JPH0244313B2 - - Google Patents
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- Publication number
- JPH0244313B2 JPH0244313B2 JP57046417A JP4641782A JPH0244313B2 JP H0244313 B2 JPH0244313 B2 JP H0244313B2 JP 57046417 A JP57046417 A JP 57046417A JP 4641782 A JP4641782 A JP 4641782A JP H0244313 B2 JPH0244313 B2 JP H0244313B2
- Authority
- JP
- Japan
- Prior art keywords
- compound
- reaction
- group
- compounds
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- 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
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- 150000001335 aliphatic alkanes Chemical class 0.000 claims description 2
- 150000001875 compounds Chemical class 0.000 description 65
- 238000006243 chemical reaction Methods 0.000 description 23
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 18
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 12
- 239000000243 solution Substances 0.000 description 11
- 239000002904 solvent Substances 0.000 description 11
- IQPQWNKOIGAROB-UHFFFAOYSA-N isocyanate group Chemical group [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 239000000203 mixture Substances 0.000 description 9
- 229920000642 polymer Polymers 0.000 description 9
- -1 aromatic diazonium salts Chemical class 0.000 description 8
- 150000002596 lactones Chemical class 0.000 description 8
- 239000012044 organic layer Substances 0.000 description 8
- 229920001228 polyisocyanate Polymers 0.000 description 8
- 239000005056 polyisocyanate Substances 0.000 description 8
- CTKINSOISVBQLD-UHFFFAOYSA-N Glycidol Chemical compound OCC1CO1 CTKINSOISVBQLD-UHFFFAOYSA-N 0.000 description 7
- 238000010538 cationic polymerization reaction Methods 0.000 description 7
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 7
- 238000006116 polymerization reaction Methods 0.000 description 7
- 239000000047 product Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 description 6
- 238000010586 diagram Methods 0.000 description 6
- 239000007864 aqueous solution Substances 0.000 description 5
- 125000003118 aryl group Chemical group 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 5
- 239000005457 ice water Substances 0.000 description 5
- 239000012948 isocyanate Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- YEJRWHAVMIAJKC-UHFFFAOYSA-N 4-Butyrolactone Chemical compound O=C1CCCO1 YEJRWHAVMIAJKC-UHFFFAOYSA-N 0.000 description 4
- 239000002841 Lewis acid Substances 0.000 description 4
- 238000005481 NMR spectroscopy Methods 0.000 description 4
- 239000000853 adhesive Substances 0.000 description 4
- 230000001070 adhesive effect Effects 0.000 description 4
- 238000009835 boiling Methods 0.000 description 4
- 239000012467 final product Substances 0.000 description 4
- 150000007517 lewis acids Chemical class 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- 239000002685 polymerization catalyst Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- NVZXHWILFYOUIQ-UHFFFAOYSA-N 1,4,6-trioxaspiro[4.4]nonan-3-ylmethanol Chemical compound O1C(CO)COC11OCCC1 NVZXHWILFYOUIQ-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 229910052943 magnesium sulfate Inorganic materials 0.000 description 3
- 235000019341 magnesium sulphate Nutrition 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- 230000000737 periodic effect Effects 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- JNSQTGQAYKGDBS-UHFFFAOYSA-N 1,4,11-trioxaspiro[4.6]undecan-3-ylmethanol Chemical compound O1C(CO)COC11OCCCCC1 JNSQTGQAYKGDBS-UHFFFAOYSA-N 0.000 description 2
- OZJPLYNZGCXSJM-UHFFFAOYSA-N 5-valerolactone Chemical compound O=C1CCCCO1 OZJPLYNZGCXSJM-UHFFFAOYSA-N 0.000 description 2
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 2
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 238000005266 casting Methods 0.000 description 2
- 239000012954 diazonium Substances 0.000 description 2
- 150000002148 esters Chemical class 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 150000002366 halogen compounds Chemical class 0.000 description 2
- 230000020169 heat generation Effects 0.000 description 2
- 150000002513 isocyanates Chemical group 0.000 description 2
- 239000010410 layer Substances 0.000 description 2
- 239000012778 molding material Substances 0.000 description 2
- XTAZYLNFDRKIHJ-UHFFFAOYSA-N n,n-dioctyloctan-1-amine Chemical compound CCCCCCCCN(CCCCCCCC)CCCCCCCC XTAZYLNFDRKIHJ-UHFFFAOYSA-N 0.000 description 2
- 238000000655 nuclear magnetic resonance spectrum Methods 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229920005862 polyol Polymers 0.000 description 2
- 150000003077 polyols Chemical class 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- RSJKGSCJYJTIGS-UHFFFAOYSA-N undecane Chemical compound CCCCCCCCCCC RSJKGSCJYJTIGS-UHFFFAOYSA-N 0.000 description 2
- PAPBSGBWRJIAAV-UHFFFAOYSA-N ε-Caprolactone Chemical compound O=C1CCCCCO1 PAPBSGBWRJIAAV-UHFFFAOYSA-N 0.000 description 2
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 1
- LQRGUWVOTVMGKW-UHFFFAOYSA-N 1,4,10-trioxaspiro[4.5]decan-3-ylmethanol Chemical compound O1C(CO)COC11OCCCC1 LQRGUWVOTVMGKW-UHFFFAOYSA-N 0.000 description 1
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 1
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 1
- AWMVMTVKBNGEAK-UHFFFAOYSA-N Styrene oxide Chemical compound C1OC1C1=CC=CC=C1 AWMVMTVKBNGEAK-UHFFFAOYSA-N 0.000 description 1
- 238000000862 absorption spectrum Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000003377 acid catalyst Substances 0.000 description 1
- HFBMWMNUJJDEQZ-UHFFFAOYSA-N acryloyl chloride Chemical compound ClC(=O)C=C HFBMWMNUJJDEQZ-UHFFFAOYSA-N 0.000 description 1
- 125000003647 acryloyl group Chemical group O=C([*])C([H])=C([H])[H] 0.000 description 1
- 238000007259 addition reaction Methods 0.000 description 1
- 125000002723 alicyclic group Chemical group 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical class 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 125000005626 carbonium group Chemical group 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 150000001989 diazonium salts Chemical class 0.000 description 1
- 125000004989 dicarbonyl group Chemical group 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 238000002290 gas chromatography-mass spectrometry Methods 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 1
- 238000001819 mass spectrum Methods 0.000 description 1
- VHRYZQNGTZXDNX-UHFFFAOYSA-N methacryloyl chloride Chemical compound CC(=C)C(Cl)=O VHRYZQNGTZXDNX-UHFFFAOYSA-N 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 238000007344 nucleophilic reaction Methods 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 229920005906 polyester polyol Polymers 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 239000003505 polymerization initiator Substances 0.000 description 1
- 238000010526 radical polymerization reaction Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 1
- 238000007039 two-step reaction Methods 0.000 description 1
- JOYRKODLDBILNP-UHFFFAOYSA-N urethane group Chemical group NC(=O)OCC JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000008096 xylene Substances 0.000 description 1
Landscapes
- Heterocyclic Carbon Compounds Containing A Hetero Ring Having Oxygen Or Sulfur (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Description
本発明は新規化合物であり、下記一般式〔1〕
で示される2−ヒドロキシメチル−1,4,6−
トリオキサスピロ〔4,m〕アルカン(ここでは
mは4〜6の整数を表わす。)さらに具体的には
2−ヒドロキシメチル−1,4,6−トリオキサ
スピロ〔4,4〕ノナン、2−ヒドロキシメチル
−1,4,6−トリオキサスピロ〔4,5〕デカ
ンおよび2−ヒドロキシメチル−1,4,6−ト
リオキサスピロ〔4,6〕ウンデカンを提供する
ものであつて、本発明に係るこれらの化合物(以
下化合物〔1〕と総称する)は、例えば重合性単
量体およびスピロオルソエステル基含有化合物の
合成原料として有用である。
(ここでmは4〜6の整数を表わす。)
化合物〔1〕はγ−ブチロラクトン、δ−バレ
ロラクトンおよびε−カプロラクトンから選ばれ
るラクトン類とグリシドールとの付加反応によつ
て製造することができ、この反応を示すと以下の
ごとくになる。
(ここでmは4〜6の整数を表わす。)
化合物〔1〕を製造するに際しては、グリシド
ール1モルに対して好ましくはラクトン類1モル
以上、さらに好ましくは1.2〜5モルのラクトン
過剰で反応させるのが適当であり、これらを例え
ば塩化メチレンやテトラヒドロフラン等のごとき
溶媒中で、触媒としてBF3OEt2、SnCl4、TiCl4、
FeCl3等のごときルイス酸を使用して反応させ
る。反応温度に特に制限はないが、0℃〜60℃で
行なうのが望ましい。
望ましい製造方法の1例としては、ラクトン類
とラクトン類に対して1〜10重量倍量の溶媒とを
反応器に仕込み、液温を所定温度に維持しつつ、
通常ラクトン類と溶媒からなる溶媒に対して0.03
〜3重量%(ラクトン類に対しては0.05〜10重量
%)の触媒を添加し、続いてグリシドールを単独
でまた5重量倍程度までの溶媒との溶液として滴
下する方法がある。
反応の進行程度は反応液を例えばガスクロマト
グラフまたは液体クロマトグラフで分析すること
によつて容易に知ることができ、反応終了時には
反応後にアルカリを加えて酸触媒を中和する。反
応液からの化合物〔1〕の分離取得は、例えばつ
ぎのようにして行なわれる。反応後を氷水により
冷却しながら、これにアルカリ水溶液例えば稀水
酸化ナトリウム水溶液を添加し撹拌混合後、水層
と有機層に分別する。有機層中の未反応ラクトン
がほぼ零になるまで上記操作を繰り返した後有機
層を水洗し、次に硫酸マグネシウムにより有機層
を脱水する。つぎに溶媒を留去し、残渣を減圧蒸
留することにより、化合物〔1〕を取得する。
スピロオルソエステル化合物のカチオン重合に
関しては、ジヤーナル・オブ・マクロモレキユラ
ー・サイエンス、ケミストリイ(Journal of
Macromolecular Science、Chemistry)、A9(5)、
849〜865(1975)などに記載されているが、本発
明の化合物〔1〕も同様にカチオン重合し、重合
物を与える。
本発明の化合物〔1〕のカチオン重合は、一般
によく知られている方法、すなわちカチオン重合
開始剤の存在下例えば紫外線、赤外線、熱または
マイクロ波などによつて行なわれる。
紫外線照射の場合のカチオン重合触媒として、
例えば
φ−N+≡N・PE6 -、φ−N+≡N・BF4 -などの
芳香族ジアゾニウム塩;φ−I−φ・BF4 -等の
芳香族ハロニウム塩;
等の周期律表第Va族元素の芳香族オニウム塩;
The present invention is a new compound, which has the following general formula [1]
2-hydroxymethyl-1,4,6-
Trioxaspiro[4,m]alkane (here, m represents an integer of 4 to 6) More specifically, 2-hydroxymethyl-1,4,6-trioxaspiro[4,4]nonane, 2 -Hydroxymethyl-1,4,6-trioxaspiro[4,5]decane and 2-hydroxymethyl-1,4,6-trioxaspiro[4,6]undecane, comprising: These compounds (hereinafter collectively referred to as compounds [1]) are useful, for example, as raw materials for the synthesis of polymerizable monomers and spiro-orthoester group-containing compounds. (Here, m represents an integer of 4 to 6.) Compound [1] can be produced by an addition reaction between lactones selected from γ-butyrolactone, δ-valerolactone, and ε-caprolactone and glycidol. , this reaction is as follows. (Here, m represents an integer of 4 to 6.) When producing compound [1], the reaction is carried out with an excess of lactone of preferably 1 mol or more, more preferably 1.2 to 5 mol, of lactone per 1 mol of glycidol. It is suitable to use BF 3 OEt 2 , SnCl 4 , TiCl 4 , etc. as a catalyst in a solvent such as methylene chloride or tetrahydrofuran.
The reaction is carried out using a Lewis acid such as FeCl3 . There is no particular restriction on the reaction temperature, but it is preferably carried out at 0°C to 60°C. As an example of a desirable production method, lactones and a solvent in an amount of 1 to 10 times the weight of the lactones are charged into a reactor, and while maintaining the liquid temperature at a predetermined temperature,
0.03 for solvents usually consisting of lactones and solvents
There is a method in which ~3% by weight (0.05~10% by weight for lactones) of catalyst is added, and then glycidol is added dropwise either alone or as a solution with a solvent up to about 5 times the weight. The degree of progress of the reaction can be easily determined by analyzing the reaction solution using, for example, a gas chromatograph or a liquid chromatograph, and when the reaction is completed, an alkali is added after the reaction to neutralize the acid catalyst. Separation and acquisition of compound [1] from the reaction solution is performed, for example, as follows. After the reaction is cooled with ice water, an alkaline aqueous solution such as a dilute aqueous sodium hydroxide solution is added thereto, stirred and mixed, and then separated into an aqueous layer and an organic layer. After repeating the above operation until the amount of unreacted lactone in the organic layer becomes almost zero, the organic layer is washed with water, and then the organic layer is dehydrated with magnesium sulfate. Next, the solvent is distilled off, and the residue is distilled under reduced pressure to obtain compound [1]. Regarding the cationic polymerization of spiro-orthoester compounds, please refer to the Journal of Macromolecular Science and Chemistry.
Macromolecular Science, Chemistry), A9(5),
849-865 (1975), the compound [1] of the present invention is similarly cationically polymerized to give a polymer. The cationic polymerization of the compound [1] of the present invention is carried out by a generally well-known method, that is, by using, for example, ultraviolet rays, infrared rays, heat, or microwaves in the presence of a cationic polymerization initiator. As a cationic polymerization catalyst in the case of ultraviolet irradiation,
For example, aromatic diazonium salts such as φ-N + ≡N·PE 6 - and φ-N + ≡N·BF 4 - ; aromatic halonium salts such as φ-I-φ·BF 4 - ; Aromatic onium salts of Group Va elements of the periodic table, such as;
【式】等の周期律表第 a族元素の芳香族オニウム塩;Periodic table number of [formula] etc. Aromatic onium salt of group a element;
【式】等の周期律表第
a−a族元素のジカルボニル錯化合物が使用
されうる。
また、その他合カチオン重合触媒としては、例
えばBF3、FeCl3、SnCl4、SbF3、TiCl4などのル
イス酸;BF3OEt2、BF3−アニリンコンブレツク
ス等のごときルイス酸とO、S、Nなどを有する
化合物との配位化合物;ルイス酸のオキソニウム
塩、ジアゾニウム塩、カルボニウム塩;ハロゲン
化合物、混合ハロゲン化合物または過ハロゲン酸
誘導体などがあげられる。
触媒の使用量は一般に重合しようとする単量体
に対し、0.001〜10重量%好ましくは0.1から5重
量%の範囲が好適である。
重合温度に関する制限は特にないが、通常常温
〜200℃で行なわれる。
重合時に溶媒を使用する場合は、生長カチオン
と反応してその活性を低下させない化合物を選ぶ
ことが望ましい。使用に適した溶媒としては、ヘ
キサン、オクタン等の脂肪族炭化水素;トルエ
ン、キシレン等の芳香族炭化水素;塩化メチレ
ン、1,1−ジクロルエタン等のハロゲン化炭化
水素その他がある。
また本発明の化合物〔1〕の官能基(OH基)
を利用して、求核反応により種々のスピロオルソ
エステル基を含有する化合物を合成する事が出来
る。
その化合物を例示すると、例えば次の一般式
〔2〕で示されるラジカル重合体基をもつ単量体
(以下化合物〔2〕という)がある。
(ここでRは水原子又はメチル基を表わし、mは
4〜6の整数を表わす。)
化合物〔2〕は化合物〔1〕とアクリル酸クロ
ライドまたはメタクリル酸クロライド(以下(メ
タ)アクリル酸クロライドと略記する)との脱塩
化水素反応により合成され、その反応式を示すと
以下のごとくになる。
(ここでRは、mは一般式〔2〕と同義である。)
上記反応は例えば化合物〔1〕を適当な溶媒中
で、トリエチルアミン等の有機塩基性物質の存在
下、(メタ)アクリル酸クロライドを滴下して脱
塩化水素させる。
上記化合物〔2〕は、(メタ)アクリロイル基
を利用して、単独でまたはエチレン性不飽和化合
物とラジカル重合させることにより、重合物にス
ピロオルソエステル基を導入することができる有
用な化合物である。
また他の例としては、化合物〔1〕とイソシア
ネート化合物と反応させることにより、スピロオ
ルソエステル基を含有すする下記一般式〔3〕で
示されるウレタン化合物(以下化合物〔3〕とい
う)がある。
(ここでQはイソシアネートまたはウレタン化合
物残基を表わし、mは4〜6の整数を表わしnは
1以上の整数を表わす。)
化合物〔3〕の整造法に関して説明すると以下
の()または()の方法がある。
() イソシアネート化合物と化合物〔1〕のウ
レタン化反応。
() 下記化合物(A)、(B)および(C)のウレタン化反
応。
(A) イソシアネート基を少なくとも2個有する
ポリイソシアネート化合物の少なくとも1
種。
(B) ヒドロキシル基を少なくとも2個有するポ
リヒドロキシ化合物の少なくとも1種。
(C) 一般式〔1〕で示されるスピロオルソエス
テルの少なくとも1種。
上記()、()で使用されうるイソシアネー
ト化合物としては、脂肪族および芳香族モノイソ
シアネートあるいは分子内に2個以上のイソシア
ネート基を有する脂肪族、脂環族および芳香族ポ
リイソシアネートがあり、また他の原料である二
つ以上のヒドロキシル基をもつポリヒドロキシ化
合物としては、多価アルコール、ポリエステルポ
リオール、ポリエーテルポリオール、ポリマーポ
リオールがある。
それらの化合物を具体的に例示するとモノイソ
シアネートとしては特開昭56−167688号公報第2
頁左下欄13行目から同頁右下欄6行目に記載され
ている、また分子内に2個以上のイソシアネート
基を有するイソシアネートおよびポリヒドロキシ
化合物としては特開昭57−21417号公報第5頁左
上欄下から3行目から第6頁右上欄下から4行目
に記載されている化合物等であり、これらのいず
れを用いてもよい。
上記()の化合物(A)、(B)および(C)をウレタン
化反応させることにより、ウレタン基をもつスピ
ロオルソエステルを製造する方法の1例を例示す
ると代表的な方法は二段反応による製法で、まず
第1の工程で、ポリイソシアネート化合物とポリ
ヒドロキシ化合物とのウレタン化反応により末端
および/または側鎖にイソシアネート基を有する
部分ウレタン化物を製造する。このときポリヒド
ロキシ化合物に含まれる水酸基1当量に対て、ポ
リイソシアネート化合物のイソシアネート基は約
1.1当量以上の割合で反応させるのがよく、この
当量比を変化させることにより、最終の生成組成
物の分子量を調節することができる。水酸基1当
量に対して、イソシアネート基が約1.1当量より
低い割合で使用されたときは、最終生成組成物の
分子量が著しく大きくなり粘度が増大したり、硬
化性が充分でない場合がある。
また水酸基に対するイソシアネート基の当量比
を大きくする事により、最終生成組成物におい
て、部分ウレタン化ポリイソシアネート化合物の
イソシアネート基を化合物〔1〕でウレタン化た
下記化合物〔4〕で示される化合物(以下化合物
〔4〕という。)の割合を大きくする事が出来る。
Y(−NH−COO−X)f 〔4〕
(ここでXはA dicarbonyl complex compound of an element of group a-a of the periodic table, such as [Formula] may be used. In addition, other combined cationic polymerization catalysts include, for example, Lewis acids such as BF 3 , FeCl 3 , SnCl 4 , SbF 3 , TiCl 4 ; Lewis acids such as BF 3 OEt 2 , BF 3 -aniline complexes, and O, S , N, etc.; oxonium salts, diazonium salts, and carbonium salts of Lewis acids; halogen compounds, mixed halogen compounds, and perhalogen acid derivatives. The amount of catalyst used is generally 0.001 to 10% by weight, preferably 0.1 to 5% by weight, based on the monomer to be polymerized. Although there are no particular restrictions regarding the polymerization temperature, it is usually carried out at room temperature to 200°C. When using a solvent during polymerization, it is desirable to choose a compound that does not react with the growing cation and reduce its activity. Suitable solvents for use include aliphatic hydrocarbons such as hexane and octane; aromatic hydrocarbons such as toluene and xylene; halogenated hydrocarbons such as methylene chloride, 1,1-dichloroethane, and others. Further, the functional group (OH group) of the compound [1] of the present invention
Using this, various compounds containing spiro-orthoester groups can be synthesized by nucleophilic reactions. An example of such a compound is a monomer having a radical polymer group represented by the following general formula [2] (hereinafter referred to as compound [2]). (Here, R represents a water atom or a methyl group, and m represents an integer of 4 to 6.) Compound [2] is a compound [1] and acrylic acid chloride or methacrylic acid chloride (hereinafter referred to as (meth)acrylic acid chloride). The reaction formula is as follows. (Here, R and m have the same meaning as in general formula [2].)
In the above reaction, for example, compound [1] is dehydrochlorinated by dropping (meth)acrylic acid chloride in a suitable solvent in the presence of an organic basic substance such as triethylamine. The above compound [2] is a useful compound that can introduce a spiro-orthoester group into a polymer by using a (meth)acryloyl group alone or by radical polymerization with an ethylenically unsaturated compound. . Another example is a urethane compound represented by the following general formula [3] (hereinafter referred to as compound [3]) containing a spiro-orthoester group by reacting compound [1] with an isocyanate compound. (Here, Q represents an isocyanate or urethane compound residue, m represents an integer of 4 to 6, and n represents an integer of 1 or more.) The following () or ( ) There is a method. () Urethane-forming reaction between an isocyanate compound and compound [1]. () Urethanization reaction of the following compounds (A), (B) and (C). (A) at least one polyisocyanate compound having at least two isocyanate groups;
seed. (B) At least one polyhydroxy compound having at least two hydroxyl groups. (C) At least one type of spiroorthoester represented by the general formula [1]. Isocyanate compounds that can be used in () and () above include aliphatic and aromatic monoisocyanates, aliphatic, alicyclic and aromatic polyisocyanates having two or more isocyanate groups in the molecule, and others. Examples of polyhydroxy compounds having two or more hydroxyl groups that are raw materials include polyhydric alcohols, polyester polyols, polyether polyols, and polymer polyols. Specific examples of these compounds include monoisocyanates as described in JP-A-56-167688 No. 2.
Isocyanates and polyhydroxy compounds having two or more isocyanate groups in the molecule, which are described from line 13 in the lower left column of the page to line 6 in the lower right column of the same page, are disclosed in JP-A No. 57-21417 No. 5. These are the compounds described in the third line from the bottom of the upper left column of the page to the fourth line from the bottom of the upper right column of page 6, and any of these may be used. An example of a method for producing a spiro-orthoester having a urethane group by subjecting the compounds (A), (B) and (C) in () above to a urethanization reaction is as follows: A typical method is a two-step reaction. In the production method, in the first step, a partially urethanized product having an isocyanate group at the terminal and/or side chain is produced by a urethanization reaction between a polyisocyanate compound and a polyhydroxy compound. At this time, the isocyanate group of the polyisocyanate compound is approximately 1 equivalent of hydroxyl group contained in the polyhydroxy compound.
It is preferable to carry out the reaction at a ratio of 1.1 equivalents or more, and by changing this equivalent ratio, the molecular weight of the final product composition can be adjusted. If the isocyanate group is used in a ratio lower than about 1.1 equivalents per equivalent of hydroxyl group, the molecular weight of the final product composition may become significantly large, resulting in increased viscosity or insufficient curability. In addition, by increasing the equivalent ratio of isocyanate groups to hydroxyl groups, in the final product composition, a compound represented by the following compound [4] in which the isocyanate group of a partially urethanized polyisocyanate compound is urethanized with compound [1] [4]) can be increased. Y(-NH-COO-X)f [4] (where X is
【式】
で示される基を、Yは部分ウレタン化ポリイソシ
アネート残基を、fはポリイソシアネート化合物
の価数に相当する整数を、またmは4〜6の整数
を表わす。)
この化合物〔4〕は2個以上のスピロオルソエ
ステル基を有することになり、これは多官能重合
性化合物であるから最終の生成組成物を硬化させ
るとき、橋かけ結合の生成度を増大させるのに役
立つ。
該ウレタン化反応は、、発熱による急激な温度
上昇をさけるために、必要に応じポリイソシアネ
ート化合物にポリヒドロキシ化合物を分割添加、
または滴下することによつて温度を調節しながら
行なう。
次に第2の工程では、第1の工程でえられた部
分ウレタン化物の末端および/または側鎖のイソ
シアネート基に化合物〔1〕を反応させ結合させ
る。なお、この種の部分ウレタン化物のある物は
市販されており、本発明においてはかかる市販品
を利用することもできる。
この部分ウレタン化物に化合物〔1〕を添加す
る割合は、部分ウレタン化物中の残存イソシアネ
ート基の当量数と化合物〔1〕の水酸基の当量数
とが等しくなるようにするのが一般的である。目
的により化合物〔1〕の割合を当量数以上にする
こともできる。
該ウレタン化反応は発熱による急激な温度上昇
をさけるため、部分ウレタン化物に化合物〔1〕
を分割添加または滴下することによつて、温度を
調節しながら進める。
一般に従来のカチオン重合性モノマーは重合時
に例えばエチレンオキシド23%、プロピレンオキ
シド17%、スチレンオキシド9%、エピクロルヒ
ドリン12%等と非常に大きな体積収縮を伴う。重
合時の体績収縮が大きいと、例えば成形材料とし
て使用した場合に寸法精度ができないとか、注型
材料として利用した場合にはうめこみ物に収縮に
よるひずみがかかるとか、型との接着力の低下や
隙間が生じるなどの問題がある。また、塗料とし
て使用した場合、内部ひずみによる塗板との密着
性の低下やそりがおこるとか、接着剤として使用
した場合、内部ひずみによる接着力の低下やそ
り、変形などの使用上の問題を生ずる。
本発明の化合物〔1〕、化合物〔1〕から誘導
される化合物〔2〕の重合体、および化合物
〔1〕から製造される化合物〔3〕等は、いずれ
もスピロオルソエステル基がカチオン開環重合を
し、しかも重合時の体積収縮が非常に小さいとい
う特長をもつている。従つて本発明の化合物
〔1〕及び化合物〔1〕より誘導される各種の化
合物は、成形材料、複合材料、接着剤、注型材
料、塗料などに利用出来る極めて有用な化合物で
ある。
つぎに本発明の実施例、参考例を掲げ本発明を
具体的に説明する。
実施例 1
撹拌機、コンデンサー、温度計及び滴下ロート
を備えた4つ口2フラスコに、γ−ブチロラク
トン215.2g(2.5モル)及び塩化メチレン1000ml
を仕込み、滴下ロートにグリシドール74.1g(1
モル)及び塩化メチレン150mlを仕込んだ。釜液
を氷水で10℃に冷却後、BF3、OEt2を1.5ml添加
した。釜液を撹拌しながら約1.5時間かけて、グ
リシドール溶液を滴下した。滴下後さらに5時間
撹拌した。なお反応の間釜液は水で冷却し、約10
℃に保持した。次にトリエチルアミン3mlを加
え、触媒を失活させた。次に反応液を氷水で冷却
し、撹拌しながら10%NaOH水溶液1000mlを
徐々に加え、添加完了後30分間撹拌した後、アル
カリ水溶液層と有機層を分離した。この有機層を
500mlの水で洗浄した。次に硫酸マグネシウムで
脱水した後、、脱溶剤をした。その残渣にトリ
(n−オクチル)アミン0.2gを添加した後、減圧
蒸留し、沸点83℃/0.7mmHgにおいて、2−ヒド
ロキシメチル−1,4,6−トリオキサスピロ
〔4,4〕ノナン11.9g(収率7.4%)を得た。
その物性値は下記の通りである。
Γ沸点;83℃/0.7mmHg
Γ比重;1.196(25℃)
ΓIR(赤外吸収スペクトル);3450cm-1(O−H)、
1334cm-1、1247cm-1、1132cm-1、1042cm-1、
954cm-1
ΓNMR(核磁気共鳴スペクトル)(CDCl3中);
δ(ppm);3.4〜4.6(7H、3CH2−O、CH−
O)、1.8〜2.3(4H、C−CH2−CH2)
実施例 2
実施例1と同様なフラスコにε−カプロラクト
ン285g(2.5モル)、塩化メチレン1000ml及びト
リエチルアミン0.7mlを仕込み、滴下ロートにグ
リシドール74.1g(1モル)及び塩化メチレン
150mlを仕込んだ。釜液を氷水10℃に冷却後、
BF3OEt2を1.5ml添加した。釜液を撹拌しながら
約2時間かけてグリシドール溶液を滴下した。さ
らに5時間撹拌した。なお反応の間釜液は水で冷
却し、約10℃に保持した。次にトリエチルアミン
3mlを加え触媒を失活させた。次に反応液を氷水
で冷却しながら10%NaOH水溶液1000mlを徐々
に加え、30分撹拌した後、アルカリ水溶液と有機
層を分離した。この有機層を500mlの水で洗浄し
遠心分離により分離する操作を2回行なつた後、
硫酸マグネシウムで脱水した。
次にトリ(n−オクチル)アミン0.2gを添加
後脱溶剤を行ない、さらに減圧蒸留し沸点95℃/
0.7mmHgにおいて、2−ヒドロキシメチル−1,
4,6−トリオキサスピロ〔4,6〕ウンデカン
13.3g(収率7.1%)を得た。
その物性値は下記の通りである。
Γ沸点;95℃/0.7mmHg
Γ比重;1.161/25℃
ΓIR;3450cm-1(O−H)、1240cm-1、1133cm-1、
1072cm- 1、1037cm-1、960cm-1
ΓNMR(CDCl3中);
δ(ppm);3.4〜4.5(7H、3CH2−O、CH−O)
1.9〜2.1(2H、In the group represented by the formula: Y represents a partially urethanized polyisocyanate residue, f represents an integer corresponding to the valence of the polyisocyanate compound, and m represents an integer of 4 to 6. ) This compound [4] has two or more spiro-orthoester groups, and since it is a polyfunctional polymerizable compound, it increases the degree of cross-linking when curing the final product composition. useful for. In the urethanization reaction, in order to avoid a rapid temperature rise due to heat generation, a polyhydroxy compound is added to the polyisocyanate compound in portions as necessary.
Alternatively, the temperature may be controlled by dripping. Next, in the second step, compound [1] is reacted and bonded to the terminal and/or side chain isocyanate groups of the partially urethanized product obtained in the first step. Note that some partially urethanized products of this type are commercially available, and such commercial products can also be used in the present invention. The ratio of adding compound [1] to this partially urethanized product is generally such that the number of equivalents of residual isocyanate groups in the partially urethanized product is equal to the number of equivalents of hydroxyl groups in compound [1]. Depending on the purpose, the proportion of compound [1] can be increased to an equivalent number or more. In the urethanization reaction, in order to avoid rapid temperature rise due to heat generation, compound [1] is added to the partially urethanized product.
Proceed while controlling the temperature by adding in portions or dropwise. In general, conventional cationic polymerizable monomers undergo very large volume shrinkage during polymerization, such as 23% ethylene oxide, 17% propylene oxide, 9% styrene oxide, 12% epichlorohydrin, etc. If the actual shrinkage during polymerization is large, for example, when used as a molding material, dimensional accuracy may not be achieved, when used as a casting material, the injected material may be subject to distortion due to shrinkage, or the adhesive strength with the mold may be affected. There are problems such as deterioration and gaps. In addition, when used as a paint, internal strain may cause a decrease in adhesion to the painted plate and warping, and when used as an adhesive, internal strain may cause problems such as a decrease in adhesive strength, warpage, and deformation. . In the compound [1] of the present invention, the polymer of compound [2] derived from compound [1], and the compound [3] produced from compound [1], the spiro-orthoester group is cationically ring-opened. It polymerizes, and its volumetric shrinkage during polymerization is extremely small. Therefore, the compound [1] of the present invention and various compounds derived from the compound [1] are extremely useful compounds that can be used in molding materials, composite materials, adhesives, casting materials, paints, etc. Next, the present invention will be specifically explained with reference to Examples and Reference Examples. Example 1 215.2 g (2.5 mol) of γ-butyrolactone and 1000 ml of methylene chloride were placed in a 4-necked 2 flask equipped with a stirrer, condenser, thermometer, and dropping funnel.
and add 74.1 g of glycidol (1 g) to the dropping funnel.
mol) and 150 ml of methylene chloride were charged. After cooling the pot solution to 10° C. with ice water, 1.5 ml of BF 3 and OEt 2 were added. The glycidol solution was added dropwise to the pot solution over about 1.5 hours while stirring. After the addition, the mixture was further stirred for 5 hours. During the reaction, the pot liquid was cooled with water and heated for about 10 minutes.
It was kept at ℃. Next, 3 ml of triethylamine was added to deactivate the catalyst. Next, the reaction solution was cooled with ice water, and while stirring, 1000 ml of a 10% NaOH aqueous solution was gradually added. After the addition was completed, the mixture was stirred for 30 minutes, and then the alkali aqueous solution layer and the organic layer were separated. This organic layer
Washed with 500ml of water. Next, after dehydrating with magnesium sulfate, the solvent was removed. After adding 0.2 g of tri(n-octyl)amine to the residue, it was distilled under reduced pressure, and at a boiling point of 83°C/0.7 mmHg, 2-hydroxymethyl-1,4,6-trioxaspiro[4,4]nonane 11.9 g (yield 7.4%). Its physical property values are as follows. Γ boiling point: 83℃/0.7mmHg Γ specific gravity: 1.196 (25℃) ΓIR (infrared absorption spectrum): 3450cm -1 (O-H),
1334cm -1 , 1247cm -1 , 1132cm -1 , 1042cm -1 ,
954cm -1 ΓNMR (Nuclear Magnetic Resonance Spectrum) (in CDCl 3 ); δ (ppm); 3.4-4.6 (7H, 3CH2 -O, CH-
O), 1.8 to 2.3 (4H, C-CH 2 -CH 2 ) Example 2 285 g (2.5 mol) of ε-caprolactone, 1000 ml of methylene chloride, and 0.7 ml of triethylamine were charged into the same flask as in Example 1, and the mixture was poured into a dropping funnel. Glycidol 74.1g (1 mol) and methylene chloride
I prepared 150ml. After cooling the pot liquid to ice water at 10℃,
1.5 ml of BF 3 OEt 2 was added. The glycidol solution was added dropwise to the pot over about 2 hours while stirring the solution. The mixture was further stirred for 5 hours. During the reaction, the pot liquid was cooled with water and maintained at about 10°C. Next, 3 ml of triethylamine was added to deactivate the catalyst. Next, 1000 ml of a 10% NaOH aqueous solution was gradually added to the reaction solution while cooling it with ice water, and after stirring for 30 minutes, the alkali aqueous solution and the organic layer were separated. After washing this organic layer with 500 ml of water and separating it by centrifugation twice,
Dehydrated with magnesium sulfate. Next, 0.2 g of tri(n-octyl)amine was added, the solvent was removed, and the boiling point was 95℃/
At 0.7 mmHg, 2-hydroxymethyl-1,
4,6-trioxaspiro[4,6]undecane
13.3g (yield 7.1%) was obtained. Its physical property values are as follows. Γ Boiling point: 95℃/0.7mmHg Γ Specific gravity: 1.161/25℃ ΓIR: 3450cm -1 (O-H), 1240cm -1 , 1133cm -1 ,
1072 cm -1 , 1037 cm -1 , 960 cm -1 Γ NMR (in CDCl 3 ); δ (ppm); 3.4-4.5 (7H, 3CH2 -O, CH-O)
1.9~2.1 (2H,
【式】)1.4〜1.9
(6H、CH2−CH2−CH2)
Γ質量スペクトル(GC−MS);
親ピーク;m/e=188
参考例 1
実施例1で得た化合物にカチオン重合触媒とし
てBF3OEt2を3モル%添加て80℃において3時
間加熱し透明のやわらかい重合物を得た。
この重合物はIR分析より1730cm-1のエステル
の吸収が認められた。重合による体積収縮率ほ
ぼゞ0であつた。
参考例 2
実施例2で得られた化合物にカチオン重合触媒
としてBF3OEt2を3モル%添加して80℃におい
て3時間加熱し透明のやわらかい重合物を得た。
この重合物はIR分析により1730cm-1のエステ
ルの吸収が認められた。また重合による体積収縮
率はほぼ0であつた。[Formula]) 1.4-1.9 (6H, CH 2 -CH 2 -CH 2 ) Γ mass spectrum (GC-MS); Parent peak; m/e = 188 Reference example 1 A cationic polymerization catalyst was added to the compound obtained in Example 1. 3 mol% of BF 3 OEt 2 was added thereto and heated at 80° C. for 3 hours to obtain a transparent soft polymer. IR analysis revealed that this polymer had ester absorption at 1730 cm -1 . The volume shrinkage rate due to polymerization was approximately 0. Reference Example 2 3 mol% of BF 3 OEt 2 was added as a cationic polymerization catalyst to the compound obtained in Example 2, and the mixture was heated at 80° C. for 3 hours to obtain a transparent soft polymer. An IR analysis of this polymer revealed that it had an ester absorption of 1730 cm -1 . Further, the volume shrinkage rate due to polymerization was approximately 0.
第1図は実施例1で得た2−ヒドロキシメチル
−1,4,6−トリオキサスピロ〔4,4〕ノナ
ンのIR図であり、第2図は同化合物のNMR図で
あり、第3図は実施例2で得た2−ヒドロキシメ
チル−1,4,6−トリオキサスピロ〔4,6〕
ウンデカンのIR図であり、第4図は同化合物の
NMR図である。
Figure 1 is an IR diagram of 2-hydroxymethyl-1,4,6-trioxaspiro[4,4]nonane obtained in Example 1, Figure 2 is an NMR diagram of the same compound, and Figure 3 is an NMR diagram of the same compound. The figure shows 2-hydroxymethyl-1,4,6-trioxaspiro[4,6] obtained in Example 2.
This is an IR diagram of undecane, and Figure 4 shows the IR diagram of the same compound.
It is an NMR diagram.
Claims (1)
メチル−1,4,6−トリオキサスピロ〔4,
m〕アルカン。 (ここでmは4〜6の整数を表わす。)[Scope of Claims] 1 2-hydroxymethyl-1,4,6-trioxaspiro[4,
m] Alkane. (Here, m represents an integer from 4 to 6.)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57046417A JPS58164592A (en) | 1982-03-25 | 1982-03-25 | 2-hydroxymethyl-1, 4, 6-trioxaspiro(4, m)alkane |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57046417A JPS58164592A (en) | 1982-03-25 | 1982-03-25 | 2-hydroxymethyl-1, 4, 6-trioxaspiro(4, m)alkane |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58164592A JPS58164592A (en) | 1983-09-29 |
| JPH0244313B2 true JPH0244313B2 (en) | 1990-10-03 |
Family
ID=12746568
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57046417A Granted JPS58164592A (en) | 1982-03-25 | 1982-03-25 | 2-hydroxymethyl-1, 4, 6-trioxaspiro(4, m)alkane |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58164592A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61243823A (en) * | 1985-04-23 | 1986-10-30 | Dainippon Ink & Chem Inc | Highly branched polyester ether copolymer and curable composition containing same |
| US5231197A (en) * | 1992-06-01 | 1993-07-27 | General Electric Company | Method for producing ethylenically unsaturated graftable orthoesters |
-
1982
- 1982-03-25 JP JP57046417A patent/JPS58164592A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58164592A (en) | 1983-09-29 |
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