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JPS632237B2 - - Google Patents
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JPS632237B2 - - Google Patents

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Publication number
JPS632237B2
JPS632237B2 JP57153195A JP15319582A JPS632237B2 JP S632237 B2 JPS632237 B2 JP S632237B2 JP 57153195 A JP57153195 A JP 57153195A JP 15319582 A JP15319582 A JP 15319582A JP S632237 B2 JPS632237 B2 JP S632237B2
Authority
JP
Japan
Prior art keywords
water
crystallization material
ions
crystallization
hydroxyapatite
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP57153195A
Other languages
Japanese (ja)
Other versions
JPS5942087A (en
Inventor
Hiroji Seki
Masaaki Ichinose
Naohisa Ueda
Takao Mineo
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.)
Ataka Kogyo KK
Original Assignee
Ataka Kogyo KK
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 Ataka Kogyo KK filed Critical Ataka Kogyo KK
Priority to JP15319582A priority Critical patent/JPS5942087A/en
Publication of JPS5942087A publication Critical patent/JPS5942087A/en
Publication of JPS632237B2 publication Critical patent/JPS632237B2/ja
Granted legal-status Critical Current

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  • Removal Of Specific Substances (AREA)
  • Water Treatment By Sorption (AREA)

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は水中リン酸イオンをヒドロキシアパタ
イトとして骨炭よりなる晶析材に晶析させて除去
するための水処理用晶析材の活性化方法に関す
る。
[Detailed Description of the Invention] [Technical Field of the Invention] The present invention relates to a method for activating a crystallizing material for water treatment for crystallizing and removing phosphate ions in water as hydroxyapatite in a crystallizing material made of bone char. .

〔発明の技術的育景とその問題点〕[Technical development of inventions and their problems]

一般に人体排泄物あるいは洗剤には有機リン化
合物あるいは無機性リン酸塩が様々の状態で存在
しているが、これらは下、廃水中に排出される場
合が多く、しかも通常の下、廃水処理工程では十
分に除去されることなく大部分が無機リン酸イオ
ンとして水中に残存する。そして、このリン酸イ
オンは環境水域の富栄養化をもたらし、水質を汚
濁して公害発生の原因となるので、このリン酸イ
オンを除去するための第3次処理(高度処理)が
必要とされる。
Generally, organic phosphorus compounds or inorganic phosphates exist in various states in human excreta or detergents, but these are often discharged into wastewater, and moreover, during normal wastewater treatment processes, However, most of the phosphate ions remain in the water as inorganic phosphate ions without being sufficiently removed. These phosphate ions cause eutrophication of environmental water bodies, contaminate water quality, and cause pollution, so tertiary treatment (advanced treatment) is required to remove these phosphate ions. Ru.

従来、リン酸イオンの除去法としては金属塩あ
るいは消石灰を用いた凝集沈澱法がよく知られて
いる。これは水中のリン酸イオンを金属イオンあ
るいは消石灰と反応させ難溶性塩を生成し、これ
を沈澱分離する方法であるが、添加する薬品を多
量に必要とし、また発生する汚泥の量も多いため
多額の処理費用を要する方法となつている。
Conventionally, a coagulation precipitation method using metal salts or slaked lime is well known as a method for removing phosphate ions. This method involves reacting phosphate ions in water with metal ions or slaked lime to generate poorly soluble salts, which are separated by precipitation, but this method requires a large amount of added chemicals and also generates a large amount of sludge. This method requires a large amount of processing cost.

このような従来法の欠点を解消し、簡単な操作
で効率よく水中のリン酸イオンを除去するため
に、ヒドロキシアパタイトの晶析現象を利用し
た、いわゆる晶析脱リン法が開発された。この方
法は被処理水にカルシウムイオン(Ca2+)を少
量加えることにより、水中に溶存するリン酸イオ
ン(PO4 3-)をヒドロキシアパタイト(Ca5
(PO43OH)の微結晶として析出させ、このヒド
ロキシアパタイトを含みかつ単なる沈降では分離
困難なコロイド状被処理水を骨炭又はリン酸塩鉱
物よるなる晶析材と直ちに接触させることによ
り、そのヒドロキシアパタイトの微結晶を晶析材
に広く分布しているヒドロキシアパタイトの結晶
に晶析させ、リン酸イオンを順次除去しようとす
るものである。この方法により、多量の汚泥発生
を伴わず少量の薬品添加で効率よくリン酸イオン
を除去できることとなる。
In order to eliminate these drawbacks of the conventional method and efficiently remove phosphate ions from water with simple operations, a so-called crystallization dephosphorization method that utilizes the crystallization phenomenon of hydroxyapatite has been developed. In this method, by adding a small amount of calcium ions (Ca 2+ ) to the water to be treated, phosphate ions (PO 4 3- ) dissolved in the water are converted into hydroxyapatite (Ca 5
(PO 4 ) 3 OH) is precipitated as microcrystals, and the colloidal water containing hydroxyapatite, which is difficult to separate by mere sedimentation, is brought into immediate contact with a crystallizing material made of bone char or phosphate minerals. The purpose is to crystallize the hydroxyapatite microcrystals into hydroxyapatite crystals widely distributed in the crystallization material, and sequentially remove phosphate ions. By this method, phosphate ions can be efficiently removed by adding a small amount of chemicals without generating a large amount of sludge.

一般に、この方法においては晶析材の選定が重
要な因子であり、その晶析材の性能が本方式の処
理結果を決定づける。すなわち通常考えられる晶
析材としてはアパタイトを主成分とした骨炭、リ
ン酸塩鉱物があるが、これらの性能はその成分・
組成、晶析材の表面状態、結晶の活性化の程度等
により異なつており、晶析材の種類によつてはリ
ン除去性能が劣るもの、長期に亘つてその性能が
持続しないもの、あるいは予め被処理水に何らか
の前処理を施しておく必要があるものなどが存在
する。
Generally, in this method, the selection of the crystallization material is an important factor, and the performance of the crystallization material determines the processing results of this method. In other words, the crystallization materials that are usually considered include bone char and phosphate minerals whose main component is apatite, but the performance of these materials depends on their composition and
It varies depending on the composition, the surface condition of the crystallization material, the degree of crystal activation, etc., and depending on the type of crystallization material, the phosphorus removal performance may be poor, the performance may not last for a long time, or the phosphorus removal performance may be There are some types of water that require some kind of pretreatment on the water to be treated.

ここで、晶析材として骨炭を使用する場合、晶
析材の表面に不純物として有機物や一部の無機物
が含まれ、特に10%程度含まれている炭素が有機
物の吸着に関与し、晶析材としての性能を低下さ
せるという問題があつた。
When bone char is used as a crystallization material, the surface of the crystallization material contains organic substances and some inorganic substances as impurities. In particular, carbon, which contains about 10%, participates in the adsorption of organic substances, causing crystallization. There was a problem that the performance as a material deteriorated.

〔発明の目的〕[Purpose of the invention]

本発明は上述のような問題に鑑み、被処理水中
に分散生成したヒドロキシアパタイトを晶析させ
る骨炭よりなる晶析材を水酸基を有するアルカリ
剤の水溶液と接触させることにより晶析材の表面
の不純物質を洗い流すとともにヒドロキシアパタ
イトの構成物質である水酸イオンを補填して晶析
材を活性化させようとするものである。
In view of the above-mentioned problems, the present invention eliminates impurities on the surface of the crystallization material by bringing the crystallization material made of bone char, which crystallizes the hydroxyapatite dispersed in the water to be treated, into contact with an aqueous solution of an alkaline agent having a hydroxyl group. The purpose is to wash away the crystallization material and supplement the hydroxyl ions, which are the constituents of hydroxyapatite, to activate the crystallization material.

〔発明の概要〕[Summary of the invention]

本発明はリン酸イオンを含む被処理水にカルシ
ウムイオンを加えてヒドロキシアパタイトを生成
させ、このヒドロキシアパタイトをアパタイトを
主成分とする骨炭よりなる晶析材に晶析させて水
中リン酸イオンを除去する水処理方法において、
前記晶析材を水酸基を有するアルカリ剤と接触さ
せることにより晶析材を洗浄しかつ晶析材に水酸
イオンを補填しようとするものである。
The present invention adds calcium ions to treated water containing phosphate ions to generate hydroxyapatite, and removes phosphate ions in the water by crystallizing this hydroxyapatite in a crystallization material made of bone char whose main component is apatite. In the water treatment method,
This method attempts to clean the crystallization material and replenish the crystallization material with hydroxyl ions by bringing the crystallization material into contact with an alkaline agent having a hydroxyl group.

〔発明の構成及び作用〕[Structure and operation of the invention]

晶析材はアパタイトを主成分とした骨炭よりな
る粒状物であり、アルカリ水溶液としては、水酸
化ナトリウム、水酸化カルシウム等の水酸基を有
するアルカリ剤の水溶液でPH10以上に調整したも
のが用いられる。晶析材とアルカリ水溶液の接触
の方法としては、晶析材をアルカリ水溶液に浸漬
させるかまたは、カラムに充填した晶析材層にア
ルカリ水溶液を通液する方法がある。アルカリ水
溶液の使用量は晶析材と十分に接触しかつ反応さ
せるために晶析材の容量と同容量以上とする。ア
ルカリ処理後の晶析材は、水洗又は脱リン処理用
被処理水又は処理水を用いて十分に洗浄する。た
だし軽度のアルカリ処理の場合は洗浄を省略でき
る。
The crystallizing material is a granular material made of bone charcoal mainly composed of apatite, and the alkaline aqueous solution used is an aqueous solution of an alkaline agent having a hydroxyl group, such as sodium hydroxide or calcium hydroxide, adjusted to a pH of 10 or higher. Methods for bringing the crystallization material into contact with the alkaline aqueous solution include immersing the crystallization material in the alkaline aqueous solution or passing the alkaline aqueous solution through a crystallization material layer packed in a column. The amount of the alkaline aqueous solution to be used is equal to or greater than the volume of the crystallization material in order to sufficiently contact and react with the crystallization material. The crystallized material after the alkali treatment is thoroughly washed with water or with treated water or treated water for dephosphorization treatment. However, in the case of mild alkali treatment, cleaning can be omitted.

以上のようにして骨炭よりなる晶析材をアルカ
リ水溶液と接触させることにより、骨炭に含まれ
ている有機物や一部の無機物から成る不純物質が
洗い流されヒドロキシアパタイトの結晶が露呈さ
れて晶析材の表面が活性化される。さらに、アル
カリ水溶液中の水酸イオンがヒドロキシアパタイ
トの構成分子である水酸基を晶析材に補填し、晶
析材が水酸イオンの過剰な状態となり、ヒドロキ
シアパタイトの結晶成長を促進させる。
By bringing the crystallization material made of bone char into contact with the alkaline aqueous solution as described above, impurities made of organic substances and some inorganic substances contained in the bone char are washed away, hydroxyapatite crystals are exposed, and the crystallization material is exposed. surface is activated. Furthermore, the hydroxyl ions in the alkaline aqueous solution supplement the hydroxyl groups, which are the constituent molecules of hydroxyapatite, to the crystallization material, and the crystallization material becomes in a state of excess hydroxyl ions, promoting crystal growth of hydroxyapatite.

尚晶析材の活性化処理は、脱リンに晶析材とし
て使用する以前、或いは脱リンに使用の途中の何
れの場合に施してもよい。
The activation treatment of the crystallization material may be performed either before it is used as a crystallization material for dephosphorization or during use for dephosphorization.

〔発明の効果〕〔Effect of the invention〕

本発明によれば、リン酸イオンを含む被処理水
にカルシウムイオンを加えてヒドロキシアパタイ
トを生成させ、このヒドロキシアパタイトを骨炭
よりなる晶析材に晶析させて水中のリン酸イオン
を除去する水処理方法において、前記晶析材を、
水酸基を有するアルカリ剤の水溶液と接触させる
ことにより、骨炭よりなる晶析材の表面がアルカ
リ剤によつて洗浄され有機物等の不純物質が除去
されて活性化されるとともに水酸イオンが補填さ
れて晶析反応を促進させるため、長期にわたつて
晶析作用を有効に続行させることができる。した
がつて水中のリン酸イオンの除去を効率良く安定
して長期間連続して行うことが出来る。
According to the present invention, calcium ions are added to treated water containing phosphate ions to generate hydroxyapatite, and the hydroxyapatite is crystallized using a crystallization material made of bone char to remove phosphate ions from the water. In the treatment method, the crystallization material is
By bringing it into contact with an aqueous solution of an alkaline agent having hydroxyl groups, the surface of the crystallizing material made of bone char is washed with the alkaline agent, impurities such as organic matter are removed and activated, and hydroxyl ions are replenished. Since the crystallization reaction is promoted, the crystallization action can be effectively continued for a long period of time. Therefore, phosphate ions in water can be efficiently and stably removed continuously for a long period of time.

〔発明の実施例〕[Embodiments of the invention]

実施例 1 直径5cm、高さ150cmの円筒カラムを2本用意
し、これに粒径0.5〜1.0mmの骨炭2を各々充填
しカラムNo.1およびNo.2とする。
Example 1 Two cylindrical columns with a diameter of 5 cm and a height of 150 cm are prepared, and each column is filled with bone char 2 having a particle size of 0.5 to 1.0 mm to form columns No. 1 and No. 2.

カラムNo.2については予め飽和水酸化カルシウ
ム溶液を骨炭充填量の2倍に相当する量通液した
のち水洗し充填骨炭を活性化しておく。
Regarding column No. 2, a saturated calcium hydroxide solution was passed in an amount equivalent to twice the amount of bone char packed, and then washed with water to activate the packed bone char.

次に各々のカラムに被処理水(原水)として下
水二次処理水を用い、これに水酸化カルシウムを
添加しPH8〜9に調整したものを連続的に空塔速
度(SV)2/―骨炭・時で通水し、各処理
水のPO4 3-イオン量を測定した。
Next, secondary treated sewage water was used as the water to be treated (raw water) in each column, and calcium hydroxide was added to it to adjust the pH to 8-9, which was then continuously fed to the superficial velocity (SV) 2/- bone char.・Water was passed through the water at various times, and the amount of PO 4 3- ions in each treated water was measured.

この結果P換算で1.52〜2.02mg/程度の
PO4 3-イオンを含む被処理水の通水50日後におけ
る各カラムの処理水PO4 3-イオン量はP換算でカ
ラムNo.1は0.42mg/、カラムNo.2は0.16mg/
となつており(当日の被処理水PO4 3-イオン量は
P換算で1.88mg/)、水酸化カルシウムを用い
た活性化処理の効果は明らかであつた。
As a result, P conversion was approximately 1.52 to 2.02 mg/
The amount of PO 4 3- ions in the treated water in each column after 50 days of flowing the water containing PO 4 3- ions was 0.42 mg/in terms of P for column No. 1 and 0.16 mg/in for column No. 2.
(The amount of PO 4 3- ions in the water to be treated on that day was 1.88 mg/in terms of P), and the effect of the activation treatment using calcium hydroxide was clear.

実施例 2 直径30cm、高さ300cmの円筒タンクに粒径0.5〜
1.0の骨炭を約100充填し、これに被処理水とし
て水酸化カルシウムでPH8〜9に調整した下水二
次処理水を空塔速度2/―骨炭・時で通水し
て水中のリン酸イオンを除去する装置がある。
Example 2 Particle size 0.5~ in a cylindrical tank with a diameter of 30 cm and a height of 300 cm
Approximately 100 pieces of 1.0 bone char are filled, and secondary treated sewage water adjusted to pH 8-9 with calcium hydroxide is passed through this as water to be treated at a superficial velocity of 2/- bone char/hour to remove phosphate ions in the water. There is a device to remove it.

ある期間通水後1%水酸化ナトリウム溶液100
を通液したのち水洗することにより骨炭の活性
化処理を実施した。
After passing water for a certain period of time, 1% sodium hydroxide solution 100%
The bone char was activated by passing a solution through it and then washing it with water.

活性化処理前後における処理水PO4 3-イオン量
の測定結果を図に示す。
The measurement results of the amount of PO 4 3- ions in the treated water before and after the activation treatment are shown in the figure.

すなわち活性化以前の処理水PO4 3-イオンはP
換算で0.4〜0.5mg/であるのに対し、本発明に
よる方法で活性化処理したのちはその処理水
PO4 3-イオン(P換算)は、0.1〜0.2mg/に低
下し、活性化処理の効果は明らかであつた。
In other words, the treated water PO 4 3- ion before activation is P
Converted to 0.4 to 0.5 mg/, whereas after activation treatment by the method of the present invention, the treated water
PO 4 3- ion (in terms of P) decreased to 0.1 to 0.2 mg/, and the effect of the activation treatment was clear.

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

図は実施例―2の方法で脱リン処理した処理水
中のリン酸イオン濃度と通水日数の関係を示す図
表である。
The figure is a chart showing the relationship between the phosphate ion concentration in treated water dephosphorized by the method of Example-2 and the number of days of water flow.

Claims (1)

【特許請求の範囲】[Claims] 1 リン酸イオンを含む被処理水にカルシウムイ
オンを加えてヒドロキシアパタイトを生成させ、
このヒドロキシアパタイトを骨炭よりなる晶析材
に晶析させて水中のリン酸イオンを除去する水処
理方法において、前記晶析材を、水酸基を有する
アルカリ剤の水溶液と接触させることを特徴とす
る水処理用晶析材の活性化方法。
1 Add calcium ions to treated water containing phosphate ions to generate hydroxyapatite,
A water treatment method in which phosphate ions in water are removed by crystallizing this hydroxyapatite in a crystallization material made of bone char, characterized in that the crystallization material is brought into contact with an aqueous solution of an alkaline agent having a hydroxyl group. Method for activating crystallization material for processing.
JP15319582A 1982-09-02 1982-09-02 Activating method of crystallizing material for water treatment Granted JPS5942087A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP15319582A JPS5942087A (en) 1982-09-02 1982-09-02 Activating method of crystallizing material for water treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP15319582A JPS5942087A (en) 1982-09-02 1982-09-02 Activating method of crystallizing material for water treatment

Publications (2)

Publication Number Publication Date
JPS5942087A JPS5942087A (en) 1984-03-08
JPS632237B2 true JPS632237B2 (en) 1988-01-18

Family

ID=15557117

Family Applications (1)

Application Number Title Priority Date Filing Date
JP15319582A Granted JPS5942087A (en) 1982-09-02 1982-09-02 Activating method of crystallizing material for water treatment

Country Status (1)

Country Link
JP (1) JPS5942087A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS59139994A (en) * 1983-01-31 1984-08-11 Ebara Infilco Co Ltd Catalytic dephosphorization
JPH0711181Y2 (en) * 1992-06-18 1995-03-15 日清紡績株式会社 Pad material for pad type clearer device

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5425516B2 (en) * 1974-01-23 1979-08-28
JPS50152544A (en) * 1974-05-29 1975-12-08
JPS57209682A (en) * 1981-06-22 1982-12-23 Ebara Infilco Co Ltd Catalytic dephosphorization

Also Published As

Publication number Publication date
JPS5942087A (en) 1984-03-08

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