JPS6025416B2 - Method for producing 9,10-secodehydroabietic acid - Google Patents

Method for producing 9,10-secodehydroabietic acid

Info

Publication number
JPS6025416B2
JPS6025416B2 JP51104774A JP10477476A JPS6025416B2 JP S6025416 B2 JPS6025416 B2 JP S6025416B2 JP 51104774 A JP51104774 A JP 51104774A JP 10477476 A JP10477476 A JP 10477476A JP S6025416 B2 JPS6025416 B2 JP S6025416B2
Authority
JP
Japan
Prior art keywords
acid
secodehydroabietic
rosin
producing
abietic
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
Application number
JP51104774A
Other languages
Japanese (ja)
Other versions
JPS5331650A (en
Inventor
良計 井上
耕治 山根
雅久 石上
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Harima Chemical Inc
Original Assignee
Harima Chemical Inc
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Harima Chemical Inc filed Critical Harima Chemical Inc
Priority to JP51104774A priority Critical patent/JPS6025416B2/en
Publication of JPS5331650A publication Critical patent/JPS5331650A/en
Publication of JPS6025416B2 publication Critical patent/JPS6025416B2/en
Expired legal-status Critical Current

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements 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

【発明の詳細な説明】 本発明は式(1) 式(1) で示される9・10−セコデヒドロアピェチン酸の製造
方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing 9,10-secodehydroapietic acid represented by formula (1).

9・10−セコデヒドロアビェチン酸はその構造が特異
であり、アビェチン酸と同じ分子量を有するに拘らず酸
化に対してはアビェチン酸よりも安定であり、そのアル
カリ塩の界面活性は他の樹脂酸のアルカリ塩と相違しな
いが、水に対する溶解性において優れているから、界面
活性剤として特異な用途が期待でき、またその構造から
して可塑剤、潤滑剤などへの用途も期待できるものであ
るが、本発明はこの9・10−セコデヒドロアビェチン
酸を容易な操作で、しかも好収率で製造し得る方法を提
供せんとするものである。
9,10-Secodehydroabietic acid has a unique structure, and although it has the same molecular weight as abietic acid, it is more stable against oxidation than abietic acid, and the surface activity of its alkaline salt is higher than that of other abietic acids. Although it is not different from alkali salts of resin acids, it has excellent solubility in water, so it can be expected to have unique uses as a surfactant, and because of its structure, it can also be used as a plasticizer, lubricant, etc. However, the object of the present invention is to provide a method for producing 9,10-secodehydroabietic acid with easy operations and a good yield.

また、本発明は9・10−セコデヒドロアビェチン酸の
経済的な精製方法を提供せんとするものである。
Further, the present invention aims to provide an economical method for purifying 9,10-secodehydroabietic acid.

一般に天然物として存在するロジンは樹脂酸と呼ばれる
水素化フェナンスレンのカルボン酸の譲導体を主成分と
するものであるが、このロジンには生松脂より得られる
ガムロジン、パルプ廃液中から得られるトール油中の樹
脂酸分を蒸留により分離することにより得られるトール
油ロジン、或は松板中より抽出することにより得られる
ウッドロジンなどがある。
Generally, rosin that exists as a natural product is mainly composed of a carboxylic acid derivative of hydrogenated phenanthrene called resin acid, but this rosin includes gum rosin obtained from raw pine resin and tall oil obtained from pulp waste liquid Examples include tall oil rosin, which is obtained by separating the resin acid content therein by distillation, and wood rosin, which is obtained by extracting from pine wood.

そしてロジンの主成分である樹脂酸はその構造からして
アビェチン酸系、ピマール酸系、ィソピマール酸系など
に分類されるが、アビェチン酸系樹脂酸にはァビェチン
酸とアビェチン酸の異性体であるパラストリン酸、ネオ
アピェチン酸、レボピマール酸などがある。しかし乍ら
ロジン中には式(1) で示される9・10−セコデヒドロアピェチン酸のよう
にシクロヘキサン環にカルボキシル基のついた構造を有
するシクロヘキサンカルボン酸の誘導体は殆んど含有さ
れていない。
Resin acids, which are the main components of rosin, are classified into abietic acid, pimaric acid, and isopimaric acid based on their structure, but abietic acid resin acids include abietic acid and isomers of abietic acid. These include parastophosphoric acid, neoapietic acid, and levopimaric acid. However, rosin contains almost no derivatives of cyclohexanecarboxylic acid, which has a structure in which a carboxyl group is attached to the cyclohexane ring, such as 9,10-secodehydroapietic acid shown by formula (1). do not have.

一方、上記のシクロヘキサンカルボン酸の誘導体は石油
化学製品又は他の化学物質より有機合成反応により製造
されることは知られているが、この方法によれば多段の
反応経路を必要とし経済的に不利益である。
On the other hand, it is known that the above-mentioned cyclohexanecarboxylic acid derivatives can be produced by organic synthesis reactions from petrochemical products or other chemicals, but this method requires multiple reaction routes and is economically undesirable. It's profit.

ところが、アビェチン酸又はロジンに0.1〜10重量
%の1・1′−ジチオージ−2−ナフトールを添加して
加熱することを特徴とする本発明の方法によれば、上記
したシクロヘキサンカルボン酸構造の式(1)で示され
る9・10−セコデヒドロアビェチン酸を比較的簡単な
操作により一段反応で好収率で製造することができる。
However, according to the method of the present invention, which is characterized in that 0.1 to 10% by weight of 1,1'-dithiodi-2-naphthol is added to abietic acid or rosin and heated, the above-mentioned cyclohexanecarboxylic acid structure 9,10-Secodehydroabietic acid represented by the formula (1) can be produced in a good yield in a one-step reaction by relatively simple operations.

本発明において使用するアピヱチン酸又はロジンは周知
のとおり天然物として容易に入手しうるものである。触
媒として使用する1・1′ージチオージー2−ナフトー
ルは独特許611144号による方法を用いて、Na2
S、S、NaOH及び8ナフトールを原料として容易に
合成できる。
As is well known, apietic acid or rosin used in the present invention is easily available as a natural product. The 1,1'-dithiodi-2-naphthol used as a catalyst was prepared using a method according to German Patent No. 611144.
It can be easily synthesized using S, S, NaOH and 8-naphthol as raw materials.

本発明における反応は操作としては容易であり、0.1
〜10重量%の上記1・1′−ジチオージ−2−ナフト
ールをアビヱチン酸又はロジンに添加し、25000以
下好ましくは200q○付近の温度で加熱することによ
り、アビェチン酸に対し50〜55wt%の9・10−
セコデヒドロアビェチン酸が生成する。
The reaction in the present invention is easy to operate, and 0.1
By adding ~10% by weight of the above 1,1'-dithiodi-2-naphthol to abietic acid or rosin and heating at a temperature of 25,000 or less, preferably around 200q○, 50 to 55% by weight of 9 to abietic acid is added.・10-
Secodehydroabietic acid is produced.

アビェチン酸が消失する時点において9・10ーセコデ
ヒドロアビェチン酸の他にデヒドロアビェチン酸力20
〜25wt%、デイソプロピルデヒドロアビェチン酸が
10〜15M%生成する。なお、1・1′−ジチオージ
ー2ーナフトールの添加量は実験結果に基き0.1〜1
の重量%とした。これらの混合物は種々の方法により精
製することができるが本発明においては最も経済的な方
法として蒸留する方法を採用した。すなわち減圧蒸留で
分留することにより、比較的沸点の低い蟹分は除去され
、9・10ーセコデヒドロアビェチン酸が15〜2仇の
%のデイソプロピルデヒドロアビヱチン酸との混合物と
して得られた。すなわち9・10−セコデヒドロァピェ
チン酸が75〜80%の純度まで精製された。蒸留精製
する前の9・10−セコデヒドロアビェチン酸、デヒド
ロアビェチン酸及びディソプロピルデヒドロアビェチン
酸の混合物は室温において幾分かの流動性を示す程度の
ものであるが、蒸留精製によって得られた9・10ーセ
コデヒドロアビェチン酸とディソプロピルデヒドロアビ
ヱチン酸の混合物は粘椀な液状物となる。
At the time when abietic acid disappears, in addition to 9,10-secodehydroabietic acid, dehydroabietic acid power 20
-25 wt% and 10-15 M% of deisopropyl dehydroabietic acid. The amount of 1,1'-dithiodi-2naphthol added is 0.1 to 1 based on experimental results.
% by weight. These mixtures can be purified by various methods, but in the present invention, distillation was adopted as the most economical method. That is, by fractionating by vacuum distillation, crab components with a relatively low boiling point are removed, and a mixture of 9,10-secodehydroabietic acid and 15 to 2% deisopropyl dehydroabietic acid is obtained. Obtained. That is, 9,10-secodehydroapietic acid was purified to a purity of 75-80%. The mixture of 9,10-secodehydroabietic acid, dehydroabietic acid and disopropyl dehydroabietic acid before distillation purification exhibits some fluidity at room temperature, The mixture of 9,10-secodehydroabietic acid and disopropyl dehydroabietic acid obtained by distillation purification becomes a viscous liquid.

この9・10−セコデヒドロアビヱチン酸は本明細書の
冒頭で述べたように界面活性剤として特異な用途が期待
される外、可塑剤、潤滑剤への用途も期待される有用な
物質である。
As mentioned at the beginning of this specification, this 9,10-secodehydroabietic acid is expected to have unique uses as a surfactant, and is also a useful substance that is expected to be used as a plasticizer and lubricant. It is.

以下本発明の具体例を例示する。Specific examples of the present invention will be illustrated below.

実施例 1 アビェチン酸10碇邦‘こ対し、1・1′−ジチオ−ジ
ー2−ナフトールを1部加えて20000に昇温後各時
間における反応物の組成を追跡した。
Example 1 To 10 liters of abietic acid, 1 part of 1,1'-dithio-di-2-naphthol was added, and after raising the temperature to 20,000 ℃, the composition of the reactant was monitored at each time.

組成分析にはガスクロマトグラフィ一を使用した。分析
結果を表−1に示す。セコデヒドロアビェチン酸は二つ
の異性体として、ガスクロマトグラフィ一にあらわれて
おり、表−1には二つの異性体の総和として示されてい
る。‐表 ‐ 【 (総て数値はガスクロマトグラフイ‐での面積努で示さ
れている。
Gas chromatography was used for compositional analysis. The analysis results are shown in Table-1. Secodehydroabietic acid appears as two isomers in gas chromatography, and is shown in Table 1 as the sum of the two isomers. -Table- [(All values are expressed in area measured by gas chromatography.

)実施例 2実施例1において得られた反応混合物50
0夕を充填物をつめた内径4仇駁し高さ400側の糟蟹
塔を使用し減圧蒸留した。
) Example 2 Reaction mixture obtained in Example 1 50
Distillation was carried out under reduced pressure using a 400 mm tall clay tower filled with a filler.

結果を表−川こ示す。さらに第1回目の留分中9・10
−セコデヒドロアビェチン酸の多い留分(■、■)の混
合物を再度精留した。結果を表−mに示す。表−U ■+■ 39.7wt※(収率) 表‐m 収率は表‐0の蜜分■,■の混合物を100衆とした時
の値で示す。
The results are shown in the table below. Furthermore, during the first distillation 9.10
- The mixture of fractions rich in secodehydroabietic acid (■, ■) was rectified again. The results are shown in Table m. Table-U ■+■ 39.7wt* (yield) Table-m The yield is shown as the value when the mixture of honey components ■ and ■ in Table-0 is taken as 100 units.

Claims (1)

【特許請求の範囲】[Claims] 1 アビエチン酸又はロジンに0.1〜110重量%の
1・1′−ジチオ−ジ−2−ナフトーールを添加して加
熱することを特徴とする9・10−セコデヒドロアビエ
チン酸の製造方法。
1. A method for producing 9,10-secodehydroabietic acid, which comprises adding 0.1 to 110% by weight of 1,1'-dithio-di-2-naphthol to abietic acid or rosin and heating the mixture.
JP51104774A 1976-08-31 1976-08-31 Method for producing 9,10-secodehydroabietic acid Expired JPS6025416B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP51104774A JPS6025416B2 (en) 1976-08-31 1976-08-31 Method for producing 9,10-secodehydroabietic acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP51104774A JPS6025416B2 (en) 1976-08-31 1976-08-31 Method for producing 9,10-secodehydroabietic acid

Publications (2)

Publication Number Publication Date
JPS5331650A JPS5331650A (en) 1978-03-25
JPS6025416B2 true JPS6025416B2 (en) 1985-06-18

Family

ID=14389815

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51104774A Expired JPS6025416B2 (en) 1976-08-31 1976-08-31 Method for producing 9,10-secodehydroabietic acid

Country Status (1)

Country Link
JP (1) JPS6025416B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01164812U (en) * 1988-05-10 1989-11-17
JPH0495718U (en) * 1991-01-17 1992-08-19

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01164812U (en) * 1988-05-10 1989-11-17
JPH0495718U (en) * 1991-01-17 1992-08-19

Also Published As

Publication number Publication date
JPS5331650A (en) 1978-03-25

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