JP3067859B2 - Urethane curing agent and method for producing the same - Google Patents

Urethane curing agent and method for producing the same

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Publication number
JP3067859B2
JP3067859B2 JP3245680A JP24568091A JP3067859B2 JP 3067859 B2 JP3067859 B2 JP 3067859B2 JP 3245680 A JP3245680 A JP 3245680A JP 24568091 A JP24568091 A JP 24568091A JP 3067859 B2 JP3067859 B2 JP 3067859B2
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JP
Japan
Prior art keywords
curing agent
polyether
urethane curing
reaction
producing
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 - Lifetime
Application number
JP3245680A
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Japanese (ja)
Other versions
JPH0578442A (en
Inventor
和仁 板東
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Daicel Corp
Original Assignee
Daicel Chemical Industries Ltd
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Priority to JP3245680A priority Critical patent/JP3067859B2/en
Publication of JPH0578442A publication Critical patent/JPH0578442A/en
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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/30Low-molecular-weight compounds
    • C08G18/38Low-molecular-weight compounds having heteroatoms other than oxygen
    • C08G18/3819Low-molecular-weight compounds having heteroatoms other than oxygen having nitrogen
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/48Polyethers
    • C08G18/50Polyethers having heteroatoms other than oxygen
    • C08G18/5021Polyethers having heteroatoms other than oxygen having nitrogen

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  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Polyurethanes Or Polyureas (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明はロケットモーター用コン
ポジット系固体推進薬に使用される燃料結合剤に用いら
れるウレタン硬化剤に関する。更に詳しくは、酸化剤、
粘結剤、助燃剤、燃焼触媒等から成るコンポジット系固
体推進薬において、その粘結剤の主成分である燃料結合
剤として用いられるアジド系ポリエーテル用のウレタン
硬化剤に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a urethane curing agent used as a fuel binder for a composite solid propellant for a rocket motor. More specifically, an oxidizing agent,
The present invention relates to a urethane curing agent for azide-based polyether used as a fuel binder, which is a main component of a binder, in a composite solid propellant comprising a binder, an auxiliary agent, a combustion catalyst, and the like.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】近年、
コンポジット系固体推進薬の燃焼特性を改善するために
燃料結合剤としてアジド基を有するポリエーテルを使用
する方法が注目されている。一般に粘結剤中のアジド基
含有量が多いほど、推進薬とした場合の燃焼特性、特に
比推力の向上が大きいことが知られている。
2. Description of the Related Art In recent years,
Attention has been paid to a method of using a polyether having an azide group as a fuel binder in order to improve the combustion characteristics of a composite solid propellant. In general, it is known that the larger the azide group content in the binder, the greater the improvement in the combustion characteristics when used as a propellant, particularly the specific thrust.

【0003】これまでに、ポリエーテル中のアジド基量
を多くすることを目的とし、一般式(II)
In order to increase the azide group content in the polyether, the general formula (II)

【0004】[0004]

【化2】 Embedded image

【0005】(式中、p は正の数を表す。)で示される
アジドメチル基を側鎖に有するポリエーテル(米国特許
第4,268,450号) や、さらにポリエーテル中のアジド基
量を多くすることが可能である一般式(III)
(Wherein p represents a positive number) A polyether having an azidomethyl group in the side chain represented by the following formula (US Pat. No. 4,268,450) and the amount of azide group in the polyether may be increased. Possible general formula (III)

【0006】[0006]

【化3】 Embedded image

【0007】(式中、q, rは正の数を示す。)で示され
る3,3−ビスアジドメチルオキセタン(以下BAMOと
略記する)とテトラヒドロフラン(以下THFと略記す
る)とのコポリマーからなるポリエーテル(特開平2−
239178号公報) が提案されている。一方、前記ポリエー
テルをウレタン硬化するために用いるイソシアネート化
合物としては、一般式(IV)
(Wherein q and r are positive numbers) consisting of a copolymer of 3,3-bisazidomethyloxetane (hereinafter abbreviated as BAMO) and tetrahydrofuran (hereinafter abbreviated as THF). Polyether (JP-A-2-
239178) has been proposed. On the other hand, as the isocyanate compound used for urethane-curing the polyether, general formula (IV)

【0008】[0008]

【化4】 Embedded image

【0009】(式中、s は約2乃至約20の間の正の数を
表す。)及び一般式(V)
Wherein s represents a positive number between about 2 and about 20 and the general formula (V)

【0010】[0010]

【化5】 Embedded image

【0011】(式中、t は約2乃至約20の間の正の数を
表す)で示されるアジド基を有する硬化剤(特開昭64−
29414 号公報)が提案されている。しかし、これらの硬
化剤中のアジド基含有量は、ポリエーテルの検討状況と
比較して低レベルであり、よりアジド基含有量の多い硬
化剤の開発が要求されていた。
(Wherein t represents a positive number between about 2 and about 20)
No. 29414) has been proposed. However, the content of the azide group in these curing agents is lower than that of polyethers, and the development of a curing agent having a higher azide group content has been required.

【0012】[0012]

【課題を解決するための手段】以上の問題点を解決する
ため、本発明者はBAMOに着目し鋭意検討を行った結
果、特定の反応方法によりアジド基含有量の多いウレタ
ン硬化剤が得られることを見出し、本発明を完成するに
至った。即ち、本発明は、一般式(I)
Means for Solving the Problems In order to solve the above problems, the present inventors have conducted intensive studies focusing on BAMO, and as a result, a urethane curing agent having a large azide group content can be obtained by a specific reaction method. This led to the completion of the present invention. That is, the present invention provides a compound represented by the general formula (I):

【0013】[0013]

【化6】 Embedded image

【0014】(式中、n,m は0以上の整数で、かつ1≦
(n+m)≦10、R は飽和アルキレン基を示す。)で表わさ
れるウレタン硬化剤、およびハロゲン化炭化水素中に、
BAMO、反応開始剤としてBF3O(C2H5)2 及び分子量調
節剤としてジオール成分を一括に仕込み反応させて得ら
れる両末端が水酸基のポリエーテルに、ヘキサメチレン
ジイソシアネート(以下HMDIと略記する)を反応さ
せて合成することを特徴とする前記一般式(I)で表わ
されるウレタン硬化剤の製造方法を提供するものであ
る。
(Wherein, n and m are integers of 0 or more and 1 ≦
(n + m) ≦ 10, and R represents a saturated alkylene group. In the urethane curing agent represented by) and a halogenated hydrocarbon,
BAMO, BF 3 O (C 2 H 5 ) 2 as a reaction initiator, and a diol component as a molecular weight regulator are collectively charged and reacted. ) To produce a urethane curing agent represented by the general formula (I).

【0015】一般式(I)において、(n+m)の値は1〜
10、特に1〜5の範囲にあることが好ましい。(n+m)の
値が10を超えると硬化剤の結晶性が大きくなり、推進薬
の製造が困難になる。また一般式(I)において、R で
示される飽和アルキレン基としては、−CH2CH2−、−CH
2CH2CH2−、−CH2CH2CH2CH2−、
In the general formula (I), the value of (n + m) is 1 to
It is preferably in the range of 10, especially 1 to 5. When the value of (n + m) exceeds 10, the crystallinity of the curing agent increases, and it becomes difficult to produce a propellant. In formula (I), saturated alkylene group represented by R, -CH 2 CH 2 -, - CH
2 CH 2 CH 2 −, −CH 2 CH 2 CH 2 CH 2 −,

【0016】[0016]

【化7】 Embedded image

【0017】等が挙げられ、特に−CH2CH2−、−CH2CH2
CH2−、−CH2CH2CH2CH2− が好ましい。本発明の硬化剤
の原料である両末端が水酸基のポリエーテルは、ハロゲ
ン化炭化水素中に、BAMO、反応開始剤としてBF3O(C
2H5)2 及び分子量調節剤としてジオール成分を一括に仕
込み反応させて得られる。反応温度は−20〜30℃、特に
−10〜20℃の範囲にあることが好ましい。反応温度が−
20℃未満であると反応がほとんど進行しないために実用
的でない。また反応温度が30℃を超えると反応速度が大
きくなり、反応熱により異常反応を起こす。
And particularly, -CH 2 CH 2- , -CH 2 CH 2
CH 2 — and —CH 2 CH 2 CH 2 CH 2 — are preferred. The polyether having hydroxyl groups at both ends, which is a raw material of the curing agent of the present invention, contains BAMO in a halogenated hydrocarbon, and BF 3 O (C
2 H 5 ) 2 and a diol component as a molecular weight regulator are prepared and reacted at once. The reaction temperature is preferably in the range of -20 to 30C, particularly preferably in the range of -10 to 20C. The reaction temperature is-
If the temperature is lower than 20 ° C., the reaction hardly proceeds, so that it is not practical. When the reaction temperature exceeds 30 ° C., the reaction rate increases, and an abnormal reaction occurs due to the heat of the reaction.

【0018】本発明に用いられるハロゲン化炭化水素と
しては、ジクロロメタン、クロロホルム、1,1 −ジクロ
ロエタン、1,2 −ジクロロエタン、1,1,2 −トリクロロ
エタン、四塩化炭素等が挙げられるが、特にジクロロメ
タンが好ましい。ハロゲン化炭化水素の使用量は特に限
定されないが、反応原料に対し1.0 〜10重量倍使用する
のが好ましい。また、分子量調節剤として用いるジオー
ル成分は特に限定されないが、1,2 −エタンジオール、
1,2 −プロパンジオール、1,3 −プロパンジオール、1,
2 −ブタンジオール、1,3 −ブタンジオール、1,4 −ブ
タンジオール、2,3 −ブタンジオール等が挙げられ、特
に1,2 −エタンジオール、1,3 −プロパンジオール、1,
4 −ブタンジオールが好ましい。これらの分子量調節剤
とBAMOとのモル比を変化させることにより任意の分
子量の両末端水酸基のポリエーテルを得ることができ
る。
Examples of the halogenated hydrocarbon used in the present invention include dichloromethane, chloroform, 1,1-dichloroethane, 1,2-dichloroethane, 1,1,2-trichloroethane, and carbon tetrachloride. Is preferred. Although the amount of the halogenated hydrocarbon is not particularly limited, it is preferably used in an amount of 1.0 to 10 times the weight of the reaction raw material. The diol component used as the molecular weight regulator is not particularly limited, but includes 1,2-ethanediol,
1,2-propanediol, 1,3-propanediol, 1,
2-butanediol, 1,3-butanediol, 1,4-butanediol, 2,3-butanediol and the like, particularly 1,2-ethanediol, 1,3-propanediol,
4-butanediol is preferred. By changing the molar ratio between these molecular weight regulators and BAMO, polyethers having hydroxyl groups at both ends having an arbitrary molecular weight can be obtained.

【0019】更に、本発明の硬化剤の原料である両末端
水酸基のポリエーテルの製造に用いられるハロゲン化炭
化水素、反応開始剤(BF3O(C2H5)2)、BAMO及び分子
量調節剤(ジオール成分)に含まれる水分は500ppm以
下、特に100ppm以下であることが好ましい。また、反応
開始剤として用いられるBF3O(C2H5)2 の添加量は、分子
量調節剤に対して0.1 〜2倍モル、特に0.2〜1倍モル
の範囲が好ましい。添加量が分子量調節剤に対して0.1
倍モル未満になると反応速度が小さくなるために実用的
ではない。また、2倍モルを超えると副反応が起こるた
めに得られるポリエーテルの分子量分布が広がってしま
うため好ましくない。
Further, a halogenated hydrocarbon, a reaction initiator (BF 3 O (C 2 H 5 ) 2 ), a BAMO, and a molecular weight control used for producing a polyether having hydroxyl groups at both terminals, which are raw materials of the curing agent of the present invention. The water content of the agent (diol component) is preferably 500 ppm or less, particularly preferably 100 ppm or less. The amount of BF 3 O (C 2 H 5 ) 2 used as a reaction initiator is preferably 0.1 to 2 times, more preferably 0.2 to 1 time the mol of the molecular weight regulator. The amount added is 0.1 relative to the molecular weight regulator.
If the molar ratio is less than twice, the reaction rate is reduced, so that it is not practical. On the other hand, if the molar ratio exceeds 2 times, a side reaction occurs, and the molecular weight distribution of the obtained polyether is undesirably widened.

【0020】さらに上記方法により得られたポリエーテ
ルを精製後、直接、又は溶媒中でHMDIと反応させた
後、過剰のHMDIを減圧下にて除去することにより、
本発明のウレタン硬化剤を得ることができる。この場
合、ポリエーテル中の水分は500ppm以下、特に300ppm以
下にまで除去することが好ましい。
Further, after purifying the polyether obtained by the above method and reacting it directly or in a solvent with HMDI, excess HMDI is removed under reduced pressure to obtain
The urethane curing agent of the present invention can be obtained. In this case, it is preferable to remove water in the polyether to 500 ppm or less, particularly to 300 ppm or less.

【0021】[0021]

【実施例】以下、本発明を実施例によって更に具体的に
説明するが、本発明はこれらの実施例に限定されるもの
ではない。
EXAMPLES Hereinafter, the present invention will be described more specifically with reference to examples, but the present invention is not limited to these examples.

【0022】実施例1 <BAMOの合成>3,3 −ビスクロルメチルオキセタン
200gを窒素吹き込み管を有するガラス製セパラブルフラ
スコにとり、ジメチルホルムアミド670.5 g及びアジ化
ソーダ183.8 gを加え、温室にてよく混合した。次にオ
イルバスで上記混合液をゆっくりと90℃に加温した。温
度を引き続き90℃に保ち、撹拌しながら2時間反応を行
い、BAMOを合成した。反応終了後混合液の温度を室
温まで下げ、塩化メチレン1.5リットル及び水1.5リット
ルを加え、分液ロートにて分液した。分液後、下層液
(塩化メチレン溶液) を分取した。更に、分液ロートを
用いて、分取した塩化メチレン溶液を水1.5リットルで
2〜3回水洗し、最後に分取した下層液中に溶け込んで
いる水分を無水硫酸ナトリウムを加えて脱水した。その
後この溶液を濾過し、ロータリーエバポレーターにて塩
化メチレンを除去した。更に、圧力3mmHg、温度120 〜
140 ℃の条件にて蒸留精製し、無色透明又は淡黄白色の
BAMOを得た。GC (ガスクロマトグラフィー) にて純
度を測定した結果、99.9%以上であった。また、カール
フィッシャー法にて含水量を測定した結果、60ppm 以下
であった。
Example 1 <Synthesis of BAMO> 3,3-bischloromethyloxetane
200 g was placed in a glass separable flask having a nitrogen blowing tube, 670.5 g of dimethylformamide and 183.8 g of sodium azide were added, and mixed well in a greenhouse. Next, the mixture was slowly heated to 90 ° C. in an oil bath. The temperature was continuously maintained at 90 ° C., and the reaction was carried out for 2 hours with stirring to synthesize BAMO. After completion of the reaction, the temperature of the mixture was lowered to room temperature, 1.5 liter of methylene chloride and 1.5 liter of water were added, and the mixture was separated with a separating funnel. After separation, the lower layer solution (methylene chloride solution) was separated. Further, using a separating funnel, the separated methylene chloride solution was washed with 1.5 liters of water two to three times, and water dissolved in the lower layer liquid finally collected was dehydrated by adding anhydrous sodium sulfate. Thereafter, this solution was filtered, and methylene chloride was removed with a rotary evaporator. Furthermore, pressure 3mmHg, temperature 120 ~
Purification by distillation at 140 ° C. yielded a colorless, transparent or pale yellow-white BAMO. The purity was measured by GC (gas chromatography) and found to be 99.9% or more. The water content was measured by the Karl Fischer method and found to be 60 ppm or less.

【0023】<ポリエーテルの製造>常法に従って脱水
精製した 1,2−エタンジオール16.7ミリモル、塩化メチ
レン23.1g及び前記BAMO53.3ミリモルを予め窒素置
換したフラスコに入れ十分混合した。更に0℃にて反応
開始剤であるBF3O(C2H5)2 を8.3 ミリモル(1,2 −エタ
ンジオールに対して0.5 倍モル)添加し、温度を0℃に
保ちながら5日間反応を継続した。その後、蒸留水を添
加して反応を停止した後、飽和重曹水を添加して BF3O
(C2H5)2 を中和した。更に蒸留水500ml を加え、十分
に混合した後、分液ロートにて分液し、下層液(塩化メ
チレン溶液)を分取した。更に分液ロートを用い、分取
した塩化メチレン溶液を水500ml で2〜3回水洗し、反
応開始剤を完全に除去した。その後ロータリーエバポレ
ーターにて塩化メチレンを除去し、更に減圧下にて加熱
し、残留溶剤、残留水分等を除去し、ポリエーテルを得
た。水酸基価から求めた数平均分子量は600 また、両末
端は全て水酸基となっていた。
<Production of polyether> 16.7 mmol of 1,2-ethanediol, 23.1 g of methylene chloride and 53.3 mmol of BAMO, which were dehydrated and purified according to a conventional method, were placed in a flask previously purged with nitrogen, and mixed well. Further, at 0 ° C., 8.3 mmol of BF 3 O (C 2 H 5 ) 2 as a reaction initiator was added (0.5 times the mole of 1,2-ethanediol), and the reaction was carried out for 5 days while maintaining the temperature at 0 ° C. Continued. Thereafter, the reaction was stopped by adding distilled water, and then saturated aqueous sodium hydrogen carbonate was added to add BF 3 O
(C 2 H 5 ) 2 was neutralized. Further, 500 ml of distilled water was added thereto, mixed well, and then separated by a separating funnel to separate a lower layer solution (methylene chloride solution). Using a separating funnel, the separated methylene chloride solution was washed with 500 ml of water two to three times to completely remove the reaction initiator. Thereafter, methylene chloride was removed with a rotary evaporator, and the mixture was further heated under reduced pressure to remove residual solvent, residual moisture, and the like, to obtain polyether. The number average molecular weight determined from the hydroxyl value was 600, and both terminals were all hydroxyl groups.

【0024】<硬化剤の製造>上記ポリエーテル10g、
塩化メチレン30gを予め窒素置換したフラスコに入れ十
分混合した。更にHMDI6.73g(ポリエーテルの水酸
基に対して1.2 倍量)を添加し、室温にて1日間撹拌
し、反応させた。その後、ロータリーエバポレーターを
用いて塩化メチレンを除去し、さらに65℃、0.1mmHg の
条件にて過剰のHMDIを完全に除去し、15.6gの硬化
剤を製造した。滴定法を用いて分析した結果、ポリエー
テルの両端に完全にHMDIが反応していた。
<Production of curing agent> 10 g of the above polyether,
30 g of methylene chloride was placed in a flask which had been previously purged with nitrogen and mixed well. Further, 6.73 g of HMDI (1.2 times the amount of the hydroxyl group of the polyether) was added, and the mixture was stirred at room temperature for 1 day to be reacted. Thereafter, methylene chloride was removed using a rotary evaporator, and excess HMDI was completely removed under the conditions of 65 ° C. and 0.1 mmHg to produce 15.6 g of a curing agent. As a result of analysis using a titration method, HMDI was completely reacted at both ends of the polyether.

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C08G 18/00 - 18/87 C06D 5/00 CA(STN) REGISTRY(STN)────────────────────────────────────────────────── ─── Continued on the front page (58) Field surveyed (Int. Cl. 7 , DB name) C08G 18/00-18/87 C06D 5/00 CA (STN) REGISTRY (STN)

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 一般式(I) 【化1】 (式中、n,m は0以上の整数で、かつ1≦(n+m)≦10、
R は飽和アルキレン基を示す。)で表わされるウレタン
硬化剤。
1. A compound of the general formula (I) (Where n, m is an integer of 0 or more, and 1 ≦ (n + m) ≦ 10,
R represents a saturated alkylene group. A urethane curing agent represented by).
【請求項2】 Rが−CH2CH2−、−CH2CH2CH2−、−CH2C
H2CH2CH2−の群から選択される基である請求項1記載の
ウレタン硬化剤。
Wherein R is -CH 2 CH 2 -, - CH 2 CH 2 CH 2 -, - CH 2 C
H 2 CH 2 CH 2 - urethane curing agent of claim 1, wherein a group selected from the group of.
【請求項3】 ハロゲン化炭化水素中に、3,3 −ビスア
ジドメチルオキセタン、反応開始剤としてBF3O(C2H5)2
及び分子量調節剤としてジオール成分を一括に仕込み反
応させて得られるポリエーテルに、ヘキサメチレンジイ
ソシアネートを反応させて合成することを特徴とする請
求項1又は2記載のウレタン硬化剤の製造方法。
3. A halogenated hydrocarbon containing 3,3-bisazidomethyloxetane and BF 3 O (C 2 H 5 ) 2 as a reaction initiator.
The method for producing a urethane curing agent according to claim 1 or 2, wherein the polyether obtained by batchwise charging and reacting a diol component as a molecular weight regulator is reacted with hexamethylene diisocyanate to synthesize.
JP3245680A 1991-09-25 1991-09-25 Urethane curing agent and method for producing the same Expired - Lifetime JP3067859B2 (en)

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