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JPH0637326B2 - Heat transfer member for heat exchanger - Google Patents
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JPH0637326B2 - Heat transfer member for heat exchanger - Google Patents

Heat transfer member for heat exchanger

Info

Publication number
JPH0637326B2
JPH0637326B2 JP60148824A JP14882485A JPH0637326B2 JP H0637326 B2 JPH0637326 B2 JP H0637326B2 JP 60148824 A JP60148824 A JP 60148824A JP 14882485 A JP14882485 A JP 14882485A JP H0637326 B2 JPH0637326 B2 JP H0637326B2
Authority
JP
Japan
Prior art keywords
heat transfer
heat
transfer member
mullite
gas
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 - Fee Related
Application number
JP60148824A
Other languages
Japanese (ja)
Other versions
JPS6212660A (en
Inventor
宏司 大西
克己 前田
利夫 河波
Original Assignee
株式会社ニッカト−
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 株式会社ニッカト− filed Critical 株式会社ニッカト−
Priority to JP60148824A priority Critical patent/JPH0637326B2/en
Publication of JPS6212660A publication Critical patent/JPS6212660A/en
Publication of JPH0637326B2 publication Critical patent/JPH0637326B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/14Thermal energy storage

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  • Compositions Of Oxide Ceramics (AREA)

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、熱交換器の伝熱用部材に関する。TECHNICAL FIELD The present invention relates to a heat transfer member of a heat exchanger.

従来の技術及びその問題点 熱交換器は、省エネルギーなどの見地から、発電プラン
ト、工業炉、製鉄冶金、化学プラント等における廃熱回
収や燃焼空気の予熱などの目的で広く利用されている。
これらの熱交換器の方式としては、隔壁伝熱式(sheel
型等)として、チユーブの外側に燃焼ガスなどの一次側
の高温ガスを流し、管壁を通じて伝熱により内側に流す
二次側の気体を加熱する方式、蓄熱式(plate-fin 型
等)として、ハニカム構造のローターに高温ガスを通す
ことによつて蓄熱させ、次いで低温の二次側のガスを流
して放熱させる方式などが知られている。このような方
式のうち前者の隔壁伝熱式は一般に比較的大型の熱交換
器において、また後者の蓄熱式は小型の熱交換器におい
て利用されている。
2. Description of the Related Art From the viewpoint of energy saving, heat exchangers are widely used for the purposes of waste heat recovery and preheating of combustion air in power plants, industrial furnaces, iron metallurgy, chemical plants, etc.
As a method of these heat exchangers, a partition wall heat transfer type (sheel
As a type), a high temperature gas on the primary side such as combustion gas is made to flow outside the tube, and the gas on the secondary side that is made to flow to the inside by heat transfer through the tube wall is heated, as a heat storage type (plate-fin type, etc.) A method is known in which high temperature gas is passed through a rotor having a honeycomb structure to store heat, and then a low temperature gas on the secondary side is caused to flow to release heat. Of these methods, the former partition wall heat transfer method is generally used in a relatively large heat exchanger, and the latter heat storage method is used in a small heat exchanger.

熱交換器の伝熱用部材とは、これらの熱交換器におい
て、高温ガスから低温の気体への伝熱部に用いられる材
料である。
The heat transfer member of the heat exchanger is a material used for a heat transfer part from a high temperature gas to a low temperature gas in these heat exchangers.

この熱交換器の伝熱用部材の材料としては、現在主とし
て耐熱合金が用いられているが、耐熱合金は、耐熱性が
充分でなく、通常、使用できる一次側の高温ガスの温度
は800℃程度までが限度であり、これより高温のガス
を使用する場合には冷却空気等を導入して、800℃以
下に冷却して熱交換が行なわれている。よつて得られる
二次側の気体の温度は500℃程度が限度となる。この
ためより高温のガスの利用を可能として効率のよい熱交
換を行なうために、1000℃以上の温度にも長期間耐
え得る材料の開発が要望され、セラミツクス製の伝熱用
部材についての研究が進められている。
Currently, heat-resistant alloys are mainly used as the material for the heat transfer member of this heat exchanger. However, heat-resistant alloys do not have sufficient heat resistance, and the temperature of the high temperature gas on the primary side that can normally be used is 800 ° C. Up to the limit, when using a gas having a temperature higher than this, cooling air or the like is introduced to cool the gas to 800 ° C. or lower for heat exchange. The temperature of the gas on the secondary side thus obtained is limited to about 500 ° C. Therefore, in order to enable the use of higher temperature gas and perform efficient heat exchange, it is required to develop a material that can withstand a temperature of 1000 ° C. or higher for a long time, and research on ceramic heat transfer members is required. It is being advanced.

このような伝熱用部材は、優れた耐熱性を有すると共
に、化学的安定性、耐食性、強度、耐熱衝撃性、耐摩耗
性等に優れた性質を有することが必要とされ、長期間に
亘る耐久性を有することが望まれている。セラミツクス
製の部材は、特に高温や腐蝕性ガスに対して優れた耐久
性を示すものであり、隔壁伝熱式にはSiC、Si
等が、蓄熱式には、コージライト、スポンジユメン等
のリシア系セラミツクス、チタン酸アルミニウム等が用
いられている。
Such a heat transfer member is required to have excellent heat resistance as well as excellent properties such as chemical stability, corrosion resistance, strength, thermal shock resistance, and abrasion resistance, and for a long period of time. It is desired to have durability. The ceramic member has excellent durability especially against high temperature and corrosive gas, and the partition wall heat transfer type is SiC, Si 3 N.
No. 4, etc., in the heat storage type, cordierite, lithia ceramics such as sponge Yumen, aluminum titanate and the like are used.

これらのうち、SiCは、高温強度、熱伝熱性、耐食性
等の点では優れているものの、隔壁のガスリークが生じ
易く、薄壁化が困難であり、高温の燃焼ガスに対する化
学的安定性や耐熱衝撃性に難点があり、また経済性も劣
るものである。
Of these, SiC is excellent in high-temperature strength, heat transfer property, corrosion resistance, etc., but it is apt to cause gas leaks in the partition walls, and it is difficult to make the wall thin, and chemical stability and heat resistance against high-temperature combustion gas are high. It has drawbacks in impact and is inferior in economic efficiency.

SiはSiCに比して耐熱衝撃性に優れているも
のの、高温強度、化学的安定性等に劣るものである。ま
た、SiC及びSiは共に非酸化物からなるため
に、1200℃程度以上の高温の開放雰囲気や酸化雰囲
気では耐酸化性が悪く、酸化分解して長期間に亘る使用
が困難であるという欠点がある。
Si 3 N 4 is superior to SiC in thermal shock resistance, but is inferior in high temperature strength, chemical stability and the like. Further, since both SiC and Si 3 N 4 are made of non-oxides, they have poor oxidation resistance in an open atmosphere or an oxidizing atmosphere at a high temperature of about 1200 ° C. or higher, and are difficult to be used for a long period of time due to oxidative decomposition. There is a drawback that.

蓄熱式の熱交換器に用いられているコージライト、リシ
ア系セラミツクス、チタン酸アルミニウム等は、熱膨脹
が少なく、耐酸化性に優れているものの、耐熱性が悪
く、コージライトは約1200℃、リシア系セラミツク
スは約1000℃、チタン酸アルミニウムは約1200
℃までしか使用できず、更に耐食性、高温安定性、高温
強度、耐摩耗等も満足すべきものではない。
Cordierite, lithia-based ceramics, aluminum titanate, etc. used in heat storage type heat exchangers have low thermal expansion and are excellent in oxidation resistance, but have poor heat resistance, and cordierite is approximately 1200 ° C. System ceramics is about 1000 ℃, aluminum titanate is about 1200
It can only be used up to ℃, and it is not satisfactory in corrosion resistance, high temperature stability, high temperature strength, wear resistance, etc.

上記した如く、現在知られているセラミツクス製の伝熱
用部材は、高温での使用に対して充分満足すべきもので
はなく、このため1000℃以上、より望ましくは12
00℃以上の温度で長期間安定に使用し得る伝熱用部材
の開発が望まれている。
As described above, the currently known ceramic heat transfer members are not sufficiently satisfactory for use at high temperatures. Therefore, the temperature is 1000 ° C. or higher, more preferably 12 ° C. or higher.
It is desired to develop a heat transfer member that can be stably used for a long period of time at a temperature of 00 ° C or higher.

問題点を解決するための手段 本発明者は、高温での使用に長期間耐え得る熱交換器の
伝熱用部材を見出すべく、鋭意研究を重ねてきた。その
結果特定の条件を満足するムライト焼結体からなる伝熱
用部材は、1000℃以上、更には1200℃以上の高
温ガスを熱源とする場合においても、長期間の繰り返し
使用に耐え得るものであることを見出し、ここに本発明
を完成した。
Means for Solving the Problems The inventors of the present invention have conducted extensive studies to find a heat transfer member for a heat exchanger that can withstand use at high temperatures for a long time. As a result, the heat transfer member composed of the mullite sintered body that satisfies the specific conditions can withstand repeated use for a long period of time even when a high temperature gas of 1000 ° C. or higher, further 1200 ° C. or higher is used as the heat source. It was found that there is, and the present invention was completed here.

即ち、本発明は、i)ムライト結晶からなり、SiO2
結晶を含有しない結晶相及び5容積%以下のガラスマト
リツクス相からなり、ii)熱膨脹係数が5.1×10
−6/℃以下、かさ密度が3.0g/cm以上、145
0℃で48時間熱処理後の室温での残存膨脹率が0.2
%以下、であるムライト焼結体からなる熱交換器の伝熱
用部材に係わる。
That is, the present invention comprises i) a mullite crystal, and SiO 2
It consists of a crystal phase containing no crystals and a glass matrix phase of 5% by volume or less, and ii) has a coefficient of thermal expansion of 5.1 × 10 5.
−6 / ° C. or less, bulk density of 3.0 g / cm 3 or more, 145
The residual expansion coefficient at room temperature after heat treatment at 0 ° C for 48 hours is 0.2.
% Or less, the present invention relates to a heat transfer member of a heat exchanger made of a mullite sintered body.

本発明伝熱用部材は、以下の条件を満足するムライト焼
結体からなるものである。
The heat transfer member of the present invention is made of a mullite sintered body that satisfies the following conditions.

a)焼結体における結晶相は、ムライト結晶からなり、
SiO2結晶を含まない。
a) The crystal phase in the sintered body is composed of mullite crystals,
Does not contain SiO 2 crystals.

AlとSiOとの2成分系において常圧下で析
出する結晶相は、Al結晶、ムライト結晶及びS
iO結晶(主としてクリストバライト晶)である。こ
こでムライト結晶とは、化学式3Al・2SiO
(Al71.8重量%、SiO28.2重量
%)で表わされるムライト結晶だけでなく、ムライト固
溶体も含むものとする。
In the binary system of Al 2 O 3 and SiO 2 , the crystal phases precipitated under normal pressure are Al 2 O 3 crystals, mullite crystals and S.
It is an iO 2 crystal (mainly cristobalite crystal). Here, the mullite crystal has a chemical formula of 3Al 2 O 3 .2SiO.
2 (Al 2 O 3 71.8% by weight, SiO 2 28.2% by weight) as well as a mullite solid solution are included.

本発明伝熱用部材を構成する焼結体における結晶相は、
ムライト結晶のみからなり、焼結体の粉末X線回折によ
りSiO結晶及びAl結晶の回折ピークが観察
されてはならない。
The crystal phase in the sintered body constituting the heat transfer member of the present invention,
Diffraction peaks of SiO 2 crystal and Al 2 O 3 crystal should not be observed by powder X-ray diffraction of a sintered body, which consists of mullite crystal only.

SiO結晶が焼結体中に析出する場合には、焼成過程
で液相ができ、焼結性の向上、強度の向上などに有効で
あり、更に高温では液相の塑性変形による靭性の向上が
得られるものの、次に示す如き欠点がある。
When SiO 2 crystals are precipitated in the sintered body, a liquid phase is formed during the firing process, which is effective for improving the sinterability and strength, and at high temperature, the toughness is improved by the plastic deformation of the liquid phase. However, there are the following drawbacks.

即ち、SiO結晶とムライト結晶との熱膨脹率の差に
より、熱サイクルにおいて歪みが増大し、また高温ガス
に含まれる周辺の壁材から生じた揮発成分や燃料から生
じたアルカリ元素、硫黄、バナジウム、灰分等がSiO
と反応して、SiO結晶を変質させ、伝熱用部材の
耐久性が劣るものとなる。また、焼結体の熱膨脹係数を
小さくするためにもSiO晶の存在は好ましくない。
従つて、本発明伝熱用部材では、SiO結晶相が存在
してはならない。
That is, due to the difference in the coefficient of thermal expansion between the SiO 2 crystal and the mullite crystal, the strain increases in the thermal cycle, and the volatile components generated from the surrounding wall material contained in the high temperature gas and the alkali elements, sulfur, and vanadium generated from the fuel. , Ash content is SiO
2 react with, denature the SiO 2 crystals, and that poor durability of the heat transfer member. In addition, the presence of SiO 2 crystals is not preferable in order to reduce the thermal expansion coefficient of the sintered body.
Therefore, in the heat transfer member of the present invention, the SiO 2 crystal phase should not exist.

また、Al結晶が存在する場合には、熱伝導率は
高くなるものの燃料や壁材からのアルカリ元素が高温に
おいてAl結晶と反応してβ−Al結晶を
形成させて焼結体の組織を変質劣化させる。また、Al
結晶とムライト結晶との熱膨脹の差による歪みの
増大や残存膨脹の増大等により耐熱衝撃性が低下すると
いう弊害も生じる。従つて本発明伝熱用部材では、Al
結晶も存在してはならない。
Further, when Al 2 O 3 crystals are present, the thermal conductivity increases, but the alkali element from the fuel or wall material reacts with the Al 2 O 3 crystals at high temperature to form β-Al 2 O 3 crystals. Then, the structure of the sintered body is deteriorated and deteriorated. Also, Al
There is also a problem that the thermal shock resistance is lowered due to an increase in strain due to a difference in thermal expansion between the 2 O 3 crystal and the mullite crystal, an increase in residual expansion, and the like. Therefore, in the heat transfer member of the present invention, Al
No 2 O 3 crystals should also be present.

尚、ムライト結晶は、アスペクト比が2程度以上の針状
結晶の場合は、粒状結晶に比して熱的特性や機械的特性
等に優れたものとなり好ましい。
Incidentally, the mullite crystal is preferable in the case of an acicular crystal having an aspect ratio of about 2 or more because it has excellent thermal characteristics and mechanical characteristics as compared with the granular crystal.

b)焼結体におけるガラスマトリツクス相は5容積%以
下とする。
b) The glass matrix phase in the sintered body is 5% by volume or less.

ガラスマトリツクス相の含有率の測定は以下の方法によ
つて行なう。
The content of the glass matrix phase is measured by the following method.

即ち、まず伝熱用部材の任意の部分から、厚さ1mm以上
の板状試片を切り出し、その表面をダイヤモンド砥石で
粗仕上げし、次いで800番以上の砥石で中仕上げす
る。続いて3μm以下のダイヤモンド粒又はベンガラ、
酸化クロム等の微粉で鏡面になるまで仕上げを行なつた
後、表面付着物を除去して測定試料とする。この試料の
表面に常法に従つて蒸着膜を形成させた後、走査型電子
顕微鏡により、試料表面を3000〜5000倍で写真
撮影する。この顕微鏡写真を写真−Iとする。次いで試
料表面から蒸着膜を除去し、HF1%水溶液中に0〜5
℃で24時間浸漬した後、洗浄、乾燥し、更に、上記し
た場合と同様にして顕微鏡写真撮影を行なう。この顕微
鏡写真を写真−IIとする。写真−I及びIIは試料の同一
部分の少なくとも1000μm以上の面積の部分につ
いての写真とする。
That is, first, a plate-shaped sample having a thickness of 1 mm or more is cut out from an arbitrary portion of the heat transfer member, the surface thereof is roughly finished with a diamond grindstone, and then the surface of the plate is intermediately finished with a grindstone of 800 or more. Subsequently, diamond grains or red iron oxide of 3 μm or less,
After finishing with a fine powder of chromium oxide or the like until it becomes a mirror surface, the adhered substances on the surface are removed to obtain a measurement sample. After forming a vapor-deposited film on the surface of this sample according to a conventional method, the sample surface is photographed at 3000 to 5000 times with a scanning electron microscope. This micrograph is referred to as Photo-I. Then, the vapor deposition film is removed from the sample surface, and 0 to 5 is added to the HF 1% aqueous solution.
After soaking at 24 ° C. for 24 hours, it is washed and dried, and then a micrograph is taken in the same manner as described above. This micrograph is designated as Photo-II. Photos-I and II are photographs of the same portion of the sample having an area of at least 1000 μm 2 or more.

写真−Iからは、試料表面の気泡、亀裂等が凹状となつ
て観察される。この凹状とし観察される部分の面積を求
めて凹部の面積率を算出する。写真−IIからは、気泡、
亀裂の他に、HF処理によつて除去されたガラスマトリ
ツクス部分も凹状となつて観察される。写真−IIから算
出した凹部の面積率と写真−Iから算出した凹部の面積
率との差を試料中のガラスマトリツクス相の表面積割合
とする。ガラスマトリツクス相は、焼結体全体にほぼ均
一に存在するので、上記方法によって求められるガラス
マトリツクス相の面積割合を焼結体中のガラスマトリツ
クス相の容積%とすることができる。このような方法に
より求められるガラスマトリツクス相は、原料中に混入
したアルカリ金属酸化物とAl及びSiOとが
反応して低融物となることによつて生成したものであ
る。
From Photo-I, bubbles, cracks, etc. on the surface of the sample are observed to be concave. The area ratio of the concave portion is calculated by obtaining the area of the portion observed as the concave shape. From Photo-II, bubbles,
In addition to the cracks, the glass matrix parts removed by the HF treatment are also observed to be concave. The difference between the area ratio of the recesses calculated from Photo-II and the area ratio of the recesses calculated from Photo-I is defined as the surface area ratio of the glass matrix phase in the sample. Since the glass matrix phase exists substantially uniformly throughout the sintered body, the area ratio of the glass matrix phase obtained by the above method can be defined as the volume% of the glass matrix phase in the sintered body. The glass matrix phase obtained by such a method is formed by the reaction of the alkali metal oxide mixed in the raw material with Al 2 O 3 and SiO 2 to form a low melt.

ガラスマトリツクス相が5容積%を上回るとムライト結
晶とガラスマトリツクス相との熱膨脹の相違によつて高
温強度が低下し、またガラスマトリツクス相に、燃料や
壁材からのアルカリ元素、硫黄、バナジウム等の成分が
優先的に浸透し、組織を膨脹させ、熱サイクルによる強
度の低下を招き、その結果耐久性が劣るものとなるので
好ましくない。ガラスマトリツクス相は3%以下とする
ことがより好ましい。
When the glass matrix phase exceeds 5% by volume, the high temperature strength decreases due to the difference in thermal expansion between the mullite crystal and the glass matrix phase, and the glass matrix phase contains alkali elements, sulfur, and sulfur from fuel and wall materials. Components such as vanadium preferentially permeate and expand the structure, resulting in a decrease in strength due to heat cycles, resulting in poor durability, which is not preferable. The glass matrix phase is more preferably 3% or less.

c)熱膨脹係数が5.1×10−6/℃以下であり、か
つ1500℃で48時間熱処理を行なつた後の室温での
残存膨脹率が0.2%以下とする。
c) The coefficient of thermal expansion is 5.1 × 10 −6 / ° C. or less, and the residual expansion coefficient at room temperature after heat treatment at 1500 ° C. for 48 hours is 0.2% or less.

本発明に於ては、熱膨脹係数は、室温から800℃まで
5℃/分で昇温した場合の平均線膨脹係数によつて表わ
す。
In the present invention, the coefficient of thermal expansion is represented by the average coefficient of linear expansion when the temperature is raised from room temperature to 800 ° C. at 5 ° C./min.

ムライト焼結体は、ムライト結晶に固溶する成分やガラ
スマトリツクス相の成分、量等によつてその膨脹係数は
異なるものとなる。本発明伝熱用部材は、熱膨脹係数が
5.1×10−6/℃以下のものに限定され、より望ま
しくは4.9×10−6/℃以下のものとする。熱膨脹
係数が5.1×10−6/℃を上回ると、一次側ガスと
二次側ガスとの熱勾配により伝熱用部材の一次側と二次
側の壁面での熱膨脹の差が大きくなつて、その結果大き
な応力が生じ、破損に至る場合が生じるので不適当であ
る。
The expansion coefficient of the mullite sintered body varies depending on the components dissolved in the mullite crystals, the components of the glass matrix phase, the amount, and the like. The heat transfer member of the present invention is limited to one having a thermal expansion coefficient of 5.1 × 10 −6 / ° C. or less, and more preferably 4.9 × 10 −6 / ° C. or less. When the coefficient of thermal expansion exceeds 5.1 × 10 −6 / ° C., the difference in thermal expansion between the primary side wall and the secondary side wall surface of the heat transfer member becomes large due to the thermal gradient between the primary side gas and the secondary side gas. As a result, a large stress is generated, which may lead to damage, which is unsuitable.

残存膨脹率は次の方法により測定する。即ち、まず両端
面を平行に研削、研磨した棒状試料を電気炉で1450
℃まで加熱し、更に1450℃で48時間保持した後徐
冷し、熱処理前後の室温で測定した試料の長さから、熱
処理後に残存する伸びの比率を求め残存膨脹率とする。
残存膨脹率が0.2%を上回ると隔壁伝熱式交換器の伝
熱用部材では、両端が固定されているので使用中に機械
的応力が付加されることとなり、破損、変形等の原因と
なつて熱サイクルに対する耐久性に劣るものとなる。ま
た、二次側ガスの導入、排出部分のシーリングが劣るも
のとなつてガスリークが発生することにもなるので不適
当である。また、蓄熱式交換器においても、残存膨脹率
が0.2%を上回ると熱衝撃抵抗、耐食性、対摩耗性等
が低下することになる。従つて残存膨脹率は0.2%以
下であることが必要であり、好ましくは0,1%以下と
する。
The residual expansion rate is measured by the following method. That is, first, a rod-shaped sample whose both end faces were ground and polished in parallel was 1450 in an electric furnace.
The sample is heated to 0 ° C., kept at 1450 ° C. for 48 hours, then gradually cooled, and the ratio of the elongation remaining after the heat treatment is calculated from the length of the sample measured at room temperature before and after the heat treatment to obtain the residual expansion coefficient.
When the residual expansion coefficient exceeds 0.2%, both ends of the heat transfer member of the partition wall heat transfer type exchanger are fixed, so mechanical stress is applied during use, causing damage, deformation, etc. Therefore, the durability against heat cycle becomes poor. In addition, since the sealing of the secondary gas introduction / exhaust portion is inferior, a gas leak may occur, which is not suitable. Further, also in the heat storage type exchanger, if the residual expansion coefficient exceeds 0.2%, the thermal shock resistance, the corrosion resistance, the wear resistance, etc. are deteriorated. Therefore, it is necessary that the residual expansion coefficient is 0.2% or less, and preferably 0.1% or less.

d)かさ密度は3.0g/cm以上とする。d) The bulk density is 3.0 g / cm 3 or more.

かさ密度が3.0g/cmを下回ると、機械的強度が低
下し、また燃焼ガスに含まれるアルカリ成分等が伝熱用
部材に吸着し易くなり、アルカリ成分等が部材と反応し
て部材の劣化が顕著となつて耐久性に劣るものとなる。
従つて、伝熱用部材のかさ密度は、3.0g/cm以上
であることが必要であり、好ましくは3.05g/cm
以上とする。
When the bulk density is less than 3.0 g / cm 3 , the mechanical strength is lowered, and the alkaline components contained in the combustion gas are easily adsorbed on the heat transfer member, and the alkaline components react with the members to cause the members to react. Markedly deteriorates, resulting in poor durability.
Therefore, the bulk density of the heat transfer member needs to be 3.0 g / cm 3 or more, and preferably 3.05 g / cm 3
That is all.

本発明伝熱用部材は、例えば以下に示す方法によつて作
製することができる。
The heat transfer member of the present invention can be produced, for example, by the method described below.

即ち、まずアルミナゾル、アルミニウムの塩化物、硫酸
塩、硝酸塩等のアルミニウム化合物とシリカゾル、エチ
ルシリケート等のケイ素化合物とを所定のAl/Siの
比率になるように配合した液状の原料を調製する。液状
原料の濃度は高くするほうが経済的には好ましいが、両
成分が均一に分散し、ムライト結晶を生成し易くするた
めには、ゾル溶液の場合には30%以下、塩の溶液の場
合には2モル%以下程度とすることが適当である。
That is, first, a liquid raw material is prepared by mixing an aluminum sol, an aluminum compound such as aluminum chloride, a sulfate or a nitrate with a silicon compound such as silica sol or ethyl silicate so as to have a predetermined Al / Si ratio. It is economically preferable to increase the concentration of the liquid raw material, but in order to easily disperse both components evenly and form mullite crystals, in the case of a sol solution, 30% or less, and in the case of a salt solution, Is appropriately about 2 mol% or less.

液状原料におけるAl/Siの比率は、焼結体の熱膨脹
係数を小さくするためには、Al量がムライト中
への固溶限定以下となるようにすることが適当であり、
Alが約69〜74重量%、SiOが約26〜
31重量%となる比率とすればよい。また、Al
とSiOの合計量は、焼結体中に98重量%以上とす
ることが好ましい。また熱膨脹係数を小さくするために
は、MgO、B等を原料中に少量存在させること
も有効であり、このために、液状原料中にMg成分やB
分を少量添加してもよい。
In order to reduce the thermal expansion coefficient of the sintered body, it is appropriate that the Al / Si ratio in the liquid raw material be such that the amount of Al 2 O 3 is below the solid solution limit in mullite.
Al 2 O 3 is approximately 69 to 74% by weight, and SiO 2 is approximately 26 to
The ratio may be 31% by weight. In addition, Al 2 O 3
The total amount of SiO 2 and SiO 2 is preferably 98% by weight or more in the sintered body. In addition, in order to reduce the coefficient of thermal expansion, it is effective to allow a small amount of MgO, B 2 O 3 or the like to be present in the raw material.
A small amount may be added.

液状原料を調製した後Al分及びSi分が均一に分散さ
れるように液状原料を充分に混合し、この液状原料から
アルミニウム化合物とケイ素化合物とが均一に混合した
粉体を形成させる。液状原料から粉体試料を得る方法と
しては、アルミニウム化合物とケイ素化合物とを均一に
共沈させた後乾燥させる方法、液状原料から水分を蒸発
させて粉体試料を得る方法、液状原料を噴霧させて熱分
解する方法等を例示できる。
After the liquid raw material is prepared, the liquid raw material is thoroughly mixed so that the Al content and the Si content are uniformly dispersed, and a powder in which an aluminum compound and a silicon compound are uniformly mixed is formed from the liquid raw material. As a method for obtaining a powder sample from a liquid raw material, a method of uniformly coprecipitating an aluminum compound and a silicon compound and then drying, a method of evaporating water from the liquid raw material to obtain a powder sample, and a method of spraying the liquid raw material A thermal decomposition method or the like can be exemplified.

このようにして得られた粉体試料を成形後の焼成工程で
の寸法変化を少なくするために900〜1350℃、好
ましくは980〜1280℃で焙焼する。焙焼後の粉体
試料に未反応のSiOやAl、或いは非晶質相
等が多量に存在する場合には、以後の工程で粉体試料の
凝集や分離が生じ易くなるので好ましくない。また、焼
結体の残存膨脹を少なくするためにも、粉体試料を焙焼
工程でムライト化させておくことが好ましい。このため
焙焼条件は、粉体試料のムライト化が進むような条件と
することが適切であり、具体的には、焙焼後の粉体試料
にムライトのX線回折ピークが生じるような条件で焙焼
し、SiOやAlの回折ピークが生じない程度
まで焙焼することが好ましい。
The powder sample thus obtained is roasted at 900 to 1350 ° C., preferably 980 to 1280 ° C. in order to reduce the dimensional change in the firing step after molding. When a large amount of unreacted SiO 2 , Al 2 O 3 , or an amorphous phase is present in the powder sample after roasting, aggregation or separation of the powder sample easily occurs in the subsequent steps, which is preferable. Absent. Further, in order to reduce the residual expansion of the sintered body, it is preferable to make the powder sample mullite in the roasting step. For this reason, it is appropriate that the roasting conditions are such that the mullite of the powder sample proceeds, and specifically, the X-ray diffraction peak of mullite is generated in the powder sample after roasting. It is preferable to roast in (1) and roast to such an extent that a diffraction peak of SiO 2 or Al 2 O 3 does not occur.

次いで得られた粉体試料を粉砕し分散させる。粉砕によ
り粉体の平均粒度を2μm程度以下、比表面積を1m
/g程度以上とすることが好ましい。平均粒度が2μm
を上回ると粉体の成形、焼成時に成形体内部に欠陥が生
じ易くなり、また比表面積を1m/gを下回ると焼結
性が劣るものとなるので好ましくない。また、粉砕工程
で、粉体を微細化することにより、密度の高い焼結体と
することができる。このために、粉体の平均粒径を1μ
m以下とすることがより好ましい。粉体の粉砕及び分散
は、常法に従えばよく、例えばボールミル、振動ミル、
アトリツシヨンミル、遠心ミル等を使用すればよい。
Then, the obtained powder sample is pulverized and dispersed. By pulverization, the average particle size of the powder is about 2 μm or less, and the specific surface area is 1 m 2.
/ G or more is preferable. Average particle size is 2 μm
If it exceeds the range, defects are likely to occur inside the molded body during the molding and firing of the powder, and if the specific surface area falls below 1 m 2 / g, the sinterability tends to be poor, such being undesirable. In addition, by pulverizing the powder in the pulverizing step, a sintered body having a high density can be obtained. For this purpose, the average particle size of the powder is 1μ
More preferably, it is m or less. The pulverization and dispersion of the powder may be carried out according to a conventional method, for example, a ball mill, a vibration mill,
An attrition mill, a centrifugal mill or the like may be used.

次いで、このようにして調製した粉体を用いて、セラミ
ツクスの製造における常法に従つて、鋳込み成形、押出
し成形、プレス成形等の方法で所定の形状に成形した
後、焼成することにより本発明伝熱用部材が得られる。
焼成温度は、通常、常圧下で1550〜1750℃程
度、好ましくは、1600〜1650℃程度とすればよ
い。一般に、焼成温度が高くなるとガラスマトリツクス
相が多くなり、また、密度が高くなる傾向にある。一
方、焼成温度を低くすると逆に、ガラスマトリツクス相
が少なくなり、密度が低くなる傾向にある。また、残存
膨脹を少なくするには、焼成温度を高くしすぎることな
く、やや低めの温度で長時間焼成することが好ましい。
また、アスペクト比を大きくするためには、焼成温度を
高くしすぎないことか好ましい。従つて、原料組成、成
形条件等に応じて前記したa)〜d)の条件を満足する
焼結体が得られるような具体的な焼成温度を適宜決定す
ればよい。また焼成時間も焼成温度、原料組成、成形条
件等に応じて前記a)〜d)の条件を満足するように適
宜決定すればよい。
Then, by using the powder thus prepared, according to a conventional method in the production of ceramics, after molding into a predetermined shape by a method such as cast molding, extrusion molding, and press molding, the present invention A member for heat transfer is obtained.
The firing temperature is usually about 1550 to 1750 ° C, preferably about 1600 to 1650 ° C under normal pressure. Generally, as the firing temperature increases, the glass matrix phase tends to increase and the density tends to increase. On the other hand, when the firing temperature is lowered, on the contrary, the glass matrix phase tends to decrease and the density tends to decrease. Further, in order to reduce the residual expansion, it is preferable to perform firing at a rather low temperature for a long time without raising the firing temperature too high.
Further, in order to increase the aspect ratio, it is preferable that the firing temperature is not too high. Therefore, a specific firing temperature may be appropriately determined so that a sintered body satisfying the above conditions a) to d) can be obtained according to the raw material composition, the molding conditions, and the like. Also, the firing time may be appropriately determined so as to satisfy the above conditions a) to d) depending on the firing temperature, the raw material composition, the molding conditions, and the like.

本発明伝熱用部材では、ガラスマトリツクス相の存在量
を少なくし、また熱膨脹係数を小さくするためには、N
a、K等のアルカリ物質の含有量は酸化物換算で0.2
重量%以下とすることが好ましく、0.1重量%以下と
することがより好ましい。このため不純物含有量が少な
い原料を使用するか、或いは粉体試料の調製工程におい
て脱アルカリ処理を行なうことが好ましい。また、熱膨
脹係数を小さくするためには、原料中にCaOが混入す
ることを防ぐようにすることが好ましい。
In the heat transfer member of the present invention, in order to reduce the existing amount of the glass matrix phase and to reduce the thermal expansion coefficient, N
The content of alkaline substances such as a and K is 0.2 in terms of oxide.
It is preferably not more than 0.1% by weight, more preferably not more than 0.1% by weight. Therefore, it is preferable to use a raw material having a low content of impurities or to carry out dealkalization treatment in the step of preparing the powder sample. Further, in order to reduce the coefficient of thermal expansion, it is preferable to prevent CaO from being mixed in the raw material.

本発明では、上記した方法で液状原料から粉体試料を調
製することによつて、Al分及びSi分が微小部分まで
均一に混合した焼結性に優れた粉体が得られる。従つ
て、本発明伝熱用部材の如く、ガラスマトリツクス相や
不純物量が少ない場合にも高強度を有し、耐熱衝撃抵抗
性等に優れたムライト焼結体を得ることができる。
In the present invention, by preparing a powder sample from the liquid raw material by the above-mentioned method, a powder having excellent sinterability in which Al and Si are evenly mixed to a minute portion can be obtained. Therefore, like the heat transfer member of the present invention, it is possible to obtain a mullite sintered body having high strength even when the glass matrix phase and the amount of impurities are small and having excellent thermal shock resistance and the like.

発明の効果 本発明の伝熱用部材は、耐熱性、耐熱衝撃低抗性、熱的
安定性等に優れ、かつ、高強度を有するムライト焼結体
からなるものであり、下記の如き優れた特性を有する。
EFFECTS OF THE INVENTION The heat transfer member of the present invention is made of a mullite sintered body having excellent heat resistance, thermal shock resistance, thermal stability, etc., and high strength. Have characteristics.

1.1200℃以上の高温においても、機械的強度、耐
食性等に優れ、このため伝熱用部材として使用する場合
に壁厚を薄くしても充分使用に耐え得るものである。よ
つて熱交換器の熱効率の向上や軽量化が図れる。
1. Even at a high temperature of 1200 ° C. or higher, it has excellent mechanical strength, corrosion resistance, etc. Therefore, when it is used as a heat transfer member, it can withstand use even if the wall thickness is thin. Therefore, the heat efficiency and the weight of the heat exchanger can be improved.

2.耐熱衝撃性に優れたものであり、一次側ガスと二次
側ガスの導入時の温度差を高く設定できる。
2. It has excellent thermal shock resistance, and can set a high temperature difference when introducing the primary gas and the secondary gas.

3.熱サイクルに対して熱安定性が良好であり、耐久性
が優れたものである。
3. It has good thermal stability against heat cycles and excellent durability.

4.燃焼ガスや壁材からの揮発分中に含まれる腐蝕性成
分や粉じんに対して高い耐久性を有する。
4. It has high durability against corrosive components and dust contained in volatile components from combustion gas and wall materials.

上記した如く、本発明伝熱用部材は優れた性質を有する
ものであつて1000℃以上、更には1200℃の温度
の一次側ガスを用いる熱交換器の伝熱用部材として長期
間安定に使用し得るものであり、特に隔壁伝熱方式の熱
交換器の伝熱用部材として有用である。また、本発明伝
熱用部材は、同様な性質が要求される搬送用セラミツク
ローラー、炉心管、匣鉢、セツター、バーナーノズル等
としても使用し得るものである。
As described above, the heat transfer member of the present invention has excellent properties and can be stably used for a long period of time as a heat transfer member of a heat exchanger using a primary side gas at a temperature of 1000 ° C. or more and 1200 ° C. In particular, it is useful as a heat transfer member of a partition wall heat transfer type heat exchanger. Further, the heat transfer member of the present invention can be used as a transportation ceramic roller, a furnace tube, a sagger, a setter, a burner nozzle, etc., which are required to have similar properties.

実施例 以下に実施例及び比較例を示して本発明を一層詳細に説
明する。
EXAMPLES The present invention will be described in more detail with reference to Examples and Comparative Examples below.

実施例1〜2及び比較例1〜4 0.5モル%の塩化アルミニウム溶液と20%のシリカ
ゾル溶液とを第1表に示すAlとSiOとの比
率になるように配合した溶液を調製した。次いでこの溶
液を均質になるように充分混合した後、アンモニア水で
中和共沈させて、その沈澱分を乾燥し、1250℃で焙
焼してムライト化した粉末を得た。ただし、実施例2で
は、MgOが粉体中に0.5%含まれるように、Mg
(NO溶液を液体試料中に添加した後、粉末を調
製した。また、比較例3では、焙焼後の粉末にアルミナ
晶が残留していた。
Examples 1 and 2 and Comparative Examples 1 to 4 Solutions in which 0.5 mol% aluminum chloride solution and 20% silica sol solution were blended so as to have a ratio of Al 2 O 3 and SiO 2 shown in Table 1. Was prepared. Then, this solution was thoroughly mixed so as to be homogeneous, then neutralized and coprecipitated with aqueous ammonia, and the precipitate was dried and roasted at 1250 ° C. to obtain mullite powder. However, in Example 2, the content of MgO should be 0.5% so that MgO is contained in the powder.
(NO 3) 2 solution was added to the liquid sample to prepare a powder. Further, in Comparative Example 3, alumina crystals remained in the powder after roasting.

次いで上記粉末をボールミルにより湿式で24時間粉砕
し、分散させて原料粉末を得た。この原料粉末に2%の
PVAを加えた後、静水圧成形法により成形圧2トン/
cmで外径20mm、内径16mm、長さ600mmのチユー
ブ状に成形し、第2表の各温度で約3時間焼成してムラ
イト質の焼結体を得た。
Next, the above powder was wet-milled for 24 hours by a ball mill and dispersed to obtain a raw material powder. After adding 2% PVA to this raw material powder, a molding pressure of 2 tons /
It was molded into a tube shape having an outer diameter of 20 mm, an inner diameter of 16 mm and a length of 600 mm in cm 2 , and was fired at each temperature shown in Table 2 for about 3 hours to obtain a mullite sintered body.

焼結体の結晶相におけるムライト結晶及びアルミナ結晶
の容積割合、焼結体におけるガラスマトリツクス相の容
積割合、熱膨脹係数、残存膨脹率及びかさ密度を第2表
に示す。
Table 2 shows the volume ratio of the mullite crystals and the alumina crystals in the crystal phase of the sintered body, the volume ratio of the glass matrix phase in the sintered body, the coefficient of thermal expansion, the residual expansion coefficient and the bulk density.

試験1 実施例1〜2及び比較例1〜4のチユーブをLPGを燃
料とする窯炉の煙道において、燃焼ガスの温度が135
0℃、1300℃及び1100℃となる各部分にガスの
流れに垂直となる様に設置した。各チユーブが各々のガ
ス温度に達した後、チユーブ片方からチユーブ内に50
℃の空気を導入し、5時間各温度に保ち、その後放冷し
た。この操作には、昇温、冷却を含めて48時間を要し
た。この操作を繰り返し行なつた場合にチユーブに破
損、亀裂等が生じてガスリークを起こし再使用できなく
なるまでの繰り返し回数を求めた。また、かさ密度2.
6g/cmのSiCからなるチユーブ及びかさ密度3.
1g/cmのSiからなるチユーブについても同
様に試験を行なつた。結果を第3表に示す。
Test 1 In the flue of a kiln in which the tubes of Examples 1 and 2 and Comparative Examples 1 to 4 were fueled with LPG, the temperature of the combustion gas was 135.
It was installed in each part at 0 ° C., 1300 ° C. and 1100 ° C. so as to be perpendicular to the gas flow. After each tube has reached its respective gas temperature, 50 from one tube into the tube.
C. Air was introduced, the temperature was maintained for 5 hours, and then the mixture was allowed to cool. This operation required 48 hours including heating and cooling. When this operation was repeated, the number of repetitions was calculated until the tube was damaged, cracked, or the like to cause a gas leak and the tube could not be reused. Also, the bulk density 2.
A tube made of 6 g / cm 3 of SiC and a bulk density of 3.
The same test was performed on a tube made of 1 g / cm 3 of Si 3 N 4 . The results are shown in Table 3.

試験2 実施例1〜2及び比較例1〜4のチユーブを長さ5mmに
輪切りしたものを試験片として、バナジムを500ppm
、ナトリウムを50ppm 含有する灯油の燃焼ガスで加
熱して、1100℃及び1450℃の各温度に各々50
時間保ち、耐食試験を行なつた。耐食試験前後の円環試
料による曲げ強さを室温で測定した結果を第4表に示
す。
Test 2 Vanadium was added to 500 ppm of vanadium as test pieces obtained by cutting the tubes of Examples 1 and 2 and Comparative Examples 1 to 4 into 5 mm long pieces.
, Heated with combustion gas of kerosene containing 50ppm of sodium, 50 at each temperature of 1100 ℃ and 1450 ℃.
The time was kept and a corrosion resistance test was conducted. Table 4 shows the results of measuring the bending strength of the circular ring sample before and after the corrosion resistance test at room temperature.

試験3 実施例1〜2及び比較例1〜4と同様の方法で外径2mm
の球状の伝熱用部材を作製した。この球状の伝熱用部材
を内径80mmのパイプ中に10cmの高さまで充填し、そ
の両端を耐熱合金の金網でふたをした。次いでバーナー
でパイプの一方の口から高温ガスを吹き付けて、3分間
加熱して、パイプの中央部の温度を1100℃とした。
次に、30℃の空気を高温ガスを吹き付けた方向と同方
向に該パイプ中に3分間吹き込む操作を100回繰り返
した後、伝熱用部材を取り出し、クラツクの発生の有無
を調べた。
Test 3 Outer diameter 2 mm in the same manner as in Examples 1-2 and Comparative Examples 1-4
A spherical heat transfer member was produced. This spherical heat transfer member was filled in a pipe having an inner diameter of 80 mm to a height of 10 cm, and both ends thereof were covered with a wire mesh of a heat resistant alloy. Then, a high temperature gas was blown from one end of the pipe with a burner and heated for 3 minutes to bring the temperature of the central portion of the pipe to 1100 ° C.
Then, the operation of blowing air at 30 ° C. into the pipe in the same direction as the high-temperature gas was blown for 3 minutes was repeated 100 times, and then the heat transfer member was taken out and examined for the occurrence of cracks.

その結果実施例1の伝熱用部材では、パイプの入口から
4〜6mmまでの部分の球にクラツクが入つたものが認め
られ、また実施例2の伝熱用部材ではクラツクの発生は
なかつた。また、高温ガスを導入した方向と逆方向から
パイプ中に30℃の空気を導入した場合には、実施例1
及び2の伝熱用部材では、クラツクの発生は認められな
かつた。一方比較例1及び比較例4の伝熱用部材では、
高温ガスと同方向から空気を導入した場合にはパイプの
入口から約4〜5cmまでの部分の球にクラツクが入つた
ものが多数認められ、また、比較例2及び比較例3の伝
熱用部材ではパイプの入口から約2cmまでの部分の球に
クラツクの入つたものが多数認められた。また、比較例
1〜4では、パイプのへの空気の導入を逆方向から行な
つた場合にも球にクラツクの発生が認められた。
As a result, in the heat transfer member of Example 1, it was recognized that cracks were contained in the sphere in the portion 4 to 6 mm from the pipe inlet, and in the heat transfer member of Example 2, no crack was generated. . In addition, when air at 30 ° C. was introduced into the pipe from the direction opposite to the direction in which the high temperature gas was introduced, Example 1
No cracking was observed in the heat transfer members of Nos. 2 and 2. On the other hand, in the heat transfer members of Comparative Example 1 and Comparative Example 4,
When air was introduced from the same direction as the high temperature gas, a large number of cracks were found in the sphere in the portion of about 4 to 5 cm from the inlet of the pipe, and for heat transfer in Comparative Examples 2 and 3. As for the members, many balls with cracks were found in the sphere in the part up to about 2 cm from the entrance of the pipe. Also, in Comparative Examples 1 to 4, cracking was observed in the balls even when the air was introduced into the pipe from the opposite direction.

以上の試験結果から、本発明伝熱用部材は、1000℃
以上の高温ガスを熱源とする場合にも繰り返し使用し耐
え得るものであり、また、バナジウム、ナトリウム等の
腐蝕性成分を含有する燃焼ガスによる強度の低下も少な
いことが明らかである。
From the above test results, the heat transfer member of the present invention is 1000 ° C.
It is clear that it can withstand repeated use even when the above high-temperature gas is used as a heat source, and that there is little reduction in strength due to combustion gas containing corrosive components such as vanadium and sodium.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】i)ムライト結晶からなり、SiO2結晶
を含有しない結晶相及び5容積%以下のガラスマトリッ
クス相からなり、 ii)熱膨脹係数が5.1×10-6/℃以下、かさ密度が
3.0g/cm以上、1450℃で48時間熱処理後の
室温での残存膨脹率が0.2%以下、 であるムライト焼結体からなる熱交換器の伝熱用部材。
1. A mullite crystal, a crystal phase containing no SiO 2 crystals and a glass matrix phase of 5% by volume or less, and ii) a coefficient of thermal expansion of 5.1 × 10 −6 / ° C. or less and a bulk density. Is 3.0 g / cm 3 or more, and the residual expansion coefficient at room temperature after heat treatment at 1450 ° C. for 48 hours is 0.2% or less, which is a mullite sintered body.
JP60148824A 1985-07-05 1985-07-05 Heat transfer member for heat exchanger Expired - Fee Related JPH0637326B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60148824A JPH0637326B2 (en) 1985-07-05 1985-07-05 Heat transfer member for heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60148824A JPH0637326B2 (en) 1985-07-05 1985-07-05 Heat transfer member for heat exchanger

Publications (2)

Publication Number Publication Date
JPS6212660A JPS6212660A (en) 1987-01-21
JPH0637326B2 true JPH0637326B2 (en) 1994-05-18

Family

ID=15461543

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60148824A Expired - Fee Related JPH0637326B2 (en) 1985-07-05 1985-07-05 Heat transfer member for heat exchanger

Country Status (1)

Country Link
JP (1) JPH0637326B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS589333A (en) * 1981-07-08 1983-01-19 Hitachi Ltd Semiconductor device
DE3902701A1 (en) * 1988-01-30 1989-08-10 Toshiba Kawasaki Kk METHOD FOR PRODUCING A SEMICONDUCTOR ARRANGEMENT
JP5292690B2 (en) * 2006-10-31 2013-09-18 新日鐵住金株式会社 Heat storage member and heat exchanger using the same

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5729437B2 (en) * 1974-10-31 1982-06-22
DE2920795A1 (en) * 1979-05-22 1980-12-04 Max Planck Gesellschaft HIGH-STRENGTH AND TEMPERATURE-RESISTANT CERAMIC MOLDED BODY, ESPECIALLY MULLIT, ITS PRODUCTION AND USE

Also Published As

Publication number Publication date
JPS6212660A (en) 1987-01-21

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