JPH0514690B2 - - Google Patents
Info
- Publication number
- JPH0514690B2 JPH0514690B2 JP12589784A JP12589784A JPH0514690B2 JP H0514690 B2 JPH0514690 B2 JP H0514690B2 JP 12589784 A JP12589784 A JP 12589784A JP 12589784 A JP12589784 A JP 12589784A JP H0514690 B2 JPH0514690 B2 JP H0514690B2
- Authority
- JP
- Japan
- Prior art keywords
- group
- aralkyl
- monosubstituted
- general formula
- polyhydric phenols
- 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
Links
- 125000003710 aryl alkyl group Chemical group 0.000 claims description 22
- 150000002989 phenols Chemical class 0.000 claims description 19
- 150000001875 compounds Chemical class 0.000 claims description 17
- GHMLBKRAJCXXBS-UHFFFAOYSA-N resorcinol Chemical compound OC1=CC=CC(O)=C1 GHMLBKRAJCXXBS-UHFFFAOYSA-N 0.000 claims description 17
- 125000003118 aryl group Chemical group 0.000 claims description 14
- QIGBRXMKCJKVMJ-UHFFFAOYSA-N Hydroquinone Chemical compound OC1=CC=C(O)C=C1 QIGBRXMKCJKVMJ-UHFFFAOYSA-N 0.000 claims description 10
- YCIMNLLNPGFGHC-UHFFFAOYSA-N catechol Chemical compound OC1=CC=CC=C1O YCIMNLLNPGFGHC-UHFFFAOYSA-N 0.000 claims description 10
- 239000003377 acid catalyst Substances 0.000 claims description 6
- 125000000217 alkyl group Chemical group 0.000 claims description 6
- 125000004432 carbon atom Chemical group C* 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 239000007864 aqueous solution Substances 0.000 claims description 5
- 125000005843 halogen group Chemical group 0.000 claims description 4
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 3
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims 1
- 150000008442 polyphenolic compounds Chemical class 0.000 claims 1
- 235000013824 polyphenols Nutrition 0.000 claims 1
- 238000006243 chemical reaction Methods 0.000 description 23
- 230000000052 comparative effect Effects 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- 239000000243 solution Substances 0.000 description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 8
- 229960001755 resorcinol Drugs 0.000 description 8
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- XYLMUPLGERFSHI-UHFFFAOYSA-N alpha-Methylstyrene Chemical compound CC(=C)C1=CC=CC=C1 XYLMUPLGERFSHI-UHFFFAOYSA-N 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 238000005406 washing Methods 0.000 description 5
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 239000013078 crystal Substances 0.000 description 4
- 239000000539 dimer Substances 0.000 description 3
- 238000006471 dimerization reaction Methods 0.000 description 3
- 238000004817 gas chromatography Methods 0.000 description 3
- ICLPNZMYHDVKKI-UHFFFAOYSA-N 1,1,3-trimethyl-3-phenyl-2h-indene Chemical compound C12=CC=CC=C2C(C)(C)CC1(C)C1=CC=CC=C1 ICLPNZMYHDVKKI-UHFFFAOYSA-N 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000005755 formation reaction Methods 0.000 description 2
- OIPPWFOQEKKFEE-UHFFFAOYSA-N orcinol Chemical compound CC1=CC(O)=CC(O)=C1 OIPPWFOQEKKFEE-UHFFFAOYSA-N 0.000 description 2
- MMSLOZQEMPDGPI-UHFFFAOYSA-N p-Mentha-1,3,5,8-tetraene Chemical compound CC(=C)C1=CC=C(C)C=C1 MMSLOZQEMPDGPI-UHFFFAOYSA-N 0.000 description 2
- WQGWDDDVZFFDIG-UHFFFAOYSA-N pyrogallol Chemical compound OC1=CC=CC(O)=C1O WQGWDDDVZFFDIG-UHFFFAOYSA-N 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- CNHDIAIOKMXOLK-UHFFFAOYSA-N toluquinol Chemical compound CC1=CC(O)=CC=C1O CNHDIAIOKMXOLK-UHFFFAOYSA-N 0.000 description 2
- 239000013638 trimer Substances 0.000 description 2
- FKIJMTKJEMUCQG-UHFFFAOYSA-N 1,2-dimethyl-3-prop-1-en-2-ylbenzene Chemical compound CC(=C)C1=CC=CC(C)=C1C FKIJMTKJEMUCQG-UHFFFAOYSA-N 0.000 description 1
- KTZVZZJJVJQZHV-UHFFFAOYSA-N 1-chloro-4-ethenylbenzene Chemical compound ClC1=CC=C(C=C)C=C1 KTZVZZJJVJQZHV-UHFFFAOYSA-N 0.000 description 1
- WQDGTJOEMPEHHL-UHFFFAOYSA-N 1-chloro-4-prop-1-en-2-ylbenzene Chemical compound CC(=C)C1=CC=C(Cl)C=C1 WQDGTJOEMPEHHL-UHFFFAOYSA-N 0.000 description 1
- VNAFWALXWOAPCK-UHFFFAOYSA-N 1-phenyl-2,3-dihydro-1h-indene Chemical compound C1CC2=CC=CC=C2C1C1=CC=CC=C1 VNAFWALXWOAPCK-UHFFFAOYSA-N 0.000 description 1
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 description 1
- ZTMADXFOCUXMJE-UHFFFAOYSA-N 2-methylbenzene-1,3-diol Chemical compound CC1=C(O)C=CC=C1O ZTMADXFOCUXMJE-UHFFFAOYSA-N 0.000 description 1
- BTOVVHWKPVSLBI-UHFFFAOYSA-N 2-methylprop-1-enylbenzene Chemical compound CC(C)=CC1=CC=CC=C1 BTOVVHWKPVSLBI-UHFFFAOYSA-N 0.000 description 1
- YNGIFMKMDRDNBQ-UHFFFAOYSA-N 3-ethenylphenol Chemical compound OC1=CC=CC(C=C)=C1 YNGIFMKMDRDNBQ-UHFFFAOYSA-N 0.000 description 1
- PGSWEKYNAOWQDF-UHFFFAOYSA-N 3-methylcatechol Chemical compound CC1=CC=CC(O)=C1O PGSWEKYNAOWQDF-UHFFFAOYSA-N 0.000 description 1
- REWLXMVGEZMKSG-UHFFFAOYSA-N 3-prop-1-en-2-ylphenol Chemical compound CC(=C)C1=CC=CC(O)=C1 REWLXMVGEZMKSG-UHFFFAOYSA-N 0.000 description 1
- JLBJTVDPSNHSKJ-UHFFFAOYSA-N 4-Methylstyrene Chemical compound CC1=CC=C(C=C)C=C1 JLBJTVDPSNHSKJ-UHFFFAOYSA-N 0.000 description 1
- JQVAPEJNIZULEK-UHFFFAOYSA-N 4-chlorobenzene-1,3-diol Chemical compound OC1=CC=C(Cl)C(O)=C1 JQVAPEJNIZULEK-UHFFFAOYSA-N 0.000 description 1
- CGVSVWWXNAFRRH-UHFFFAOYSA-N 4-ethenylbenzene-1,3-diol Chemical compound OC1=CC=C(C=C)C(O)=C1 CGVSVWWXNAFRRH-UHFFFAOYSA-N 0.000 description 1
- FUGYGGDSWSUORM-UHFFFAOYSA-N 4-hydroxystyrene Chemical compound OC1=CC=C(C=C)C=C1 FUGYGGDSWSUORM-UHFFFAOYSA-N 0.000 description 1
- FNYDIAAMUCQQDE-UHFFFAOYSA-N 4-methylbenzene-1,3-diol Chemical compound CC1=CC=C(O)C=C1O FNYDIAAMUCQQDE-UHFFFAOYSA-N 0.000 description 1
- ZBCATMYQYDCTIZ-UHFFFAOYSA-N 4-methylcatechol Chemical compound CC1=CC=C(O)C(O)=C1 ZBCATMYQYDCTIZ-UHFFFAOYSA-N 0.000 description 1
- XESZUVZBAMCAEJ-UHFFFAOYSA-N 4-tert-butylcatechol Chemical compound CC(C)(C)C1=CC=C(O)C(O)=C1 XESZUVZBAMCAEJ-UHFFFAOYSA-N 0.000 description 1
- BGNXCDMCOKJUMV-UHFFFAOYSA-N Tert-Butylhydroquinone Chemical compound CC(C)(C)C1=CC(O)=CC=C1O BGNXCDMCOKJUMV-UHFFFAOYSA-N 0.000 description 1
- QROGIFZRVHSFLM-QHHAFSJGSA-N [(e)-prop-1-enyl]benzene Chemical compound C\C=C\C1=CC=CC=C1 QROGIFZRVHSFLM-QHHAFSJGSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- AJPXTSMULZANCB-UHFFFAOYSA-N chlorohydroquinone Chemical compound OC1=CC=C(O)C(Cl)=C1 AJPXTSMULZANCB-UHFFFAOYSA-N 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- -1 dihydroxyisopropenylstyrene Chemical group 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 229920001568 phenolic resin Polymers 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 229940079877 pyrogallol Drugs 0.000 description 1
- 238000011002 quantification Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 150000003440 styrenes Chemical class 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000004250 tert-Butylhydroquinone Substances 0.000 description 1
- 235000019281 tert-butylhydroquinone Nutrition 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
本発明はアラルキルモノ置換多価フエノール類
の製造方法に関する。更に詳しくは、アラルキル
モノ置換多価フエノール類を高収率で製造する方
法に関する。
アラルキルモノ置換多価フエノール類は、エポ
キシン樹脂原料、フエノール樹脂の改質剤、ポリ
エステル原料、安定剤、顕色剤として有用な化合
物である。
従来から、これらアラルキルモノ置換多価フエ
ノール類の合成については、いくつかその検討が
なされている。例えば、J.Org.Chem.,17 243
〜248(1951)には、フエノール類とスチレンのア
ラルキル化反応条件についての研究結果が報告さ
れている。触媒としては硫酸触媒が有用であり、
収率を高めるために、スチレンをトルエンの如
き、溶媒で希釈して用いているが、アラルキルジ
置換体の生成が多く、アラルキルモノ置換体を収
率は決して高くない。又、スチレン類同志の2量
化がかなり進行してしまうことが追試の結果、明
らかとなつた。
又、米国特許2247404号明細書には、濃塩酸を
触媒とし、多価フエノール類の融点近くで反応さ
せる方法が記載されているが、この方法を追試し
た所、アラルキルモノ置換体の収率は低く、芳香
族不飽和化合物の2量化反応が主に起こつた。例
えばα−メチルスチレンを用いると、1,3,3
−トリメチル−1−フエニルインダンが主に生成
することが分かり、目的物であるアラルキルモノ
置換体は極少量しか得られなかつた。又、特開昭
58−140085号明細書には、リン酸触媒を用いて、
100〜170℃の反応温度で多価フエノール類と芳香
不飽和化合物を反応させる方法が示されている
が、この方法に於いても追試の結果、芳香族不飽
和化合物の2量化が主に起つてしまい、目的とす
る、アラルキルモノ置換体が収率良く、得られな
いことが明らかになつた。
本発明者らは、上述の欠点を改良し、高収率、
高純度でアラルキルモノ置換多価フエノールを製
造する方法について鋭意検討した結果、多価フエ
ノール類の水溶液と芳香族不飽和化合物を酸触媒
の存在に接触させると、芳香族不飽和化合物の2
量化は、ほとんど起こらず、目的とするアラルキ
ルモノ置換体が極めて収率良く得られることを見
い出し、本発明に致つた。
すなわち、本発明は、一般式(A)
(但し、R1:−H基、−OH基、ハロゲン基、炭
素数1〜4のアルキル基)
で表わされる多価フエノール類と、一般式(B)
(但し、R2:−H基、炭素数1〜4のアルキル
基
R3,R4:−H基、−OH基、ハロゲン基、炭素
数1〜4のアルキル基)
で表わされる芳香族不飽和化合物の少なくとも一
種と反応させて、下記一般式(C)
(但し、R1,R2,R3,R4は前記定義と同じであ
る。)
で表わされるアラルキルモノ置換多価フエノール
類を製造する際に酸触媒を用い、かつ、一般式(A)
で表わされる多価フエノール類の水溶液と芳香族
不飽和化合物を接触させることを特徴とするアラ
ルキルモノ置換多価フエノール類の製造方法であ
る。
本発明方法によると、アラルキルジ置換体、及
び芳香族不飽和化合物を2量体は、ほとんど生成
せず、アラルキルモノ置換体を高収率、高純度で
製造できる。
本発明に於ける多価フエノール類としては、カ
テコール、4−メチルカテコール、6−メチルカ
テコール、4−tert−プチルカテコール、レゾル
シン、4−メチル−レゾルシン、2−メチル−レ
ゾルシン、5−メチル−レゾルシン、4−クロル
レゾルシン、2−メチル−ハイドロキノン、2−
tert−ブチルハイドロキノン、2−クロル−ハイ
ドロキノン、ハイドロキノン、ピロガロール等が
例示されるが、特に好ましくは、カテコール、レ
ゾルシン、ハイドロキノンが選ばれる。一方、一
般式(B)で表わされる、芳香族不飽和化合物として
は、その具体例として、ステレン、α−メチルス
チレン、β−メチルスチレン、ジメチルスチレ
ン、ジメチル−α−メチルスチレン、p−メチル
スチレン、p−メチル−α−メチルスチレン、p
−クロルスチレン、p−クロル−α−メチルスチ
レン、p−ヒドロキシ−スチレン、m−ヒドロキ
シスチレン、m−ヒドロキシイソプロペニルベン
ゼン、2,4−ジヒドロキシスチレン、2,4−
ジヒドロキシイソプロペニルスチレンが例示でき
る。
かかる、多価フエノール類と芳香族不飽和化合
物の使用量は、多価フエノール類に対し、芳香族
不飽和化合物0.5〜1モル量が好ましい。
本発明において使用する酸触媒は一般に使用さ
れているものでよく、例えば硫酸、塩酸、リン酸
等が例示できる。
酸量は、水量100部に対し、2〜30重量部が好
ましく、2重量部未満だと、反応速度が低く、
又、30重量部を越えると、アラルキルジ置換体、
及び芳香族不飽和化合物の2量体が生成し好まし
くない。
又は、本発明方法の特徴は、多価フエノール類
を水に溶解した水溶液の形で使用することである
が、その使用量は使用する多価フエノール類によ
つて異なるが、一般的には、水量100重量部に対
して、20〜200重量部が好ましい。
反応濃度は、通常、40〜90℃の範囲で行なうの
が好ましいが、特に好ましくは、60〜80℃が望ま
れる。アラルキル化反応は、多価フエノール類、
酸触媒混合水溶液に、一般式(B)で表わされる芳香
族不飽和化合物を徐々い添加するのが好ましい。
添加時間は通常1〜8時間が好ましいが、特に好
ましくは1〜4時間が望まれる。該、芳香族不飽
和化合物を添加した后、さらに、2〜4時間熱成
反応を行なう方が好ましい。反応終了后、反応液
は、油層と水層に分液され、水層は、次の反応に
繰り返し使用される。一方、油層は、温水洗浄
后、冷却すると、固化するが、温水洗浄后、冷却
することなしに、有機溶媒に溶解し再結晶するこ
とが出来る。この様にして、得た、アラルキルモ
ノ置換多価フエノール類は高純度を有しており、
前記、各種の用途に使用できるものである。
以下に、本発明を実施例にて詳しく説明する。
実施例 1
撹拌機、温度計、及びコンデンサーを装着した
ガラス製反応器に、レゾルシン100重量部、濃硫
酸5重量部水100重量部を仕込み、80℃に加熱し、
α−メチルスチレン100重量部を、4時間で滴下
し、滴下後、同温度で3時間反応させた。反応終
了后、反応液は静置して、2層に分け、下層の油
層を分離し、温水洗浄後、トルエン溶媒にて再結
晶させた。
得られた生成物
の収量は184重量部であり、(収率95.3%)又、こ
の純度は99.9%であつた。
比較例 1
実施例1と同様な反応器を用いて、レゾルシン
100重量部、濃硫酸5重量部を仕込み、120℃に加
熱し、α−メチルスチレン100重量部を4時間か
けて滴下し、滴下後、同温度で8時間反応させ
た。反応終了後、反応液を温水洗浄して得られた
油層を、トルエン溶媒にて再結晶した所、得られ
た結晶の収量は40重量部であり、純度も92%と低
いものであつた。反応液をガスクロマトグラフイ
ーで分析した所、α−メチルスチレンの2量体で
ある。1,3,3−トリメチル−1−フエニルイ
ンダンが多量生成していた。又、GPC分析の結
果8量体成分がこれまた多量に認められた。
実施例 2
実施例1のレゾルシンに代えてカテコール用
い、実施例1と同様に反応を行ない、得られた油
層をトルエン溶媒にて再結晶した所、得られた結
晶
の収量は、178g、(収率92.2%)であり、又、こ
の純度は、99.9%であつた。
比較例 2
比較例1と同様に、レゾルシンに代えて、カテ
コールを用い、比較例1と同様の仕込み量で120
〜150℃に加熱し、α−メチルステレンを、これ
また比較例1と同様に添加した。反応終了后、反
応液を温水洗浄して得られた油層をトルエン溶媒
にて再結晶した所、得られた結晶の収量は、25重
量部であり、純度も90%と低いものであつた。反
応液をガスクロマトグラフイーで分析した所、比
較例1と同様に、1,3,3−トリメチル−1−
フエニルインダンが多量に認められると共に、不
明成分もかなり認められた。又、GPC分析の結
果、アラルキルジ置換体に基づく3量体の生成も
多く認められた。
実施例 3
実施例1のレゾルシンに代えて、ハイドロキノ
ンを用い、実施例1と同様な反応条件で反応を行
ない、得られた油層をトルエン溶媒にて再結晶し
た所、得られた結晶
The present invention relates to a method for producing aralkyl monosubstituted polyhydric phenols. More specifically, the present invention relates to a method for producing aralkyl monosubstituted polyhydric phenols in high yield. Aralkyl monosubstituted polyhydric phenols are compounds useful as epoxin resin raw materials, phenolic resin modifiers, polyester raw materials, stabilizers, and color developers. Conventionally, several studies have been made regarding the synthesis of these aralkyl monosubstituted polyhydric phenols. For example, J.Org.Chem., 17 243
248 (1951), the results of research on the aralkylation reaction conditions of phenols and styrene are reported. A sulfuric acid catalyst is useful as a catalyst;
In order to increase the yield, styrene is used diluted with a solvent such as toluene, but aralkyl di-substituted products are often produced, and the yield of aralkyl mono-substituted products is not high. Additionally, additional tests revealed that dimerization of styrene compounds progressed considerably. In addition, US Patent No. 2,247,404 describes a method of reacting polyhydric phenols near their melting point using concentrated hydrochloric acid as a catalyst, but when this method was repeated, the yield of aralkyl monosubstituted product was The dimerization reaction of aromatic unsaturated compounds mainly occurred. For example, when α-methylstyrene is used, 1,3,3
It was found that -trimethyl-1-phenylindane was mainly produced, and only a very small amount of the target aralkyl monosubstituted product was obtained. Also, Tokukai Akira
In the specification of No. 58-140085, using a phosphoric acid catalyst,
A method of reacting polyhydric phenols with aromatic unsaturated compounds at a reaction temperature of 100 to 170°C has been shown, but additional tests have shown that even with this method, dimerization of aromatic unsaturated compounds mainly occurs. It became clear that the desired aralkyl monosubstituted product could not be obtained in good yield. The present inventors have improved the above-mentioned drawbacks and achieved high yield,
As a result of intensive studies on a method for producing highly pure aralkyl monosubstituted polyhydric phenols, we found that when an aqueous solution of polyhydric phenols and an aromatic unsaturated compound are brought into contact with the presence of an acid catalyst, 2 of the aromatic unsaturated compounds
It has been found that quantification hardly occurs and the desired aralkyl monosubstituted product can be obtained in extremely good yield, leading to the present invention. That is, the present invention provides general formula (A) (However, R 1 : -H group, -OH group, halogen group, alkyl group having 1 to 4 carbon atoms) and the general formula (B) (However, R 2 : -H group, alkyl group having 1 to 4 carbon atoms R 3 , R 4 : -H group, -OH group, halogen group, alkyl group having 1 to 4 carbon atoms) By reacting with at least one saturated compound, the following general formula (C) (However, R 1 , R 2 , R 3 , and R 4 are the same as defined above.) When producing an aralkyl monosubstituted polyhydric phenol represented by the formula (A), an acid catalyst is used, and the general formula (A)
This is a method for producing aralkyl monosubstituted polyhydric phenols, which is characterized by contacting an aqueous solution of polyhydric phenols represented by the formula with an aromatic unsaturated compound. According to the method of the present invention, aralkyl disubstituted products and dimers of aromatic unsaturated compounds are hardly produced, and aralkyl monosubstituted products can be produced in high yield and with high purity. Polyhydric phenols in the present invention include catechol, 4-methylcatechol, 6-methylcatechol, 4-tert-butylcatechol, resorcin, 4-methyl-resorcin, 2-methyl-resorcin, 5-methyl-resorcin. , 4-chlorresorcinol, 2-methyl-hydroquinone, 2-
Examples include tert-butylhydroquinone, 2-chloro-hydroquinone, hydroquinone, pyrogallol, and particularly preferably catechol, resorcinol, and hydroquinone. On the other hand, specific examples of aromatic unsaturated compounds represented by the general formula (B) include sterene, α-methylstyrene, β-methylstyrene, dimethylstyrene, dimethyl-α-methylstyrene, and p-methylstyrene. , p-methyl-α-methylstyrene, p
-Chlorstyrene, p-chloro-α-methylstyrene, p-hydroxy-styrene, m-hydroxystyrene, m-hydroxyisopropenylbenzene, 2,4-dihydroxystyrene, 2,4-
An example is dihydroxyisopropenylstyrene. The amount of the polyhydric phenols and aromatic unsaturated compound to be used is preferably 0.5 to 1 mol of the aromatic unsaturated compound relative to the polyhydric phenol. The acid catalyst used in the present invention may be any commonly used acid catalyst, such as sulfuric acid, hydrochloric acid, phosphoric acid, etc. The amount of acid is preferably 2 to 30 parts by weight per 100 parts of water, and if it is less than 2 parts by weight, the reaction rate is low;
In addition, if it exceeds 30 parts by weight, aralkyl di-substituted product,
and dimers of aromatic unsaturated compounds are produced, which is undesirable. Alternatively, a feature of the method of the present invention is that polyhydric phenols are used in the form of an aqueous solution dissolved in water, and the amount used varies depending on the polyhydric phenols used, but in general, It is preferably 20 to 200 parts by weight per 100 parts by weight of water. The reaction concentration is usually preferably carried out in a range of 40 to 90°C, particularly preferably 60 to 80°C. In the aralkylation reaction, polyhydric phenols,
It is preferable to gradually add the aromatic unsaturated compound represented by the general formula (B) to the acid catalyst mixed aqueous solution.
The addition time is usually preferably 1 to 8 hours, particularly preferably 1 to 4 hours. After adding the aromatic unsaturated compound, it is preferable to carry out a thermal formation reaction for 2 to 4 hours. After the reaction is completed, the reaction solution is separated into an oil layer and an aqueous layer, and the aqueous layer is repeatedly used for the next reaction. On the other hand, an oil layer solidifies when cooled after washing with hot water, but can be dissolved in an organic solvent and recrystallized without cooling after washing with hot water. The aralkyl monosubstituted polyhydric phenols obtained in this way have high purity,
As mentioned above, it can be used for various purposes. The present invention will be explained in detail below using Examples. Example 1 A glass reactor equipped with a stirrer, a thermometer, and a condenser was charged with 100 parts by weight of resorcinol, 5 parts by weight of concentrated sulfuric acid, and 100 parts by weight of water, and heated to 80°C.
100 parts by weight of α-methylstyrene was added dropwise over 4 hours, and after the addition, the reaction was allowed to proceed at the same temperature for 3 hours. After the reaction was completed, the reaction solution was allowed to stand still, divided into two layers, and the lower oil layer was separated, washed with warm water, and then recrystallized from a toluene solvent. the product obtained The yield was 184 parts by weight (yield 95.3%), and the purity was 99.9%. Comparative Example 1 Using the same reactor as in Example 1, resorcinol
100 parts by weight of concentrated sulfuric acid and 5 parts by weight of concentrated sulfuric acid were charged, heated to 120°C, and 100 parts by weight of α-methylstyrene was added dropwise over 4 hours. After the dropwise addition, the mixture was reacted at the same temperature for 8 hours. After the reaction was completed, the oil layer obtained by washing the reaction solution with warm water was recrystallized from a toluene solvent, and the yield of the obtained crystals was 40 parts by weight, and the purity was as low as 92%. Analysis of the reaction solution by gas chromatography revealed that it was a dimer of α-methylstyrene. A large amount of 1,3,3-trimethyl-1-phenylindane was produced. Furthermore, as a result of GPC analysis, a large amount of octamer component was also observed. Example 2 The reaction was carried out in the same manner as in Example 1, using catechol instead of resorcinol in Example 1, and the obtained oil layer was recrystallized from a toluene solvent. The yield was 178 g (92.2% yield), and the purity was 99.9%. Comparative Example 2 Similar to Comparative Example 1, catechol was used instead of resorcinol, and the amount of preparation was the same as Comparative Example 1.
Heated to ˜150° C. and added α-methylsterene, also as in Comparative Example 1. After the reaction was completed, the oil layer obtained by washing the reaction solution with hot water was recrystallized in a toluene solvent, and the yield of the obtained crystals was 25 parts by weight, and the purity was as low as 90%. When the reaction solution was analyzed by gas chromatography, it was found that 1,3,3-trimethyl-1-
A large amount of phenylindane was observed, as well as a considerable amount of unknown components. Furthermore, as a result of GPC analysis, the formation of many trimers based on aralkyl di-substituted products was also observed. Example 3 Hydroquinone was used in place of resorcinol in Example 1, and a reaction was carried out under the same reaction conditions as in Example 1. The obtained oil layer was recrystallized from a toluene solvent, and the obtained crystals were
【式】の収量は174g(収率
90%)であり、又、この純度は99.8%であつた。
比較例 3
比較例1と同様に、レゾルシンに代えて、ハイ
ドロキノンを用い、さらに濃硫酸に代えて濃塩酸
を用いて、比較例1と同様な仕込み量で、140℃
に加熱し、α−メチルスチレンを、これまた比較
例1と同様に添加した。反応液終了后、反応液を
温水洗浄して得られた油層をトルエン溶媒を用い
て再結晶した所、得られた結晶の収量は、30重量
部であり、純度も87%と低いものであつた。比較
例−1、比較例−2と同様に反応液をガスクロマ
トグラフイーで分析した所、1,3,3−トリメ
チル−1−フエニルインダンが多量に検出される
と共に、不明成分も多量に検出された。又、
GPC分析の結果からアラルキルジ置換体に基づ
く3量体の多量認められた。The yield of [Formula] was 174 g (90% yield), and the purity was 99.8%. Comparative Example 3 Similar to Comparative Example 1, hydroquinone was used instead of resorcinol, and concentrated hydrochloric acid was used instead of concentrated sulfuric acid.
and α-methylstyrene was added, again in the same manner as in Comparative Example 1. After the reaction solution was finished, the oil layer obtained by washing the reaction solution with warm water was recrystallized using a toluene solvent, and the yield of the obtained crystals was 30 parts by weight, and the purity was as low as 87%. Ta. When the reaction solution was analyzed by gas chromatography in the same manner as Comparative Example-1 and Comparative Example-2, a large amount of 1,3,3-trimethyl-1-phenylindane was detected, as well as a large amount of unknown components. . or,
From the results of GPC analysis, a large amount of trimers based on aralkyl di-substituted products was observed.
Claims (1)
素数1〜4のアルキル基) で表わされる多価フエノール類と、一般式(B) (但し、R2:−H基又は炭素数1〜4のアルキ
ル基、R3,R5:−H基、−OH基、ハロゲン基又
は炭素数1〜4のアルキル基) で表わされる芳香族不飽和化合物の少なくとも一
種とを酸触媒を用い反応させて、下記、一般式(C) (但し、R1,R2,R3及びR4は前記定義と同じで
ある。) で表わされるアラルキルモノ置換多価フエノール
類を製造するにおいて一般式(A)で表わされる多価
フエノール類の水溶液と一般式(B)で表わされる芳
香族不飽和化合物を接触させることを特徴とする
アラルキルモノ置換多価フエノール類の製造方
法。 2 一般式(A)で表わされる多価フエノール類がカ
テコール、ハイドロキノン又はレゾルシンである
特許請求範囲第1項記載のアラルキルモノ置換多
価フエノール類の製造方法。[Claims] 1 General formula (A) (However, R 1 : -H group, OH group, halogen group, or alkyl group having 1 to 4 carbon atoms) and the general formula (B) (However, R 2 : -H group or alkyl group having 1 to 4 carbon atoms; R 3 , R 5 : -H group, -OH group, halogen group, or alkyl group having 1 to 4 carbon atoms) The following general formula (C) is obtained by reacting at least one unsaturated compound with an acid catalyst. (However, R 1 , R 2 , R 3 and R 4 are the same as defined above.) In producing the aralkyl monosubstituted polyhydric phenols represented by the formula (A), 1. A method for producing aralkyl monosubstituted polyhydric phenols, which comprises contacting an aqueous solution with an aromatic unsaturated compound represented by the general formula (B). 2. The method for producing an aralkyl monosubstituted polyphenol according to claim 1, wherein the polyvalent phenol represented by the general formula (A) is catechol, hydroquinone, or resorcinol.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12589784A JPS615037A (en) | 1984-06-18 | 1984-06-18 | Production of aralkyl monosubstituted polyhydric phenolic compound |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12589784A JPS615037A (en) | 1984-06-18 | 1984-06-18 | Production of aralkyl monosubstituted polyhydric phenolic compound |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS615037A JPS615037A (en) | 1986-01-10 |
JPH0514690B2 true JPH0514690B2 (en) | 1993-02-25 |
Family
ID=14921611
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP12589784A Granted JPS615037A (en) | 1984-06-18 | 1984-06-18 | Production of aralkyl monosubstituted polyhydric phenolic compound |
Country Status (1)
Country | Link |
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JP (1) | JPS615037A (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62270881A (en) * | 1986-05-19 | 1987-11-25 | 株式会社荏原製作所 | Noise control method of pump piping |
JPS62270882A (en) * | 1986-05-19 | 1987-11-25 | 株式会社荏原製作所 | Noise control method of pump piping |
IT1223392B (en) * | 1987-12-01 | 1990-09-19 | Montedison Spa | PHENOL ALKYLATION PROCEDURE |
JP2775831B2 (en) * | 1989-04-11 | 1998-07-16 | 住友化学工業株式会社 | Positive resist composition |
JP2775852B2 (en) * | 1989-06-02 | 1998-07-16 | 住友化学工業株式会社 | Positive resist composition |
JP5261069B2 (en) * | 2008-08-13 | 2013-08-14 | 日本乳化剤株式会社 | Method for producing styrenated bisphenol compound |
-
1984
- 1984-06-18 JP JP12589784A patent/JPS615037A/en active Granted
Also Published As
Publication number | Publication date |
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JPS615037A (en) | 1986-01-10 |
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