JPH0639277A - Active paddy husk and water purifying method using same - Google Patents

Active paddy husk and water purifying method using same

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Publication number
JPH0639277A
JPH0639277A JP4299110A JP29911092A JPH0639277A JP H0639277 A JPH0639277 A JP H0639277A JP 4299110 A JP4299110 A JP 4299110A JP 29911092 A JP29911092 A JP 29911092A JP H0639277 A JPH0639277 A JP H0639277A
Authority
JP
Japan
Prior art keywords
chaff
water
carbonized
activated
acid
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
JP4299110A
Other languages
Japanese (ja)
Inventor
In O Kim
寅 伍 金
Choong Eu Song
忠 儀 宋
Chan Seong Cheong
燦 成 鄭
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.)
Korea Advanced Institute of Science and Technology KAIST
Original Assignee
Korea Advanced Institute of Science and Technology KAIST
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 Korea Advanced Institute of Science and Technology KAIST filed Critical Korea Advanced Institute of Science and Technology KAIST
Publication of JPH0639277A publication Critical patent/JPH0639277A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/20Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Hydrology & Water Resources (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Water Treatment By Sorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Silicon Compounds (AREA)

Abstract

PURPOSE: To prepare an active chaff having increased surface area and adsorption ability from chaff and to utilize the active chaff for water cleaning treatment by adding an inorg. acid and/or an alkali to carbonized chaff or silver white color chaff, heating it, thereafter filtering and drying. CONSTITUTION: An aq. soln. of an inorg. acid (such as hydrochloric acid) and/or an alkali (such as sodium hydroxide) are (or) are added to carbonized chaff or silver white color chaff, and the added substance is heated, thereafter filtered and dried. For example, a 10% aq. soln. of hydrochloric acid is added to the carbonized chaff, which is heated under reflux, and thereafter cooled to the normal temp. The surface area of the active carbonized chaff is 114 m<2> /g, which is prepared by washing the content with water, neutralizing with an aq. NaOH soln., thereafter further washing with water, filtering and drying. As a result, the active chaff having increased surface area and adsorption ability can be prepared from chaff. Various toxic contaminating substances dissolved in water can be removed by using the active chaff.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、籾殻から表面積及び吸
着能力の大きい活性籾殻を製造する方法、並びにこれを
浄水処理過程に使用して各種の有害水質汚染物質を除去
する方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing activated rice husks having a large surface area and a high adsorption capacity from rice husks and a method for removing various harmful water pollutants by using the activated rice husks in a water purification process. .

【0002】[0002]

【従来の技術】人口の増加と産業の発達に伴い、各種の
生活廃水、農蓄産廃水、工業廃水等により、地表水の水
質は急速に悪化している。水質を汚染させる各種の有害
成分の中で特に問題になるのは、各種の有害有機物質
(トリハロメタン等、以下THMsという)、重金属、
残留毒性農薬及び洗剤等で、これら有害成分をより簡便
で経済的な方法で除去するための努力が世界的に活発に
行われている。
2. Description of the Related Art With the increase of population and the development of industry, the quality of surface water is rapidly deteriorating due to various domestic wastewater, agricultural wastewater, industrial wastewater and the like. Among various harmful components that pollute water quality, various harmful organic substances (trihalomethane, etc., hereinafter referred to as THMs), heavy metals,
Efforts to remove these harmful components with residual toxic pesticides and detergents by a simpler and more economical method are being actively carried out worldwide.

【0003】例えば、トリハロメタンは水中に溶解した
有機物がハロゲン原子と反応して生成するから、水処理
過程でTHMsの生成を抑制するには、i)原水に含ま
れる有機物質(THMsの前駆物質)を除去し、これの
濃度を極少化するか、ii)塩素消毒の代りに、二酸化塩
素かオゾンのようにトリハロメタン等を生成させない別
の消毒剤を使用しなければならない。この場合、強力な
酸化剤である二酸化塩素やオゾンは、水中の有機物質を
酸化させ、THMsを生成する前駆物質の濃度を減らす
ことになる。THMs前駆物質の濃度を減らす別の手段
としては、植物性活性炭で水中に含まれる有機物質等を
吸着、凝集、濾過する方法を挙げることができる。しか
し、これらの酸化剤及び活性炭は価格が高く、特にオゾ
ンの場合は、残留オゾンによる毒性を除くために、活性
炭層を通過して残ったオゾンを除去しなければならない
難点がある。
For example, trihalomethane is produced by reacting an organic substance dissolved in water with a halogen atom. Therefore, in order to suppress the production of THMs in a water treatment process, i) an organic substance contained in raw water (a precursor of THMs) Must be removed and the concentration thereof must be minimized, or ii) chlorine disinfection must be replaced with another disinfectant that does not produce trihalomethanes such as chlorine dioxide or ozone. In this case, chlorine dioxide and ozone, which are strong oxidizers, oxidize the organic substances in the water and reduce the concentration of precursors that produce THMs. As another means of reducing the concentration of the THMs precursor, there can be mentioned a method of adsorbing, aggregating and filtering an organic substance contained in water with plant activated carbon. However, these oxidizers and activated carbon are expensive, and in the case of ozone in particular, there is a drawback that ozone remaining after passing through the activated carbon layer must be removed in order to remove toxicity due to residual ozone.

【0004】[0004]

【発明が解決しようとする課題】本発明では、このよう
な公知技術の問題点を解消するため、米の生産時に副産
物として得られる籾殻から、表面活性の大きい所謂活性
籾殻を製造し、これを浄水過程に使用し、先に言及した
各種の有害汚染物質を効果的に除去することで、浄水処
理のための新しくしかも進歩した方法を提供する。
In the present invention, in order to solve the above-mentioned problems of the known art, so-called activated rice husk having a large surface activity is produced from rice husk obtained as a by-product at the time of rice production. It provides a new and improved method for water purification by using it in the water purification process and effectively removing various harmful pollutants mentioned above.

【0005】韓国の稲の生産量は、年間約547万トン
であり、副産物である籾殻も130余万トンに達する。
現在、籾殻は一般的な方法で炭化させ、製鉄所の熔湯
(鉄湯)保温剤として使用されている。炭化籾殻の組成
はシリケート(Si含有量約20〜30%)と炭素(約
30〜50%)が大部分であり、微量のカリウム、カル
シウム、マグネシウム、アルミニウム、鉄及びマンガン
等が含まれている。この炭化籾殻以外にも、炭素を完全
に酸化させ、大部分がシリケートである銀白色の籾殻も
又生産されている。
The annual production of rice in Korea is about 5.47 million tons, and the amount of rice husk as a by-product reaches 1.3 million tons.
At present, rice husks are carbonized by a general method and used as a heat retaining agent for molten metal (iron hot water) in an iron mill. The composition of the carbonized rice husk is mainly composed of silicate (Si content: about 20 to 30%) and carbon (about 30 to 50%), and contains a trace amount of potassium, calcium, magnesium, aluminum, iron, manganese and the like. . In addition to this carbonized rice husk, silver-white rice husk, which is a silicate mostly made by completely oxidizing carbon, is also produced.

【0006】[0006]

【課題を解決するための手段】本発明は、炭化籾殻又は
銀白色籾殻に、無機酸(塩酸、硫酸、硝酸、燐酸、HF
等)、及び/又はアルカリ(NaOH、KOH等)水溶
液を加え、加熱した後、濾過後、乾燥処理し、表面積と
それに伴う吸着能力を大きく増大させた活性籾殻の製造
方法である。本発明では、このように化学的処理によっ
て表面活性を増大させた籾殻を、各々活性炭化籾殻又は
活性銀白色籾殻と命名することにする。各種活性籾殻の
元素分析結果を第1表に示した。
The present invention provides carbonized rice hulls or silver white rice hulls with inorganic acids (hydrochloric acid, sulfuric acid, nitric acid, phosphoric acid, HF).
Etc.) and / or an alkali (NaOH, KOH, etc.) aqueous solution, and after heating, filtration and drying treatment, a method for producing active rice husk in which the surface area and the adsorbing capacity associated therewith are greatly increased. In the present invention, rice husks whose surface activity has been increased by such a chemical treatment are named activated carbonized rice husks or activated silver white rice husks, respectively. Table 1 shows the results of elemental analysis of various active rice husks.

【0007】[0007]

【表1】 [Table 1]

【0008】第2表に示すように、炭化籾殻は、処理前
には表面積が約103m2/gであったが、酸処理後には1
14m2/gに、アルカリ処理後には400〜450m2/gに
大きく増大した。又銀白色籾殻も、処理前には表面積が
4.6m2/gであったが、酸又はアルカリ処理後には6〜
8m2/gに若干増大した。
As shown in Table 2, the surface area of the carbonized rice hulls was about 103 m 2 / g before the treatment, but it was 1 after the acid treatment.
It increased to 14 m 2 / g and to 400 to 450 m 2 / g after alkali treatment. Also, the surface area of silver-white rice husks was 4.6 m 2 / g before the treatment, but after surface treatment with acid or alkali,
Slightly increased to 8 m 2 / g.

【0009】[0009]

【表2】 [Table 2]

【0010】[0010]

【表3】 [Table 3]

【0011】[0011]

【表4】 [Table 4]

【0012】この場合、炭化籾殻及び銀白色籾殻は、酸
及びアルカリ処理過程で水溶性シリケートと微量の金属
成分が除去され、新しい細孔を形成し、表面積が増加す
るものと考えられる。又活性炭化籾殻は、第2表の表面
分析結果に示すように、ミクロ細孔からマクロ細孔迄を
持っていて、特に有機物吸着に効果的な直径20Å以上
である細孔の表面積が180〜190m2/gで、全体表面
積の40〜50%を占めているのが特徴である。これと
は対照的に、既存の植物性活性炭の場合には、この範囲
の細孔の表面積は、原料によって異なるが全体表面積の
6〜30%(58〜210m2/g)であった。
In this case, it is considered that the water-soluble silicate and a trace amount of metal components are removed from the carbonized rice husk and the silver white rice husk during the treatment with acid and alkali to form new pores and increase the surface area. As shown in the surface analysis results in Table 2, the activated carbonized husk has micropores to macropores, and the surface area of the pores having a diameter of 20 Å or more, which is particularly effective for adsorbing organic substances, is 180 to It is 190 m 2 / g and occupies 40 to 50% of the total surface area. In contrast to this, in the case of existing plant activated carbon, the surface area of pores in this range was 6 to 30% (58 to 210 m 2 / g) of the total surface area depending on the raw material.

【0013】本発明の浄水又は廃水処理方法は、活性炭
化籾殻及び活性銀白色籾殻の増大した表面活性を利用
し、これをi)浄水処理過程で微細な粉末を投入する
か、ii)浄水過程の濾過槽に使用する既存の植物性活性
炭の代りに投入し、原水に溶解している各種の有機物
質、重金属成分、残留農薬成分、洗剤等を効果的に除去
することを特徴とする。
The method for treating water or wastewater of the present invention utilizes the increased surface activity of activated carbonized rice husks and activated silver white rice husks, i) adding fine powder in the water purification treatment process or ii) water purification process It is characterized in that it is put in place of the existing plant activated carbon used in the above-mentioned filtration tank to effectively remove various organic substances, heavy metal components, residual pesticide components, detergents and the like dissolved in raw water.

【0014】[0014]

【実施例】本発明による新しい吸着剤である活性炭化籾
殻と活性銀白色籾殻の製造方法、及び水中の各種有害物
質に対するこれらの除去能力について、次に実施例を挙
げてより詳細に説明する。
EXAMPLES The method for producing activated carbonized rice husks and activated silver white rice husks, which are new adsorbents according to the present invention, and their removal ability for various harmful substances in water will be described in more detail with reference to the following examples.

【0015】実施例1.活性炭化籾殻の製造 1.1.活性炭化籾殻(A)の製造 炭化籾殻60g をフラスコに入れ、10%塩酸水溶液7
00mlを加え、約2時間加熱還流した後、常温に冷却し
た。内容物を2〜3回水で洗浄し、NaOH水溶液で中
和した後、更に水で2〜3回洗い、濾過、乾燥した。こ
のようにして製造した活性炭化籾殻の表面積は114m2
/gであった。
Example 1. Production of activated carbonized rice husks 1.1. Production of activated carbonized rice husk (A) 60 g of carbonized rice husk was put in a flask and 10% hydrochloric acid aqueous solution 7
After adding 00 ml and heating under reflux for about 2 hours, the mixture was cooled to room temperature. The contents were washed with water 2-3 times, neutralized with an aqueous NaOH solution, further washed with water 2-3 times, filtered and dried. The surface area of the activated carbonized rice husk thus produced is 114 m 2
It was / g.

【0016】1.2.活性炭化籾殻(B)の製造 炭化籾殻60g をフラスコに入れ、10%NaOH水溶
液700mlを加え、約2時間加熱還流した後、常温に冷
却した。内容物を2〜3回水で洗浄し、稀塩酸で中和し
た後、更に水で2〜3回洗浄した。濾過、乾燥した活性
炭化籾殻の表面積は380〜450m2/gであった。
1.2. Production of Activated Carbonized Husk (B) 60 g of carbonized chaff was put in a flask, 700 ml of 10% NaOH aqueous solution was added, and the mixture was heated under reflux for about 2 hours and then cooled to room temperature. The contents were washed with water 2-3 times, neutralized with dilute hydrochloric acid, and then further washed 2-3 times with water. The surface area of the filtered and dried activated carbon hulls was 380 to 450 m 2 / g.

【0017】1.3.活性炭化籾殻(AB)及び活性炭
化籾殻(BA)の製造 炭化籾殻60g をフラスコに入れ、10%塩酸水溶液7
00mlを加え、約2時間加熱還流した後、常温に冷却し
た。内容物を2〜3回水で洗浄し、濾過した後、これを
更にフラスコに入れ、10%NaOH水溶液700mlを
加え、約2時間加熱還流した。常温に冷却した後、水で
2〜3回洗浄し、稀塩酸で中和した後、更に水で2〜3
回洗浄した。濾過後、乾燥した活性炭化籾殻(AB)の
表面積は216m2/gであった。上の実験を、アルカリ処
理次いで酸処理の順で行った場合の活性炭化籾殻(B
A)の表面積は294m2/gであった。
1.3. Manufacture of activated carbonized rice hulls (AB) and activated carbonized rice hulls (BA) 60 g of carbonized rice hulls were placed in a flask and 10% aqueous hydrochloric acid solution 7
After adding 00 ml and heating under reflux for about 2 hours, the mixture was cooled to room temperature. The contents were washed with water 2-3 times and filtered, and then placed in a flask, 700 ml of 10% NaOH aqueous solution was added, and the mixture was heated under reflux for about 2 hours. After cooling to room temperature, wash with water 2-3 times, neutralize with dilute hydrochloric acid, and then with water 2-3 times.
Washed twice. After filtration, the surface area of the dried activated carbonized rice hulls (AB) was 216 m 2 / g. Activated carbonized rice husks (B) when the above experiment was carried out in the order of alkali treatment and then acid treatment (B
The surface area of A) was 294 m 2 / g.

【0018】実施例2.活性銀白色籾殻の製造 実施例1.1及び1.3の方法と同様に、銀白色籾殻を
活性化した結果、表面積は6〜8m2/gであった。
Example 2. Production of activated silver white rice husks As a result of activating the silver white rice husks in the same manner as in Examples 1.1 and 1.3, the surface area was 6 to 8 m 2 / g.

【0019】実施例3.浄水処理過程で活性籾殻使用
時、水のpH、濁度、BOD、CODの変化測定 実施例1及び実施例2で製造した活性炭化籾殻(B)及
び活性銀白色籾殻(AB)を微細な粉末にした後、30
mgを原水1L に添加して約150rpm で30分間撹拌し
た。これにポリアルミニウムクロライド12mgを追加添
加した後、6分間更に撹拌した後約70rpm に速度を減
速させ、20分間更に撹拌した後室温に放置した。浮遊
物を完全に沈澱させた後、上澄液を取り、pH、濁度、B
OD及びCODを測定した。対照群には既存の植物性活
性炭を使用した。濁度はHACHRatio/XR 濁度計で測
定し、BODは公知資料["Standard Methods for the
Examination of Water and Waste Water", Washington
DC 17ed, (1989) 参照]に従い測定し、CODはDr. La
nge 社の分光光度計で測定した。
Example 3. Measurement of changes in pH, turbidity, BOD, and COD of water when activated rice husks are used in the water purification process A fine powder of activated carbonized rice husks (B) and activated silver white rice husks (AB) produced in Examples 1 and 2 30 after
mg was added to 1 L of raw water and stirred at about 150 rpm for 30 minutes. After additionally adding 12 mg of polyaluminum chloride, the mixture was further stirred for 6 minutes, then the speed was reduced to about 70 rpm, further stirred for 20 minutes and then left at room temperature. After the suspension was completely precipitated, the supernatant was taken and the pH, turbidity, B
OD and COD were measured. Existing plant activated carbon was used as a control group. Turbidity was measured with a HACH Ratio / XR Turbidimeter, and BOD was measured using known materials ["Standard Methods for the
Examination of Water and Waste Water ", Washington
DC 17ed, (1989)], and COD is Dr. La.
It was measured with a spectrophotometer manufactured by nge.

【0020】第3表に示したように、pH、濁度について
は、活性炭化籾殻(B)、活性銀白色籾殻(AB)、既
存植物性活性炭はすべて似た効能を現わしたが、BOD
とCODについては、活性炭化籾殻(B)で処理した場
合は活性銀白色籾殻(AB)や既存の植物性活性炭で処
理した場合よりもずっと優秀であった。
As shown in Table 3, with respect to pH and turbidity, activated carbonized rice husks (B), activated silver white rice husks (AB), and existing plant activated carbon all showed similar effects.
And COD were much better when treated with activated carbonized rice husk (B) than when treated with activated silver white rice husk (AB) or existing plant activated carbon.

【0021】[0021]

【表5】 [Table 5]

【0022】実施例4.浄水処理過程で活性籾殻使用
時、トリハロメタン生成濃度の測定 4.1.原水(水源池で採取)にポリアルミニウムクロ
ライド(12mg/L)とCl2(0.5ppm)を入れ、約15
0rpm で6分間撹拌した後、70rpm に撹拌速度を減ら
し、20分間更に撹拌した後、室温で放置した。浮遊物
が完全に沈澱した後、上澄液の一部を取り、生成したT
HMsの濃度を分析した。分析結果は第4表参照。
Example 4. Measurement of trihalomethane production concentration when using active rice husks in water purification process 4.1. Put polyaluminum chloride (12mg / L) and Cl 2 (0.5ppm) into raw water (collected at the water source pond),
After stirring at 0 rpm for 6 minutes, the stirring speed was reduced to 70 rpm, stirring was continued for 20 minutes, and the mixture was left at room temperature. After the suspension was completely settled, a part of the supernatant was removed to form T
The concentration of HMs was analyzed. See Table 4 for analysis results.

【0023】4.2.実施例4.1.から得た上澄液
を、植物性活性炭層(直径6cm×高さ20cm、280g)
又は活性炭化籾殻(B)層(直径6cm×高さ20cm、5
0g)を通じ、濾過した後、濾過液をガスクロマトグラフ
ィー(Purge and Trap, ECD)を利用し、THMsの濃度
を比較分析した。分析結果は第4表参照。
4.2. Example 4.1. The supernatant obtained from the above was used as a plant activated carbon layer (diameter 6 cm x height 20 cm, 280 g)
Or activated carbonized rice husk (B) layer (diameter 6 cm x height 20 cm, 5
After filtering through 0 g), the filtrate was subjected to gas chromatography (Purge and Trap, ECD) for comparative analysis of THMs concentration. See Table 4 for analysis results.

【0024】[0024]

【表6】 [Table 6]

【0025】実施例5.活性炭化籾殻(B)を使用し
た、水中の残留毒性農薬除去のための実験 本実験では、本発明により製造した活性炭化籾殻(B)
の残留毒性農薬に対する吸着、除去能力を、既存の植物
性活性炭と比較するために、毒性の強い殺虫剤であるダ
イアジノン、フェニトロチオン及びパラチオンを、各々
6ppm 、12ppm 及び18ppm の濃度で溶解している水
溶液(国内上水道水質基準値の300倍)を、植物性活
性炭層(直径6cm×高さ20cm、280g )又は活性炭
化籾殻(B)層(直径6cm×高さ20cm、50g)を通じ
て濾過した後、各濾過液をガスクロマトグラフィーを利
用して分析した。
Example 5. Experiment for Removing Residual Toxic Pesticide in Water Using Activated Carbonized Husk (B) In this experiment, the activated carbonized rice husk (B) produced by the present invention was used.
In order to compare its ability to adsorb and remove residual toxic pesticides from existing plant activated carbon, an aqueous solution in which the highly toxic insecticides diazinon, fenitrothion and parathion are dissolved at concentrations of 6 ppm, 12 ppm and 18 ppm, respectively. After filtering (300 times the standard value of water quality in Japan) through a plant activated carbon layer (diameter 6 cm x height 20 cm, 280 g) or activated carbonized rice hulls (B) layer (diameter 6 cm x height 20 cm, 50 g), each The filtrate was analyzed using gas chromatography.

【0026】第5表の結果からわかるように、植物性活
性炭層を通じて濾過した場合には、15L 目からダイア
ジノン、フェニトロチオン及びパラチオンが各々1.2
ppm、1.4ppm 及び3.2ppm の濃度で濾液から検出
されたが、活性炭化籾殻(B)層を通じて濾過した場合
には、30L 迄どの農薬も検出されなかった。
As can be seen from the results in Table 5, when filtered through the plant activated carbon layer, diazinon, fenitrothion and parathion were found to be 1.2 each from the 15th locus.
It was detected in the filtrate at concentrations of ppm, 1.4 ppm and 3.2 ppm, but no pesticide was detected up to 30 L when filtered through the activated charcoal husk (B) layer.

【0027】[0027]

【表7】 [Table 7]

【0028】実施例6.活性炭化籾殻(B)を利用し
た、水中に溶解したフェノールの除去ための実験 本実験では、本発明により製造した活性炭化籾殻(B)
の有機毒性化合物であるフェノールに対する吸着、除去
能力を、既存の植物性活性炭と比較するために、フェノ
ールが4.47ppm の濃度で溶解している水溶液(国内
上水道水質基準値の900倍)を、植物性活性炭層(直
径6cm×高さ20cm、280g)又は活性炭化籾殻(B)
層(直径6cm×高さ20cm、50g)を通じて濾過した
後、各濾過液をガスクロマトグラフィーを利用して分析
した。第6表の結果からわかるように、植物性活性炭層
を通じて濾過した場合には、15L 目から既に42ppb
のフェノールが濾液から検出されたが、活性炭化籾殻
(B)層を通じて濾過した場合には、15L 迄フェノー
ルが全く検出されず、30L を通過した後に12ppb の
フェノールが検出された。
Example 6. Experiment for Removal of Phenol Dissolved in Water Using Activated Carbonized Husk (B) In this experiment, the activated carbonized rice husk (B) produced by the present invention was used.
In order to compare the adsorption and removal capacity for phenol, which is an organic toxic compound of, with existing plant activated carbon, an aqueous solution containing phenol dissolved at a concentration of 4.47 ppm (900 times the standard value for domestic water supply water quality) Vegetable activated carbon layer (diameter 6 cm x height 20 cm, 280 g) or activated carbonized rice husk (B)
After filtration through a layer (diameter 6 cm x height 20 cm, 50 g) each filtrate was analyzed using gas chromatography. As can be seen from the results in Table 6, when filtered through a plant activated carbon layer, it was already 42 ppb from the 15th locus.
Of phenol was detected from the filtrate, but when filtered through the layer of activated charcoal husk (B), no phenol was detected up to 15 L, and 12 ppb of phenol was detected after passing 30 L.

【0029】[0029]

【表8】 [Table 8]

【0030】実施例7.活性炭化籾殻(B)を利用し
た、水中に溶解した界面活性剤の除去のための実験 本実験では、活性炭化籾殻(B)の陰イオン界面活性剤
に対する吸着、除去能力を、既存の植物性活性炭と比較
するために、4.47ppm のナトリウムドデシルベンゼ
ンスルホン酸水溶液(国内上水道水質基準値の約10
倍)を、植物性活性炭層(直径6cm×高さ20cm、28
0g)又は活性炭化籾殻(B)層(直径6cm×高さ20c
m、50g)を通じて濾過した後、各濾過液を吸光光度法
(メチレンブルー法)を利用して分析した。第7表から
わかるように植物性活性炭層の場合には、5L 目で既に
0.47ppm の界面活性剤が検出されたが、活性炭化籾
殻(B)層を通じて濾過した場合には、30L 迄殆ど検
出されなかった。
Example 7. Experiment for Removal of Surfactant Dissolved in Water Using Activated Carbonized Rice Husks (B) In this experiment, the ability of activated carbonized rice husks (B) to adsorb and remove anionic surfactants from existing plant To compare with activated carbon, an aqueous solution of 4.47 ppm of sodium dodecylbenzene sulfonic acid (about 10
Double the amount of the vegetable activated carbon layer (diameter 6 cm x height 20 cm, 28
0g) or activated carbonized rice husk (B) layer (diameter 6 cm x height 20 c
After filtering through m, 50 g), each filtrate was analyzed by absorptiometry (methylene blue method). As can be seen from Table 7, in the case of the plant activated carbon layer, 0.47 ppm of the surfactant was already detected at the 5th liter, but when filtered through the activated charcoal husk (B) layer, it was almost up to 30L. Not detected.

【0031】[0031]

【表9】 [Table 9]

【0032】実施例8.活性炭化籾殻を利用した、水中
に溶解した金属成分の除去のための実験(I) 5.1g のFeCl3 ・6H2 O、7.41g のCuC
2 、3.8g のMnCl2 ・4H2 O、15.93g
のZn(NO3)2 ・6H2 O、1.35g のCr(NO
3)2 ・9H2 O、0.6g のPb(NO3)2 及び0.1
g のCd(NO3)2 ・4H2 Oをフラスコに入れ、蒸留
水で満たして1L とした。この溶液10mlに100ppm
のHg2+溶液10mlを補い、35L に稀釈して使用し
た。この水溶液を植物性活性炭層(直径6cm×高さ20
cm、280g)又は各種活性炭化籾殻層(直径6cm×高さ
20cm、50g)を通じて濾過した後、各濾過液を原子吸
光分析器(AA)、誘導結合プラズマ分光器(ICP)
又は誘導結合プラズマ質量分析器(ICP−Mass)
を利用して分析した。第8表からわかるように、植物性
活性炭の場合には、1L 目から既に大部分の金属イオン
が濾液から検出されたが、活性炭化籾殻(AB)、活性
炭化籾殻(BA)又は活性炭化籾殻(B)層を通じて濾
過した場合には、Mn2+及びZn2+以外の大部分の金属
イオンは、30L を通過する迄殆ど検出されなく、特に
Cr3+、Pb2+及びHg2+イオンは、45L を通過する
迄全く検出されなかった。
Example 8. Experiment for Removal of Metal Components Dissolved in Water Using Activated Carbonized Husks (I) 5.1 g FeCl 3 .6H 2 O, 7.41 g CuC
l 2 , 3.8 g of MnCl 2 .4H 2 O, 15.93 g
Zn (NO 3 ) 2 .6H 2 O, 1.35 g of Cr (NO
3) 2 · 9H 2 O, 0.6g of Pb (NO 3) 2 and 0.1
g of Cd (NO 3 ) 2 .4H 2 O was placed in the flask and filled with distilled water to 1 L. 100ppm in 10ml of this solution
10 g of Hg 2+ solution was used and diluted to 35 L for use. This aqueous solution is used as a plant activated carbon layer (diameter 6 cm x height 20
cm, 280 g) or various activated carbonized rice husk layers (diameter 6 cm x height 20 cm, 50 g), and then each filtrate is analyzed by atomic absorption spectrometer (AA), inductively coupled plasma spectrometer (ICP)
Or inductively coupled plasma mass spectrometer (ICP-Mass)
Was analyzed. As can be seen from Table 8, in the case of plant activated carbon, most of the metal ions were already detected in the filtrate from the 1st eye, but activated carbonized rice hulls (AB), activated carbonized rice hulls (BA) or activated carbonized rice hulls were used. When filtered through layer (B), most of the metal ions other than Mn 2+ and Zn 2+ were barely detected until they passed through 30 L, especially Cr 3+ , Pb 2+ and Hg 2+ ions. Was not detected at all until it passed 45 L.

【0033】[0033]

【表10】 [Table 10]

【0034】[0034]

【表11】 [Table 11]

【0035】実施例9.活性炭化籾殻(B)を使用し
た、水中に溶解した金属成分の除去のための実験(II) 9.1.各種金属イオン水溶液の調製 1.44g のCd(NO3)・4H2 O、1.45g のH
g(NO3)2 、1.96g のPb(NO3)2 、0.38
g のMnCl2 ・4H2 O、0.769g のZnSO4
・6H2 O、0.054g のCr(NO3)・9H2 O、
0.254g のFeCl3 ・6H2 O、1.11g のC
uCl2 又は0.062g のCa(CH3 CO2)2 を各
々35L の水に溶かして使用した。
Example 9. Experiment (II) for removal of metal components dissolved in water using activated carbonized rice hulls (B) 9.1. Preparation of various metal ion aqueous solutions 1.44 g of Cd (NO 3 ) .4H 2 O, 1.45 g of H
g (NO 3 ) 2 , 1.96 g of Pb (NO 3 ) 2 , 0.38
g MnCl 2 .4H 2 O, 0.769 g ZnSO 4
6H 2 O, 0.054 g of Cr (NO 3 ) 9H 2 O,
0.254 g FeCl 3 .6H 2 O, 1.11 g C
uCl 2 or 0.062 g of Ca (CH 3 CO 2 ) 2 were used, each dissolved in 35 L of water.

【0036】9.2.実施例9.1で調製した各々の金
属イオン水溶液を、活性炭化籾殻(B)層(直径6cm×
高さ20cm、50g)を通じて濾過した後、各濾過液を原
子吸光分析器(AA)、誘導結合プラズマ分光器(IC
P)又は誘導結合プラズマ質量分析器(ICP−Mas
s)を利用し分析した。第9表に示すように、活性炭化
籾殻(B)は実験した大部分の金属イオンに対し優れた
吸着能力を示した。
9.2. Each aqueous solution of metal ions prepared in Example 9.1 was treated with an activated carbonized rice hull (B) layer (diameter 6 cm ×
After filtering through a height of 20 cm and 50 g), each filtrate was analyzed by atomic absorption spectrometer (AA), inductively coupled plasma spectrometer (IC).
P) or inductively coupled plasma mass spectrometer (ICP-Mas
s) was used for analysis. As shown in Table 9, the activated carbonized rice hulls (B) showed excellent adsorption ability for most of the metal ions tested.

【0037】[0037]

【表12】 [Table 12]

【0038】[0038]

【発明の効果】以上の幾つかの実験結果からわかるよう
に、本発明により製造した活性炭化籾殻は、非常に大き
い吸着能力とイオン交換能力により、水中の各種汚染物
質を凝集、吸着、濾過過程を通じて、効果的でしかも経
済的に除去することができる新しい吸着剤である。
As can be seen from the above experimental results, the activated carbonized rice husk produced according to the present invention has a very large adsorption capacity and ion exchange capacity, so that various pollutants in water are aggregated, adsorbed and filtered. Is a new adsorbent that can be effectively and economically removed through.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 炭化籾殻又は銀白色籾殻に、無機酸及び
/又はアルカリを加え、加熱した後、濾過、乾燥するこ
とを特徴とする、表面積と吸着能力の大きい活性籾殻の
製造方法。
1. A method for producing active rice husk having a large surface area and adsorption ability, which comprises adding inorganic acid and / or alkali to carbonized rice husks or silver white rice husks, heating, filtering and drying.
【請求項2】 無機酸が塩酸、硫酸、硝酸、HF及び燐
酸から選択された酸の水溶液である請求項1の活性籾殻
の製造方法。
2. The method for producing active rice husks according to claim 1, wherein the inorganic acid is an aqueous solution of an acid selected from hydrochloric acid, sulfuric acid, nitric acid, HF and phosphoric acid.
【請求項3】 アルカリが水酸化ナトリウム及び水酸化
カリウムから選択されたアルカリの水溶液である請求項
1の活性籾殻の製造方法。
3. The method for producing active rice husks according to claim 1, wherein the alkali is an aqueous solution of an alkali selected from sodium hydroxide and potassium hydroxide.
【請求項4】 請求項1〜3のいずれか1項の方法で製
造された活性籾殻を使用し、水中に溶解している各種の
有害汚染物質を除去することを特徴とする、浄水又は廃
水の処理方法。
4. Purified water or wastewater, characterized in that various kinds of harmful pollutants dissolved in water are removed by using the active rice husk produced by the method according to any one of claims 1 to 3. Processing method.
JP4299110A 1991-10-17 1992-10-13 Active paddy husk and water purifying method using same Pending JPH0639277A (en)

Applications Claiming Priority (2)

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KR910018329 1991-10-17

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