JP2001353429A - Method for producing microporous membrane made of plant waste as main raw material - Google Patents

Method for producing microporous membrane made of plant waste as main raw material

Info

Publication number
JP2001353429A
JP2001353429A JP2000169738A JP2000169738A JP2001353429A JP 2001353429 A JP2001353429 A JP 2001353429A JP 2000169738 A JP2000169738 A JP 2000169738A JP 2000169738 A JP2000169738 A JP 2000169738A JP 2001353429 A JP2001353429 A JP 2001353429A
Authority
JP
Japan
Prior art keywords
main raw
producing
raw material
microporous membrane
pressure
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
JP2000169738A
Other languages
Japanese (ja)
Inventor
Ryohei Mihara
良平 三原
Katsuhiro Mihara
功裕 三原
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
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 Individual filed Critical Individual
Priority to JP2000169738A priority Critical patent/JP2001353429A/en
Publication of JP2001353429A publication Critical patent/JP2001353429A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To provide a method for producing a novel filter utilizing waste plant material. SOLUTION: This method for producing porous filter is constituted in such a manner that bean-curd refuse, sawdust, waste paper and chaff are used as the main raw material, water is added to an oxidation reagent or a binder, a kneaded matter is prepared, thereafter, the kneaded matter is immediately charged into high temperature and pressure equipment, a prescribed heat and pressure are applied while cabonizing the kneaded matter and the cabonized kneaded matter is cooled after the application of heat and pressure is completed.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】豆腐、コーヒー、ビールの絞り粕、おから
や木紛のおかこ、古紙、籾殻等を主原料として活性炭か
ら細多孔質性膜を製造することに関するものである。
[0001] The present invention relates to the production of a fine porous membrane from activated carbon using tofu, coffee, beer squeezed cake, okara or wood powder, waste paper, rice husk, etc. as main raw materials.

【0002】[0002]

【従来の技術】豆腐、コーヒー、ビールの絞り粕、おか
らや木紛のおかこ、古紙、籾殻等は焼いて灰を、肥料に
使用する、炭化粉は吸湿性を利用して防腐措置の環境保
全に使う用途のみであり、特定用途の技術は見当たらな
いのです。
2. Description of the Related Art Tofu, coffee, beer pomace, okara and wood flour, waste paper, rice husk, etc. are burned to use ashes and fertilizers. It is only used for environmental protection, and there is no technology for a specific application.

【0003】[0003]

【発明が解決しょうとする課題】上記の豆腐、コーヒ
ー、ビールの絞り粕、おからや木紛のおかこ、古紙、籾
殻等は使う用途もなく、近年、環境の問題により、やっ
かいな物として扱い、産業廃棄物として処理されてい
る。そのもの廃棄物をもって、よりよい素材を製造する
ことを見いだし、上記の廃棄物を炭化して、その炭化物
の成分の種類を変化させることによりこの細孔径を1.
0umの範囲で制御した種々の膜を製造し、上記の材料
の用途を解決しょうとする課題です。
The above-mentioned tofu, coffee, beer pomace, okara and wood powder, waste paper, rice husk, etc. have no use. Treated and treated as industrial waste. It has been found that a better raw material can be produced using the waste itself, and the above-mentioned waste is carbonized, and the type of the component of the carbide is changed to reduce the pore size to 1.
It is an issue to manufacture various films controlled in the range of 0um to solve the use of the above materials.

【0004】[0004]

【課題を解決するための手段】課題を解決する手段の前
に膜を製造するという目的と用途では、上記炭化物から
1.0umの範囲で制御した膜を製造することが出来た
としたら、1.0umのサイズ膜であれば、分子の大き
さで分離出来るので理想的分子ふるい膜ができること
で、全世界の研究者達が必死に研究をしております。
(細綱目のサイズを1um分子とほぼ同じサイズ)とい
った小さな均一、且つ完全な膜が必要とされます。この
ような膜を作ることは、今のところはありません。ある
としたら使う用途として、例、二酸化炭素や水蒸素の分
離以外に自動車のディーゼル車から排出されるNO
微粒子(特に黒煙微粒子)の分離膜にも利用でき、これ
も緊急に解決を迫られている課題の一つです。
For the purpose and application of manufacturing a film before the means for solving the problem, if it is possible to manufacture a film controlled in the range of 1.0 μm from the above carbide, 1. With a 0 um size membrane, researchers can study the world by desperately trying to create an ideal molecular sieving membrane because it can be separated by the size of the molecule.
A small, uniform and complete membrane (the size of a fine mesh is about the same as a 1um molecule) is required. There is currently no way to make such a membrane. As applications that use Once there, eg, also be used for separation membranes of NO 2 and particulates emitted from diesel vehicles car other than the separation of carbon dioxide and water蒸素(particularly black smoke particles), which is also urgently solved Is one of the issues that are urgent.

【0005】分子ふるい膜の研究は、有機高分子膜を中
心に進められている国もあるが、たとえできたとしても
有機物は分子間結合が柔らかく、分子運動(ミクロブラ
ウン運動)を行なうため1um前後の超微細な孔の場
合、この分子運動により孔がふさがれてしまうという欠
点がありますが、材料は無機物の活性炭で分子結合が強
く超微細孔も明確に存在しているので、有機高分子材料
と比べ格段の透過量を有する等の特性を発揮します。無
機膜を活性炭で製造することに成功することでその膜は
成膜性が抜群に良く、さらに融着等の手法で簡単にシー
ルできる。
[0005] In some countries, research on molecular sieve membranes has been focused on organic polymer membranes. However, even if it is possible, organic substances have a soft intermolecular bond and perform molecular motion (micro-Brownian motion). In the case of ultra-fine pores before and after, there is a drawback that the pores are blocked by this molecular motion, but the material is inorganic activated carbon, which has strong molecular bonds and ultra-fine pores. Demonstrates characteristics such as having a remarkable amount of transmission compared to materials. By successfully manufacturing an inorganic film with activated carbon, the film has excellent film-forming properties and can be easily sealed by a technique such as fusion.

【0006】おから、おかこ、木紛、古紙、籾殻等の主
原材料を酸化反応剤には過酸化水素、水、結着剤を加え
PHを調整した、混練物を用いて、高温、高圧装置のシ
リンダーの中へ混練物を入れ加熱する。エネルギーは電
気ヒーターでよく温度制御は、センサーでも良い、電気
ヒーターにより温度800〜900℃に上昇させる。目
標温度はセンサーでよいが、シリンダーに入れた炭化物
を温度800〜900℃に上昇させ、いったん上昇した
らセンサーより、温度は停止される。スイッチ(ブレー
カー)が止まるのを確認して装置のピストンで炭化物を
押さえ、圧力5〜50気圧で数秒間圧を加える、大気温
度より、10〜20℃度高めで取り出しても良く、常温
で取り出しても良い、水洗いして、細多孔質性膜状フィ
ルター商品となる。
[0006] The main raw materials such as okara, oysters, wood powder, waste paper, rice hulls and the like are adjusted to pH by adding hydrogen peroxide, water and a binder as an oxidizing reactant. The kneaded material is put into the cylinder of the device and heated. The energy may be increased by an electric heater, and the temperature may be controlled by a sensor. The target temperature may be a sensor, but the carbide in the cylinder is raised to a temperature of 800 to 900 ° C., and once the temperature is raised, the temperature is stopped by the sensor. After confirming that the switch (breaker) stops, press the carbide with the piston of the device and apply pressure for several seconds at a pressure of 5 to 50 atm. It may be taken out at 10 to 20 ° C higher than the ambient temperature, or taken out at room temperature. It may be washed with water to obtain a fine porous membrane filter product.

【0007】本発明の酸化反応剤としては、水酸化カリ
ウム、過酸化水素、シリカ(SIO)でも良く、どれ
でも1点を使用する。また結着剤としては、アルキン酸
ナトリウム、木質系油のリクニンでどれでも1点で良
い、ガス体として、O、Nでも良い。
The oxidation reactant of the present invention may be potassium hydroxide, hydrogen peroxide or silica (SIO 2 ), and one of them is used. In addition, any one of sodium alkinate and lignin of wood-based oil may be used as the binder, and O 2 and N 2 may be used as the gas.

【0008】上記、混練物を加熱する時、酸化剤は脱水
と反応して水酸化カリウムと水が発生する、水(水蒸
気)が炭素と反応して一酸化炭素を生成することで、炭
素が消費され活性炭となり、その時細多孔質性増加す
る。またこの時、大気に出たガス(水酸化カリウム)は
最終的には炭酸カリウムになることで無害ガスとなる。
When the above kneaded material is heated, the oxidizing agent reacts with dehydration to generate potassium hydroxide and water, and water (steam) reacts with carbon to form carbon monoxide. It is consumed and becomes activated carbon, at which time the microporosity increases. Further, at this time, the gas (potassium hydroxide) released to the atmosphere becomes harmless gas by finally becoming potassium carbonate.

【0009】上記手段で得られた商品の特性としては、
細孔径(多孔体)より小さな分子は吸着することが出来
るが、大きな分子は吸着することが出来なく、本発明の
分子ふるい膜の作用を示す、可能性の素材細多孔質性膜
の製造方法にこげつけた。
The characteristics of the product obtained by the above means include:
Molecules smaller than the pore diameter (porous material) can be adsorbed, but large molecules cannot. It is possible to exhibit the effect of the molecular sieve membrane of the present invention. I was sorry.

【0010】[0010]

【発明の実施の形態】上記の原材料等と反応剤と結着剤
と水で混練物を得り、高温、高圧装置のシリンダーの内
へ混練物を入れ800℃に加熱して、炭化させ、その間
ピストンで圧を5気圧加げる、目標温度、圧を確認した
後電源を止め温度を低下させることで、商品細多孔質性
のふるい状になる。
BEST MODE FOR CARRYING OUT THE INVENTION A kneaded material is obtained from the above-mentioned raw materials and the like, a reactant, a binder, and water, and the kneaded material is placed in a cylinder of a high-temperature, high-pressure apparatus, heated to 800 ° C., and carbonized. In the meantime, a pressure of 5 atm is applied by the piston, and after confirming the target temperature and the pressure, the power supply is turned off and the temperature is lowered, whereby the product becomes a fine porous sieve.

【0011】[0011]

【実施例1】 1.主材料、コーヒーの絞り粕、おから水分80%のも
の500g 2.水酸化カリウム(86%含有)水溶性500g 3.シリカ(SIO 99%) 10 g 4.鉱物水溶液 5.上記、1+2+3を混練する材料を用いた。 6.高温、高圧装置3lを用いて、4の材料を装置のシ
リンダー内に入れ温度700℃で40分加熱した後ヒー
ター電源を止める。その時、装置内のピストンで圧を5
気圧加える。圧を加える時、バルブを15度角から順々
に開いて行き手作用で5〜10分で全開に開く。商品は
大気温度で取り出した。
Embodiment 1 1. Main material, coffee grounds, okara water 80% 500g 2. Potassium hydroxide (86% content) water-soluble 500 g 3. Silica (SIO 2 99%) 10 g Mineral aqueous solution 5. The material for kneading 1 + 2 + 3 was used. 6. Using a high-temperature, high-pressure apparatus 3l, put the material 4 into a cylinder of the apparatus, heat it at a temperature of 700 ° C for 40 minutes, and turn off the heater power. At that time, a pressure of 5
Add atmospheric pressure. When pressure is applied, the valve is opened sequentially from a 15-degree angle and fully opened by hand in 5 to 10 minutes. Products were removed at ambient temperature.

【実施例2】その他、原材料2種(豆腐、ビール)の絞
り粕も実施例1と同様の実験をした。結果は実施例1と
同様だった。
Example 2 In addition, the same experiment as in Example 1 was carried out for squeezed cake of two kinds of raw materials (tofu and beer). The results were the same as in Example 1.

【実施例3】 1.主材料、木粉のおかこ、古紙、籾殻、水分20%用
い、500g 2.水酸化カリウム(86%含有)150g 3.アルキン酸350g 4.結着剤鉱物水溶液 5.水10gを上記材料1+2+3+4で混練物を用い
た。 以下同様実施例1、同様で実施した結果実施例1同様
Embodiment 3 1. 1. Main material, wood flour, used paper, rice husk, 20% moisture, 500 g 2. 150 g of potassium hydroxide (containing 86%) 3. Alkynic acid 350 g 4. Aqueous binder mineral solution A mixture of 10 g of water and the above materials 1 + 2 + 3 + 4 was used. Hereinafter, the same operation as in Example 1 was performed, and the same result as in Example 1 was obtained.

【実施例4】実施装置ガラス、直径25、長さ1
10、T形を用いた。本発明品の左方向弁は、直
径22円筒形、長さ100、を用いた。そ
れに対して右方向弁は、従来の備長炭を発明同様直径2
の円筒形、長さ100のものに用いて、
Tの下部より20×50mm管から煙を流す装置
を用いた。T形の装置、Tの下部より煙を送り流す、右
方向に従来、市上の備長炭、左方向に発明品の廃材の活
性炭フィルターを取付け、各々受け実施したところ表1
に示す。
Example 4 Example device glass, diameter 25 m / m , length 1
A 10 m / m , T type was used. The left direction valve of the product of the present invention used a cylindrical shape having a diameter of 22 m / m and a length of 100 m / m . On the other hand, the right-hand valve uses a conventional Bincho charcoal with a diameter of 2
Used for 2 m / m cylindrical, 100 m / m long,
A device that allowed smoke to flow from a tube of 20 m / m × 50 mm from the lower part of T was used. T-type device, smoke wasted from the lower part of T. Conventionally, Bincho charcoal on the city was installed in the right direction, and activated carbon filter of waste material of the invention was installed in the left direction.
Shown in

【表1】 [Table 1]

【0012】[0012]

【発明の効果】上記の実施であるように、従来の備長炭
は分子が広く大きな物と、小さなものには分離出来て
も、小さい煙(ガス体)はだめだった。物質の比重差は
小さなサイズの細孔を有するフィルター通過出来ないこ
とを利用したもので、例えば、ノルマルブタンという分
子の大きさは、0.49nmで、イソブタンという0.
56nmである。よって粉のサイズの間の細孔径、例え
ば、ノルマルブタンとイソブタンが分離出来る。よって
二酸化炭素と窒素、酸素の分子サイズで分けることが困
難である。(ということは従来の備長炭である)発明品
活性炭フィルターの特性として細孔径より小さな分子は
吸着することが確認出来たことは、大きな煙(ガス)体
は吸着しないという、言い換えれば分子フルイ(フィル
ター)作用を示す可能性がある。今後は細孔構造の評価
や、単に通常の活性炭の置き換えではなく、高表面積活
性炭の特性を生かした利用方法を開発(検討)する。
As described above, the conventional Bincho charcoal has a large molecule and can be separated into a large one and a small one, but no small smoke (gas). The difference in specific gravity of the substance is based on the fact that the substance cannot pass through a filter having small-sized pores. For example, the size of the molecule of normal butane is 0.49 nm, and the molecular weight of isobutane is 0.4%.
56 nm. Thus, pore sizes between powder sizes, for example, normal butane and isobutane can be separated. Therefore, it is difficult to separate the molecular sizes of carbon dioxide, nitrogen and oxygen. As a characteristic of the activated carbon filter of the invention, it has been confirmed that molecules smaller than the pore diameter are adsorbed, which means that large smoke (gas) bodies are not adsorbed, in other words, molecular sieve ( (Filter) action. In the future, we will develop (examine) the evaluation of the pore structure and the utilization method that makes use of the characteristics of high surface area activated carbon instead of simply replacing ordinary activated carbon.

【0015】産業廃棄物とされる、廃材や活性炭として
利用することにより、社会に大きく貢献出来る技術と確
信して、やみません。
I am convinced that this technology can greatly contribute to society by using it as industrial waste, waste material or activated carbon.

【図面の簡単な説明】[Brief description of the drawings]

【図1】 本発明の実施例の工程を示すブロックであ
る。 1.主原料の混合混練ライン。 2.混練物を形成(ダンゴ状)に作る。 3.高温、高圧を装置機を用いその中に2を入れる。 4.加熱、加圧を行なう目的、温度、圧力を確認。 5.装置5のブルブを開く。 6 装置5から製品を取り出す(活性炭フィルター)。
FIG. 1 is a block diagram showing the steps of an embodiment of the present invention. 1. Mixing and kneading line for main raw materials. 2. The kneaded material is formed (dango-shaped). 3. High temperature and high pressure are used and 2 is put in it. 4. Confirm the purpose of heating and pressurization, temperature and pressure. 5. Open the burb of device 5. 6 Take out the product from the device 5 (activated carbon filter).

フロントページの続き Fターム(参考) 4D006 GA41 KE16Q KE16R MA22 MB03 MC05X NA05 NA39 NA62 PB64 PB65 PC80 4D012 BA01 CA01 CA03 CA15 CG05 4G066 AA04B BA03 BA23 CA28 CA35 CA43 DA01 DA02 EA09 FA03 FA20 FA23 Continued on front page F term (reference) 4D006 GA41 KE16Q KE16R MA22 MB03 MC05X NA05 NA39 NA62 PB64 PB65 PC80 4D012 BA01 CA01 CA03 CA15 CG05 4G066 AA04B BA03 BA23 CA28 CA35 CA43 DA01 DA02 EA09 FA03 FA20 FA23

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】豆腐、コーヒー、ビールの絞り粕、おから
や木材のおかこ、古紙、籾殻を主原料として細多孔質性
膜を製造することを特徴とする製造方法。
1. A method for producing a microporous membrane using tofu, coffee, beer pomace, okara and wood stalks, waste paper, and rice husk as main raw materials.
【請求項2】請求項1.の主原料の水分を調整しそれに
酸化反応剤と結着剤、水を加入して極超短波を与え混練
しながら、ゲル状化物を得り、高温、高圧で炭化加水分
解反応を行ない、細多孔質性膜を製造することを特徴と
する製造方法。
2. The method of claim 1. The water content of the main raw material is adjusted, and an oxidation reactant, a binder, and water are added to the mixture to give an ultra-high frequency wave and knead the mixture to obtain a gelled product. A method for producing a porous film.
【請求項3】請求項1.2.で細多孔質性製造に、高
温、高ガス圧を加入して、細多孔質性膜の大、小を制御
することを可能にした構成物質を種々に変化させ、分離
特性を変えることを特徴とする細多孔質性膜製造方法。
(3) Claim 1.2. By applying high temperature and high gas pressure to the production of microporous materials, it is possible to control the size and size of the microporous membrane in various ways and change the separation characteristics. A method for producing a fine porous film.
JP2000169738A 2000-04-27 2000-04-27 Method for producing microporous membrane made of plant waste as main raw material Pending JP2001353429A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
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Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
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Publications (1)

Publication Number Publication Date
JP2001353429A true JP2001353429A (en) 2001-12-25

Family

ID=18672553

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000169738A Pending JP2001353429A (en) 2000-04-27 2000-04-27 Method for producing microporous membrane made of plant waste as main raw material

Country Status (1)

Country Link
JP (1) JP2001353429A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7947114B2 (en) 2005-08-05 2011-05-24 Ntnu Technology Transfer As Carbon membranes

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7947114B2 (en) 2005-08-05 2011-05-24 Ntnu Technology Transfer As Carbon membranes

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