JPH01138108A - Inorganic silazane high-polymer, its production and use thereof - Google Patents

Inorganic silazane high-polymer, its production and use thereof

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Publication number
JPH01138108A
JPH01138108A JP63074918A JP7491888A JPH01138108A JP H01138108 A JPH01138108 A JP H01138108A JP 63074918 A JP63074918 A JP 63074918A JP 7491888 A JP7491888 A JP 7491888A JP H01138108 A JPH01138108 A JP H01138108A
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JP
Japan
Prior art keywords
inorganic silazane
weight
inorganic
polymer
silazane
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.)
Granted
Application number
JP63074918A
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Japanese (ja)
Other versions
JP2613787B2 (en
Inventor
Toru Funayama
舟山 徹
Mikiro Arai
新井 幹郎
Takeshi Isoda
礒田 武志
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.)
SEKIYU SANGYO KATSUSEIKA CENTER
Tonen General Sekiyu KK
Japan Petroleum Energy Center JPEC
Original Assignee
SEKIYU SANGYO KATSUSEIKA CENTER
Petroleum Energy Center PEC
Toa Nenryo Kogyyo KK
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Publication of JPH01138108A publication Critical patent/JPH01138108A/en
Application granted granted Critical
Publication of JP2613787B2 publication Critical patent/JP2613787B2/en
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Abstract

PURPOSE:To obtain a suitable silicon nitride precursor having specific mol.wt., SiH2/SiH3 ratio, Si, N and H contents and obtain a coating agent, etc., having excellent heat-resistance, etc., by heating an inorganic silazane in a basic solvent, etc. CONSTITUTION:A high-polymer of an inorganic silazane having a number- average mol.wt. of 200-500,000, a radio of SiH2 group/SiH3 group of 2.5-8.4 in 1mol. and containing 50-70wt.% of Si, 20-34wt.% of N and 5-9wt.% of H can be produced by heating an inorganic silazane in a basic solvent or a solvent containing a basic compound. A coating agent or a binder can be produced by using the polymer as an essential component.

Description

【発明の詳細な説明】 〔技術分野〕 本発明は無機シラザン高重合体、その製造方法及びその
用途に関し、更に詳しくは窒化珪素および窒化珪素含有
セラミックスの前暉体として使用することのできる無機
シラザン高重合体、その製造方法及び該無機シラザン高
重合体を必須成分としたコーティング剤及びバインダー
に関する。
[Detailed Description of the Invention] [Technical Field] The present invention relates to an inorganic silazane polymer, a method for producing the same, and its uses, and more specifically, an inorganic silazane that can be used as a precursor for silicon nitride and silicon nitride-containing ceramics. The present invention relates to a high polymer, a method for producing the same, and a coating agent and binder containing the inorganic silazane high polymer as an essential component.

従来、窒化珪素の製造方法としては、■金属シリコン粉
末を窒素又はアンモニア気流中で、1300℃〜150
0°Cで加熱して直接窒化するシリコン直接窒化法、■
シリカ又は含シリカ物質を炭素と共に窒素雰囲気下で加
熱し、尿素でシリカを還元して、生成するケイ素と窒素
とを反応させるシリカ還元法、■四塩化珪素とアンモニ
アとを高温で直接反応せしめる気相合成法、■四塩化珪
素をアンモノリシスして得られるシリコンジイミドを非
酸化性雰囲気中で加熱して窒化珪素を得るイミド熱分解
法等が採用されている。
Conventionally, methods for producing silicon nitride include: heating metal silicon powder at 1300°C to 150°C in a nitrogen or ammonia stream;
Silicon direct nitriding method, which heats at 0°C and directly nitrides,■
A silica reduction method in which silica or a silica-containing substance is heated together with carbon in a nitrogen atmosphere, the silica is reduced with urea, and the resulting silicon reacts with nitrogen. ■ A method in which silicon tetrachloride and ammonia are directly reacted at high temperatures. Phase synthesis method, (2) imide thermal decomposition method in which silicon diimide obtained by ammonolysis of silicon tetrachloride is heated in a non-oxidizing atmosphere to obtain silicon nitride, etc. are employed.

しかしながら、上記■の方法の場合には、反応時間が長
く、加熱工程が煩雑である上、得られる窒化珪素は粗大
で不純物を多く含むβ型窒化珪素が主体であり、■の方
法の場合には1.原料の精製が困難なばかりでなく、反
応時間が長く、得られる生成物はα型窒化珪素とβ型窒
化珪素の混合系であり、■の方法の場合には、生成した
窒化珪素は一般に非晶質であり、■の方法の場合には、
高純度のα型窒化珪素を収率よく製造し得るという利点
が有るものの、窒化珪素前駆体であるシリコンジイミド
(Si(NH)、)xは溶媒に溶けないために実質的に
用途が限定されざるを得ない等の欠点があった。
However, in the case of method (2) above, the reaction time is long, the heating process is complicated, and the silicon nitride obtained is mainly β-type silicon nitride that is coarse and contains many impurities. is 1. Not only is it difficult to purify the raw materials, the reaction time is long, and the product obtained is a mixed system of α-type silicon nitride and β-type silicon nitride. It is crystalline, and in the case of method ■,
Although it has the advantage of being able to produce high-purity α-type silicon nitride with good yield, the silicon diimide (Si(NH))x, which is a silicon nitride precursor, is not soluble in solvents, so its uses are essentially limited. There were some unavoidable drawbacks.

更に、最近、有機ポリシラザンを熱分解して得られるポ
リシラザンを800〜2000℃で加熱して窒化珪素を
合成する方法も提案されている(斉藤肇、繊維学会誌 
VoQ38Nal第65頁〜第72頁[1982年])
が、この方法では窒化珪素と同時に炭化珪素や遊離の炭
素が生成するという欠点が有った。
Furthermore, a method has recently been proposed in which silicon nitride is synthesized by heating polysilazane obtained by thermally decomposing organic polysilazane at 800 to 2000°C (Hajime Saito, Journal of the Japan Institute of Textile Technology)
VoQ38Nal pages 65-72 [1982])
However, this method has the disadvantage that silicon carbide and free carbon are produced simultaneously with silicon nitride.

一方、溶媒に可溶である無機ポリシラザンは。On the other hand, inorganic polysilazane is soluble in solvents.

1921年に5tack(Ber、54.(1921)
、p740)等によって合成されており、1983年に
は5eyferth (Go+am、 Am、Cera
m、soc、c−13/14. (g3))等によって
、これが窒化珪素前駆体として有用であることが証明さ
れている。本発明者等は、かかる観点に注目し無機ポリ
シラザンを加熱処理することにより、高純度のα型窒化
珪素を得る方法を提案した(特開昭59−207812
号)。
5tack in 1921 (Ber, 54. (1921)
, p740), etc., and in 1983, 5eyferth (Go+am, Am, Cera
m, soc, c-13/14. (g3)) etc., it has been proven that this is useful as a silicon nitride precursor. The present inventors focused on this point of view and proposed a method for obtaining highly pure α-type silicon nitride by heat-treating inorganic polysilazane (Japanese Patent Application Laid-Open No. 59-207812
issue).

しかしながら、従来の無機ポリシラザンの製造方法にお
いては、何れの場合も気化性の高いジクロロシランを原
料として用いるために、■反応装置のガス配管又は反応
器壁に生成したポリシラザンが固着してガス流路を閉塞
する恐れがある、■上記弊害を防止するためには反応温
度を低温に維持してジクロロシランの飛散を防止する必
要が有る、■ジクロロシランは毒性及び引火性が強いの
で低温密閉容器に入れて利用せねばならないなど取扱が
煩雑である等の欠点があった。更に2合成されたポリシ
ラザンは5tack等の場合には、−(SiHJH)n
−の構造を有するn=7〜8のオリゴマーにすぎず常温
では粘性のある液体であり、5eyferth等の場合
には、5tack等の場合より複雑な構造を有し、5i
−H/N−Hのプロトン比が約3.3のオイル状液体で
あるが、約200℃で加熱するか室温で3日〜5日放置
することにより固化するものであり、いずれのポリシラ
ザンの場合であっても、常温で賦形化した窒化珪素焼結
体のための前駆体として十分な性質を有していると言え
るものではなかった。
However, in the conventional manufacturing method of inorganic polysilazane, since highly volatile dichlorosilane is used as a raw material in all cases, the polysilazane produced sticks to the gas piping or the reactor wall of the reactor and damages the gas flow path. - In order to prevent the above-mentioned adverse effects, it is necessary to maintain the reaction temperature at a low temperature to prevent dichlorosilane from scattering. - Dichlorosilane is highly toxic and flammable, so it should not be stored in a closed container at low temperatures. There were disadvantages such as complicated handling, such as having to put it in and use it. Furthermore, in the case of 5tack etc., the synthesized polysilazane is -(SiHJH)n
It is only an oligomer of n=7 to 8 having a structure of - and is a viscous liquid at room temperature.
It is an oily liquid with a -H/N-H proton ratio of about 3.3, but it solidifies by heating at about 200°C or leaving it at room temperature for 3 to 5 days. Even in the case of sintered silicon nitride, it could not be said that it had sufficient properties as a precursor for a silicon nitride sintered body shaped at room temperature.

したがって、より高い分子量と曳糸性を有する窒化珪素
の前駆体として有用な無機シラザン及びこのものをより
収率よくかつより容易に合成できる方法の開発が望まれ
ていた。
Therefore, it has been desired to develop an inorganic silazane useful as a precursor of silicon nitride having a higher molecular weight and stringiness, and a method for easily synthesizing this inorganic silazane with higher yield.

一方、金属材料や無機材料の表面のコーティング剤とし
ては、シリコン系塗料、ポリチタノカルボシラン系塗料
、更にはポリ(ジシリル)シラザン重合体等(特公昭6
1−38933号公報)を使用する方法が知られている
On the other hand, coating agents for the surfaces of metal and inorganic materials include silicone paints, polytitanocarbosilane paints, and even poly(disilyl)silazane polymers (Special Publications No. 6).
1-38933) is known.

しかしながら、シリコーン系塗料は200℃以上の高温
雰囲気下でも耐熱効果に優れた被膜を与えるものの、ピ
ンホールが発生し易く、またこのピンホールの発生を防
止するためにその被膜の膜厚を厚くすると焼成中に被膜
にクラックやブリスターが生じたり剥離が生ずる場合が
ある。このような現象は300℃以上の温度領域下にお
いて特に顕著にみられるため、シリコーン系塗料を用い
る場合には、シリコーン樹脂の架橋密度を減少させる必
要があり、このため形成被膜の表面硬度が低下するとい
う難点が生じる。
However, although silicone paints provide a film with excellent heat resistance even in high-temperature atmospheres of 200°C or higher, they tend to generate pinholes, and in order to prevent the formation of pinholes, the film thickness of the film must be increased. Cracks, blisters, or peeling may occur in the coating during firing. This phenomenon is particularly noticeable at temperatures above 300°C, so when using silicone paints, it is necessary to reduce the crosslinking density of the silicone resin, which reduces the surface hardness of the formed film. This poses a problem.

また、ポリチタノカルボシラン系塗料は低温焼成(40
0℃以下)における表面硬度が充分でない上、原料製造
工程が複雑であり、その製造コストが高価となるという
欠点がある。
In addition, polytitanocarbosilane paints are fired at low temperatures (40
The disadvantages are that the surface hardness at temperatures below 0° C. is not sufficient, the raw material manufacturing process is complicated, and the manufacturing cost is high.

また、ポリ(ジシル)シラザン系重合体を用いる方法は
、750℃以上の高温下で不活性雰囲気又は真空中で熱
分解を行うプロセスを採る必要があり。
Furthermore, the method using a poly(disyl)silazane polymer requires a process of thermal decomposition at a high temperature of 750° C. or higher in an inert atmosphere or in a vacuum.

その施行性に多く困難さを伴う。同様にポリシラザンか
ら得られた窒化珪素の被覆膜についての報告もなされて
いるが、クラックが生じており十分実用的価値を有する
ものが得られていない(L S、 CobliB et
 al、“Formation of Ceramic
Compositions Utilizing Po
lymer Pyrolysis”。
There are many difficulties in its implementation. Similarly, a report has been made on a silicon nitride coating film obtained from polysilazane, but cracks occur and a film with sufficient practical value has not been obtained (LS, CobliB et al.
al, “Formation of Ceramic
Compositions Utilizing Po
lymer pyrolysis”.

P271−285、Materials 5cienc
e Re5earch vaultEmergent 
Process Methods For High−
TechnologyCeramics  edite
d  by  R,F、Dabis  et、al、P
lenunPress N、Y、)。
P271-285, Materials 5cienc
eRe5earch vaultEmergent
Process Methods For High-
Technology Ceramics edit
d by R, F, Davis et, al, P
lenunPress N, Y,).

〔目 的〕〔the purpose〕

本発明の第1の目的は、窒化珪素前駆体として好適な新
規な無機シラザン高重合体及びこのものを工業的に有利
に製造する方法を提供することにあり、第2の目的は耐
熱性、耐摩耗性及び耐薬品性に優れると共に、表面硬度
の高い被膜を形成し得るコーティング剤を提供すること
にある。更に第3の目的は、セラミックス成形体、特に
セラミックス成形焼結体用のバインダーを提供すること
にある。
The first object of the present invention is to provide a novel inorganic silazane polymer suitable as a silicon nitride precursor and an industrially advantageous method for producing the same, and the second object is to provide heat resistance, It is an object of the present invention to provide a coating agent that has excellent abrasion resistance and chemical resistance and can form a film with high surface hardness. A third object is to provide a binder for ceramic molded bodies, particularly ceramic molded sintered bodies.

〔楕 成〕[Oval formation]

本発明によれば、第1の発明として、数平均分子量が2
00〜500000であり、1分子中のSiH,基と5
i82基の比(SiH,基/5iHi基)が2.5〜8
.4であって、しかも元素比率がSi:59重量%〜7
0重量%、N:20重量2〜34重量%、H:5重量2
〜9重量%である無機シラザン高重合体が提供され、第
2の発明として、無機シラザンを塩基性溶媒中又は塩基
性化合物を含む溶媒中で加熱することを特徴とする数平
均分子量が200〜500000であり、1分子中のS
iH,基とS i H、基の比(SiH,基/ S i
 t(、基)が2.5〜8.4であって、しかも元素比
率がSi:59重量%〜70重i%、N:20重量%〜
34重量%、11:5重量X〜9重M%である無機シラ
ザン高重合体の製造方法が提供され、第3の発明として
、数平均分子量が200〜500000であり、1分子
中のSiH3基と5i82基の比(SiH,基/SiH
3基)が2.5〜8.4であって、しかも元素比率がS
i:59重量%〜70重量%、 N:20重量%〜34
f%、H:5重址%〜9重景%である無機シラザン高重
合体を必須成分としたコーティング剤が提供される。更
に、第4の発明として数平均分子量が200〜5000
00であり、1分子中のSiH,基と5it(□基の比
(Sin2基/5iHz基)が2.5〜8.4であって
、しかも元素比率がSi:59重景%〜70重量%、N
:20重量%〜34量%、H:5重量%〜9重量%であ
る無機シラザン高重合体を必須成分としたバインダーが
提供される。
According to the present invention, as the first invention, the number average molecular weight is 2.
00 to 500,000, and the SiH group in one molecule and 5
The ratio of i82 groups (SiH, group/5iHi group) is 2.5 to 8
.. 4, and the element ratio is Si: 59% by weight to 7
0% by weight, N: 20% by weight 2-34% by weight, H: 5% by weight
A second invention provides an inorganic silazane high polymer having a number average molecular weight of 200 to 9% by weight, characterized in that the inorganic silazane is heated in a basic solvent or in a solvent containing a basic compound. 500,000, and S in one molecule
The ratio of iH, groups to S i H, groups (SiH, groups / Si
t (group) is 2.5 to 8.4, and the element ratio is Si: 59% to 70% by weight, N: 20% by weight to
34% by weight, 11:5% by weight X to 9% by weight and the ratio of 5i82 groups (SiH, groups/SiH
3) is 2.5 to 8.4, and the element ratio is S
i: 59% to 70% by weight, N: 20% to 34% by weight
A coating agent is provided which contains an inorganic silazane high polymer as an essential component, with f% and H: 5% to 9%. Furthermore, as a fourth invention, the number average molecular weight is 200 to 5000.
00, the ratio of SiH groups to 5it (□ groups (Si2 groups/5iHz groups) in one molecule is 2.5 to 8.4, and the element ratio is Si: 59% to 70% by weight %, N
Provided is a binder containing an inorganic silazane high polymer as an essential component: 20% to 34% by weight and H: 5% to 9% by weight.

本発明の無機シラザン高重合体の出発原料として用いら
れる原料無機シラザンは、次の一般式で表わされる骨格
を有するものである。
The raw material inorganic silazane used as a starting material for the inorganic silazane high polymer of the present invention has a skeleton represented by the following general formula.

本発明の原料無機シラザンは、100〜50,000の
数平均分子量を有するもので、環状無機シラザン、鎖状
無機シラザンあるいはそれらの混合物から構成される。
The raw material inorganic silazane of the present invention has a number average molecular weight of 100 to 50,000 and is composed of a cyclic inorganic silazane, a chain inorganic silazane, or a mixture thereof.

本発明において好ましく用いられる原料無機シラザンは
、数平均分子量300〜2000好ましくは600〜1
400の鎖状無機シラザンである。
The raw material inorganic silazane preferably used in the present invention has a number average molecular weight of 300 to 2000, preferably 600 to 1.
400 chain inorganic silazane.

前記で示した無機シラザンは、下記に示す如き従来公知
の方法で合成することができる。
The inorganic silazane shown above can be synthesized by a conventionally known method as shown below.

■ 本発明者特許出WL(時開60−1.45903)
・SiH□CQ 2+2Py −+ SiH,CQ2・
2Py adduct・5iH2CQ、・2Pyadd
uct+3NH,−+  −(SiH2NH殆+2NH
,CQ +2P、y■ D、 5eyferthら(U
SP 4,397,828)CI2CQ 。
■ Inventor's patent issued WL (Jikai 60-1.45903)
・SiH□CQ 2+2Py −+ SiH,CQ2・
2Py adduct・5iH2CQ,・2Pyadd
uct+3NH, -+ -(SiH2NH mostly +2NH
, CQ +2P, y■ D, 5eyferth et al. (U
SP 4,397,828) CI2CQ.

・5i82CQ 2+3NH3−→ −(Si)12N
)I+t1+2NH,Cα■ A、 5tack (B
er、 54. (1921)、 P−740)■ W
2N、 5cantlinら、 Inorg、 Che
w、 1972.11本発明においては、前記出発原料
である無機シラザンを塩基性溶媒又は塩基性化合物を添
加した溶媒中で加熱し、脱水素重縮合反応(以下、単に
重縮合反応とも言う)させる。この場合、塩基性化合物
としては、窒素やリンの如き塩基性元素を含有する化合
物、例えば、第3級アミン類や、立体障害性の基を有す
る2級アミン類、フォスフイン等を用いることができる
。本発明で用いる反応溶媒は、非塩基性溶媒にこのよう
な塩基性化合物を添加した溶媒あるいは塩基性化合物自
体からなる溶媒である。非塩基性溶媒に塩基性化合物を
添加する場合、塩基性化合物の添加量は、非塩基性溶媒
100重量部に対し少なくとも5重景部、好ましくは2
0重量部以上である。塩基性化合物の添加量がこれより
少なくなると、重縮合反応が円滑に促進されない。
・5i82CQ 2+3NH3−→ −(Si)12N
)I+t1+2NH,Cα■ A, 5tack (B
er, 54. (1921), P-740) ■ W
2N, 5cantlin et al., Inorg, Che
w, 1972.11 In the present invention, the inorganic silazane, which is the starting material, is heated in a basic solvent or a solvent to which a basic compound has been added to cause a dehydrogenation polycondensation reaction (hereinafter also simply referred to as a polycondensation reaction). . In this case, as the basic compound, a compound containing a basic element such as nitrogen or phosphorus, such as tertiary amines, secondary amines having a sterically hindered group, phosphine, etc. can be used. . The reaction solvent used in the present invention is a solvent obtained by adding such a basic compound to a non-basic solvent, or a solvent consisting of the basic compound itself. When adding a basic compound to a non-basic solvent, the amount of the basic compound added is at least 5 parts by weight, preferably 2 parts by weight, per 100 parts by weight of the non-basic solvent.
It is 0 parts by weight or more. If the amount of the basic compound added is less than this, the polycondensation reaction will not be smoothly promoted.

前記塩基性化合物又は塩基性溶媒としては、出発原料で
ある無機シラザンを分解しないものであれば任意のもの
が使用できる。このようなものとしては、例えば、トリ
メチルアミン、ジメチルエチルアミン、ジエチルメチル
アミン及びトリエチルアミン等のトリアルキルアミン、
ピリジン、ピコリン、ジメチルアニリン、ピラジン、ピ
リミジン、ピリダジン及びこれらの誘導体等の第3級ア
ミン類の他、ピロール、3−ピロリン、ピラゾール、2
−ピラゾリン、及びそれらの混合物等を挙げることがで
きる。また、非塩基性溶媒としては、例えば、脂肪族炭
化水素、脂環式炭化水素、芳香族炭化水素の炭化水素溶
媒、ハロゲン化メタン、ハロゲン化エタン、ハロゲン化
ベンゼン等のハロゲン化炭化水素、脂肪族エーテル、脂
環式エーテル等のエーテル類が使用できる。好ましい溶
媒は、塩化メチレン、クロロホルム、四塩化炭素、ブロ
モホルム、塩化エチレン、塩化エチリデン、トリクロロ
エタン、テトラクロロエタン等のハロゲン化炭化水素、
エチルエーテル、イソプロピルエーテル、エチルブチル
エーテル、ブチルエーテル、1.2−ジオキシエタン、
ジオキサン、ジメチルジオキサン、テトラヒドロフラン
、テトラヒドロピラン等のエーテル類、ペンタン、ヘキ
サン、イソヘキサン、メチルペンタン、ヘプタン、イソ
へブタン、オクタン、イソオクタン、シクロペンタン、
メチルシクロペンタン、シクロヘキサン、メチルシクロ
ヘキサン、ベンゼン、トルエン、キシレン、エチルベン
ゼン等の炭化水素等である。
Any basic compound or basic solvent can be used as long as it does not decompose the inorganic silazane that is the starting material. These include, for example, trialkylamines such as trimethylamine, dimethylethylamine, diethylmethylamine and triethylamine;
In addition to tertiary amines such as pyridine, picoline, dimethylaniline, pyrazine, pyrimidine, pyridazine and their derivatives, pyrrole, 3-pyrroline, pyrazole,
-pyrazoline, and mixtures thereof. Examples of non-basic solvents include hydrocarbon solvents such as aliphatic hydrocarbons, alicyclic hydrocarbons, and aromatic hydrocarbons; halogenated hydrocarbons such as halogenated methane, halogenated ethane, and halogenated benzene; Ethers such as group ethers and alicyclic ethers can be used. Preferred solvents include halogenated hydrocarbons such as methylene chloride, chloroform, carbon tetrachloride, bromoform, ethylene chloride, ethylidene chloride, trichloroethane, and tetrachloroethane;
Ethyl ether, isopropyl ether, ethyl butyl ether, butyl ether, 1,2-dioxyethane,
Ethers such as dioxane, dimethyldioxane, tetrahydrofuran, and tetrahydropyran, pentane, hexane, isohexane, methylpentane, heptane, isohbutane, octane, isooctane, cyclopentane,
These include hydrocarbons such as methylcyclopentane, cyclohexane, methylcyclohexane, benzene, toluene, xylene, and ethylbenzene.

本発明の重縮合反応は、前記した如き溶媒中で実施され
るが、この場合、原料無機シラザンの溶媒中濃度は0.
1重量%〜50重量%、好ましくは1重量%〜12重量
%である。無機シラザンの濃度がこれより低いと分子間
重縮合反応が十分進行せず、またそれより高いと分子間
重縮合反応が進みすぎてゲルを生成するようになる。反
応温度は、−78℃〜300℃、好ましくは一40℃〜
200℃であり、それより低い温度では重縮合反応が十
分進行せず、それより高い温度では重縮合反応が進みす
ぎてゲルを生成する。反応雰囲気としては、大気の使用
が可能であるが、好ましくは、水素雰囲気や、乾燥窒素
、乾燥アルゴン等の不活性ガス雰囲気あるいはそれらの
混合雰囲気が使用される。本発明における重縮合反応に
おいては、副生物の水素によって反応の際圧力がかかる
が、必ずしも加圧は必要でなく、常圧を採用することが
できる。なお、反応時間は、出発原料の無機シラザンの
種類、濃度および塩基性化合物又は塩基性溶媒の種類、
濃度、重縮合反応温度など諸条件により異なるが、−船
釣に0.5時間〜20時間の範囲とすれば充分である。
The polycondensation reaction of the present invention is carried out in the solvent as described above, but in this case, the concentration of the raw material inorganic silazane in the solvent is 0.
1% to 50% by weight, preferably 1% to 12% by weight. If the concentration of inorganic silazane is lower than this, the intermolecular polycondensation reaction will not proceed sufficiently, and if it is higher than this, the intermolecular polycondensation reaction will proceed too much and a gel will be produced. The reaction temperature is -78°C to 300°C, preferably -40°C to
The temperature is 200° C. At lower temperatures, the polycondensation reaction does not proceed sufficiently, and at higher temperatures, the polycondensation reaction proceeds too much and forms a gel. As the reaction atmosphere, air can be used, but preferably a hydrogen atmosphere, an inert gas atmosphere such as dry nitrogen or dry argon, or a mixed atmosphere thereof is used. In the polycondensation reaction of the present invention, pressure is applied during the reaction due to hydrogen as a by-product, but pressurization is not necessarily necessary and normal pressure can be employed. Note that the reaction time depends on the type and concentration of the inorganic silazane as a starting material, the type of basic compound or basic solvent,
Although it varies depending on various conditions such as concentration and polycondensation reaction temperature, a range of 0.5 to 20 hours is sufficient for boat fishing.

重縮合反応の最適条件は出発原料の無機シラザンの平均
分子量、分子量分布等によって異なる。
The optimum conditions for the polycondensation reaction vary depending on the average molecular weight, molecular weight distribution, etc. of the inorganic silazane starting material.

条件設定の一般的な考慮は、出発原料のポリシラザンの
平均分子量が低い程よりきびしい条件(温度、反応時間
)が必要とされるということである。
A general consideration in setting conditions is that the lower the average molecular weight of the starting polysilazane, the more stringent conditions (temperature, reaction time) are required.

本発明の重縮合反応においては、無機シラザン高重合体
、即ち、高分子量化された無機シラザンを含む溶媒溶液
が得られるが、この場合、その溶液組成を調整して、塩
基性化合物又は塩基性溶媒含量を、全溶媒中30重量%
以下、好ましくは5重量%以下にするのがよい。塩基性
化合物又は塩基性溶媒は、無機シラザン高重合体の分子
間重縮合反応触媒として作用するため、その全溶媒に対
する割合が余りにも多くなると、室温で長時間保存して
いる間にゲルを生成する。この溶液組成の調整は2例え
ば、前記重縮合反応で得られた無機シラザン高重合体溶
液を蒸発処理して、それに含まれる塩基性化合物もしく
は溶媒を蒸発除去した後、非塩基性(非反応性)溶媒を
添加することによって行うことができる。溶液中の塩基
性化合物の含量が高い場合や1反応溶媒として塩基性化
合物自体を用いる場合は、前記した塩基性化合物の蒸発
除去と非塩基性溶媒添加とからなる溶液組成調整操作を
繰返し行うことによって安定性の良い溶液組成とするこ
とができる0本発明において無機シラザン高重合体の安
定溶液を形成するための非塩基性溶媒としては、前記で
示した如き脂肪族炭化水素、脂環式炭化水素、芳香族炭
化水素、ハロゲン化炭化水素、脂肪族エーテル、脂環式
エーテル等を用いることができる。
In the polycondensation reaction of the present invention, a solvent solution containing an inorganic silazane high polymer, that is, a high molecular weight inorganic silazane, is obtained. Solvent content is 30% by weight in total solvent
The content is preferably 5% by weight or less. Basic compounds or basic solvents act as catalysts for the intermolecular polycondensation reaction of inorganic silazane polymers, so if their proportion to the total solvent is too large, gels may form during long-term storage at room temperature. do. Adjustment of this solution composition is carried out in step 2. For example, the inorganic silazane polymer solution obtained in the polycondensation reaction is evaporated to remove the basic compound or solvent contained therein, and then the non-basic (non-reactive) ) This can be done by adding a solvent. When the content of the basic compound in the solution is high or when the basic compound itself is used as one reaction solvent, the above-mentioned solution composition adjustment operation consisting of evaporation removal of the basic compound and addition of a non-basic solvent should be repeated. As the non-basic solvent for forming a stable solution of the inorganic silazane polymer in the present invention, aliphatic hydrocarbons and alicyclic carbonates as shown above can be used. Hydrogen, aromatic hydrocarbons, halogenated hydrocarbons, aliphatic ethers, alicyclic ethers, etc. can be used.

本発明における無機シラザンの重縮合反応は、次の如き
素反応を含んでいるものと考えられる。
The polycondensation reaction of inorganic silazane in the present invention is considered to include the following elementary reactions.

(1)前記一般式(1)において、 I H 本発明の無機シラザン高重合体は、前記のように原料無
機シラザンの重縮合反応によって生成された重合体であ
り、無機シラザン分子中に新しい架橋結合が生じて高分
子量化されたものである。
(1) In the general formula (1), I H The inorganic silazane high polymer of the present invention is a polymer produced by the polycondensation reaction of raw material inorganic silazane as described above, and has new crosslinks in the inorganic silazane molecules. It has a high molecular weight due to bonding.

即ち、本発明の無機シラザン高重合体は、前記のように
数平均分子量100〜50,000の無機シラザンを原
料として用い、これを架橋高分子化することによって形
成されることから、その分子量は、当然のことながら、
原料無機シラザンの分子量よりも増加されたものとなる
。−船釣には、本発明の目的とする無機シラザン高重合
体は、数平均分子量200〜soo 、 ooo、好ま
しくは、1 、500〜10,000を有する。
That is, since the inorganic silazane polymer of the present invention is formed by crosslinking and polymerizing inorganic silazane having a number average molecular weight of 100 to 50,000 as a raw material as described above, its molecular weight is ,As a matter of course,
The molecular weight is higher than that of the raw material inorganic silazane. - For boat fishing, the inorganic silazane polymer targeted by the present invention has a number average molecular weight of 200 to 1,500 to 10,000, preferably 1,500 to 10,000.

本発明の無機シラザン高重合体は5分子構造的には前記
の如き特徴を有し、原料無機シラザンと区別されるもの
であるが、その他、多くの枝分れ構造を有する点もその
特徴の1つである。この枝分れ構造のために、本発明の
無機シラザン高重合体は、原料無機シラザンに比して高
分子量化されたものでありながら、むしろ溶媒可溶性に
おいて改善された結果を与える。例えば、5eyfer
th等が先に提案した無機シラザンは、−3i−H/N
−1(のプロトン比が約3.3のオイル状液体であるが
、約200℃で加熱するか室温で3〜5日放置すること
により固化するものであった。これに対し、本発明の無
機シラザン高重合体は、200〜soo、oooの分子
量を持ち、1分子中のS i t(、基の数は、通常、
原料無機シラザンの2倍以上に増加し、溶媒再可溶性を
有する6本発明の無機シラザン高重合体が原料無機シラ
ザンに比してより多くの枝分れ構造を有する理由は、本
発明における重縮合反応では、重縮合反応以外に、例え
ば、次のような反応が起ることによるものと考えられる
The inorganic silazane polymer of the present invention has the above-mentioned characteristics in terms of the pentamolecular structure and is distinguished from the raw material inorganic silazane, but it also has many branched structures. There is one. Due to this branched structure, the inorganic silazane polymer of the present invention has a higher molecular weight than the raw material inorganic silazane, but rather provides improved solvent solubility. For example, 5eyfer
The inorganic silazane previously proposed by th et al.
-1 is an oily liquid with a proton ratio of about 3.3, but it solidifies by heating at about 200°C or leaving it at room temperature for 3 to 5 days. The inorganic silazane polymer has a molecular weight of 200 to soo, ooo, and the number of groups in one molecule is usually
The reason why the inorganic silazane high polymer of the present invention has more branched structure than the raw material inorganic silazane is that the inorganic silazane polymer of the present invention has more branched structure than the raw material inorganic silazane. In addition to the polycondensation reaction, it is thought that the following reactions occur, for example.

本発明の無機シラザン高重合体の枝分れ構造は。The branched structure of the inorganic silazane high polymer of the present invention is as follows.

例えば、’ HNMRスペクトル測定により得られる(
SiH,)/ (SiHs ) ((SiH2) :δ
4.8における5L−H共鳴の面積の1/2、(SiH
i ) ”δ4.4における5i−H共鳴面積の1/3
〕比によって評価することができる。原料無機シラザン
の場合、(SiH,)/ (SiHi )比は、5.0
〜19.0の範囲であるが、本発明の無機シラザン高重
合体の場合、それぞれ、265〜8.4の低められた値
となる。無機シラザン高重合体のSiH□/SiH3比
が上記範囲でない場合、凝固性、賦形性等が劣り、本発
明の所期の目的を達成することができない。
For example, 'HNMR spectroscopy gives (
SiH, )/(SiHs) ((SiH2) :δ
1/2 of the area of 5L-H resonance in 4.8, (SiH
i) “1/3 of the 5i-H resonance area at δ4.4
] It can be evaluated by the ratio. In the case of raw material inorganic silazane, the (SiH,)/(SiHi) ratio is 5.0
~19.0, but in the case of the inorganic silazane high polymers of the present invention, the values are lowered from 265 to 8.4, respectively. If the SiH□/SiH3 ratio of the inorganic silazane high polymer is not within the above range, coagulation properties, shaping properties, etc. will be poor, and the intended purpose of the present invention will not be achieved.

本発明の無機シラザン高重合体は、前記の如き分子構造
的特徴を有するとともに、物性的には、架橋結合を有し
ながら、有機溶媒に可溶であり、特に溶液から溶媒を除
去して得られた固体重合体は、溶媒に対して再可溶性を
有するという大きな特徴を示す。従来の無機シラザンの
場合、安定性が悪く、その溶液から溶媒を除去すると樹
脂状固体を生成し、このものは溶媒に不溶であったが、
本発明の無機シラザン高重合体はこのような傾向を示さ
ない。従って、従来の無機シラザンの場合、固体重合体
としての取扱いが不可能ないし著しく困難であったのに
対し、本発明の無機シラザン高重合体は固体重合体とし
て容易に取扱うことができる。
The inorganic silazane polymer of the present invention has the above-mentioned molecular structural characteristics, and in terms of physical properties, it is soluble in organic solvents while having cross-linked bonds, and in particular, it can be obtained by removing the solvent from the solution. The obtained solid polymer exhibits a major feature of being re-soluble in a solvent. Conventional inorganic silazane has poor stability, and when the solvent is removed from its solution, it produces a resinous solid, which is insoluble in the solvent.
The inorganic silazane polymer of the present invention does not exhibit this tendency. Therefore, while conventional inorganic silazane is impossible or extremely difficult to handle as a solid polymer, the inorganic silazane high polymer of the present invention can be easily handled as a solid polymer.

更に本発明の無機シラザン高重合体は元素比率がSi:
59重ff1%−70重i%、N:20重量%〜34重
量%、H:5重量%〜9重量%であることを特徴とする
特本発明の無機シラザン高重合体の好ましい元素比率は
Si:61重量%〜68重量で、N:25重量%〜33
重量算、H:5重量%−8重量2であり、更に好ましい
元素比率はSi:64重量%−68重量%、 N:27
重量%−33重量%、 H:5重量%−7重量%である
Furthermore, the inorganic silazane polymer of the present invention has an elemental ratio of Si:
The preferred element ratios of the inorganic silazane high polymer of the present invention are: 59% by weight ff1% - 70% by weight, N: 20% by weight - 34% by weight, H: 5% by weight - 9% by weight. Si: 61% to 68% by weight, N: 25% to 33% by weight
Weight calculation: H: 5% by weight - 8% by weight 2, more preferable element ratios are Si: 64% by weight - 68% by weight, N: 27
% by weight - 33% by weight, H: 5% by weight - 7% by weight.

無機シラザン高重合体の元素比率が上記範囲を満たさな
いと固体重合体として容易に取り扱うことが困難となっ
て本発明の所期の目的を達成することができない。
If the element ratio of the inorganic silazane high polymer does not satisfy the above range, it will be difficult to easily handle it as a solid polymer, making it impossible to achieve the intended purpose of the present invention.

本発明において、前記無機シラザン高重合体を用いてコ
ーティング剤を形成するには、通常無機シラザン高重合
体を溶剤に溶解させればよい。溶剤としては、脂肪族炭
化水素、脂環式炭化水素、芳香族炭化水素の炭化水素溶
媒、ハロゲン化メタン、ハロゲン化エタン、ハロゲン化
ベンゼン等のハロゲン化炭化水素、脂肪族エーテル、脂
環式エーテル等のエーテル類が使用できる。好ましい溶
媒は、塩化メチレン、クロロホルム、四塩化炭素、ブロ
モホルム、塩化エチレン、塩化エチリデン、トリクロロ
エタン、テトラクロロエタン等のハロゲン化炭化水素、
エチルエーテル、イソプロピルエーテル、エチルブチル
エーテル、ブチルエーテル、1,2−ジオキシエタン、
ジオキサン、ジメチルジオキサン、テトラヒドロフラン
、テトラヒドロビラン等のエーテル類、ペンタンヘキサ
ン、イソヘキサン、メチルペンタン、ヘプタン、イソへ
ブタン、オクタン、イソオクタン、シクロペンタン、メ
チルシクロペンタン、シクロヘキサン、メチルシクロヘ
キサン、ベンゼン、トルエン、キシレン、エチルベンゼ
ン等の炭化水素等である。
In the present invention, in order to form a coating agent using the inorganic silazane high polymer, it is usually sufficient to dissolve the inorganic silazane high polymer in a solvent. Examples of solvents include hydrocarbon solvents such as aliphatic hydrocarbons, alicyclic hydrocarbons, and aromatic hydrocarbons, halogenated hydrocarbons such as halogenated methane, halogenated ethane, and halogenated benzene, aliphatic ethers, and alicyclic ethers. Ethers such as can be used. Preferred solvents include halogenated hydrocarbons such as methylene chloride, chloroform, carbon tetrachloride, bromoform, ethylene chloride, ethylidene chloride, trichloroethane, and tetrachloroethane;
Ethyl ether, isopropyl ether, ethyl butyl ether, butyl ether, 1,2-dioxyethane,
Ethers such as dioxane, dimethyldioxane, tetrahydrofuran, tetrahydrobilane, pentanehexane, isohexane, methylpentane, heptane, isohbutane, octane, isooctane, cyclopentane, methylcyclopentane, cyclohexane, methylcyclohexane, benzene, toluene, xylene, These include hydrocarbons such as ethylbenzene.

これらの溶剤を使用する場合、前記無機シラザン高重合
体の溶解度や溶剤の蒸発速度を調節するために、2種類
以上の溶剤を混合してもよい。
When using these solvents, two or more types of solvents may be mixed in order to adjust the solubility of the inorganic silazane polymer and the evaporation rate of the solvent.

溶剤の使用量(割合)は採用するコーティング方法によ
り作業性がよくなるように選択され、また無機シラザン
高重合体の平均分子量、分子量分布、その構造によって
異なるが、コーティング剤中溶剤は90重量%程度まで
混合することができ、好ましくは10重量%−50重量
%の範囲で混合することができる。
The amount (proportion) of the solvent used is selected to improve workability depending on the coating method employed, and varies depending on the average molecular weight, molecular weight distribution, and structure of the inorganic silazane polymer, but the solvent content in the coating agent is approximately 90% by weight. It is possible to mix up to 50% by weight, preferably in the range of 10% to 50% by weight.

また、必要に応じて適当な充填剤を加えてもよい。充填
剤の例としてはシリカ、アルミナ、ジルコニア、マイカ
を始めとする酸化物系無機物あるいは炭化珪素、窒化珪
素等の非酸化物系無機物の微粉等が挙げられる。また用
途によってはアルミニウム、亜鉛、銅等の金属粉末の添
加も可能である。さらに充填剤の例を詳しく述べれば、
ケイ砂。
Further, a suitable filler may be added as necessary. Examples of fillers include fine powders of oxide-based inorganic substances such as silica, alumina, zirconia, and mica, and non-oxide-based inorganic substances such as silicon carbide and silicon nitride. Depending on the application, it is also possible to add metal powders such as aluminum, zinc, copper, etc. If we look at examples of fillers in more detail,
Silica sand.

石英、ツバキュライト、ケイ藻土などのシリカ系:合成
無定形シリカ:カオリナイト、雲母、滑石、ウオラスト
ナイト、アスベスト、ケイ酸カルシウム、ケイ酸アルミ
ニウム等のケイ酸塩ニガラス粉末、ガラス球、中空ガラ
ス球、ガラスフレーク、泡ガラス球等のガラス体:窒化
ホウ素、炭化ホウ素、窒化アルミニウム、炭化アルミニ
ウム、窒化ケイ素、炭化ケイ素、ホウ化チタン、窒化チ
タン、炭化チタン等の非酸化物系無機物:炭酸カルシウ
ム:酸化亜鉛、アルミナ、マグネシア、酸化チタン、酸
化ベリリウム等の金属酸化物:硫酸バリウム、二硫化モ
リブデン、二硫化タングステン、弗化炭素その他無機物
ニアルミニウム、ブロンズ、鉛、ステンレススチール、
亜鉛等の金属粉末:カーボンブラック、コークス、黒鉛
、熱分解炭素、中空刃−ボン球等のカーボン体等があげ
られる。
Silica-based products such as quartz, tubaculite, and diatomaceous earth: Synthetic amorphous silica: Kaolinite, mica, talc, wollastonite, asbestos, calcium silicate, aluminum silicate, and other silicates, glass powder, glass spheres, and hollow glass. Glass bodies such as spheres, glass flakes, and bubble glass bulbs: Non-oxide-based inorganic substances such as boron nitride, boron carbide, aluminum nitride, aluminum carbide, silicon nitride, silicon carbide, titanium boride, titanium nitride, and titanium carbide: calcium carbonate : Metal oxides such as zinc oxide, alumina, magnesia, titanium oxide, beryllium oxide, etc.: Barium sulfate, molybdenum disulfide, tungsten disulfide, carbon fluoride and other inorganic materials Nialuminum, bronze, lead, stainless steel,
Metal powders such as zinc: carbon bodies such as carbon black, coke, graphite, pyrolytic carbon, and hollow blade-bond balls.

これら充填剤は、針状(ウィスカーを含む。)、粒状、
鱗片状等種々の形状のものを単独又は2種以上混合して
用いることができる。又、これら充填剤の粒子の大きさ
は1回に塗布可能な膜厚よりも小さいことが望ましい。
These fillers are acicular (including whiskers), granular,
Those in various shapes such as scales can be used alone or in combination of two or more kinds. Further, it is desirable that the particle size of these fillers is smaller than the thickness of a film that can be coated at one time.

また充填剤の添加量は無機シラザン高重合体1重量部に
対し、0.05重量部〜10重量部の範囲であり、特に
好ましい添加量は0.2重量部〜3重量部の範囲である
。又、充填剤の表面をカップリング剤処理、蒸着、メツ
キ等で表面処理して使用してもよい。
Further, the amount of the filler added is in the range of 0.05 parts by weight to 10 parts by weight, and a particularly preferable amount is in the range of 0.2 parts by weight to 3 parts by weight, based on 1 part by weight of the inorganic silazane high polymer. . Further, the surface of the filler may be treated with a coupling agent, vapor deposition, plating, etc. before use.

更に、コーティング剤には、必要に応じて各種顔料、レ
ベリング剤、消泡剤、帯電防止剤、紫外線吸収剤、PI
(調整剤、分散剤、表面改質剤、可塑剤、乾燥促進剤、
流れ止め剤を加えてもよい。
Furthermore, the coating agent may contain various pigments, leveling agents, antifoaming agents, antistatic agents, ultraviolet absorbers, and PI.
(conditioner, dispersant, surface modifier, plasticizer, drying accelerator,
Anti-flow agents may be added.

このように調製されたコーティング剤は均一に溶解、分
解させて金属、セラミックス、プラスチック等の基盤に
コーティングされる。コーティングとしての塗布手段と
しては、通常の塗布方法、つまり浸漬、ロール塗り、バ
ー塗り、刷毛塗り、スプレー塗り、フロー塗り等が用い
られる。又、塗布前に基盤をヤスリかけ、脱脂、各種ブ
ラスト等で表面処理しておくとコーティング組成物の付
着性能は向上する。このような方法でコーティングし、
充分乾燥させた後、加熱・焼成する。この焼成によって
無機シラザン高重合体は架橋、縮合して硬化し、強靭な
被覆を形成する。
The coating agent thus prepared is uniformly dissolved and decomposed to coat a substrate such as metal, ceramics, plastic, etc. As a coating means, conventional coating methods such as dipping, roll coating, bar coating, brush coating, spray coating, flow coating, etc. are used. Furthermore, if the substrate is surface treated by sanding, degreasing, various types of blasting, etc. before application, the adhesion performance of the coating composition will be improved. Coating in this way,
After thoroughly drying, heat and bake. By this baking, the inorganic silazane high polymer is crosslinked, condensed, and hardened to form a tough coating.

上記焼成条件は無機シラザン高重合体の分子量や構造に
よって異なるが0.5〜10℃7分の緩やかな昇温速度
で100℃〜1000℃の範囲の温度で焼成する。
The above-mentioned firing conditions vary depending on the molecular weight and structure of the inorganic silazane polymer, but the firing is performed at a temperature in the range of 100°C to 1000°C with a gradual temperature increase rate of 0.5°C to 10°C for 7 minutes.

好ましい焼成温度は200℃〜500℃の範囲である。The preferred firing temperature is in the range of 200°C to 500°C.

焼成雰囲気は空気中あるいは不活性ガスのいずれであっ
てもよいが、非酸化性雰囲気であれば5L−N結合を、
酸化又は加水解性雰囲気であれば5i−0結合の被膜を
形成するので、基盤に応じて雰囲気を適当に選択するこ
とができる。
The firing atmosphere may be air or an inert gas, but if it is a non-oxidizing atmosphere, the 5L-N bond can be formed.
Since a film of 5i-0 bonds is formed in an oxidizing or hydrolytic atmosphere, the atmosphere can be appropriately selected depending on the substrate.

したがって、本発明のコーティング剤は、鉄、アルミニ
ウム、銅、ステンレス鋼、黄銅等の金属類やセラミック
スの表面保護剤として更には電子部品用の多属配線の絶
縁膜としても好適なものである。
Therefore, the coating agent of the present invention is suitable as a surface protective agent for metals such as iron, aluminum, copper, stainless steel, brass, etc. and ceramics, and also as an insulating film for multi-metal wiring for electronic components.

前記無機シラザン高重合体を用いてバインダーとして使
用するためには通常以下に述べる手法が用いられる。即
ち、無機シラザン高重合体は、キシレン等の有機溶剤に
可溶である。
In order to use the inorganic silazane high polymer as a binder, the following method is usually used. That is, the inorganic silazane high polymer is soluble in organic solvents such as xylene.

したがって、このような溶剤中に、各種セラミックス粉
末と無機シラザン高重合体とを添加し、混合することに
よって、容易にセラミックス粉体中に、バインダーとし
て均一に分散させることが可能である。ここで、無機シ
ラザン高重合体は、解こう剤(分散剤)としても作用す
るため、本スラリーは造粒用あるいはスラリー成形用に
達した均質なスラリーとなる。故に、成形法としては、
金型プレス法、ラバープレス法などのプレス成形法、押
出し法、シート法、持込み法などのスラリー成形法を適
用することができる。
Therefore, by adding various ceramic powders and an inorganic silazane high polymer to such a solvent and mixing them, it is possible to easily disperse them uniformly as a binder in the ceramic powder. Here, since the inorganic silazane high polymer also acts as a peptizer (dispersant), the present slurry becomes a homogeneous slurry suitable for granulation or slurry molding. Therefore, as a forming method,
Press molding methods such as a mold press method and a rubber press method, slurry molding methods such as an extrusion method, a sheet method, and a carry-in method can be applied.

以上のようにして得られた成形体を焼結すると、無機シ
ラザン高重合体は、熱分解し、水素が揮散し、活性度の
高いSiとNがセラミックス粒子と反応し、焼結用バイ
ンダーとして作用し、粒子間を強固に結合する。ここで
、この結合力は、熱分解”収率の高いプレセラミックポ
リマーを用いる程、さらに、結合に関与しない過剰の炭
素を残存させないプレセラミックポリマーを用いる程強
固であるため、本質的に有機基を有することなく、熱分
解後、高純度なSi3N、組成となる無機シラザン高重
合体は、焼結用バインダーとして適したプレセラミック
ポリマーと言える。また、このSi3N4の形態は、通
常、非晶質あるいは1oooÅ以下という極めて小さな
結晶粒子という形でセラミックス粒子間を充てんするた
め、粒成鰍抑制剤としての役割をも果す。
When the molded body obtained as described above is sintered, the inorganic silazane high polymer is thermally decomposed, hydrogen is volatilized, highly active Si and N react with the ceramic particles, and the inorganic silazane high polymer is used as a binder for sintering. It acts to form strong bonds between particles. Here, this bonding force is stronger as a preceramic polymer with a higher pyrolysis yield is used, and furthermore, a preceramic polymer that does not leave excess carbon that does not participate in bonding is stronger, so it is essentially an organic group. The inorganic silazane polymer, which has a composition of high purity Si3N after thermal decomposition, can be said to be a preceramic polymer suitable as a binder for sintering. Alternatively, since it fills the spaces between ceramic particles in the form of extremely small crystal grains of 100 Å or less, it also plays a role as a grain growth suppressant.

以上の反応は、約400℃より始まり、約1500℃で
完了する。故に、5L3N4. SiCなどの非酸化物
に代表される無機焼結セラミックスにおいては、従来、
1700℃以上という高温焼結が行われてきたが、本発
明によれば1300〜1500℃程度で、比較的低密度
であるにもかかわらず、機械的特性に優れたセラミック
ス成形焼結体が得られる。
The above reaction starts at about 400°C and is completed at about 1500°C. Therefore, 5L3N4. Conventionally, inorganic sintered ceramics represented by non-oxides such as SiC,
High-temperature sintering of 1700°C or higher has been performed, but according to the present invention, a ceramic molded sintered body with excellent mechanical properties can be obtained at a temperature of about 1300 to 1500°C, despite having a relatively low density. It will be done.

また、無機シラザン高重合体の添加量は、目的とする焼
結体の特性、例えば、強度、密度、加工性などに応じ、
制限なく増減することが可能である。これは、従来のプ
レセラミックポリマーと異なり、重合度をコントロール
することにより、融解の度合いを低減し、多量添加時に
おいても成形体の軟化を防止することができるためであ
る。
In addition, the amount of the inorganic silazane high polymer added depends on the characteristics of the desired sintered body, such as strength, density, workability, etc.
It is possible to increase or decrease without limit. This is because, unlike conventional preceramic polymers, by controlling the degree of polymerization, the degree of melting can be reduced and softening of the molded body can be prevented even when a large amount is added.

このようなバインダーを用いてセラミックスを成形する
には、前記の如く、溶剤中にセラミックス粉末と無機シ
ラザン高重合体を添加し混合してスラリーを作成してス
ラリー成形するか、あるいはこのスラリーから溶剤を蒸
発させて造粒粉を作成してプレス成形すればよい。
In order to mold ceramics using such a binder, as described above, ceramic powder and inorganic silazane high polymer are added to a solvent and mixed to create a slurry and then slurry molded, or from this slurry to a solvent. can be evaporated to create granulated powder, which can then be press-molded.

一例として、プレス法を適用するためには、スプレード
ライヤーにより、スラリー中の溶剤を蒸発させ、造粒粉
とすればよい。このとき、無機ポリシラザンは、造粒の
ための成形用バインダーとして働くと同時に、焼結体バ
インダー(焼結助剤)として、セラミックス粉体中に均
一に混合されたことになる。このようにして得られた造
粒粉をプレス成形することにより、所定の形状の成形体
を得ることができる。また、スラリー成形法によれば、
造粒粉を経ずに直接成形用かつ焼結用バインダーが均一
に混合された成形体を得ることができる。
For example, in order to apply the press method, the solvent in the slurry may be evaporated using a spray dryer to form granulated powder. At this time, the inorganic polysilazane acts as a molding binder for granulation and is uniformly mixed into the ceramic powder as a sintered body binder (sintering aid). By press-molding the granulated powder obtained in this way, a molded article having a predetermined shape can be obtained. Also, according to the slurry molding method,
A molded body in which binder for molding and sintering is uniformly mixed can be obtained directly without using granulated powder.

なお、本発明では、無機シラザン高重合体を溶剤に溶解
した溶液にセラミックス成形体(焼結体)を浸漬して、
成形体(焼結体)中に無機シラザン高重合体を含浸した
セラミックス成形体を焼成することによって、セラミッ
クス成形体(焼結体)を緻密化することも可能である。
In addition, in the present invention, a ceramic molded body (sintered body) is immersed in a solution in which an inorganic silazane high polymer is dissolved in a solvent.
It is also possible to densify a ceramic molded body (sintered body) by firing a ceramic molded body in which the molded body (sintered body) is impregnated with an inorganic silazane high polymer.

溶剤としては、脂肪族炭化水素、脂環式炭化水素、芳香
族炭化水素の炭化水素溶媒、ハロゲン化メタン、ハロゲ
ン化エタン、ハロゲン化ベンゼン等のハロゲン化炭化水
素、脂肪族エーテル、脂環式エーテル等のエーテル類な
どが使用できる。好ましい溶媒は、塩化メチレン、クロ
ロホルム、四塩化炭素、ブロモホルム、塩化エチレン、
塩化エチリデン、トリクロロエタン、テトラクロロエタ
ン等のハロゲン化炭化水素、エチルエーテル、イソプロ
ピルエーテル、エチルブチルエーテル、ブチルエーテル
、1.2−ジオキシエタン、ジオキサン、ジメチルジオ
キサン、テトラヒドロフラン、テトラヒドロピラン等の
エーテル類、ペンタン、ヘキサン、イソヘキサン、メチ
ルペンタン、ヘプタン、イソへブタン、オクタン、イソ
オクタン、シクロペンタン、メチルシクロペンタン、シ
クロヘキサン、メチルシクロヘキサン、ベンゼン、トル
エン、キシレン、エチルベンゼン等の炭化水素等である
Examples of solvents include hydrocarbon solvents such as aliphatic hydrocarbons, alicyclic hydrocarbons, and aromatic hydrocarbons, halogenated hydrocarbons such as halogenated methane, halogenated ethane, and halogenated benzene, aliphatic ethers, and alicyclic ethers. Ethers such as can be used. Preferred solvents are methylene chloride, chloroform, carbon tetrachloride, bromoform, ethylene chloride,
Halogenated hydrocarbons such as ethylidene chloride, trichloroethane, and tetrachloroethane, ethers such as ethyl ether, isopropyl ether, ethyl butyl ether, butyl ether, 1,2-dioxyethane, dioxane, dimethyldioxane, tetrahydrofuran, and tetrahydropyran, pentane, hexane, and isohexane , methylpentane, heptane, isohbutane, octane, isooctane, cyclopentane, methylcyclopentane, cyclohexane, methylcyclohexane, benzene, toluene, xylene, ethylbenzene, and other hydrocarbons.

得られたセラミックス成形体を焼成して無機シラザン高
重合体をセラミックス化し、セラミックス成形焼結体を
得ることができる。焼成条件は真空中、不活性ガス、還
元性ガス、炭化水素ガスのうちから選ばれる少なくとも
1種からなる雰囲気中で600〜2300℃の温度範囲
内で加熱焼結する。
The obtained ceramic molded body is fired to turn the inorganic silazane polymer into a ceramic, thereby obtaining a ceramic molded sintered body. Firing conditions include heating and sintering in a temperature range of 600 to 2300° C. in a vacuum, in an atmosphere consisting of at least one selected from inert gas, reducing gas, and hydrocarbon gas.

こうして得られる焼結体は、用いたセラミックス粒子あ
るいはウィスカーの間をポリシラザンが加熱分解して生
成した非晶質または1000Å以下の極めて微細な粒子
によってうめられた組織となる。
The sintered body thus obtained has a structure filled with amorphous or extremely fine particles of 1000 Å or less, which are generated by thermal decomposition of polysilazane between the ceramic particles or whiskers used.

こうして、本発明によれば、プレセラミックポリマーと
してポリシラザンを選択し、かつ側鎖に有機基を有しな
いポリシラザンを選択することによって、低温焼成で機
械的性質及び化学的性質に優れたセラミックス成形焼結
体が得られる。
Thus, according to the present invention, by selecting polysilazane as the preceramic polymer and selecting polysilazane having no organic group in the side chain, ceramic forming and sintering with excellent mechanical and chemical properties can be achieved by firing at a low temperature. You get a body.

〔効 果〕〔effect〕

本発明の無機シラザン高重合体は、前記の如き分子構造
的及び物性的特徴を有するもので、種々の分野に利用す
ることができる。次に、本発明の無機シラザン高重合体
の用途的及び製法的特徴を示す。
The inorganic silazane polymer of the present invention has the above-mentioned molecular structure and physical characteristics, and can be used in various fields. Next, the usage and production characteristics of the inorganic silazane high polymer of the present invention will be shown.

■ 無機シラザン高重合体は、有機溶媒に可溶であり、
焼成して窒化ケイ素あるいは窒化ケイ素含有セラミック
スに変換できるため、高性能のセラミックス成形体すな
わち、高温機械強度が高く、耐熱性、耐食性、耐酸化性
、耐熱[!性に優れた連続繊維、フィルム、被覆膜を容
易に得ることができる。また、セラミックス収率が高い
ので、焼結用結合剤、含浸剤等としての利用も可能であ
る。
■ Inorganic silazane high polymers are soluble in organic solvents,
Since it can be converted into silicon nitride or silicon nitride-containing ceramics by firing, it can be converted into a high-performance ceramic molded body, that is, a high-temperature mechanical strength, heat resistance, corrosion resistance, oxidation resistance, and heat resistance [! Continuous fibers, films, and coatings with excellent properties can be easily obtained. Moreover, since the ceramic yield is high, it can also be used as a binder for sintering, an impregnating agent, etc.

■ 無機シラザン高重合体は、その重合体中に分解を促
進する残留触媒等の不純物の混入がないため、安定性が
向上し、取扱いが容易になり、その上高温焼成後のセラ
ミックスの純度が向上する。
■ Inorganic silazane high polymers do not contain impurities such as residual catalysts that promote decomposition, so they have improved stability and are easier to handle, and they also improve the purity of ceramics after high-temperature firing. improves.

■ 無機シラザン高重合体は、原料無機シラザンに比べ
て架橋構造、分子量が増加するため、凝固性が向上し、
常温ですみやかに賦形化することが可能となる。
■ Inorganic silazane high polymers have an increased crosslinked structure and molecular weight compared to the raw material inorganic silazane, resulting in improved coagulation properties.
It becomes possible to form the product quickly at room temperature.

■ 遷移金属等の触媒を用いないため、生成物と触媒と
の分離工程を必要としない。
■ Since a catalyst such as a transition metal is not used, there is no need for a separation process between the product and the catalyst.

■ 重合体中に触媒が残存しないため、安定性が向上し
、溶媒を除き、単離後も長期保存が可能である。
■ Since no catalyst remains in the polymer, stability is improved and long-term storage is possible even after removal of the solvent and isolation.

■ 高価で危険な触媒を使用しないため、低コストで安
全である。
■ It is low cost and safe because it does not use expensive and dangerous catalysts.

■ 高分子量のため、高温焼成時の蒸発損失が小さいの
で、セラミックス収率が向上する。
■ Due to its high molecular weight, evaporation loss during high-temperature firing is small, improving ceramic yield.

■ 不純物の混入がないため、高温焼成後のセラミック
スの純度が向上する。
■ Since there are no impurities mixed in, the purity of ceramics after high-temperature firing is improved.

■ 無機シラザン高重合体を紡糸する場合、紡糸助剤を
添加せずに連続紡糸が可能となる。
■ When spinning an inorganic silazane high polymer, continuous spinning is possible without adding a spinning aid.

〔実施例〕〔Example〕

以下、実施例により本発明を更に詳細に説明する。 Hereinafter, the present invention will be explained in more detail with reference to Examples.

参考例 1 内容積500m Qの四つロフラスコにガス吹きこみ管
、メカニカルスターラー、ジュワーコンデンサーを装置
した。反応器内部を脱酸素した乾燥窒素で置換した後、
四つロフラスコに脱気した乾燥ピリジン280m Qを
入れ、これを氷冷した。次にジクロロシラン51.6g
を加えると白色固体状のアダクト(Si)I、C(12
・2C,H,N)が生成した。反応混合物を氷冷し、攪
拌しながら、水酸化ナトリウム管及び活性炭管を通して
精製したアンモニア30.0gを吹き込んだ。
Reference Example 1 A four-loop flask with an internal volume of 500 m and Q was equipped with a gas blowing pipe, a mechanical stirrer, and a dewar condenser. After replacing the inside of the reactor with deoxygenated dry nitrogen,
280 mQ of degassed dry pyridine was placed in a four-necked flask and cooled on ice. Next, 51.6g of dichlorosilane
When added, a white solid adduct (Si) I, C (12
・2C, H, N) were generated. The reaction mixture was ice-cooled, and while stirring, 30.0 g of purified ammonia was blown into the reaction mixture through a sodium hydroxide tube and an activated carbon tube.

反応終了後、反応混合物を遠心分離し、乾燥ピリジンを
用いて洗浄した後、更に窒素雰囲気下で濾過して、濾液
520m Qを得た。濾液5mQから溶媒を減圧留去す
ると樹脂状固体無機シラザン0.98gが得られた。
After the reaction was completed, the reaction mixture was centrifuged, washed with dry pyridine, and further filtered under a nitrogen atmosphere to obtain 520 mQ of filtrate. The solvent was distilled off from 5 mQ of the filtrate under reduced pressure to obtain 0.98 g of resinous solid inorganic silazane.

得られたポリマーの数平均分子量はGPCによす測定し
たところ、1020であった。 また、このポリマーの
IR(赤外吸収)スペクトル(溶媒:乾燥〇−キシレン
;無機シラザンの濃度:9.8g/ Q )を検討する
と、波数(■−1) 3350及び1175のN)Iに
基づく吸収; 2170(i =3.14)のSiHに
基づく吸収;1020〜820のSiH及び5iNSi
に基づく吸収を示すことが確認された。またこのポリマ
ーの18NMR(プロトン核磁気共鳴)スペクトル(6
0MI(z、溶媒CDCΩ3/基準物質TMS )を検
討すると、いずれも幅広い吸収を示していることが確認
された。即ち64.8及び4.4 (br、 5iH)
 ; 1.5(br、N)りの吸収が確認された。
The number average molecular weight of the obtained polymer was determined to be 1020 by GPC. In addition, when examining the IR (infrared absorption) spectrum of this polymer (solvent: dry 〇-xylene; concentration of inorganic silazane: 9.8 g/Q), it was found that Absorption; absorption based on SiH of 2170 (i = 3.14); SiH of 1020-820 and 5iNSi
It was confirmed that the absorption based on In addition, the 18NMR (proton nuclear magnetic resonance) spectrum (6
When examining 0MI (z, solvent CDCΩ3/reference material TMS), it was confirmed that all of them exhibited broad absorption. i.e. 64.8 and 4.4 (br, 5iH)
; Absorption of 1.5 (br, N) was confirmed.

参考例 2 参考例1と同一の装置を用いて反応を行った。Reference example 2 The reaction was carried out using the same apparatus as in Reference Example 1.

即ち、参考例1で示した四つロフラスコに脱気した乾燥
ジクロロメタン260m Aを入れ、これを氷冷した。
That is, 260 mA of degassed dry dichloromethane was placed in the four-loaf flask shown in Reference Example 1, and cooled on ice.

次にジクロロシラン25.0gを加えた。この溶液を氷
冷し、攪拌しながら、水酸化ナトリウム管及び活性炭管
を通して精製したアンモニア22.3gを窒素との混合
ガスとして吹き込んだ。反応、中ガス流路に粉霧が生成
したので、ガス流路を時々たたいて閉塞を防いだ。
Next, 25.0 g of dichlorosilane was added. This solution was ice-cooled, and while stirring, 22.3 g of purified ammonia was blown into the solution as a mixed gas with nitrogen through a sodium hydroxide tube and an activated carbon tube. During the reaction, powder mist was generated in the gas flow path, so the gas flow path was occasionally tapped to prevent clogging.

反応混合物を参考例1と同様処理すると、粘性油状無機
シラザンが4.9g得られた。得られたポリマーの数平
均分子量はGPCにより測定したところ620であった
The reaction mixture was treated in the same manner as in Reference Example 1 to obtain 4.9 g of viscous oily inorganic silazane. The number average molecular weight of the obtained polymer was 620 as measured by GPC.

参考例3 参考例1と同一の装置を用いて反応を行なった。Reference example 3 The reaction was carried out using the same apparatus as in Reference Example 1.

すなわち参考例1で示した四つロフラスコに脱気した乾
燥ベンゼン300m mを入れ、これを水冷した。
That is, 300 mm of degassed dry benzene was placed in the four-loaf flask shown in Reference Example 1 and cooled with water.

次にジクロロシラン24.0gを加えた。この溶液を水
冷し、撹拌しながら、水酸化ナトリウム管および活性炭
管を通して精製したアンモニア23.8gを窒素との混
合ガスとして吹き込んだ。反応中ガス流路に粉霧が生成
したので、ガス流路を時々たたいて閉塞を防いた。
Next, 24.0 g of dichlorosilane was added. This solution was cooled with water, and while stirring, 23.8 g of purified ammonia was blown into the solution as a mixed gas with nitrogen through a sodium hydroxide tube and an activated carbon tube. During the reaction, powder mist was generated in the gas flow path, so the gas flow path was occasionally tapped to prevent clogging.

反応混合物を参考例1と同様に処理すると粘性油状無機
シラザンが3.1g得られた。得られたポリマーの数平
均分子量はGPCにより測定したところ360であった
The reaction mixture was treated in the same manner as in Reference Example 1 to obtain 3.1 g of viscous oily inorganic silazane. The number average molecular weight of the obtained polymer was 360 as measured by GPC.

実施例1 参考例1で得られた無機シラザンのピリジン溶液(無機
シラザンの濃度、 5.24重量%)100mffを内
容積300+n Qの耐圧反応容器に入れ、窒素雰囲気
、密閉系で150℃で3時間攪拌しながら反応を行なっ
た。この間大量の気体が発生した。反応前後で圧力は1
.O1cg/ci上昇した。室温に冷却後、乾燥エチル
ベンゼン200m Qを加え、圧力3−5n3−5n、
温度50〜70℃で溶媒を除いたところ、4.68gの
白色粉末が得られた。この粉末は、トルエン、テトラヒ
ドロフラン、クロロホルムおよびその他の有機溶媒に可
溶であった。
Example 1 100 mff of the inorganic silazane pyridine solution obtained in Reference Example 1 (concentration of inorganic silazane, 5.24% by weight) was placed in a pressure-resistant reaction vessel with an internal volume of 300+nQ, and heated at 150°C in a closed system in a nitrogen atmosphere for 30 minutes. The reaction was carried out with stirring for hours. During this time, a large amount of gas was generated. The pressure is 1 before and after the reaction.
.. O1cg/ci increased. After cooling to room temperature, add 200m Q of dry ethylbenzene, pressure 3-5n3-5n,
When the solvent was removed at a temperature of 50 to 70°C, 4.68 g of white powder was obtained. This powder was soluble in toluene, tetrahydrofuran, chloroform and other organic solvents.

前記重合体粉末の数平均分子量は、GPCにより測定し
たところ2470であった。また、そのIRスペクトル
(溶媒:エチルベンゼン)の分析の結果、波数(国−’
)3350および1175のNHに基づく吸収; 21
70のSiHに基づく吸収;1020〜820のSiH
および5iNSiに基づく吸収を示すことが確認された
。さらに、前記重合体粉末の18NMRスペクトル(C
DCQ 、 、 TMS)を分析したところ、いずれも
幅広い吸収を示している、すなわち64.8(br、 
SiH.)、δ4.4(br、 SiH,)。
The number average molecular weight of the polymer powder was 2470 as measured by GPC. In addition, as a result of analysis of its IR spectrum (solvent: ethylbenzene), the wavenumber (country-'
) NH-based absorption of 3350 and 1175; 21
Absorption based on SiH of 70; SiH of 1020-820
It was confirmed that the absorption based on 5iNSi and 5iNSi was exhibited. Furthermore, the 18NMR spectrum (C
DCQ, , TMS) were analyzed and all showed a wide absorption, i.e. 64.8 (br, TMS).
SiH. ), δ4.4 (br, SiH,).

δ1.5(br、NH)の吸収が観測された。(Si)
It)/(SIHa)=4.1であった。
Absorption at δ1.5 (br, NH) was observed. (Si)
It)/(SIHa)=4.1.

実施例2 参考例1で得られた無機シラザンのピリジン溶液(無機
シラザンの濃度、 6.18重量%)200mRを内容
積300a+ Qの耐圧反応容器に入れ、窒素雰囲気、
密閉系で120℃で3時間攪拌をしながら反応を行なっ
た。この間大量の気体が発生したが、ガスクロマトグラ
フィー(GC)測定により、この気体は水素であった。
Example 2 200 mR of the inorganic silazane pyridine solution obtained in Reference Example 1 (concentration of inorganic silazane, 6.18% by weight) was placed in a pressure-resistant reaction vessel with an internal volume of 300 a+Q, and a nitrogen atmosphere was added.
The reaction was carried out in a closed system at 120° C. for 3 hours with stirring. During this time, a large amount of gas was generated, which was determined to be hydrogen by gas chromatography (GC) measurement.

反応前後における圧力上昇は2.0kg/dであった。The pressure increase before and after the reaction was 2.0 kg/d.

室温に冷却後、乾燥。−キシレン400mQを加え、圧
力3〜5mmHg、温度50〜70℃で溶媒を除いたと
ころ、白色粉末が10.9g得られ、この粉末は有機溶
媒に可溶であった。
After cooling to room temperature, dry. - When 400 mQ of xylene was added and the solvent was removed at a pressure of 3 to 5 mmHg and a temperature of 50 to 70°C, 10.9 g of white powder was obtained, and this powder was soluble in the organic solvent.

前記重合体粉末の数平均分子量は、GPCにより測定し
たところ1950であった。
The number average molecular weight of the polymer powder was 1950 as measured by GPC.

得られた改質無機シラザン高重合体の元素分析結果は次
の通りであった。(重量%) Si:62.7. N:25.7. O:3.52. 
C:4.4. H:5.00実施例3 実施例2で得られた無機シラザン高重合体を窒素中で1
400℃まで昇温速度3℃/分で加熱し、3時間焼成す
ることで茶かっ色粉末を79.6重量%の収率で得た。
The results of elemental analysis of the obtained modified inorganic silazane high polymer were as follows. (% by weight) Si: 62.7. N:25.7. O: 3.52.
C:4.4. H: 5.00 Example 3 The inorganic silazane high polymer obtained in Example 2 was dissolved in nitrogen for 1
The mixture was heated to 400° C. at a temperature increase rate of 3° C./min and fired for 3 hours to obtain a brown powder with a yield of 79.6% by weight.

得られたセラミックスの粉末X線回折測定を行なったと
ころ、2θ=20.。にα−3i3N4の(101)回
折線、2θ=22.9’にα−3i、 N4の(110
)回折線。
Powder X-ray diffraction measurement of the obtained ceramic revealed that 2θ=20. . (101) diffraction line of α-3i3N4, α-3i, N4 (110) at 2θ=22.9'
) Diffraction lines.

20 =26.4@にα−3i3N4の(200)回折
線、2θ=30.9”にα−3i3N4の(201)回
折線、2θ=31.7@にα−8i3N4の(002)
回折線、2θ=34.5’にα−3i、 N4の(10
2)回折線、2θ=35.2°にα−3i、 N4の(
210)回折線、2θ=38.8°にa−3iaN4の
(211)回折線、2θ=39.4°にα−3L3N4
の(112)回折線、2θ=40.1’にα−3L3N
4の(300)回折線、2θ=41.8”にα−3L、
 N4の(202)回折線、2θ=43.4°にα−3
i、 N4の(301)回折線、2θ=46.9” ニ
a−3i、N、+7)) 220) 回折i、2 B 
=48.2” ニa−5in N4の(212)回折線
、2θ=48.8°にα−3L3N4の(310)回折
線、さらニ2θ=23.3’ ニβ−5i、N、(7)
(110)回折線、2θ=26.9°にβ−3i3N4
の(200)回折線。
20 = (200) diffraction line of α-3i3N4 at 26.4@, (201) diffraction line of α-3i3N4 at 2θ = 30.9'', (002) of α-8i3N4 at 2θ = 31.7@
Diffraction line, α-3i at 2θ = 34.5', (10
2) Diffraction line, α-3i at 2θ = 35.2°, N4 (
210) Diffraction line, (211) diffraction line of a-3iaN4 at 2θ = 38.8°, α-3L3N4 at 2θ = 39.4°
(112) diffraction line, α-3L3N at 2θ=40.1'
(300) diffraction line of 4, α-3L at 2θ=41.8”,
(202) diffraction line of N4, α-3 at 2θ=43.4°
i, (301) diffraction line of N4, 2θ=46.9” Ni a-3i, N, +7)) 220) Diffraction i, 2 B
= 48.2" (212) diffraction line of N4 at 2θ = 48.8°, (310) diffraction line of α-3L3N4 at 2θ = 48.8°, and (310) diffraction line of α-3L3N4 at 2θ = 23.3' Ni β-5i, N, ( 7)
(110) diffraction line, β-3i3N4 at 2θ=26.9°
(200) diffraction line.

2 B =33.6’ ニp−3L3N4 ノ(101
) 回折線、2θ=36゜01にβ−3i、 N、の(
210)回折線、2θ=41.4’にβ5iaN4(’
) (201) 回折線、2θ=49.9”ニL−3L
、N、(7)(310)回折線、2θ=28.4’にS
iの(111)回折線、2θ=47.3@にSiの(2
20)回折線が認められ、結晶質の窒化珪素であること
が確認された。
2 B = 33.6' nip-3L3N4 ノ(101
) Diffraction line, β-3i, N, at 2θ=36°01 (
210) Diffraction line, β5iaN4('
) (201) Diffraction line, 2θ=49.9” L-3L
, N, (7) (310) diffraction line, S at 2θ=28.4'
i's (111) diffraction line, 2θ=47.3@Si's (2
20) Diffraction lines were observed, confirming that it was crystalline silicon nitride.

この結晶質窒化珪素の元素分析結果は(重量%)Si:
63.8. N:28.7. O:2.17. C:0
.36.H:0.11であった。
The elemental analysis results of this crystalline silicon nitride are (wt%) Si:
63.8. N:28.7. O:2.17. C:0
.. 36. H: 0.11.

実施例4 参考例1で得られた無機シラザンのα−ピコリン溶液(
無機シラザンの濃度、 5.86重量%)120mQを
内容積300m 11の耐圧反応容器に入れ、窒素雰囲
気、密閉系で120℃で3時間攪拌しながら反応を行な
った。この間大量の気体が発生した。実施例2と同様に
溶媒を減圧留去したところ、無機シラザン高重合体の白
色粉末が6.22g得られた。この粉末は有機溶媒に可
溶であり、その数平均分子量はGPCにより測定したと
ころ1850であった。
Example 4 α-picoline solution of inorganic silazane obtained in Reference Example 1 (
120 mQ of inorganic silazane (concentration: 5.86% by weight) was placed in a pressure-resistant reaction vessel with an internal volume of 300 m 11, and the reaction was carried out at 120° C. for 3 hours with stirring in a closed system in a nitrogen atmosphere. During this time, a large amount of gas was generated. When the solvent was distilled off under reduced pressure in the same manner as in Example 2, 6.22 g of white powder of an inorganic silazane high polymer was obtained. This powder was soluble in organic solvents, and its number average molecular weight was 1850 as measured by GPC.

実施例5 参考例2で得られた無機シラザンのピリジン溶液(無機
シラザンの濃度、 7.25重量%)100m Qを内
容積300m Qの耐圧反応容器に入れ、窒素雰囲気、
密閉系で120℃で5時間攪拌しながら反応を行なった
。この間大量の気体が発生した。実施例2と同様に溶媒
を減圧留去すると、無機シラザン高重合体の白色粉末が
6.43 g得られた。この粉末は有機溶媒に可溶であ
り、その数平均分子量はGPCにより測定をしたところ
、2030であった。
Example 5 A pyridine solution of the inorganic silazane obtained in Reference Example 2 (concentration of inorganic silazane, 7.25% by weight) was placed in a pressure-resistant reaction vessel with an internal volume of 300 m Q, and was placed in a nitrogen atmosphere.
The reaction was carried out in a closed system at 120°C with stirring for 5 hours. During this time, a large amount of gas was generated. When the solvent was distilled off under reduced pressure in the same manner as in Example 2, 6.43 g of white powder of an inorganic silazane high polymer was obtained. This powder was soluble in organic solvents, and its number average molecular weight was 2030 when measured by GPC.

実施例6 参考例3で得られた無機シラザンのピリジン溶液(無機
シラザンの濃度、 10.3重量%)100mffを内
容積30001 Qの耐圧反応容器に入れ、窒素雰囲気
、密閉系で120℃で8時間攪拌しながら反応を行なっ
た。この間大量の気体が発生した。実施例2と同様に溶
媒を減圧留去したところ、無機シラザン高重合体の白色
粉末が9..15g得られた。この粉末は有機溶媒に可
溶であり、そのGPCによる数平均分子量は1880で
あった。
Example 6 100 mff of the inorganic silazane pyridine solution obtained in Reference Example 3 (concentration of inorganic silazane, 10.3% by weight) was placed in a pressure-resistant reaction vessel with an internal volume of 30,001 Q, and heated at 120°C in a closed system in a nitrogen atmosphere at 8°C. The reaction was carried out with stirring for hours. During this time, a large amount of gas was generated. When the solvent was distilled off under reduced pressure in the same manner as in Example 2, a white powder of inorganic silazane high polymer was obtained. .. 15g was obtained. This powder was soluble in organic solvents and had a number average molecular weight of 1880 by GPC.

実施例7 実施例2で得られた無機シラザン高重合体を乾燥トルエ
ンに溶解し、82重量%の無機シラザン高重合体を含む
トルエン溶液を得た。これをノズルより加熱雰囲気中に
吐出させ、巻き取ることで無色透明の無機シラザン高重
合体連続繊維が得られた。
Example 7 The inorganic silazane high polymer obtained in Example 2 was dissolved in dry toluene to obtain a toluene solution containing 82% by weight of the inorganic silazane high polymer. This was discharged from a nozzle into a heated atmosphere and wound up to obtain a colorless and transparent inorganic silazane high polymer continuous fiber.

実施例8 実施例1の方法で製造した無機シラザン高重合体粉末(
数平均分子量2470)にオルトキシレン及び充填剤と
して炭化珪素(平均粒子径約10ミクロン)を添加し、
無機シラザン45重量%、オルトキシレン25重量%及
び炭化珪素30重量2の溶液を調製した。
Example 8 Inorganic silazane high polymer powder produced by the method of Example 1 (
Ortho-xylene and silicon carbide (average particle diameter of about 10 microns) are added as a filler to a material with a number average molecular weight of 2470,
A solution of 45% by weight of inorganic silazane, 25% by weight of ortho-xylene and 30% by weight of silicon carbide was prepared.

これをSS41基盤(70重m X 30IX 1mn
t)の表面にスプレーにて塗布した。基盤に塗布した後
不活性ガス(窒素)雰囲気の乾燥炉内で200℃、1時
間加熱乾燥した6昇温法度は3℃/分とした。その結果
厚み約160μmの被膜を得た。被膜の性能を表−1に
示す。
This is the SS41 base (70 heavy m x 30IX 1 mn
It was applied to the surface of t) by spraying. After coating the substrate, the coating was dried by heating at 200° C. for 1 hour in a drying oven under an inert gas (nitrogen) atmosphere.The temperature increase rate was 3° C./min. As a result, a coating having a thickness of about 160 μm was obtained. The performance of the coating is shown in Table 1.

検査方法は以下に示す通りである。The testing method is as shown below.

イ)外r/A:肉眼観察でクラック、色調、その地塗膜
の欠点を調べる。
b) Outside r/A: Check for cracks, color tone, and defects in the underlying coating film by visual observation.

口)鉛筆硬度:JIS K5400に準する。Mouth) Pencil hardness: According to JIS K5400.

ハ)密着性(基盤剥離試験):塗膜上に鋼ナイフで1m
m四方の素材に達する切れ目を基盤目に100個作り、
その上にセロハンテープ(種水化学工業)をはりつけた
後、そのセロハンテープを上方90°の方向に強くひき
はがした時に残っているます目の数で評価する。
c) Adhesion (substrate peeling test): 1 m with a steel knife on the coating film.
Make 100 cuts in the base material that reach m square material,
After pasting cellophane tape (Tanezu Kagaku Kogyo) on top of it, the cellophane tape is strongly peeled off in an upward direction of 90°, and the evaluation is based on the number of squares remaining.

実施例9 無機シラザン高重合体25重i%、オルトキシレン15
重量%、炭化珪素60重量%、助剤0.5重量2の溶液
を調製し、5O3304基盤に刷毛塗りにより塗布し窒
素ガス雰囲気下で00℃、1時間焼成したこと以外は実
施例の方法と同様に処理したところ被膜として表−1に
示す結果を得た。
Example 9 Inorganic silazane high polymer 25% by weight, ortho-xylene 15
A solution of 60% by weight of silicon carbide and 0.5% by weight of auxiliary agent was prepared, and the method was the same as that of the example except that it was applied by brushing onto a 5O3304 substrate and baked at 00°C for 1 hour in a nitrogen gas atmosphere. When treated in the same manner, the results shown in Table 1 were obtained as a film.

実施例1゜ 無機シラザン高重合体90重撞%及びオルトキシレン1
0重量%の溶液を調製し、5US304上に浸漬により
塗布し、空気中400℃、1時間焼成したこと以外は実
施例8の方法と同様に処理したところ被膜として表−1
に示す結果を得た。
Example 1 Inorganic silazane high polymer 90% gravity and ortho-xylene 1
A 0% by weight solution was prepared, coated on 5US304 by dipping, and treated in the same manner as in Example 8, except that it was baked in air at 400°C for 1 hour, resulting in a coating film shown in Table 1.
The results shown are obtained.

実施例11 無機ポリシラザンを用いるかわりに、実施例1の無機シ
ラザン高重合体を用いる他は、実施例1と全く同様な手
法でSi3N4焼結体を得た0本焼結体のかさ密度は2
.75g/ad、抗折強度はIL2kg/m+a”であ
り、実施例1に比べ高密度高強度の焼結体が得られた。
Example 11 A Si3N4 sintered body was obtained in exactly the same manner as in Example 1, except that the inorganic silazane high polymer of Example 1 was used instead of the inorganic polysilazane. The bulk density of the 0-piece sintered body was 2.
.. The sintered body had a bending strength of 75 g/ad and a transverse strength of IL 2 kg/m+a'', and a sintered body with higher density and higher strength than that in Example 1 was obtained.

実施例12 無機ポリシラザンを用いるかわりに無機シラザン高重合
体を用いる他は、実施例2と全く同様な手法でSiC焼
結体を得た0本焼結体のかさ密度は2.75g/a1、
抗折強度は16.4kg/am”であり、実施例2の結
果を上まわった。
Example 12 The SiC sintered body was obtained in exactly the same manner as in Example 2 except that an inorganic silazane high polymer was used instead of the inorganic polysilazane. The bulk density of the 0-wire sintered body was 2.75 g/a1,
The bending strength was 16.4 kg/am'', which exceeded the result of Example 2.

Claims (4)

【特許請求の範囲】[Claims] (1)数平均分子量が200〜500000であり、1
分子中のSiH_3基とSiH_2基の比(SiH_2
基/SiH_3基)が2.5〜8.4であって、しかも
元素比率がSi:50重量%〜70重量%、N:20重
量%〜34重量%、H:5重量%〜9重量%である無機
シラザン高重合体。
(1) The number average molecular weight is 200 to 500,000, and 1
The ratio of SiH_3 groups to SiH_2 groups in the molecule (SiH_2
group/SiH_3 group) is 2.5 to 8.4, and the element ratios are Si: 50 weight % to 70 weight %, N: 20 weight % to 34 weight %, H: 5 weight % to 9 weight %. An inorganic silazane high polymer.
(2)無機シラザンを塩基性溶媒中又は塩基性化合物を
含む溶媒中で加熱することを特徴とする請求項(1)記
載の無機シラザン高重合体の製造方法。
(2) The method for producing an inorganic silazane polymer according to claim (1), wherein the inorganic silazane is heated in a basic solvent or in a solvent containing a basic compound.
(3)請求項(1)記載の無機シラザン高重合体を必須
成分としたコーティング剤。
(3) A coating agent containing the inorganic silazane high polymer according to claim (1) as an essential component.
(4)請求項(1)記載の無機シラザン高重合体を必須
成分とするバインダー。
(4) A binder containing the inorganic silazane polymer according to claim (1) as an essential component.
JP63074918A 1987-08-13 1988-03-29 Inorganic silazane high polymer, production method thereof and use thereof Expired - Lifetime JP2613787B2 (en)

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