。 第1図は乾燥すべき陶磁器製品の例として、石
膏型1内で植木鉢2を成形する例を示す。 通常は温風乾燥してある程度収縮固化した植木
鉢2を型1から抜いて焼成する。この実態を定量
的に把握するための試験の結果、鉢自体からの脱
水はほゞ直線的経過を示し、初期に石膏型が著し
く多量の水を吸収し、空隙の形成によつて型の吸
収は減少することを知つた。石膏型の吸水特性か
ら脱型時間を定めることができた。 第2図A,Bは本発明装置に使用する円環状遠
赤外線放射素子を示し、第3図はこの放射素子を
使用した箱型乾燥器を示す。 第2図に示す放射素子3はコーデイエライト系
の円環体4内にニクロム線の発熱体5を収容した
形状とし、第3図に示す通り、反射板6で覆い、
反射板6の中央に送風筒7を通し、送風機8から
の風を乾燥すべき品物10に送り得るようにす
る。 送風機8は循環用空気量を調節可能とし、放射
素子3も強弱切換可能とした。 乾燥室11は図示の例では密閉型として内面に
反射板12を張つた断熱材壁13を有する。室内
排気は初期の多量の水蒸気の発生する時期は排出
し、所要に応じて循環路14を経て送風機8に連
結する。 放射素子として直管を使用した場合と、円環体
を使用した場合とを比較実験した結果、直管は天
端と底との温度差が著しく大きく、円環体の場合
に比較的均一に加熱されることを知つた。 乾燥間の送風については、放射と微風との組合
せが、蒸発水量が最大であり、エネルギー的にも
最も有利であることを知つた。風量が大となれば
底部のみが過早に乾燥して不良品を生ずる傾向が
ある。 前述の通り、乾燥初期には石膏型による吸水量
が著しく大きいため、1回脱型毎に石膏型を乾燥
することが望ましい。 第3図の乾燥器は乾燥室11を支持軸(図示し
ない)により角度可変自在に支持した場合を示
す。 本発明によつて明らかになつた事項は次の通り
である。 耐熱陶磁器用材料を焼成した管内に発熱体を入
れた放射素子は何れも石英ガラスに比較して遠赤
外領域での比エネルギ強度が大きく、エネルギ的
に石英ガラス管より有利である。 表面温度600〜800℃の通常使用範囲においての
放射特性はコーデイエライト系が最良であつた。
しかし、他のセラミツク材質も使用できる。 反射特性に関してはアルミニウムが最良であ
り、市販のアルミホイルが安価で大きな効果を有
する。 植木鉢等の上部円形の品物の乾燥には直管に比
較して円環体放射素子が均一加熱の点から著しく
有効である。 放射と送風とを組合せて使用することがエネル
ギ的に最も効果がある。しかし、風速は微風程度
が良く、過大風速は欠点を生ずる。 温風と放射との比較においては放射乾燥が優れ
ている。 従来の温風乾燥では8寸鉢の場合に1日に2〜
3回しか脱型できなかつたが、放射乾燥による脱
型までの所要時間は約30分であり、型乾燥の所要
時間約10分を加えても著しく能率の良い乾燥を行
ない得る。 又、本発明装置の作用効果をより明白にするた
め、第3図示の装置を使用した温風及び赤外放射
乾燥による坏土の減水速度に関する実験結果を下
記の第1表と第4図の線図により具体的に示すこ
とにする。 尚、当該実験については、同一量のエネルギー
によつて製品を温風及び放射で乾燥を行つた場
合、乾燥速度がどのように異なるかを調べるた
め、直径26cmの菓子鉢を機械ロクロ成形し、脱型
直後(水分24〜25%)第3図示の装置内にセツト
し、温風、放射とも300Wの同一電力で第1表に
示す各種の組み合せの実験を行い、その結果を第
4図の線図にて示したものである。 因つて以上の説明から明らかな通り本発明装置
によれば、放射と送風による効果的な被乾燥物の
乾燥を遂行し得るとともに放射と送風を個別的に
制御することが可能で、陶磁器乾燥のような複雑
微妙な制御の要求される乾燥について最適であ
る。
The present invention relates to an infrared drying device, and particularly to an infrared drying device used for drying ceramics and plaster molds thereof. The general drying method for ceramic products and plaster molds is hot air drying using conduction convection, but in recent years, methods such as microwave drying, vacuum drying, and infrared drying have been developed and are attracting attention. In normal hot air drying, the object to be heated is heated, and as a result, water vapor is dissipated from the surface and the object is dried. There are three elements to heat a substance: conduction, convection and radiation, and heating can be achieved by one or a combination of these elements. Hot air drying is heating drying using conduction convection, and uses air water vapor or the like as a medium, so there is a large energy loss due to heating of the inactive portion of the medium. Heating by radiation is efficient because it is directly absorbed by the object to be dried. For heating methods that use radiation, it is necessary to consider materials with good radiation efficiency. Generally, a quartz tube is used, but since the radiation efficiency is poor in a long wavelength region of 5 μm or more, that is, in a far-infrared wavelength region, it is desirable to select and use another suitable far-infrared radiation material. The shapes of conventional infrared heating elements and reflectors are straight sheathed tubes and round mirrors, and they were developed for full-surface heating for drying paint, etc.
It is difficult to uniformly irradiate round, round, deep objects such as ceramics, and for heating, and there is a drawback that they are easily cut, distorted, etc. Note that in order to increase drying efficiency, it may be desirable to use radiation and localized air blowing together, but this is rarely used for purposes other than general exhaust equipment. SUMMARY OF THE INVENTION An object of the present invention is to provide a far-infrared drying apparatus for ceramics, etc., using a radiating element that does not suffer from the above-mentioned drawbacks. The radiating element in the device of the present invention is molded from a thermal shock-resistant high-density material such as zircon-based, zircon-ferrite-based, cordierite-based, petalite-based, etc., and has a hollow cross section with a closed curve shape such as an annular shape, and a heating element is inserted into the hollow interior. . As a result of comparative measurements, the above-mentioned materials have better radiation characteristics in the far-infrared region than quartz glass tubes, but have significantly lower characteristics in the near-infrared region. It has been confirmed that ceramics and the like have good absorption characteristics in the far infrared region, and are therefore excellent as radiating elements for drying. Furthermore, by using a closed curve shape such as an annular shape, uneven heating will not occur, and the occurrence of defects will be significantly reduced. The drying device according to the present invention includes an aluminum reflector plate that is combined with the above-mentioned radiating element to perform unidirectional radiation, a blower tube in the center of the reflector plate, and a blower combined with the blower tube. Regarding the reflective properties of the reflector material, an aluminum plate is superior to a stainless steel plate, and commercially available aluminum foil is an inexpensive and effective reflective material. As a result of drying experiments, it was found that the combination of the radiation from the above-mentioned radiating element and a gentle breeze is the most effective in terms of energy. Embodiments and drawings illustrating the present invention will be described. First, the spectral radiation characteristics of various ceramic materials were tested. Zircon base material (ZrSiO 4 60%, 40% clay) as zircon type, 60% petalite, 40% frog's eye clay as petalite type, 50% cordierite siamotsu as cordierite type, 40% clay, 10% magnesite, As a zircon-ferrite system, 70% zircon base material and 30% ferrite are made into a tube shape with a diameter of 5 mm and a length of 25 mm. 1200
It was fired at ~1250°C and heated to 600-800°C, and its radiation properties were recorded and compared with those of a quartz tube and a glass tube. As a result, quartz tubes and glass tubes tend to have strong radiation characteristics in the near-infrared region with wavelengths of 5 μm or less. On the other hand, all of the samples have strong radiation characteristics in the far-infrared region of 5 μm or more, and weak radiation characteristics in the near-infrared region. Therefore, it has become clear that zircon-based, zircon-ferrite-based, petalite-based, and cordierite-based materials are more suitable for heating by far-infrared radiation than quartz tubes and glass tubes. . Furthermore, when a quartz glass tube is coated with the above-mentioned ceramic material, it has almost the same radiation characteristics in the far-infrared region of 5 μm or more, which is superior to that of the quartz glass tube, and it has better radiation characteristics in the near-infrared region. has stronger radiation characteristics than a tube made of a single material, and its value is between that of a tube made of a single material and a quartz glass tube. Therefore, if near-infrared radiation can also be used, a quartz glass tube whose outer surface is coated with a ceramic material can be effectively used. Second, the reflective properties of the mirror material were tested. In order to utilize radiation effectively, materials with high reflectance over the entire wavelength range are required. The materials tested were a standard aluminum-deposited mirror, commercially available aluminum foil for shoe wrapping, an aluminum plate, a stainless steel plate, an anodized aluminum plate, and an aluminum plate for building materials. Among the reflectance measurement samples, the aluminum foil for cushioning showed extremely good reflection characteristics in all wavelength ranges, almost the same as standard mirrors. Stainless steel sheets, which are commonly used, are particularly inferior to aluminum in the near-infrared region. Alumite processing and aluminum plates for building materials are extremely affected by the resin processing on their surfaces, and cannot be used as they are as reflectors. Third, the absorption and reflection properties of clay and gypsum were tested. The absorption properties were tested using the KBr tablet method, and the reflection properties were tested using the reflection method. The trends are similar for both materials, with long wavelengths of 5~
Absorption rate exists on the side of 6 μm or more. Therefore, long wavelength heating is effective. The reflection characteristics of both materials are approximately equal over all wavelengths, but gypsum has a prominent reflection peak around 9 μm. FIG. 1 shows an example of molding a flowerpot 2 in a plaster mold 1 as an example of a ceramic product to be dried. Usually, the flowerpot 2, which has been dried with hot air to shrink and solidify to some extent, is removed from the mold 1 and fired. As a result of a test to quantitatively understand this situation, it was found that dehydration from the pot itself followed a nearly linear process, with the plaster mold absorbing a significantly large amount of water at the beginning, and the mold absorbing water due to the formation of voids. I learned that it decreases. The demolding time could be determined from the water absorption characteristics of the plaster mold. FIGS. 2A and 2B show an annular far-infrared radiating element used in the apparatus of the present invention, and FIG. 3 shows a box-type dryer using this radiating element. The radiating element 3 shown in FIG. 2 has a shape in which a nichrome wire heating element 5 is housed in a cordierite toric body 4, and as shown in FIG. 3, it is covered with a reflecting plate 6.
A blower tube 7 is passed through the center of the reflector 6 so that air from a blower 8 can be sent to the item 10 to be dried. The air blower 8 can adjust the amount of circulating air, and the radiating element 3 can also be switched in strength. In the illustrated example, the drying chamber 11 is of a closed type and has a heat insulating wall 13 having a reflective plate 12 on its inner surface. The indoor exhaust gas is exhausted during the initial period when a large amount of water vapor is generated, and is connected to the blower 8 via the circulation path 14 as required. As a result of comparative experiments using a straight pipe and a torus as a radiating element, we found that the difference in temperature between the top and bottom of a straight pipe is significantly large, while that of a torus is relatively uniform. I learned that it gets heated. As for air blowing during drying, we learned that the combination of radiation and light wind produces the maximum amount of evaporated water and is the most advantageous in terms of energy. If the air volume is large, only the bottom part tends to dry prematurely, resulting in defective products. As mentioned above, since the amount of water absorbed by the plaster mold is extremely large in the early stage of drying, it is desirable to dry the plaster mold every time it is demolded. The dryer shown in FIG. 3 shows a case where the drying chamber 11 is supported by a support shaft (not shown) in a variable angle. The matters revealed by the present invention are as follows. Any radiating element in which a heating element is placed in a tube made of fired heat-resistant ceramic material has a higher specific energy intensity in the far infrared region than quartz glass, and is more advantageous than a quartz glass tube in terms of energy. The cordierite type had the best radiation characteristics in the normal usage range of surface temperature 600-800°C.
However, other ceramic materials can also be used. Aluminum is the best in terms of reflective properties, and commercially available aluminum foil is inexpensive and highly effective. For drying items with circular tops such as flower pots, toroidal radiating elements are significantly more effective than straight tubes in terms of uniform heating. The combination of radiation and air blowing is most effective in terms of energy. However, a light wind speed is good, and excessive wind speed will cause disadvantages. Radiant drying is superior when comparing hot air and radiant drying. With conventional hot air drying, 2 to 2 times a day for an 8-inch pot
Although the mold could only be demolded three times, the time required for demolding by radiation drying was about 30 minutes, and even if the mold drying time of about 10 minutes was added, extremely efficient drying could be achieved. In addition, in order to make the effects of the device of the present invention more clear, the experimental results regarding the water loss rate of clay due to hot air and infrared radiation drying using the device shown in Figure 3 are summarized in Table 1 and Figure 4 below. This will be illustrated in detail with a diagram. Regarding this experiment, in order to investigate how the drying speed differs when the product is dried using hot air and radiation using the same amount of energy, a confectionery pot with a diameter of 26 cm was molded using a mechanical potter's wheel. Immediately after demolding (moisture 24 to 25%), the mold was placed in the apparatus shown in Figure 3, and experiments were conducted with the various combinations shown in Table 1 using the same power of 300W for hot air and radiation, and the results are shown in Figure 4. This is shown in a diagram. As is clear from the above explanation, the apparatus of the present invention can effectively dry the material to be dried by radiation and air blowing, and can independently control radiation and air blowing. It is ideal for drying that requires complex and delicate control.

【表】【table】

【表】【table】 【図面の簡単な説明】[Brief explanation of drawings]

第1図は乾燥すべき品物の例として植木鉢成型
の断面図、第2図Aは本発明装置に使用する円環
状放射素子の平面図、第2図Bは第2図AのB−
B線に沿う拡大断面図、第3図は本発明乾燥装置
の断面図、第4図は放射と温風による減水速度の
比較を示す線図である。 1……石膏型、2……植木鉢、3……放射素
子、4……円環体、5……発熱体、6……反射
板、7……送風筒、8……送風機、10……被乾
燥体、11……乾燥室、12……反射板、13…
…断熱材壁。
FIG. 1 is a cross-sectional view of a molded flowerpot as an example of an item to be dried, FIG. 2A is a plan view of a toric radiating element used in the apparatus of the present invention, and FIG.
FIG. 3 is an enlarged sectional view taken along line B, FIG. 3 is a sectional view of the drying apparatus of the present invention, and FIG. 4 is a diagram showing a comparison of water reduction rates due to radiation and hot air. 1... Gypsum mold, 2... Flower pot, 3... Radiating element, 4... Toric body, 5... Heat generating element, 6... Reflection plate, 7... Blower tube, 8... Blower, 10... Object to be dried, 11...Drying chamber, 12...Reflector, 13...
…Insulation walls.

Claims (1)

【特許請求の範囲】[Claims] 1 断熱材壁13から成る乾燥室11と、この乾
操室11に送風筒7を乾燥室11内に装入せしめ
て装着した送風機8とこの送風機8の送風筒7の
外側に装着したジルコン系、ジルコン−フエライ
ト系、コーデイライト系、ペタライト系等の耐熱
衝撃性材料で成形した断面中空の円環体4内に発
熱体5を収容した円環状遠赤外線放射素子3と前
記送風機8の送風筒7に取付けた反射板6と前記
送風機8と乾燥室11を連通する循環路14とか
ら成る陶磁器、石膏型等の遠赤外線乾燥装置。
1 A drying chamber 11 consisting of a heat insulating wall 13, a blower 8 equipped with a blower tube 7 inserted into the drying chamber 11, and a zircon system attached to the outside of the blower tube 7 of the blower 8. , an annular far-infrared radiating element 3 in which a heating element 5 is accommodated in a toric body 4 with a hollow cross section and made of a thermal shock-resistant material such as zircon-ferrite, cordierite, or petalite, and a blower tube of the blower 8. A far-infrared drying device for ceramics, plaster molds, etc., which comprises a reflector 6 attached to a mirror 7 and a circulation path 14 communicating the blower 8 and a drying chamber 11.
JP12689581A 1981-08-13 1981-08-13 Far infrared-ray drier for pottery, gypsum mold, etc. Granted JPS5828974A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12689581A JPS5828974A (en) 1981-08-13 1981-08-13 Far infrared-ray drier for pottery, gypsum mold, etc.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12689581A JPS5828974A (en) 1981-08-13 1981-08-13 Far infrared-ray drier for pottery, gypsum mold, etc.

Publications (2)

Publication Number Publication Date
JPS5828974A JPS5828974A (en) 1983-02-21
JPH0130076B2 true JPH0130076B2 (en) 1989-06-15

Family

ID=14946524

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12689581A Granted JPS5828974A (en) 1981-08-13 1981-08-13 Far infrared-ray drier for pottery, gypsum mold, etc.

Country Status (1)

Country Link
JP (1) JPS5828974A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020240679A1 (en) * 2019-05-28 2020-12-03 三菱電機株式会社 Water treatment apparatus and water treatment method

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6054963A (en) * 1983-09-07 1985-03-29 松下電器産業株式会社 Manufacture of ceramic dielectric green sheet
JPS60255667A (en) * 1984-05-29 1985-12-17 京セラ株式会社 Infrared radiation ceramic
JPH0634376B2 (en) * 1984-06-25 1994-05-02 住友化学工業株式会社 Infrared heating method
JPH0269495U (en) * 1988-11-14 1990-05-25
JP4916183B2 (en) * 2006-02-20 2012-04-11 三洋電機株式会社 Pack battery

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS50139342U (en) * 1974-05-02 1975-11-17
JPS5344929A (en) * 1976-10-05 1978-04-22 Shimura Norifumi Antiifreezing tap

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020240679A1 (en) * 2019-05-28 2020-12-03 三菱電機株式会社 Water treatment apparatus and water treatment method

Also Published As

Publication number Publication date
JPS5828974A (en) 1983-02-21

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