JPH0429664B2 - - Google Patents
Info
- Publication number
- JPH0429664B2 JPH0429664B2 JP58062748A JP6274883A JPH0429664B2 JP H0429664 B2 JPH0429664 B2 JP H0429664B2 JP 58062748 A JP58062748 A JP 58062748A JP 6274883 A JP6274883 A JP 6274883A JP H0429664 B2 JPH0429664 B2 JP H0429664B2
- Authority
- JP
- Japan
- Prior art keywords
- thpo
- oxidation
- triisopropylbenzene
- tip
- present
- 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
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 7
- 239000001301 oxygen Substances 0.000 claims description 7
- 229910052760 oxygen Inorganic materials 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 6
- VUMCUSHVMYIRMB-UHFFFAOYSA-N 1,3,5-tri(propan-2-yl)benzene Chemical compound CC(C)C1=CC(C(C)C)=CC(C(C)C)=C1 VUMCUSHVMYIRMB-UHFFFAOYSA-N 0.000 claims description 5
- KYIKRXIYLAGAKQ-UHFFFAOYSA-N abcn Chemical compound C1CCCCC1(C#N)N=NC1(C#N)CCCCC1 KYIKRXIYLAGAKQ-UHFFFAOYSA-N 0.000 claims description 5
- 239000007864 aqueous solution Substances 0.000 claims description 3
- 239000007789 gas Substances 0.000 claims description 3
- CWGPMZVRCXTBSZ-UHFFFAOYSA-N hydrogen peroxide 1,3,5-tri(propan-2-yl)benzene Chemical compound OO.OO.OO.CC(C)C1=CC(C(C)C)=CC(C(C)C)=C1 CWGPMZVRCXTBSZ-UHFFFAOYSA-N 0.000 claims description 2
- 238000007254 oxidation reaction Methods 0.000 description 22
- SXXLKZCNJHJYFL-UHFFFAOYSA-N 4,5,6,7-tetrahydro-[1,2]oxazolo[4,5-c]pyridin-5-ium-3-olate Chemical compound C1CNCC2=C1ONC2=O SXXLKZCNJHJYFL-UHFFFAOYSA-N 0.000 description 17
- 101000799461 Homo sapiens Thrombopoietin Proteins 0.000 description 17
- 102100034195 Thrombopoietin Human genes 0.000 description 17
- 230000003647 oxidation Effects 0.000 description 12
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 6
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 230000006698 induction Effects 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- LGXAANYJEHLUEM-UHFFFAOYSA-N 1,2,3-tri(propan-2-yl)benzene Chemical compound CC(C)C1=CC=CC(C(C)C)=C1C(C)C LGXAANYJEHLUEM-UHFFFAOYSA-N 0.000 description 2
- 239000004342 Benzoyl peroxide Substances 0.000 description 2
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 235000019400 benzoyl peroxide Nutrition 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 239000003999 initiator Substances 0.000 description 2
- 238000004904 shortening Methods 0.000 description 2
- 239000012670 alkaline solution Substances 0.000 description 1
- 150000004996 alkyl benzenes Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000000039 congener Substances 0.000 description 1
- PJAYOCNSYITZCZ-UHFFFAOYSA-N hydrogen peroxide 1,3,5-tri(propan-2-yl)benzene Chemical compound OO.OO.CC(C)C1=CC(C(C)C)=CC(C(C)C)=C1 PJAYOCNSYITZCZ-UHFFFAOYSA-N 0.000 description 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-M hydroperoxide group Chemical group [O-]O MHAJPDPJQMAIIY-UHFFFAOYSA-M 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- QCDYQQDYXPDABM-UHFFFAOYSA-N phloroglucinol Chemical compound OC1=CC(O)=CC(O)=C1 QCDYQQDYXPDABM-UHFFFAOYSA-N 0.000 description 1
- 229960001553 phloroglucinol Drugs 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Description
本発明は1,3,5―トリイソプロピルベンゼ
ントリヒドロペルオキシド(以下、THPOとい
う)の製造法に関する。
THPOはフロログルシンの製造原料としてよ
く知られ、その製造法としても、1,3,5―ト
リイソプロピルベンゼン(以下、TIPという)を
アルカリ水溶液の共存下に酸素または酸素含有気
体と接触反応させることもよく知られている。
しかし、かかる従来公知の方法では、
(1) 酸化初期に誘導期が認められ、不純物の多い
TIPを原料とする場合により顕著である。
(2) 酸化時間が長い。
(3) THPOのヒドロペルオキシド基の一部また
は全部がヒドロキシル基に置換された構造のカ
ルビノール類(以下、THPOカルビノールと
いう)の生成が著しい。
(尚、このTHPOカルビノールは先に本発明者
らが見出した過酸化水素による処理などで効率よ
くTHPOとすることができ、従つて、TIPの酸
化においてはTHPOとTHPOカルビノールの合
計収率が重要となるが、THPO収率が高い程有
利であることはいうまでもない。)などの問題が
ある。
ところで、従来よりアルキルベンゼン類の酸化
における誘導期の短縮には過酸化ベンゾイルやア
ゾビスイソブチロニトリルなどの酸化開始剤の添
加が有効なことは知られているが、本発明者らは
TIPもしくはその誘導体の酸化反応における酸化
開始剤について種々検討の結果、該酸化反応にお
いては本発明に特定するアゾビス化合物が誘導期
の短縮に選択的に効果がすぐれ、しかも酸化速度
も向上するために酸化時間が短縮され、その結果
THPOのカルビノール化が防止されてTHPOの
収率も向上することを見出し、本発明に至つた。
すなわち本発明は、TIPもしくはその同族体を
アルカリ水溶液の共存下に酸素または酸素含有気
体と接触させてTHPOを製造する方法において、
TIPもしくはその同族体に対して0.01〜5モル%
の1,1′―アゾビス―(シクロヘキサン―1―カ
ルボニトリル)〔以下、AHCNという〕を添加す
ることを特徴とするTHPOの製造法である。
本発明において、TIP同族体とは1,3,5―
トリイソプロピルベンゼンモノヒドロペルオキシ
ドあるいは1,3,5―トリイソプロピルベンゼ
ンジヒドロペルオキシドのようなTHPO前駆体
を意味し、本発明の酸化反応における原料として
はTIP、TIP同族体のそれぞれ単独あるいはこれ
らの任意の割合からなる混合物が用いられる。
基本となる酸化反応自体は従来公知の方法が適
用され、特に本発明において制限されるものでは
ない。
本発明は、かかる酸化反応においてAHCNを
添加するものであるが、その添加量がTIPもしく
はその同族体に対して0.01モル%未満では効果が
認めにくく、また5モル%を越えても添加量に見
合うだけの効果が得られず、いたずらにAHCN
を消費するのみの傾向があるところから、その添
加量は通常TIPもしくはその同族体に対して0.01
〜5モル%、好ましくは0.05〜2モル%である。
AHCNの添加方法として酸化反応開始時に全
量を添加していてもよく、或いは消費速度に応じ
て分割して、または連続的に添加してもよく、そ
の方法は任意である。
かくして、本発明の方法によれば酸化反応にお
ける誘導期が短かく、酸化時間が短縮され、しか
もTHPO収率が向上するなどのすぐれた効果を
得ることができる。
以下、実施例により本発明を説明する。
実施例 1
1,3,5―トリイソプロピルベンゼン204g、
水204gおよび1,1′―アゾビスー(シクロヘキ
サン―1―カルボニトリル)0.78gを反応器に仕
込み、94〜96℃に加温する。
撹拌下に、定常的に酸素を液中に吹き込み、同
時に反応液のPHが9.5±0.4となるように濃苛性ソ
ーダ水溶液を添加しながら酸化反応を行つた。
反応開始後、一定時間毎に反応液をサンプリン
グし、THPOおよびTHPOカルビノールを分析
してそれぞれの時間における収率を求めたとこ
ろ、表―1に示す結果を得た。
比較例 1
1,1′―アゾビス―(シクロヘキサン―1―カ
ルボニトリル)と添加しない以外は実施例1と同
様にして酸化反応を行い、同様に分析してそれぞ
れの酸化時間における収率を求めたところ、表―
1に示す結果を得た。
The present invention relates to a method for producing 1,3,5-triisopropylbenzene trihydroperoxide (hereinafter referred to as THPO). THPO is well known as a raw material for producing phloroglucin, and its production method involves catalytically reacting 1,3,5-triisopropylbenzene (hereinafter referred to as TIP) with oxygen or an oxygen-containing gas in the coexistence of an aqueous alkaline solution. well known. However, in such conventionally known methods, (1) an induction period is observed at the initial stage of oxidation, and the
This is more noticeable when TIP is used as a raw material. (2) Long oxidation time. (3) The formation of carbinols (hereinafter referred to as THPO carbinols) in which part or all of the hydroperoxide groups of THPO are substituted with hydroxyl groups is remarkable. (This THPO carbinol can be efficiently converted to THPO by treatment with hydrogen peroxide, which the present inventors discovered earlier. Therefore, in the oxidation of TIP, the total yield of THPO and THPO carbinol is is important, but it goes without saying that the higher the THPO yield, the more advantageous it is.) By the way, it has been known that the addition of oxidation initiators such as benzoyl peroxide and azobisisobutyronitrile is effective in shortening the induction period in the oxidation of alkylbenzenes, but the present inventors
As a result of various studies on oxidation initiators in the oxidation reaction of TIP or its derivatives, it was found that the azobis compound specified in the present invention is selectively effective in shortening the induction period in the oxidation reaction, and also improves the oxidation rate. Oxidation time is reduced, resulting in
It was discovered that the carbinolization of THPO was prevented and the yield of THPO was improved, leading to the present invention. That is, the present invention provides a method for producing THPO by contacting TIP or a homolog thereof with oxygen or an oxygen-containing gas in the coexistence of an alkaline aqueous solution,
0.01-5 mol% based on TIP or its homolog
This is a method for producing THPO characterized by adding 1,1'-azobis-(cyclohexane-1-carbonitrile) [hereinafter referred to as AHCN]. In the present invention, TIP congeners are 1,3,5-
It means a THPO precursor such as triisopropylbenzene monohydroperoxide or 1,3,5-triisopropylbenzene dihydroperoxide, and as a raw material in the oxidation reaction of the present invention, TIP, a TIP homologue alone or any of these A mixture of proportions is used. The basic oxidation reaction itself is a conventionally known method and is not particularly limited in the present invention. In the present invention, AHCN is added in such an oxidation reaction, but if the amount added is less than 0.01 mol% with respect to TIP or its homolog, it is difficult to notice the effect, and even if it exceeds 5 mol%, the amount added is Unnecessarily using AHCN without getting the desired effect.
Since there is a tendency to only consume TIP, the amount added is usually 0.01
-5 mol%, preferably 0.05-2 mol%. AHCN may be added in its entirety at the start of the oxidation reaction, or may be added in portions or continuously depending on the consumption rate, and the method is arbitrary. Thus, according to the method of the present invention, excellent effects such as a short induction period in the oxidation reaction, a shortened oxidation time, and an improved THPO yield can be obtained. The present invention will be explained below with reference to Examples. Example 1 204 g of 1,3,5-triisopropylbenzene,
204 g of water and 0.78 g of 1,1'-azobis-(cyclohexane-1-carbonitrile) are charged into a reactor and heated to 94-96°C. While stirring, oxygen was constantly blown into the solution, and at the same time, an oxidation reaction was carried out while adding a concentrated aqueous solution of caustic soda so that the pH of the reaction solution was 9.5±0.4. After the reaction started, the reaction solution was sampled at regular intervals and THPO and THPO carbinol were analyzed to determine the yield at each time, and the results shown in Table 1 were obtained. Comparative Example 1 An oxidation reaction was carried out in the same manner as in Example 1 except that 1,1'-azobis-(cyclohexane-1-carbonitrile) was not added, and the yield at each oxidation time was determined in the same manner. However, the table...
The results shown in 1 were obtained.
【表】
収率の合計
比較例 2
1,1′―アゾビス―(シクロヘキサン―1―カ
ルボニトリル)に代えて2,2′―アゾビス―イソ
ブチロニトリルおよび過酸化ベンゾイルをそれぞ
れトリイソプロピルベンゼンに対して0.3モル%
使用する以外は実施例1と同様にしてそれぞれに
酸化反応を行い、同様に分析してそれぞれの酸化
時間における収率を求めたところ、それぞれの反
応において殆んど比較例1の結果と同様であり、
添加による効果は認められなかつた。[Table] Total yield comparison example 2 In place of 1,1'-azobis-(cyclohexane-1-carbonitrile), 2,2'-azobis-isobutyronitrile and benzoyl peroxide were used for triisopropylbenzene. 0.3 mol%
The oxidation reaction was carried out in the same manner as in Example 1 except for the use of oxidation, and the yield at each oxidation time was determined in the same manner. The results for each reaction were almost the same as in Comparative Example 1. can be,
No effect was observed due to the addition.
Claims (1)
くはその同族体をアルカリ水溶液の共存下に酸素
または酸素含有気体と接触反応させて、1,3,
5―トリイソプロピルベンゼントリヒドロペルオ
キシドを製造する方法において、1,3,5―ト
リイソプロピルベンゼンもしくはその同族体に対
して0.01〜5モル%の1,1′―アゾビスー(シク
ロヘキサン―1―カルボニトリル)を添加するこ
とを特徴とする1,3,5―トリイソプロピルベ
ンゼントリヒドロペルオキシドの製造法。1 1,3,5-triisopropylbenzene or its homolog is reacted with oxygen or oxygen-containing gas in the coexistence of an alkaline aqueous solution to produce 1,3,5-triisopropylbenzene or its analogue.
In the method for producing 5-triisopropylbenzene trihydroperoxide, 0.01 to 5 mol% of 1,1'-azobis(cyclohexane-1-carbonitrile) based on 1,3,5-triisopropylbenzene or its homolog. A method for producing 1,3,5-triisopropylbenzene trihydroperoxide, which comprises adding.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58062748A JPS59190965A (en) | 1983-04-08 | 1983-04-08 | Production of triisopropylbenzene trihydroperoxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58062748A JPS59190965A (en) | 1983-04-08 | 1983-04-08 | Production of triisopropylbenzene trihydroperoxide |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59190965A JPS59190965A (en) | 1984-10-29 |
JPH0429664B2 true JPH0429664B2 (en) | 1992-05-19 |
Family
ID=13209327
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58062748A Granted JPS59190965A (en) | 1983-04-08 | 1983-04-08 | Production of triisopropylbenzene trihydroperoxide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59190965A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP1520853B1 (en) * | 2003-09-24 | 2009-12-30 | Repsol Quimica S.A. | Process for preparation of hydroperoxides |
-
1983
- 1983-04-08 JP JP58062748A patent/JPS59190965A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS59190965A (en) | 1984-10-29 |
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