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JPS6213333B2 - - Google Patents
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JPS6213333B2 - - Google Patents

Info

Publication number
JPS6213333B2
JPS6213333B2 JP59232875A JP23287584A JPS6213333B2 JP S6213333 B2 JPS6213333 B2 JP S6213333B2 JP 59232875 A JP59232875 A JP 59232875A JP 23287584 A JP23287584 A JP 23287584A JP S6213333 B2 JPS6213333 B2 JP S6213333B2
Authority
JP
Japan
Prior art keywords
dust
phenols
cobalt
lignin
coconut shell
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
JP59232875A
Other languages
Japanese (ja)
Other versions
JPS61112035A (en
Inventor
Shigeo Hirose
Kazuyuki Kasuga
Hyoe Hatakeyama
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.)
National Institute of Advanced Industrial Science and Technology AIST
Original Assignee
Agency of Industrial Science and Technology
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 Agency of Industrial Science and Technology filed Critical Agency of Industrial Science and Technology
Priority to JP59232875A priority Critical patent/JPS61112035A/en
Publication of JPS61112035A publication Critical patent/JPS61112035A/en
Publication of JPS6213333B2 publication Critical patent/JPS6213333B2/ja
Granted 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

  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、ココヤシ殻ダストからフエノール類
を工業的に安価にかつ効率よく製造する方法に関
するものである。 本発明により得られるフエノール類は、リグニ
ン関連型のいわゆる4−ヒドロキシフエニル、グ
アヤシル及びシリンギル系フエノール類である。
これらのリグニン関連型フエノール類は、高分子
合成原料或いは、香料、医薬品等のフアインケミ
カル原料として利用される産業上有効な物質であ
る。 従来フエノール類は、石油を出発原料として製
造されている。しかし、上記のリグニン関連型フ
エノール類を製造するためには多段階の反応を経
ることは避けられない。一方リグニンを分解する
方法は、一段で効率よくリグニン関連型フエノー
ル類が得られるため効率的である。このため、バ
ニリンは、パルプ廃液中のリグノスルホン酸を原
料として、対リグニン収率約10%で工業的に製造
されている。 一方、化石資源の有限性が指摘され、その代替
資源の開発が強く要望されている。ココヤシにお
いては、その果実を採取した後のヤシ殻のおおく
は廃棄されている。現在、ココヤシ殻ダストの有
効利用法はみあたらず、フエノール類製造原料と
して検討されてはいない。 本発明者は、このココヤシ殻ダストの有効利用
に関して種々研究を重ねた結果、このものは、約
40重量パーセントもの多量なリグニンを含み(通
常約30%前後)、フエノール類製造原料として有
効であることを見出し、本発明を完成するに至つ
た。 すなわち、本発明によれば、ココヤシ殻からダ
スト部分を分離し、コバルト()を触媒として
アルカリ酸素酸化分解を行つた後に抽出法により
生成フエノール類を分離することを特徴とするコ
コヤシ殻ダストからフエノール類を製造する方法
が提供される。 本発明の方法を好ましく実施するには、先ず、
ココヤシ殻を破砕し、この破砕物をダスト部と繊
維部分とに分け、そのダスト部分を回収する。破
砕はデイスクリフアイナーにより行うのが有効で
あり、また、破砕物からダスト部分の分離は、破
砕物を水面に浮上させ、水中の沈降する繊維部分
から分離し、回収することにつて行うことができ
る。 次にこのようにして分離された、ココヤシ殻ダ
ストは、風乾などにより乾燥した後、ウイレーミ
ルなどにより粉末とし、酸化分解に供する。 本発明に用いられる分解条件は、2Nないし4N
の水酸化ナトリウムあるいは水酸化カリウムを媒
体として、酸素圧3〜10Kg/cm2、反応温度130℃
〜165℃である。なお、触媒として用いるコバル
ト()はリグニン1gに対して5〜20ミリモル
である。この場合、触媒として用いる水酸化コバ
ルト()は、硫酸コバルト()や塩化コバル
ト()を反応容器に入れ、これにアルカリを加
えた後、過酸化水素処理することによつて得られ
る。反応系に存在する水酸化コバルトの量は、濃
度1.1〜5.5重量%、好ましくは2〜4重量%であ
る。この場合、規定度調節に用いるアルカリとし
ては、水酸化ナトリウム、水酸化カリウム等の強
塩基が用いられる。また、本発明における酸化剤
としては、酸素又は空気が用いられる。 実施例 1 試料としてインドネシア産のココヤシ殻のダス
ト部分(いわゆるコイヤダスト)を用いた。コイ
ヤダストは、デイスクリフアイナーによつて繊維
部分と分離した後、ウイレーミルによつて粉末状
にした。アルコール・ベンゼン混合溶媒で脱脂し
た試料を酸化分解に供した。 コイヤダスト脱脂粉末1.0g、コバルト()及
び12%水酸化ナトリウム水溶液50mlを100ml容の
ステンレス製オートクレーブに入れ、さらに、酸
素を5Kg/cm2圧入した。なお、コバルト()は
硫酸コバルト()水和物3.0gを5%水酸化ナト
リウム水溶液40ml分散させ、これを30%過酸化水
素水10mlで酸化したものを用いた。反応混合物を
145℃に加熱し、攬拌下に6.5時間分解を行つた。 反応終了後、反応混合物を遠心分離することに
よりアルカリ性水不溶部を分け、さらに水による
洗浄を行つた。得られた、水溶液を塩酸でPH1に
酸性化し、エーテル抽出を行つた。次に、エーテ
ル抽出液を無水硫酸ナトリウムによつて乾燥した
後、エーテルを除去することにより酸化分解生成
物を得た。 酸化分解生成物の分析はガスクロマトグラフに
より行つた。すなわち、酸化分解生成物を乾燥ピ
リジンに溶解し、これにビス(トリメチルシリ
ル)アセトアミドを加えてシリル化を行い、ガス
クロマトグラフによる分析に供した。そのガスク
ロマトグラフの結果を表1に示す。測定条件は以
下の通りであつた。 カラム;ステンレス製2m、充てん材;
siliconeOV−1、カラム温度;120〜220℃、昇温
速度;5℃/min、キヤリアガス;窒素
The present invention relates to a method for industrially producing phenols from coconut shell dust at low cost and efficiently. The phenols obtained according to the present invention are lignin-related so-called 4-hydroxyphenyl, guaiacyl and syringyl phenols.
These lignin-related phenols are industrially effective substances used as raw materials for polymer synthesis or fine chemical raw materials for perfumes, pharmaceuticals, and the like. Conventionally, phenols have been produced using petroleum as a starting material. However, in order to produce the above-mentioned lignin-related phenols, it is unavoidable to go through a multi-step reaction. On the other hand, the method of decomposing lignin is efficient because lignin-related phenols can be efficiently obtained in one step. For this reason, vanillin is industrially produced from lignosulfonic acid in pulp wastewater at a yield of about 10% based on lignin. On the other hand, the finite nature of fossil resources has been pointed out, and there is a strong demand for the development of alternative resources. In coconut palms, most of the coconut shells are discarded after the fruit is harvested. Currently, there is no effective use of coconut shell dust, and it is not being considered as a raw material for producing phenols. As a result of various research into the effective use of this coconut shell dust, the present inventor found that this
It was discovered that it contains as much as 40% by weight of lignin (usually around 30%) and is effective as a raw material for producing phenols, leading to the completion of the present invention. That is, according to the present invention, phenols are obtained from coconut shell dust by separating the dust part from the coconut shell, performing alkaline oxygen oxidative decomposition using cobalt () as a catalyst, and then separating the produced phenols by an extraction method. A method is provided for manufacturing a class of products. To preferably carry out the method of the present invention, first,
The coconut shell is crushed, the crushed material is divided into a dust part and a fiber part, and the dust part is collected. It is effective to crush the dust using a disk-cliffing ironer, and to separate the dust from the crushed material, it is possible to float the crushed material to the water surface, separate it from the fibrous portion that settles in the water, and collect it. can. Next, the coconut shell dust thus separated is dried by air-drying or the like, and then pulverized by a Wiley mill or the like and subjected to oxidative decomposition. The decomposition conditions used in the present invention are 2N to 4N
of sodium hydroxide or potassium hydroxide as a medium, oxygen pressure of 3 to 10 Kg/cm 2 , reaction temperature of 130°C
~165℃. The amount of cobalt () used as a catalyst is 5 to 20 mmol per 1 g of lignin. In this case, cobalt hydroxide (2) used as a catalyst can be obtained by placing cobalt sulfate (2) or cobalt chloride (2) in a reaction vessel, adding an alkali thereto, and then treating the mixture with hydrogen peroxide. The amount of cobalt hydroxide present in the reaction system has a concentration of 1.1 to 5.5% by weight, preferably 2 to 4% by weight. In this case, as the alkali used for normality adjustment, a strong base such as sodium hydroxide or potassium hydroxide is used. Further, oxygen or air is used as the oxidizing agent in the present invention. Example 1 A dust part of a coconut shell from Indonesia (so-called coir dust) was used as a sample. The coir dust was separated from the fiber part using a disk-cliffing iner, and then pulverized using a Wiley mill. A sample degreased with an alcohol/benzene mixed solvent was subjected to oxidative decomposition. 1.0 g of coir dust degreased powder, cobalt () and 50 ml of a 12% aqueous sodium hydroxide solution were placed in a 100 ml stainless steel autoclave, and oxygen was further pressurized at 5 kg/cm 2 . For cobalt (), 3.0 g of cobalt sulfate () hydrate was dispersed in 40 ml of a 5% aqueous sodium hydroxide solution, which was then oxidized with 10 ml of 30% hydrogen peroxide. reaction mixture
The mixture was heated to 145°C and decomposed for 6.5 hours under stirring. After the reaction was completed, the reaction mixture was centrifuged to separate the alkaline water-insoluble portion, which was further washed with water. The resulting aqueous solution was acidified to PH1 with hydrochloric acid, and extracted with ether. Next, the ether extract was dried over anhydrous sodium sulfate, and the ether was removed to obtain an oxidative decomposition product. Analysis of oxidative decomposition products was performed by gas chromatography. That is, the oxidative decomposition product was dissolved in dry pyridine, bis(trimethylsilyl)acetamide was added thereto to perform silylation, and the product was subjected to analysis by gas chromatography. The gas chromatograph results are shown in Table 1. The measurement conditions were as follows. Column; stainless steel 2m, packing material;
siliconeOV-1, column temperature: 120-220℃, heating rate: 5℃/min, carrier gas: nitrogen

【表】 分析結果を表2に示す。 実施例 2 前処理として、20Kg/cm2(およそ210℃)の加
熱水蒸気で処理した後、急激に大気中に放出する
ことによる爆砕を施した試料を、実施例1と同条
件で分解した。その結果を表2にあわせて示す。
[Table] The analysis results are shown in Table 2. Example 2 A sample was pretreated with heated steam at 20 kg/cm 2 (approximately 210° C.) and then exploded by rapidly releasing it into the atmosphere, and was decomposed under the same conditions as in Example 1. The results are also shown in Table 2.

【表】【table】

Claims (1)

【特許請求の範囲】[Claims] 1 ココヤシ殻のダスト(非繊維部分)をコバル
ト()を触媒として、アルカリ存在下に酸素化
分解することを特徴とするリグニン関連型フエノ
ール類の製造方法。
1. A method for producing lignin-related phenols, which comprises oxygenating and decomposing coconut shell dust (non-fiber part) in the presence of an alkali using cobalt () as a catalyst.
JP59232875A 1984-11-05 1984-11-05 Production of phenol from coconut husk dust Granted JPS61112035A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59232875A JPS61112035A (en) 1984-11-05 1984-11-05 Production of phenol from coconut husk dust

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59232875A JPS61112035A (en) 1984-11-05 1984-11-05 Production of phenol from coconut husk dust

Publications (2)

Publication Number Publication Date
JPS61112035A JPS61112035A (en) 1986-05-30
JPS6213333B2 true JPS6213333B2 (en) 1987-03-25

Family

ID=16946198

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59232875A Granted JPS61112035A (en) 1984-11-05 1984-11-05 Production of phenol from coconut husk dust

Country Status (1)

Country Link
JP (1) JPS61112035A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103626642A (en) * 2013-11-28 2014-03-12 上海应用技术学院 Method for preparing vanillin

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2697398B2 (en) * 1990-09-07 1998-01-14 株式会社日立製作所 Vehicle structure and manufacturing method thereof
JPH0620122U (en) * 1990-12-03 1994-03-15 日本トレールモービル株式会社 Wing car roof or sidewall structure
JPH07110607B2 (en) * 1991-04-01 1995-11-29 住友軽金属工業株式会社 Bogie frame for superconducting magnetically levitated vehicles
CA2965879C (en) * 2014-10-30 2020-03-10 Organofuel Sweden Ab A mild catalytic reduction of c-o bonds and c=o bonds using a recyclable catalyst system
CN109721117B (en) * 2018-12-07 2021-05-18 南京林业大学 A kind of method for functionalized modification of syringaldehyde, obtained product and application thereof
CN109805406B (en) * 2019-02-19 2022-05-31 广东省农业科学院蚕业与农产品加工研究所 A kind of extraction method of rice bran combined with phenol ultra-high pressure-alkali-acid hydrolysis step-by-step release

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103626642A (en) * 2013-11-28 2014-03-12 上海应用技术学院 Method for preparing vanillin

Also Published As

Publication number Publication date
JPS61112035A (en) 1986-05-30

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Legal Events

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EXPY Cancellation because of completion of term