JPH02214539A - Production of catalytic material adsorbing low molecular gas - Google Patents

Production of catalytic material adsorbing low molecular gas

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Publication number
JPH02214539A
JPH02214539A JP1036879A JP3687989A JPH02214539A JP H02214539 A JPH02214539 A JP H02214539A JP 1036879 A JP1036879 A JP 1036879A JP 3687989 A JP3687989 A JP 3687989A JP H02214539 A JPH02214539 A JP H02214539A
Authority
JP
Japan
Prior art keywords
organic acid
acid compound
molecular gas
extracting
gas adsorption
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.)
Pending
Application number
JP1036879A
Other languages
Japanese (ja)
Inventor
Shunsuke Matsuo
松尾 駿介
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.)
Individual
Original Assignee
Individual
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Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP1036879A priority Critical patent/JPH02214539A/en
Publication of JPH02214539A publication Critical patent/JPH02214539A/en
Pending legal-status Critical Current

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  • Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
  • Storage Of Fruits Or Vegetables (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PURPOSE:To enhance freshness maintaining function and antibacterial function by extracting a specified org. acid compd. from raw material for extracting the org. acid compd., impregnating the extracted org. acid compd. into a microporous material, drying and crushing the material. CONSTITUTION:Saccharides are added to diatomaceous earth and lactic acid fermentation is carried out. The earth is dried by the heat of the fermentation and crushed to obtain raw material for extracting an org. acid-rich org. acid compd. This org. acid compd. is extracted from the raw material and impregnated into a microporous material under reduced pressure. The material is then dried and crushed to produce a catalytic material adsorbing low molecular gas. The org. acid compd. is preferably extracted by adding warm water to the raw material, stirring them at a constant temp. and carrying out specific gravity separation and filtration.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は低分子ガス吸着触媒材の製法に係わり、更に詳
しくは生鮮食料品の鮮度保持材、制菌材、変色防止材、
脱臭材、除湿材等、広義には食品保存材として利用する
に好適な細多孔質材料中に有機酸化合物を含浸せしめた
低分子ガス吸着触媒材の製造方法に関する。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for producing a low-molecular gas adsorption catalyst material, and more specifically to a freshness-preserving material for fresh foods, a bacteriostatic material, a discoloration prevention material,
The present invention relates to a method for producing a low-molecular gas adsorption catalyst material in which an organic acid compound is impregnated into a fine porous material suitable for use as a deodorizing material, a dehumidifying material, or in a broader sense as a food preservation material.

〔従来の技術〕[Conventional technology]

周知の通り、野菜、果実、魚肉、畜肉等の生鮮食料品に
対しては、上述した通り広義の食品保存材が適用されて
いる。即ち制菌材、鮮度保持材、変色防止材、脱臭材、
除湿材等と称されているものである。勿論、この適用の
され方に関しても、形態的には食品を収容する包装紙や
包装容器中に投入して用いる場合もあるし、フィルム状
シート状体の組成の中に混入之れで用いられる場合もあ
る。これらはラミネートフィルム、ストレッチフィルム
等の形で市場に供給され、これらフィルムが食品の包装
等に適用された時に上述した鮮度保持材の機能を果す。
As is well known, food preservatives in the broad sense described above are applied to fresh foods such as vegetables, fruits, fish, meat, and the like. In other words, antibacterial materials, freshness preservation materials, discoloration prevention materials, deodorizing materials,
This is called a dehumidifying material. Of course, in terms of how this is applied, it may be used by being put into wrapping paper or packaging containers that contain food, or it may be used by being mixed into the composition of a film-like sheet. In some cases. These are supplied to the market in the form of laminate films, stretch films, etc., and when these films are applied to food packaging etc., they function as the above-mentioned freshness preserving material.

この他に、シート状体の面に塗布された塗布材、糊料中
に混入される場合もある。
In addition, it may be mixed into a coating material or paste applied to the surface of a sheet-like body.

そして、この種の鮮度保持材等は、従来から幾つかのも
のが提案され、広く実用に供されている。
Several types of freshness-preserving materials of this kind have been proposed in the past and are in widespread use.

中でも、近時、細多孔質材料中に有機酸化合物を含浸せ
しめて成る低分子ガス吸着触媒材が、広義の意味の食品
保存材1、個別の目的ごとには鮮度保持材、制菌材、変
色防止材、脱臭材、除湿材等として有用であることが認
識されつつある。即ちサンゴ、シリカゲル、活性アルミ
ナ、合成及び天然のゼオライト、白陶土、蛭石より得ら
れるパーライト、麦飯石等の細多孔質材料、特に硫酸、
硫酸カルシウム、炭酸カルシウム、燐酸カルシウムを主
成分とする天然細多孔質物の微粉末に、80%以上の有
機酸を含む有機酸化合物、より具体的には、多価フェノ
ールと含窒素化合物の縮合物であるフェン酸、そして多
糖類として炭水化物や各種金属イオン等を多量に含む液
状の有機酸化合物を含浸させた低分子ガス吸着触媒材が
有用なものとして提案されている。そして、この低分子
ガス吸着触媒材の従来の製法は次の通りである。
Among these, recently, low-molecular gas adsorption catalyst materials made by impregnating organic acid compounds into fine porous materials have been used as food preservation materials in a broad sense, as freshness-preserving materials, antibacterial materials, and for specific purposes. It is becoming recognized that it is useful as a discoloration prevention material, a deodorizing material, a dehumidifying material, etc. That is, fine porous materials such as coral, silica gel, activated alumina, synthetic and natural zeolites, white china clay, perlite obtained from vermiculite, maifan stone, especially sulfuric acid,
An organic acid compound containing 80% or more of an organic acid, more specifically a condensation product of a polyhydric phenol and a nitrogen-containing compound, in a fine powder of a natural porous material mainly composed of calcium sulfate, calcium carbonate, and calcium phosphate. A low-molecular gas adsorption catalyst material impregnated with a liquid organic acid compound containing a large amount of phenic acid, a carbohydrate, various metal ions, etc. as a polysaccharide, has been proposed as a useful material. The conventional manufacturing method for this low molecular gas adsorption catalyst material is as follows.

即ち珪藻類を含む士を乾燥させる。この場合従来は、8
0%以上の含水率を呈し流動状を呈しているもともとの
土を6ケ月位常温に放置し65%程度の含水率とし、更
にビニールハウス内に広く展ばし自然乾燥させ、もって
含水率を33%程度にしていた。この後これを粉砕し、
有機酸化合物抽出用の原料を得る。この後、常法の抽出
法に従ってこの原料から上述した液状の有機酸化合物を
抽出する。
That is, diatoms containing diatoms are dried. In this case, conventionally 8
The original soil, which has a moisture content of 0% or more and is in a fluid state, is left at room temperature for about 6 months to reach a moisture content of about 65%, and then spread widely in a plastic greenhouse and allowed to air dry to reduce the moisture content. It was set at around 33%. After this, crush this,
Obtain raw materials for organic acid compound extraction. Thereafter, the above-mentioned liquid organic acid compound is extracted from this raw material according to a conventional extraction method.

この後、別個に用意した上述した各種の細多孔質材料を
、液状を呈したこの有機酸化合物中に浸漬し、有機酸化
合物を細多孔質材料の組織中に含浸せしめる。この場合
従来は常圧下で上記の浸漬操作をしていた。以後、乾燥
し、この有機酸化合物を含む細多孔質材料を粉砕し低分
子ガス吸着触媒材としていた。そして使用目的に応じた
加工を施していた。
Thereafter, the above-mentioned various fine porous materials prepared separately are immersed in this liquid organic acid compound to impregnate the organic acid compound into the structure of the fine porous materials. In this case, conventionally the above-mentioned dipping operation was performed under normal pressure. Thereafter, it was dried and the fine porous material containing this organic acid compound was pulverized to obtain a low-molecular gas adsorption catalyst material. They were then processed according to their intended use.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

上記従来技術は、それまでになかった細多孔質材料中に
有機酸化合物が含浸された低分子ガス吸着材を結果させ
る為の勝れた技術であるものの、本発明者等が、この低
分子ガス吸着材自体の改良、即ち鮮度保持機能、制菌機
能、脱臭機能、除湿機能等の向上及びこの製法の改良、
即ち生産性の向上、品質安定の為の製法の確立等を試み
た結果法の不具合があることが見出された。
Although the above-mentioned conventional technology is an excellent technique for producing a low-molecular gas adsorbent in which an organic acid compound is impregnated into a fine porous material, the present inventors Improving the gas adsorbent itself, that is, improving its freshness retention function, antibacterial function, deodorizing function, dehumidification function, etc., and improving this manufacturing method,
In other words, after trying to establish a manufacturing method to improve productivity and stabilize quality, it was discovered that there was a problem with the method.

即ち■液状の有機酸化合物を抽出する為の原料を得るに
当り、珪藻類を含む土を入手し、これを25〜35%の
含水率に乾燥させる工程が必要であるが、従来は上述し
たように最終の乾燥段階も自然乾燥に頼っていた。従っ
て、有機酸化合物抽出用原料1を基準で、およそ3〜4
週間要していた。
That is, to obtain raw materials for extracting liquid organic acid compounds, it is necessary to obtain soil containing diatoms and dry it to a moisture content of 25 to 35%. The final drying stage also relied on natural drying. Therefore, based on 1 raw material for extracting organic acid compounds, approximately 3 to 4
It took a week.

この為に生産性が著しく悪く、能率向上が望まれていた
For this reason, productivity was extremely poor, and improvements in efficiency were desired.

又■この低分子ガス吸着触媒材の鮮度保持機能や、脱臭
機能等を向上させるには、最終製品中に多糖類が可及的
多く含まれれば含まれる程鮮度保持等の効果が良い車が
確認されているが、従来は珪藻類を含む土に何等の添加
物も添加せず単にこれを自然乾燥して原料を得ているの
で、多糖類の含有量に一定の限度があり、更に完全が望
まれる所であった。
In addition, in order to improve the freshness preservation function and deodorization function of this low molecular gas adsorption catalyst material, the more polysaccharides are included in the final product, the better the freshness preservation effect will be. However, in the past, the raw material was simply dried naturally without adding any additives to the soil containing diatoms, so there was a certain limit to the polysaccharide content, and even more completely. It was a desirable place.

更に■従来技術の場合抽出された液状の有機酸化合物中
に細多孔質材料を浸漬し、液状有機酸化合物を細多孔質
材料中に含浸せしめる工程は、常圧下で実施しているの
で、多くの実験の結果、細多孔質材料の組織のすみずみ
に液状有機酸化合物が浸透し難い事が判った。より具体
的に言えば、細多孔質材料は、それ自体連続気泡組織を
有し、比表面積が大であるから、これを有効に用いるに
は細多孔の内部に迄液状の有機酸混合物を含浸させるこ
とが必要な所、従来は常圧下の操作である為細多孔質材
料の最外側の面に液状の有機酸化合物が付着し、中へ浸
透する度合が少ない事が確認された。
Furthermore, in the case of the prior art, the process of immersing a fine porous material in the extracted liquid organic acid compound and impregnating the liquid organic acid compound into the fine porous material is carried out under normal pressure, so As a result of the experiment, it was found that it is difficult for liquid organic acid compounds to penetrate into every corner of the microporous material's structure. More specifically, since the fine porous material itself has an open cell structure and has a large specific surface area, in order to effectively use it, it is necessary to impregnate the inside of the fine pores with a liquid organic acid mixture. It was confirmed that the liquid organic acid compound adhered to the outermost surface of the microporous material and was less likely to penetrate into the microporous material because it was conventionally operated under normal pressure.

従って細多孔質材料の量に対する液状の有機酸化合物の
量をより多くするのに限度があり、最終製品の低分子ガ
ス吸着触媒材の鮮度保持機能、脱臭機能、除湿機能等の
向上に一定の限度があった。
Therefore, there is a limit to increasing the amount of liquid organic acid compound relative to the amount of porous material, and it takes a certain amount of effort to improve the freshness retention function, deodorization function, dehumidification function, etc. of the final product's low molecular gas adsorption catalyst material. There was a limit.

〔目的〕〔the purpose〕

従って本発明の目的とする所は、有機酸化合物が含浸せ
しめられた細多孔質材料より成る低分子ガス吸着触媒材
を製造するに際して、特に、有機酸化合物抽出用原料を
得べく珪藻類を含む士の乾燥工程を改良し、上記乾燥時
間をより短縮し量産性を付与すると共に、同時に最終製
品の低分子ガス吸着触媒材中に、その効用をよりよく発
揮させる為の多糖類を可及的に多く含ませる事を可能に
する製法を提供するにあり、加えて細多孔質材料中に液
状の有機酸化合物を含浸させる工程を改良し、細多孔質
材料の組織内部にまで有機酸化合物をよりよく浸透せし
め、細多孔質材料の量に対する含浸有機酸化合物の量を
可及的に大となし、よりよく鮮度保持等の効果を発揮せ
しめる為の製法を提供するにある。
Therefore, an object of the present invention is to produce a low-molecular gas adsorption catalyst material made of a fine porous material impregnated with an organic acid compound, and in particular to obtain a raw material for extracting an organic acid compound, We have improved the drying process of the drying process to further shorten the drying time and increase mass productivity, and at the same time, we have added as much polysaccharide as possible to the low molecular gas adsorption catalyst material of the final product in order to better demonstrate its effectiveness. In addition, we have improved the process of impregnating a liquid organic acid compound into a fine porous material, and we have also improved the process of impregnating a liquid organic acid compound into a fine porous material. It is an object of the present invention to provide a manufacturing method for better permeation, maximizing the amount of impregnated organic acid compound relative to the amount of fine porous material, and better exhibiting effects such as maintaining freshness.

〔課題を解決する為の手段〕 〔作用〕上記目的を達成
する為に本発明は次の技術的手段を有する。
[Means for Solving the Problem] [Operation] In order to achieve the above object, the present invention has the following technical means.

先ず珪藻類を含む土を乾燥、粉砕して有機酸化合物抽出
用の原料を得る工程は次の通りである。
First, the process of drying and pulverizing soil containing diatoms to obtain a raw material for extracting organic acid compounds is as follows.

即ち、採取した段階では80%内外の含水率を呈してい
る珪藻類を含む土を倉庫等に放置し、6ケ月位かけて含
水率55〜65%程度にする。この様な土は、例えば日
本国長崎県北高来郡森山町に産出する。長い年月を経て
低温発酵で珪藻類が組成されるに至ったとされている。
That is, soil containing diatoms that exhibits a moisture content of around 80% at the stage of collection is left in a warehouse or the like, and is brought to a moisture content of about 55 to 65% over about 6 months. Such soil is produced, for example, in Moriyama-cho, Kita-Takagi-gun, Nagasaki Prefecture, Japan. It is said that diatoms were formed through low-temperature fermentation over many years.

このような性状の土に1重量部で土の0.5〜2%相当
の糖類を添加する。望°ましくは1%相当がよい、これ
を添加した後、10〜12時間経過後、60〜80℃の
温度に保ちながら40〜55時間程度かけて乳酸発酵せ
しめる。この際微量の空気をこの間連続して吹きかける
0例えば、1.00 K gの珪8;類を含む土に重量
部で1%相当の糖類を添加した場合、0.3m″/hr
の空気を吹きかける。上記乳酸発酵により、糖類が乳酸
に変えられ、その過程で発酵熱を生ずる。即ち堆積状態
の土中に発酵熱が生じ、この発酵熱で土の水分が蒸発せ
しめられ、含水率がおよそ30%内外になる。
To the soil having such properties, 1 part by weight of sugars corresponding to 0.5 to 2% of the soil is added. After 10 to 12 hours have elapsed after adding this, which is preferably equivalent to 1%, lactic acid fermentation is carried out for about 40 to 55 hours while maintaining the temperature at 60 to 80°C. At this time, a small amount of air is continuously blown during this time.For example, when sugars equivalent to 1% by weight are added to soil containing 1.00 Kg of silicon, 0.3 m''/hr
Blow out the air. The lactic acid fermentation converts sugars into lactic acid and generates fermentation heat in the process. That is, fermentation heat is generated in the piled soil, and this fermentation heat evaporates the moisture in the soil, resulting in a moisture content of around 30%.

即ち従来に比して極めて短期に乾燥が進行する、これに
より、最終製品の低分子ガス吸着触媒材全体の生産性が
著しく向上するものである。加えて、低分子ガス吸着触
媒材に、より多くの多糖類が含まれる結果となり、その
鮮度保持、除湿、脱臭、制菌等の諸作用が増加すること
が確認された。以後、次の工程の有機酸化合物抽出工程
、及び細多孔質材料への浸漬工程で必要とされる接触面
積の増大の為に、この乾燥された原料を15〜30メツ
シユアンダの粒径に粉砕する。これにより有機酸化合物
抽出用原料を製造する。
That is, drying progresses in an extremely short period of time compared to the conventional method, and as a result, the productivity of the entire low molecular gas adsorption catalyst material as a final product is significantly improved. In addition, it was confirmed that the low-molecular gas adsorption catalyst material contained more polysaccharides, and its various effects such as freshness preservation, dehumidification, deodorization, and antibacterial effects increased. Thereafter, this dried raw material is pulverized to a particle size of 15 to 30 mesh in order to increase the contact area required in the next step of organic acid compound extraction step and immersion step into the microporous material. . This produces a raw material for extracting organic acid compounds.

続いて上記の有機酸化合物抽出用原料から高度に即ち9
0%以上に有機酸を含む化合物を製造する抽出工程は次
の通りである。
Subsequently, from the above raw material for extracting organic acid compounds, a high degree of
The extraction process for producing a compound containing 0% or more of organic acid is as follows.

即ち、゛有機酸化合物抽出用原料に温水を加えて定温、
攪拌する。上記温水は、重量部で有機酸化合物抽出用原
料の8〜12%相当加え、 ’?f  −C程度の温水
を用い、 タ(℃を保って30〜90分程度、攪拌する
0次いで常法通り、20〜30時間かけて比重分離し、
ミクロン級のフィルタにかけて濾過する。これにより2
〜5ミクロン粒子の有機酸及びその化合物が得られる。
That is, ``Add hot water to the raw material for organic acid compound extraction and keep it at a constant temperature.
Stir. To the above hot water, add 8 to 12% by weight of the raw material for extracting organic acid compounds. Using hot water of about f -C, stir for about 30 to 90 minutes while maintaining the temperature (℃).
Filter through a micron-grade filter. This results in 2
~5 micron particles of organic acids and their compounds are obtained.

この有機酸化合物中には、90%以上の有機酸が含まれ
る0例えば、カルボン酸、スルホン酸、スルフィン酸、
フェノール、二/−ル、チオフェノール、オキシム、芳
香族スルホンアミド、第1級及び第2級ニトロ化合物等
、この内、多価フェノールと含窒素化合物の縮合物であ
るフミン酸を使用するのが好ましく。
This organic acid compound contains 90% or more of organic acids, such as carboxylic acid, sulfonic acid, sulfinic acid,
Among them, humic acid, which is a condensate of polyhydric phenol and nitrogen-containing compound, is used. Preferably.

特に上記乳酸発酵の結果、最終製品の低分子ガス吸着触
媒材の鮮度保持等の諸効果を向上させるのに役立つ多糖
類としての炭水化物の増加を図ることができる。そして
この液状の有機酸化合物はP H2,98〜3の範囲に
調節され、酸度はクエン酸換算で4〜5%である。
In particular, as a result of the above lactic acid fermentation, it is possible to increase carbohydrates as polysaccharides that are useful for improving various effects such as freshness retention of the final product of the low-molecular gas adsorption catalyst material. The pH of this liquid organic acid compound is adjusted to a range of 2.98 to 3, and the acidity is 4 to 5% in terms of citric acid.

次に、このようにして得られた液状の有機酸化合物を細
多孔質材料の組織中に含浸させる工程は次の通りである
Next, the step of impregnating the liquid organic acid compound thus obtained into the structure of the microporous material is as follows.

即ち、細多孔質材料としては、サンゴ、シリカゲル、活
性アルミナ、合成又は天然のゼオライト、白陶土、蛭石
より得られるパーライト、麦飯石等が考慮される。特に
、硫酸、硫酸カルシウム、炭酸カルシウム、燐酸カルシ
ウムを主成分とする天然細多孔質材の微粉末が望ましい
That is, as the fine porous material, coral, silica gel, activated alumina, synthetic or natural zeolite, white china clay, perlite obtained from vermiculite, maifan stone, etc. are considered. Particularly desirable is a fine powder of a natural porous material containing sulfuric acid, calcium sulfate, calcium carbonate, and calcium phosphate as main components.

これらの細孔はミクロン級であって、その表面積は極め
て大きく、ガスとの接触効率が極めて良い。
These pores are micron-sized, have an extremely large surface area, and have extremely high contact efficiency with gas.

さて、この細多孔性材料は、その粒径が300〜400
 メツシュ程度のものを用い、重量比で路間等の量の有
機酸化合物中に浸漬させる。この時、減圧下、即ち0.
8〜0.98気圧下で実施する事を特徴とする。即ち常
圧下で行う従来技術の場合、液状の有機酸化合物が細多
孔質材料の最外側の表面に付着し、組織の中まで浸透し
ていかないのが実情であった。その為細多孔質材料の延
べの全表面積が、鮮度保持や、脱臭作用時有効に寄与し
なかった。所がこのように減圧下で実施すると、液状の
有機酸化合物の各孔隙内への浸透がよりよ〈実施された
。而して上記の減圧工程は20〜30時間実施し、この
後の浸漬工程は40〜50時間程度実施し、20〜26
時間位定温にて放置するとよい、即ち有機酸化合物の細
多孔質材料各組織内への含浸定着を図る為である。
Now, this microporous material has a particle size of 300 to 400.
Using something similar to a mesh, it is immersed in an amount of organic acid compound equivalent to the weight ratio. At this time, under reduced pressure, that is, 0.
It is characterized by being carried out under a pressure of 8 to 0.98 atmospheres. That is, in the case of the conventional technique performed under normal pressure, the liquid organic acid compound adheres to the outermost surface of the porous material and does not penetrate into the tissue. Therefore, the total surface area of the fine porous material did not contribute effectively to freshness preservation or deodorization. However, when the process was carried out under reduced pressure, the liquid organic acid compound permeated into each pore more effectively. The above decompression step was carried out for 20 to 30 hours, and the subsequent immersion step was carried out for about 40 to 50 hours.
It is preferable to leave it at a constant temperature for a certain period of time, that is, to allow the organic acid compound to impregnate and fix within each structure of the microporous material.

以後、50〜70℃温風を用い、90〜100時間程度
、強制乾燥し含水率3〜7%にまで乾燥せしめ、続いて
粉砕し低分子ガス吸着触媒材とするものである。
Thereafter, it is forcedly dried using hot air at 50 to 70° C. for about 90 to 100 hours to a moisture content of 3 to 7%, and then pulverized to obtain a low-molecular gas adsorption catalyst material.

このようにして得た低分子ガス吸着触媒材は広義には食
品保存材、目的ごとには鮮度保持材、脱臭材、除湿材、
制菌材等として利用できる。使用態様としては、それ自
体を食品包装、容器の中に投入してもよく、即ち封入剤
として用いてもよく、フィルム、シート状体の中に混入
してもよく、塗布材、糊料中に混入してもよい。使用の
結果、野菜、果実、魚肉、畜肉等の生鮮食料品に対して
それから生ずるエチレンガスを吸着除去して、勝れた鮮
度保持効果があり、脱臭、制菌作用、変色防止作用が認
められた。
The low-molecular gas adsorption catalyst material obtained in this way can be broadly defined as a food preservation material, and can be used as a freshness-preserving material, deodorizing material, dehumidifying material, etc.
It can be used as a bacteriostatic material, etc. As for how it is used, it may be used in food packaging or containers, that is, it may be used as an encapsulant, it may be mixed into a film or sheet, or it may be used as a coating material or glue. May be mixed with As a result of its use, it adsorbs and removes the ethylene gas generated from fresh foods such as vegetables, fruits, fish, and livestock meat, and has an excellent freshness-keeping effect, as well as deodorizing, antibacterial, and discoloration prevention effects. Ta.

とりわけ、珪藻類を含む土の乾燥時間が著しく短縮され
量産性が付与されることと相まって、これを可能にする
乳酸発酵によって多糖類が増加されること、並びに細多
孔質材料の各孔隙1組織中に有機酸化合物がすみずみ迄
浸透するので、従来の繕程度の製品量で従来と略凹等の
諸効果が認められた。
In particular, the drying time of soil containing diatoms is significantly shortened and mass production is possible, the polysaccharide content is increased by lactic acid fermentation which makes this possible, and each pore structure of the microporous material is increased. Since the organic acid compound penetrates into every corner of the product, various effects such as almost denting were observed compared to the conventional product with the same amount of product as the conventional repair.

〔実施例〕〔Example〕

次に本発明製法の好適な実施例を詳述する。 Next, preferred embodiments of the production method of the present invention will be described in detail.

実施例1 含水率55%の珪藻類を含む土100 Kgに対し、糖
類を1Kg添加し、12時間経過後70℃に保持し、0
.3 m’ / hrの空気を連続供給しながら48時
間で乳酸発酵せしめ、その発酵熱により含水率30%に
乾燥し、それを粉砕して30メツシユアンダーの粒径の
有機酸抽出用原料を製造した。
Example 1 1 kg of sugars was added to 100 kg of soil containing diatoms with a moisture content of 55%, and after 12 hours, it was kept at 70°C and
.. Lactic acid fermentation was carried out for 48 hours while continuously supplying air at a rate of 3 m'/hr, and the fermentation heat dried the product to a moisture content of 30%, which was then ground to obtain a raw material for organic acid extraction with a particle size of 30 mesh. Manufactured.

これに重量部で10%相当の温水(95℃)を加え、9
5℃に保って一時間攪拌し、24時間かけて比重分離し
、濾過して、2ミクロン級の有機酸化合物を抽出した。
Add warm water (95°C) equivalent to 10% by weight to this, and
The mixture was stirred at 5° C. for 1 hour, subjected to specific gravity separation for 24 hours, and filtered to extract 2 micron-sized organic acid compounds.

その有機酸化合物を試験した新法の表1〜6の結果を得
た。
The new method tested the organic acid compounds and obtained the results shown in Tables 1-6.

表1 表2 一般性状試験成績 有害成分の試験成績 表3 各種金属の定量分析 表6 糖 分 析 結果 表4 表5 有 ア 機 酸 組 成 ノ酸分析結果 この後上記液状有411酸化合物250文中に300メ
アシユのパーライト100Kgを混合攪拌し、全体を0
.98気圧の減圧室に入れ、その状態でパーライトを有
機酸化合物中に浸漬した。この浸漬を24時間実施し、
以後48時間放置し、室温で120時間かけて乾燥し、
製品低分子ガス吸着材を得た。
Table 1 Table 2 General property test results Harmful component test results 3 Quantitative analysis of various metals 6 Sugar analysis results Table 4 Table 5 Organic acid composition NOA acid analysis results After this, 300 of the above liquid 411 acid compounds were found in 250 sentences. Mix and stir 100 kg of Meashiyu perlite, and make the whole 0.
.. The pearlite was placed in a vacuum chamber at 98 atmospheres and immersed in the organic acid compound in that state. This immersion was carried out for 24 hours,
After that, it was left for 48 hours and dried at room temperature for 120 hours.
A product low molecular gas adsorbent was obtained.

上記パーライトの化学的性質は次の表7の通りであった
・ 玉7 これを用いて鮮度保持能力試験を試みた。この結果は後
記する表8〜表14の鮮度保持能力比較試験結果として
記載する。この事から判る通り格段と鮮度保持能力が認
められた。
The chemical properties of the above pearlite were as shown in Table 7 below. Tama 7 A freshness retention ability test was attempted using this pearlite. The results are listed as the freshness retention ability comparison test results in Tables 8 to 14 below. As can be seen from this, it was recognized that the product had a remarkable ability to maintain freshness.

実施例2 上記実施例1で得たと同じ有機酸化合物300文を、3
50メツシユのサンゴ300Kgと混合攪拌し、0.9
8気圧に減圧された室でサンゴを有機酸化合物中に48
時間浸漬し、以後24時間定温保持し、60℃熱風を8
8時間かけ、含水率5%に乾燥し、粉砕して製品を得た
Example 2 300 grams of the same organic acid compound obtained in Example 1 above were
Mix and stir with 300 kg of coral of 50 mesh, 0.9
Corals are placed in an organic acid compound in a chamber with a reduced pressure of 8 atm.
After soaking for 24 hours, the temperature was maintained at a constant temperature for 24 hours.
It was dried for 8 hours to a moisture content of 5% and pulverized to obtain a product.

これを用いて鮮度保持能力試験を試みた。この結果も後
記する表8〜表14に記載する。
Using this, a freshness retention ability test was attempted. The results are also shown in Tables 8 to 14 below.

表10 表11 表13 表12 表14 上記表8〜表14に於いて、実施例1及び実施例2とは
実施例1及び2で各々製造した低分子ガス吸着触媒材を
0.03m/m X400■/■X EtOOm/腸の
フィルムに混入し、そのフィルムで各品名の検体を包入
し、温度20℃、湿度90%の室に放置してその変化を
観察したものである。又市販ポリフィルムとは、市販の
ポリフィルムで各品名の検体を包入し、上記と同じ条件
でその変化を観察したものである。
Table 10 Table 11 Table 13 Table 12 Table 14 In Tables 8 to 14 above, Example 1 and Example 2 refer to the low-molecular gas adsorption catalyst materials produced in Examples 1 and 2, respectively, at 0.03 m/m X400 ■/■ Moreover, commercially available polyfilms are those in which samples of each product name were encapsulated in commercially available polyfilms, and changes thereof were observed under the same conditions as above.

評価は「5」〜rlJの5段階で「5」は最高、「3」
は商品価値の限界で、夕方における店頭の状態を基準と
した。これらの事から判る通り生鮮食料品に対して鮮度
保持効果が認められた。
Rating is on a 5-point scale from "5" to rlJ, with "5" being the highest and "3" being the best.
is the limit of product value, and is based on the condition of the store in the evening. As can be seen from these facts, the effect of preserving freshness on fresh foods was observed.

〔効果〕〔effect〕

以上詳述した如くこの発明によれば、広義には食品保存
、目的ごとには鮮度保持、変色防止、脱臭、除湿等を有
効とする有機酸化合物が含浸せしめられた細多孔質材料
より成る低分子ガス吸着触媒材の製法を提供できること
は勿論のこと、有機酸抽出用原料の製造工程に於ける珪
藻類を含む土の乾燥段階を乳酸発酵下で実施し、その乳
酸発酵熱により乾燥するので短い時間の内に有機酸抽出
用原料を製造できると共に、この乳酸発酵により最終製
品に多糖類を増大せしめて含ますことができるから、鮮
度保持等の諸効果がよりよく発揮される。更に細多孔質
材料中に液状有機酸化合物を含浸させる工程も減圧下で
実施するので細条孔の各孔隙、組織内すみずみに有機酸
化合物が含浸するから、細孔に於けるガス吸着、等の諸
作用が効果的に発揮される低分子ガス吸着材の製法を提
供できる。
As detailed above, according to the present invention, in a broad sense, food preservation is possible, and for each purpose, it is effective to preserve freshness, prevent discoloration, deodorize, and dehumidify. Not only can we provide a method for producing molecular gas adsorption catalyst materials, but we can also carry out the drying stage of soil containing diatoms under lactic acid fermentation in the manufacturing process of raw materials for organic acid extraction, and dry it using the heat of lactic acid fermentation. Raw materials for organic acid extraction can be produced within a short period of time, and the lactic acid fermentation allows the final product to contain an increased amount of polysaccharides, so that various effects such as freshness retention are better exhibited. Furthermore, since the step of impregnating the liquid organic acid compound into the fine porous material is carried out under reduced pressure, each pore of the thin pores and every corner of the tissue is impregnated with the organic acid compound. It is possible to provide a method for producing a low-molecular gas adsorbent that effectively exhibits the following effects.

【図面の簡単な説明】[Brief explanation of the drawing]

添付図面第1図は製造工程図である。 FIG. 1 of the accompanying drawings is a manufacturing process diagram.

Claims (1)

【特許請求の範囲】 (1)珪藻類を含む土を乾燥すると共にそれを粉砕する
ことにより有機酸を高度に含む有機酸化合物の抽出用原
料を製造し、次いでその有機酸化合物の抽出用原料から
有機酸化合物を抽出し、続いて上記抽出した有機酸化合
物を細多孔質材料中に含浸せしめ、次いでそれを乾燥、
粉砕することによって製造する低分子ガス吸着触媒材の
製法に於いて; 上記珪藻類を含む土の乾燥工程は、珪藻類を含む土に糖
類を添加し乳酸発酵せしめてその際生ずる発酵熱を利用
して実施すると共に、上記細多孔質材料中に有機酸化合
物を含浸させる工程は、細多孔質材料を有機酸化合物中
に浸漬する時に減圧条件下で実施する事を特徴とする低
分子ガス吸着触媒材の製法。 (2)上記珪藻類を含む土に糖類を添加し乳酸発酵せし
めて、その際生ずる発酵熱によりこの珪藻類を含む土を
乾燥させる工程は、上記珪藻類を含む土に糖類を添加後
10〜14時間経過の後に、これらに空気を供給しつつ
且つこれらを60〜80℃の温度に保ちながら40〜5
5時間程度で実施し、もって含水率65〜50%程度の
珪藻類を含む土を上記発酵熱により含水率25〜35%
程度に乾燥させる事を特徴とする請求項第1項記載の低
分子ガス吸着触媒材の製法。 (3)上記珪藻類を含む土に添加する糖類は、重量部で
珪藻類を含む土の1%相当である事を特徴とする請求項
第2項記載の低分子ガス吸着触媒材の製法。 (4)上記有機酸化合物の抽出用原料から有機酸化合物
を抽出する工程は、有機酸化合物抽出用原料に対して温
水を加え、次いで定温攪拌し、続いて比重分離し、更に
濾過する事によって実施する事を特徴とする請求項第1
項記載の低分子ガス吸着触媒材の製法。 (5)上記有機酸化合物の抽出用原料に添加する温水は
、重量部で有機酸化合物の8〜12%相当であると共に
、定温攪拌工程は90〜95℃、30分〜1時間半実施
し、且つ比重分離工程は20〜24時間実施する事によ
り2〜5ミクロンの液状の有機酸化合物を抽出するもの
である事を特徴とする請求項第4項記載の低分子ガス吸
着触媒材の製法。 (8)上記細多孔質材料を有機酸化合物中に浸漬する時
に減圧条件下で実施する工程は、有機酸化合物と細多孔
質材料を混合攪拌後、0.8〜0.98気圧、20〜3
0時間で実施する事を特徴とする請求項第1項記載の低
分子ガス吸着触媒材の製法。 (7)上記細多孔質材料は、サンゴ、シリカゲル、活性
アルミナ、合成、天然ゼオライト、白陶土、蛭石より得
られるパーライト、麦飯石の中から選ばれたものである
事を特徴とする請求項第6項記載の低分子ガス吸着触媒
材の製法。
[Claims] (1) A raw material for extracting an organic acid compound containing a high degree of organic acid is produced by drying and pulverizing soil containing diatoms, and then a raw material for extracting the organic acid compound The organic acid compound is extracted from the organic acid compound, and then the extracted organic acid compound is impregnated into a fine porous material, which is then dried,
In the manufacturing method of a low-molecular gas adsorption catalyst material produced by pulverization; the drying process of the soil containing diatoms is performed by adding sugars to the soil containing diatoms, causing lactic acid fermentation, and utilizing the fermentation heat generated at that time. At the same time, the step of impregnating the organic acid compound into the fine porous material is carried out under reduced pressure conditions when the fine porous material is immersed in the organic acid compound. Manufacturing method of catalyst material. (2) The step of adding sugars to the diatom-containing soil, causing lactic acid fermentation, and drying the diatom-containing soil using the fermentation heat generated during the process is carried out from 10 to 30 minutes after adding sugars to the diatom-containing soil. After 14 hours, while supplying air to these and keeping them at a temperature of 60 to 80°C,
The process is carried out for about 5 hours, and the soil containing diatoms with a moisture content of about 65 to 50% is reduced to a moisture content of 25 to 35% by the above fermentation heat.
2. The method for producing a low-molecular gas adsorption catalyst material according to claim 1, wherein the material is dried to a certain degree. (3) The method for producing a low-molecular gas adsorption catalyst material according to claim 2, wherein the sugar added to the diatom-containing soil is equivalent to 1% by weight of the diatom-containing soil. (4) The step of extracting an organic acid compound from the raw material for extracting an organic acid compound is performed by adding warm water to the raw material for extracting an organic acid compound, stirring at a constant temperature, followed by specific gravity separation, and further filtration. Claim 1 characterized by carrying out
A method for producing a low-molecular gas adsorption catalyst material as described in Section 1. (5) The hot water added to the raw material for extraction of the organic acid compound is equivalent to 8 to 12% by weight of the organic acid compound, and the constant temperature stirring step is carried out at 90 to 95°C for 30 minutes to 1.5 hours. 5. The method for producing a low-molecular gas adsorption catalyst material according to claim 4, wherein the specific gravity separation step is carried out for 20 to 24 hours to extract a liquid organic acid compound with a size of 2 to 5 microns. . (8) The step of immersing the fine porous material in the organic acid compound under reduced pressure conditions is performed at 0.8 to 0.98 atm, 20 to 3
2. The method for producing a low-molecular gas adsorption catalyst material according to claim 1, wherein the method is carried out for 0 hours. (7) A claim characterized in that the fine porous material is selected from coral, silica gel, activated alumina, synthetic and natural zeolites, white china clay, perlite obtained from vermiculite, and maifan stone. 6. A method for producing a low-molecular gas adsorption catalyst material according to item 6.
JP1036879A 1989-02-16 1989-02-16 Production of catalytic material adsorbing low molecular gas Pending JPH02214539A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1036879A JPH02214539A (en) 1989-02-16 1989-02-16 Production of catalytic material adsorbing low molecular gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1036879A JPH02214539A (en) 1989-02-16 1989-02-16 Production of catalytic material adsorbing low molecular gas

Publications (1)

Publication Number Publication Date
JPH02214539A true JPH02214539A (en) 1990-08-27

Family

ID=12482066

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1036879A Pending JPH02214539A (en) 1989-02-16 1989-02-16 Production of catalytic material adsorbing low molecular gas

Country Status (1)

Country Link
JP (1) JPH02214539A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102425793B1 (en) * 2022-04-13 2022-07-27 박기호 Natural mineral Lumilite ecosystem restorating agent and method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR102425793B1 (en) * 2022-04-13 2022-07-27 박기호 Natural mineral Lumilite ecosystem restorating agent and method
KR102438279B1 (en) * 2022-04-13 2022-08-29 박기호 Natural mineral Lumilite ecosystem restorating agent and method
WO2023200046A1 (en) * 2022-04-13 2023-10-19 박기호 Ecological restoration agent using natural mineral lumilite and preparation method therefor

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