JPS607937A - Preparation of adsorbent for heavy metal - Google Patents

Preparation of adsorbent for heavy metal

Info

Publication number
JPS607937A
JPS607937A JP11384783A JP11384783A JPS607937A JP S607937 A JPS607937 A JP S607937A JP 11384783 A JP11384783 A JP 11384783A JP 11384783 A JP11384783 A JP 11384783A JP S607937 A JPS607937 A JP S607937A
Authority
JP
Japan
Prior art keywords
adsorbent
heavy metal
water
size
coal waste
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.)
Granted
Application number
JP11384783A
Other languages
Japanese (ja)
Other versions
JPH0325220B2 (en
Inventor
Shiro Ida
井田 四郎
Kenji Koike
小池 倹次
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.)
Mitsui Mining Co Ltd
Original Assignee
Mitsui Mining Co Ltd
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 Mitsui Mining Co Ltd filed Critical Mitsui Mining Co Ltd
Priority to JP11384783A priority Critical patent/JPS607937A/en
Publication of JPS607937A publication Critical patent/JPS607937A/en
Publication of JPH0325220B2 publication Critical patent/JPH0325220B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To prepare adsorbent for heavy metal of high performance inexpensively by crushing coal waste having a specified amt. of ash and carbonizing the coal waste after molding it. CONSTITUTION:Coal waste having 40-80wt% ash content is crushed, if necessary after drying, to <=100 mesh grain size. The crushed product is then mixed with an appropriate amt. of water and molded to desired shape and size. Tablets of 3-5mm. phi and 4-10mm. thickness are usually preferred usually because of its better water permeability and convenience in use when it is packed in a packed layer. The molded product is dried and charged to a carbonizing oven and is heated slowly to 700-1,000 deg.C in neutral or reducing atmosphere, maintained at the temp. for 5min-1hr to complete carbonization. The temp. elevating rate depends upon the size and shape of the molded product, but 3-20 deg.C/min is usually adequate. Obtd. adsorbent for heavy metals has extremely high adsorptivity for heavy metals such as Cd, Cu, Pb, ett.; the pressure drop in the stage of loading water is small, the material has high strength and high water resistance, and is durable for long term use and recurrent use after regeneration and inexpensive.

Description

【発明の詳細な説明】 本発明は谷柚重金属知を含む工業排水等の処理に有用な
班金嬌吸唐剤の製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a chemical agent useful for treating industrial wastewater, etc., which contains a heavy metal chloride.

谷紳の化学工業あるいは鉱業における排水には神々の重
金椙知を含むものが多く環境汚染防止のため厳しい排出
規制が行なわれている。これらの取金属知を含む排水に
ついては種々の処理方法が(U)死されており、水酸化
物沈殿法、硫化物沈殿法。
Many of the wastewater from the chemical industry or mining industry in Tanishin contains the divine Shigekin Suchi, and strict discharge regulations are in place to prevent environmental pollution. Various treatment methods have been used for wastewater containing these metals, including the hydroxide precipitation method and the sulfide precipitation method.

還元法、浮選法、フェライト法、イオン又換法。Reduction method, flotation method, ferrite method, ion exchange method.

1!k ン7i法などの中からそれぞれの排出蔚に最も
適した処理方法により処理されている。そして環境基3
17%値が厳しく、極めて高度の処理を必要とする場合
の排水処理方法としては活性炭、イオン交換樹脂などを
用いる吸看法が最適であるといわれている。しかしなが
らこの吸温法は、特に倣」d:の汚染物の除去に著しい
効果を発揮するが、比較的高価な吸着剤を必要とするた
め経済的な観点から実用化が制限されており、安価な吸
着剤の開発が望まれている。
1! The waste sludge is treated using the most suitable treatment method for each type of sludge, such as the 7i method. and environmental group 3
In cases where the 17% value is severe and extremely sophisticated treatment is required, it is said that the best method for treating wastewater is the absorption method using activated carbon, ion exchange resin, etc. However, although this endothermic method is particularly effective in removing pollutants, it requires a relatively expensive adsorbent, which limits its practical application from an economic standpoint. The development of a new adsorbent is desired.

従来この種の重金IA頬を含む排水の処理に用いられ、
あるいは病死されている吸着剤としてはイオン父換樹脂
、活性炭、珪酸塩類などがあるがいずれも比較的高価で
あり、また多くは粉末状の形態で取扱いにりく、大量の
排水の処理には不適当であった。
Traditionally, it has been used to treat wastewater containing this type of heavy metal IA,
In addition, adsorbents that have died due to disease include ionic father exchange resins, activated carbon, and silicates, but they are all relatively expensive, and most are in powder form and difficult to handle, making them unsuitable for treating large amounts of wastewater. It was appropriate.

大量の排水処理に適した充填層形式で排水処理を行なう
ためにはこれらの吸着剤を成型して使用するのが好都合
であるが、その場合成型物の弓!Ii匪が弱く長時間あ
るいはくり返しの使用に耐えられなかったり、成型によ
り比表面積が減少して圧損失が大きくなったり、吸着能
力が低下するなどの問題があった。また石炭を成型し、
乾留賦活して得られる成型活性コークスも吸着剤として
用いらパれているが重金Ut4知に対する吸沿能カレま
イL(い。
In order to treat wastewater in a packed bed format suitable for treating large amounts of wastewater, it is convenient to use these adsorbents in a molded form, but in that case, the shape of the molded material is too small! There were problems such as the Ii strength was weak and could not withstand long-term or repeated use, the specific surface area decreased due to molding and the pressure loss increased, and the adsorption capacity decreased. It also molds coal,
Molded activated coke obtained by carbonization activation is also used as an adsorbent, but it has poor adsorption capacity for heavy metals.

本元明者らは重金属類を含む排水処理方法についてイ、
!iI々検討の結果、−iA当な比率で灰分を含41′
1″る石炭ボタを成型し、乾留することにより従来σ)
欠点の改良されlこ高性能の軍金椙吸后剤を安価にjj
4造できることを見出した口 本発明ハ灰分が40〜80重量%である石炭7](夕を
粉砕し、そσ)粉砕物を成型したσ)ち最高温波700
〜1000’ct乾留することによる31i金1・へ吸
シ(’)斉11の製造方法である。
Akira Motomoto et al.
! As a result of various studies, -iA contains ash at a reasonable ratio of 41'
Conventional σ)
This high-performance gunkin sorbent is available at a low price with its shortcomings improved.
The present invention has found that it is possible to produce a coal with an ash content of 40 to 80% by weight.
This is a method for producing 31i gold 1.hesi(')ki 11 by carbonizing ~1000'ct.

本発明の重金属吸着剤は次のようにして製造する。丁な
わち灰分が40〜80重開1%である石炭ボタを必要に
より乾燥したのち100メ・ノシュリ、下の粒度に漏J
砕する。次いで適量σ)水を加えて十分に混イII L
 r r望の形状、大きさに成型する・通常は3〜5 
n+mφ×4〜1offlIl+のタブレット型が充填
層に充填した場合の通水性もよく使い易い。こσ)15
5E型r吻を乾Q)A代乾υ1炉に入れ、中性あるいは
還元雰囲気下で徐々に700〜1000℃まで昇温し、
5分〜1時間保って乾留を終る。列温速度は成型物の大
きさ。
The heavy metal adsorbent of the present invention is manufactured as follows. Coal shavings with an ash content of 40 to 80% are dried as necessary, and then 100 ml of coal is poured into the lower particle size.
crush. Next, add an appropriate amount σ) of water and mix thoroughly.
Mold into desired shape and size - usually 3 to 5
When a tablet type of n+mφ×4 to 1offlIl+ is filled in a packed bed, water permeability is good and easy to use. σ)15
Put the 5E type r snout into a drying Q) A-temperature drying furnace and gradually raise the temperature to 700 to 1000°C in a neutral or reducing atmosphere.
Hold for 5 minutes to 1 hour to complete carbonization. The heating speed depends on the size of the molded product.

形状にもよるが辿當毎分3〜20℃程度が適当である。Although it depends on the shape, a temperature of approximately 3 to 20°C per minute is appropriate.

昇温速度が半丁ぎると成型物の部分的な膨張や亀裂の原
因となり、均質で強度の茜い製品をイ(することかでき
ない。また乾留温度が低すぎると比表面積が小で製品強
度が強くならず、灰分中の成分の適正な反応が起らず、
その結果強い吸虐力を示さない。乾留温肢は最高100
0℃程度で充分であり、これ以上冒くすることはエネル
ギーσ)無駄になり1寸た吸沼剤の性能も低下する卸同
にある。
If the heating rate is too low, it may cause partial expansion or cracking of the molded product, making it impossible to produce a homogeneous and strong madder product.Also, if the carbonization temperature is too low, the specific surface area will be small and the strength of the product will be reduced. It is not strong, and the components in the ash do not react properly.
As a result, it does not show strong sucking power. Maximum carbonization temperature is 100
A temperature of about 0°C is sufficient; increasing the temperature any further will waste energy (σ) and reduce the performance of the swamp absorbent.

石炭ボタ中の灰分叫、が少な′1−きるとIl重金・、
フル類の吸ンj■能力が低下し、また粒子の粘漕力が低
下するので成型がしにくくなる。また灰分が多丁ぎると
製品の細孔構造1強度などの性状が劣化する。
There is little ash content in the coal pile.
The suction ability of the particles is reduced, and the viscous force of the particles is reduced, making it difficult to mold. Furthermore, if the ash content is too high, the properties such as the pore structure 1 strength of the product will deteriorate.

原料の石炭ボタは石炭の採掘1選炭1稈から生ずる石炭
を含んだ粘土鉱物を生成分とする副雄物であって1通常
は特に成分のhl、−1整をすることなく使用て゛きる
が、ボタの成分は産炭地や選炭処理方法等により異なる
ので特定の成分が不足する場合には必要成分を補充1−
ることにλり成分を調整して使用すれはよい。中でも本
発明の原料としてイ史用J−るには微粉ボタを主成分と
する石炭スライムが特に好都合である。またカルシウム
分の含有量の多いボタ(例えば三池炭ボタ)を使用する
と重金属類の捕Its h’Q力が峙て同上し、また処
理液σ)pHが一般的に重金属励の処理に適したアルカ
リ側になるので好4115合である。
The raw material, coal shavings, is a secondary product made from coal-containing clay minerals produced from coal mining, coal preparation, and culm, and can usually be used without adjusting the ingredients. The components of botata differ depending on the coal production area and coal preparation processing method, so if a specific component is lacking, replenish the necessary components 1-
In particular, it is good to adjust the λ component before use. Among these, coal slime containing finely divided coal as a main component is particularly suitable for use as a raw material in the present invention. Furthermore, if a pot with a high calcium content (for example, Miike charcoal pot) is used, it will have a high ability to trap heavy metals, and the pH of the treatment solution is generally not suitable for heavy metal excitation treatment. Since it is on the alkaline side, it is a good value of 4115.

本製造方法において、原料中に含まれる谷1戊分が乾箱
゛中にどのような形で反応し、また製品中にv+11”
Jなる形で存在するのか明イ亀ではないか、恐らく珪素
及びカルシウム分がボタ中に含1れる他の成分も臼めて
複雑な形で結合して、より吸尤性能を高めており1石炭
酸分は粘結剤の役割を果てとともに炉内を・還元雰囲気
とし、かつ比表面積を太きくシ、圧損失の少ない製品σ
)形成に役立っているものと推足される。1だ原A゛1
中に適切な比吊で石炭成分と粘土成分を含んでいるのt
特別な成型用バインダーを必要とゼす、水のみで成型す
ることかできるオl」点がある。
In this manufacturing method, how does the v+11'' contained in the raw materials react in the dry box?
I wonder if it exists in the form of J or not, but it is probably because the silicon and calcium components are combined with other components contained in the bottle in a complicated form, increasing the absorption performance. The carbonic acid content fulfills its role as a binder, creates a reducing atmosphere in the furnace, and creates a product with a large specific surface area and low pressure loss.
) is considered to be helpful in the formation of 1 dahara A゛1
Contains coal components and clay components in appropriate proportions.
There is an option that requires a special molding binder and can be molded using only water.

本児明Q)方法によれは、ルる乗物である石炭ボタを利
用して高性能の重合数1.i吸尤剤を製造づ−ることか
でき、その利用価値は極めて高いものである0本発明の
方法による重金属吸着剤は次のような特徴を有しており
1重金に石を含イ1する排水の処理、特に6填Jti7
形式による処理に好適である。
Akira Honji Q) According to the method, high performance polymerization number 1. The heavy metal adsorbent produced by the method of the present invention has the following characteristics, and one heavy metal contains no stone. Treatment of wastewater, especially 6-fill Jti7
Suitable for formal processing.

l)重金属類の吸崩能力が極めて高い。l) Extremely high ability to absorb and disintegrate heavy metals.

2)比表面積が大きく、適度の細孔4’44造を11シ
ており1粒1規もそろっているので装入密り現0.8以
」二で均一な充Ji+、tが可能であり1通水+1!]
、の圧j11失も小P〜 3)製品σ)強度が大で面1水性もあり、長時間の使用
やTlr生してのくり返し1更1月に耐えることができ
る。
2) It has a large specific surface area, has 11 pores with a suitable size of 4'44, and each grain is evenly spaced, so uniform charging is possible with a charging density of 0.8" or more. Yes 1 water + 1! ]
3) The product σ) has high strength and is water-resistant, so it can withstand long-term use and repeated TLR growth.

4)原料が入手し易く、その調整も面卯−で製造が容易
なので安価″1:あ之)。
4) It is inexpensive because the raw materials are easily available and the preparation is simple and easy to manufacture.

見、下’X b1Q+?’t 、 比i1*Efll 
m 参考例K ヨ’) 本’A 明&) 7j法を具体
的に説明する。
Look, bottom'X b1Q+? 't, ratio i1*Efl
m Reference Example K Yo') Book A Akira &) The 7j method will be explained in detail.

実施例及び比較例 表1に示す組成の石炭ボタを乾燥し200メツシユ以下
の粒度に粉砕した。次いて少量の水を加え。
Examples and Comparative Examples Coal shavings having the composition shown in Table 1 were dried and ground to a particle size of 200 mesh or less. Then add a little water.

よく混和したものをベレッターにより3皿11φ×5柵
のタブレット状に成型した。この成型品を乾燥したのち
300〜350℃に調整した小型ロータIJ−キルンに
装入して徐々に昇171′AL表2て示1−条件で乾留
したのち冷却し製品を得た。イれぞれの製造条件及び製
品のI吻性値を表2に示す。
The well-mixed mixture was molded into tablets of 11φ x 5 bars in 3 plates using a beretter. After drying this molded product, it was charged into a small rotor IJ-kiln adjusted to 300-350°C and gradually raised to 171' AL under the conditions shown in Table 2, followed by carbonization and cooling to obtain a product. Table 2 shows the manufacturing conditions and I-nasality values of each product.

なお3y= 2中の強j民は次のようにして側鴛した。In addition, the strong people in 3y = 2 were sidekicked in the following manner.

J I 8−J+−s 801に記載されているロヵ試
験方法の側に装置を用い、1ず回転ドラム内に1叫1以
上のh・(料35 fを装入する。次にドラムを100
0回転(50rpm)壊せたのち内容物を1前11の篩
で篩分は静その前i J=、 !lj拓二乞絆り次式で
表示する。1だ浸水後の強度は試料を水中に48時間浸
漬したのち乾燥し。
Using the equipment on the side of the Roca test method described in J I 8-J+-s 801, first charge 35 f of 1 or more h·(35 f) into the rotating drum. 100
After 0 revolutions (50 rpm), sift the contents through a No. 11 sieve. Displayed in the following format: The strength after being immersed in water for 1 hour was determined by immersing the sample in water for 48 hours and then drying it.

上記の方法で411]足した 参考イ511 実施例、比較例により製造した重金属吸沼剤及びその他
の吸沼剤を用いて谷独重金属類σ)吸温試験を行なった
411] added by the above method Reference A 511 A Tanidoku heavy metals σ) thermoabsorption test was conducted using the heavy metal swamp absorbents and other swamp absorbers produced according to the Examples and Comparative Examples.

(試験方法l) 101)I)m O)濃r[になるように各種金属イオ
ンを溶解させた標準液をつくり、各々の標準液100M
eを取りp)]を2.4,6,8.10の5段階に調整
したのち央h’D例、比較例の重金属吸λ斤剤及びその
他の吸凋剤を粉砕したもθ)それぞれ0.45’7加え
て2時間振とうしたのち1別し、P液中に残存する金属
イオン藏ヒ乞6111ボした。最適pH値におけるfi
l11足結果を表3に示すが実施例の重金11口吸AI
剤を用いると悼めて効率よく除去嘔れていることがわか
る。
(Test method l) 101) Prepare standard solutions in which various metal ions are dissolved so that I) m O) concentration r [100M of each standard solution.
After taking e and adjusting p)] to 5 levels of 2.4, 6, 8.10, the heavy metal absorbent and other absorbent of central h'D example and comparative example were crushed and θ) respectively. 0.45'7 was added and after shaking for 2 hours, the solution was separated and the metal ions remaining in the P solution were removed. fi at optimum pH value
Table 3 shows the results of 11 pairs of heavy gold 11 mouth suction AI of the example.
It can be seen that the use of the drug effectively removes vomiting.

乾留温度の低い比較例−1のサンプルは眩7a能力が低
く、灰分の含+=T位が少ない比較例−2では成型がし
にくいため製品の歩留りが悪く、また吸凋能力も低目で
ある。さらに灰分、L℃の多い比較例−3では製品強+
Ks−が著しく低下した。
The sample of Comparative Example-1, which has a low carbonization temperature, has a low glare 7a ability, and the sample of Comparative Example-2, which has a low ash content in the be. Furthermore, in Comparative Example-3 with high ash content and L℃, the product strength was +
Ks- decreased significantly.

(試1朕方法2) 天施例10重金机吸毒剤7 o m、eを141no+
φのガラス管に−150m+nの高きで充填し重金15
4随の1013pm 浴液を700m4/h+θ)速度
で通液し2時間毎にj、h過液をサンプリングし残存#
を現を測置L 7;:。結果は図1に示すとおりで長時
間にわたり効率よく除去されていることがわかる。
(Trial 1, Method 2) Heavenly Example 10 Heavy metal machine absorbent 7 o m, e 141no+
Fill a φ glass tube to a height of -150m+n with heavy metal 15
4) Pass the bath solution at a rate of 700 m4/h + θ) and sample the filtrate every 2 hours to determine the remaining #
Measure the current L 7;:. The results are shown in Figure 1, and it can be seen that the particles were efficiently removed over a long period of time.

表 1 4、(ツ1面の簡単な刊兄明 図1は実Ir10111に韮る吸姶剤Q)吸沿試験結多
)ミを示す 特許出紳人 三井鉱山株式会社
Table 1 4, (Simple publication on page 1) Figure 1 shows a patent for an absorbent Q that is similar to real Ir10111) Mitsui Mining Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 1、灰分が40〜80重量%である石炭ボタを粉砕し、
その粉砕物を成型したのち最高温度700〜1000℃
で乾留することを特徴とする重金tIi吸沿剤の製造方
法。
1. Crush coal shavings with an ash content of 40 to 80% by weight,
After molding the pulverized material, the maximum temperature is 700-1000℃.
A method for producing a heavy metal tIi absorption agent, which comprises carbonizing the heavy metal tIi absorbent.
JP11384783A 1983-06-24 1983-06-24 Preparation of adsorbent for heavy metal Granted JPS607937A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11384783A JPS607937A (en) 1983-06-24 1983-06-24 Preparation of adsorbent for heavy metal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11384783A JPS607937A (en) 1983-06-24 1983-06-24 Preparation of adsorbent for heavy metal

Publications (2)

Publication Number Publication Date
JPS607937A true JPS607937A (en) 1985-01-16
JPH0325220B2 JPH0325220B2 (en) 1991-04-05

Family

ID=14622546

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11384783A Granted JPS607937A (en) 1983-06-24 1983-06-24 Preparation of adsorbent for heavy metal

Country Status (1)

Country Link
JP (1) JPS607937A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62247541A (en) * 1986-04-18 1987-10-28 Nippon Telegr & Teleph Corp <Ntt> Interelement isolation structure of integrated circuit and manufacture thereof
EP0739858A3 (en) * 1995-04-27 1997-09-17 William C Rose Liquid separator and polishing filter thereof

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5110838A (en) * 1974-07-16 1976-01-28 Mitsubishi Chem Ind SUICHUBOOTORYO
JPS5549540A (en) * 1978-10-04 1980-04-10 Hitachi Ltd Electronic fuel injection device

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5110838A (en) * 1974-07-16 1976-01-28 Mitsubishi Chem Ind SUICHUBOOTORYO
JPS5549540A (en) * 1978-10-04 1980-04-10 Hitachi Ltd Electronic fuel injection device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62247541A (en) * 1986-04-18 1987-10-28 Nippon Telegr & Teleph Corp <Ntt> Interelement isolation structure of integrated circuit and manufacture thereof
EP0739858A3 (en) * 1995-04-27 1997-09-17 William C Rose Liquid separator and polishing filter thereof

Also Published As

Publication number Publication date
JPH0325220B2 (en) 1991-04-05

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