JPH0675708B2 - Method for removing phosphorus from liquid - Google Patents
Method for removing phosphorus from liquidInfo
- Publication number
- JPH0675708B2 JPH0675708B2 JP100090A JP100090A JPH0675708B2 JP H0675708 B2 JPH0675708 B2 JP H0675708B2 JP 100090 A JP100090 A JP 100090A JP 100090 A JP100090 A JP 100090A JP H0675708 B2 JPH0675708 B2 JP H0675708B2
- Authority
- JP
- Japan
- Prior art keywords
- phosphorus
- liquid
- dephosphorization
- added
- salt solution
- 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.)
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- Removal Of Specific Substances (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、下水,し尿等の生活排水,工場排水などに含
まれるリンを除去する方法に関するものである。TECHNICAL FIELD The present invention relates to a method for removing phosphorus contained in domestic wastewater such as sewage and human waste, factory wastewater, and the like.
液中のリンを除去するに当たり、リンを含む液をカルシ
ウムイオンの存在下で、リン除去能力を有する粒状物、
例えばリン鉱石,骨炭,MgO,スラグ類などと接触させる
方法は、接触脱リン法として確立された公知の方法であ
る。この接触脱リン法において、リン除去反応を促進さ
せるためには、リン除去反応を阻害する炭酸物質を除去
したり、促進物質としてFイオンを添加することが知ら
れている。In removing phosphorus in the liquid, a liquid containing phosphorus is added in the presence of calcium ions, and the granular material has a phosphorus removing ability.
For example, a method of contacting with phosphate rock, bone charcoal, MgO, slag, etc. is a known method established as a catalytic dephosphorization method. In this catalytic dephosphorization method, in order to accelerate the phosphorus removal reaction, it is known to remove a carbonate substance that inhibits the phosphorus removal reaction or to add F ion as a promoter.
しかしながら、下水二次処理水(通常リンとして1〜2m
g/l含有する)を対象に接触脱リン法を適用した場合、
脱炭酸(液中の炭酸物質の除去)を行っても、処理水の
リン濃度は定常的に0.2〜0.4mg/lにしかならず、この処
理水を修景用水として再利用すると、水路に藻類が繁殖
する。However, sewage secondary treated water (usually 1-2 m as phosphorus)
When the catalytic dephosphorization method is applied to (containing g / l),
Even if decarbonation (removal of carbonic acid substances in the liquid) is carried out, the phosphorus concentration of the treated water is only 0.2 to 0.4 mg / l constantly, and if this treated water is reused as scenic water, algae will grow in the waterway. Breed.
また、Fイオンを添加しても、せいぜい処理水のリン濃
度を0.2〜0.4mg/lにするのが限度であり、多量に添加す
るとCaF2の沈殿を生じ、汚泥の発生量を高めるという問
題があった。In addition, even if F ions are added, the phosphorus concentration of the treated water is limited to 0.2 to 0.4 mg / l at most, and if a large amount is added, CaF 2 precipitates and the amount of sludge generated increases. was there.
本発明は、接触脱リン法における前記従来の問題点を解
決し、極めて簡易な操作によって高いリン除去性能を達
成しうる方法を提供することを目的とするものである。An object of the present invention is to solve the above-mentioned conventional problems in the catalytic dephosphorization method and to provide a method capable of achieving high phosphorus removal performance by an extremely simple operation.
本発明は、リンを含む液をカルシウムイオンの存在下
で、リン除去能力を有する粒状物と接触させてリンを除
去する接触脱リン法において、前記リンを含む液に塩類
溶液を添加して液の電気伝導度を2,000μ/cm以上に調
整したのち接触脱リンすることを特徴とする液中のリン
除去方法である。The present invention, in the catalytic dephosphorization method of removing phosphorus by contacting a liquid containing phosphorus in the presence of calcium ions, with a granular material having a phosphorus-removing ability, a salt solution is added to the liquid containing phosphorus. The method for removing phosphorus in a liquid is characterized in that the electrical conductivity of is adjusted to 2,000 μ / cm or more and then catalytic dephosphorization is performed.
本発明の作用を、実施態様を示す図面に基づいて説明す
れば、第1図において、例えば下水を活性汚泥処理した
処理水(下水二次処理水)1を前処理工程2に導入す
る。前処理工程2では、下水二次処理水に鉱酸を添加し
て空気を吹き込むことにより、液中の炭酸物質を除去
(脱炭酸)し、その後硝石灰やCa塩を添加し、脱リン反
応に必要なCa濃度やpHが調整される。さらに、この前処
理工程2で塩類溶液7を添加し、後続する脱リン工程4
に流入する液の電気伝導度を2,000μ/cm以上に調整す
る。例えば、通常の下水には、500〜1,500μ/cmの電
気導電度があるが、塩類溶液7を流量に比例して添加す
ることによって2,000μ/cm以上とするか、前処理工程
2内又は脱リン工程4への流路内に電気伝導度計を設け
て塩類溶液の注入ポンプと連動させ、2,000μ/cm以上
の値に維持することも好ましい。The operation of the present invention will be described with reference to the drawings showing the embodiment. In FIG. 1, for example, treated water (sewage secondary treated water) 1 obtained by treating sewage with activated sludge is introduced into a pretreatment step 2. In the pretreatment step 2, mineral acid is added to the sewage secondary treated water and air is blown in to remove (decarbonate) the carbonate substances in the liquid, and then nitric lime and Ca salt are added to perform the dephosphorization reaction. The Ca concentration and pH required for this are adjusted. Further, in this pretreatment step 2, a salt solution 7 is added, followed by a dephosphorization step 4
Adjust the electric conductivity of the liquid flowing in to 2,000 μ / cm or more. For example, normal sewage has an electric conductivity of 500 to 1,500 μ / cm, but it is adjusted to 2,000 μ / cm or more by adding the salt solution 7 in proportion to the flow rate, or in the pretreatment step 2 or It is also preferable to provide an electric conductivity meter in the flow path to the dephosphorization step 4 and operate in conjunction with a salt solution injection pump to maintain the value at 2,000 μ / cm or more.
電気伝導度を高める塩類溶液としては、NaCl,MgCl2,Ba
Cl2,CaCl2等の溶液や海水を使用することができるが、
海水がより好ましい。NaCl, MgCl 2 , Ba is used as a salt solution to enhance electrical conductivity.
A solution such as Cl 2 or CaCl 2 or seawater can be used,
Seawater is more preferred.
次いで、電気伝導度を2,000μ/cm以上に調整した液
は、砂ろ過工程3で液中の濁質を除去した後、リン除去
能力を有する粒状物を充填した脱リン工程4へ移送され
る。脱リン工程4内では、リン除去能力を有する粒状物
上でリン酸カルシウムが晶析して液中のリンが除去さ
れ、脱リン処理水を得ることができる。脱リン工程4
は、上向流式,下向流式のいずれでも良く、また固定床
式でも流動床式でも良い。リン除去能力を有する粒状物
としては、リン鉱石,骨炭,軽焼マグネシア,転炉スラ
グなどが使用できる。Next, the liquid whose electric conductivity is adjusted to 2,000 μ / cm or more is transferred to the dephosphorization process 4 in which the particulate matter having the phosphorus removal ability is filled after removing the suspended matter in the liquid in the sand filtration process 3. . In the dephosphorization step 4, calcium phosphate is crystallized on the granular material having a phosphorus removing ability to remove phosphorus in the liquid, and dephosphorized water can be obtained. Dephosphorization process 4
May be either an upward flow type or a downward flow type, and may be a fixed bed type or a fluidized bed type. As the granular material having a phosphorus removing ability, phosphorus ore, bone charcoal, light burned magnesia, converter slag, etc. can be used.
なお、塩類溶液7の添加場所は、前処理工程2のみなら
ず、脱リン工程4の前であればどこでも良いが、塩類溶
液として海水を使用する時には、図示例のように砂ろ過
工程3より前に添加すれば、海水中の濁質やリンも一緒
に除去できるので、海水の浄化にもつながる。The salt solution 7 may be added not only in the pretreatment step 2 but also in any place before the dephosphorization step 4, but when seawater is used as the salt solution, the salt filtration step 3 is performed as in the illustrated example. If added before, turbidity and phosphorus in seawater can be removed together, which leads to purification of seawater.
第2図は、第1図の砂ろ過工程3と脱リン工程4を一体
化した砂ろ過・脱リン工程6を使用した例であり、下部
に砂層、上部にリン除去能力を有する粒状物質を形成さ
せておき、前処理工程2からの流出水を通水するもので
ある。FIG. 2 is an example of using the sand filtration / dephosphorization step 6 in which the sand filtration step 3 and the dephosphorization step 4 of FIG. 1 are integrated. The sand layer is at the bottom and the granular material having the phosphorus removing ability is at the top. The effluent from the pretreatment step 2 is allowed to pass through after being formed.
リンを2mg/l含有する下水二次処理水に硫酸を添加し、p
H4.5に調整するとともに、海水を添加して電気伝導度を
各種の所定値に調整したものをそれぞれ用意し、さらに
それぞれにCaCl2溶液(Caとして20,000mg/l)を添加し
てCaを60〜70mg/lに調整し、さらにNaOH溶液を添加して
pH9.0とした。Sulfuric acid was added to the secondary treated water containing sewage containing 2 mg / l of phosphorus, and p
Prepare the ones adjusted to H4.5 and the electrical conductivity adjusted to various predetermined values by adding seawater, and add CaCl 2 solution (20,000 mg / l as Ca) to each to add Ca. Adjust to 60-70 mg / l and add more NaOH solution
The pH was set to 9.0.
一方、リンを2mg/l含有する純水に、CaCl2溶液を添加し
てCaを60〜70mg/lに調整するとともに、海水を添加して
電気伝導度を各種の所定値に調整し、さらにそれぞれNa
OH溶液を添加してpH9.0とした。On the other hand, in pure water containing 2 mg / l of phosphorus, CaCl 2 solution was added to adjust Ca to 60 to 70 mg / l, and seawater was added to adjust the electrical conductivity to various predetermined values. Each Na
An OH solution was added to bring the pH to 9.0.
これらの各液1をビーカーにとり、リン鉱石を1,000m
g/l添加して1時間反応後の上澄水のリン濃度を測定
し、電気伝導度の影響をみた。これらの実験結果は第3
図に示す通りであり、電気伝導度が2,000μ/cm以上に
なると上澄水のリン濃度が著しく低下した。Put each of these liquids 1 in a beaker and add phosphorus ore to 1,000m.
After adding g / l and reacting for 1 hour, the phosphorus concentration of the supernatant water was measured to see the effect of electrical conductivity. These experimental results are the third
As shown in the figure, when the electric conductivity was 2,000 μ / cm or more, the phosphorus concentration of the supernatant water was significantly reduced.
また、電気伝導度を調整するために、海水に代えNaCl溶
液を使用した結果も第3図に併記したが、NaCl溶液より
海水の方がリン除去性能が良好であった。The results of using a NaCl solution in place of seawater to adjust the electric conductivity are also shown in FIG. 3, and seawater was better than the NaCl solution in phosphorus removal performance.
以上述べたように、本発明は、接触脱リン法において、
被処理液中のの電気伝導度を、塩類溶液を添加すること
によって2,000μ/cm以上に調整するという極めて簡易
な操作によって、リン除去性能を著しく向上させること
ができるものである。As described above, the present invention, in the catalytic dephosphorization method,
The phosphorus removal performance can be remarkably improved by the extremely simple operation of adjusting the electric conductivity of the liquid to be treated to 2,000 μ / cm or more by adding a salt solution.
第1図及び第2図はそれぞれ本発明の実施態様例を示す
系統説明図、第3図は実験結果における上澄水リン濃度
と電気伝導度との関係を示す線図である。 1……下水二次処理水、2……前処理工程、3……砂ろ
過工程、4……脱リン工程、5……脱リン処理水、6…
…砂ろ過・脱リン工程、7……塩類溶液。FIG. 1 and FIG. 2 are system explanatory diagrams each showing an embodiment of the present invention, and FIG. 3 is a diagram showing the relationship between the phosphorus concentration in supernatant water and the electrical conductivity in the experimental results. 1 ... sewage secondary treated water, 2 ... pretreatment process, 3 ... sand filtration process, 4 ... dephosphorization process, 5 ... dephosphorized water, 6 ...
... sand filtration / dephosphorization process, 7 ... salt solution.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 平沢 泉 東京都港区港南1丁目6番27号 荏原イン フィルコ株式会社内 (72)発明者 中村 弘志 東京都港区港南1丁目6番27号 荏原イン フィルコ株式会社内 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Izumi Hirasawa 1-6-27 Konan, Minato-ku, Tokyo Ebara In Filco Co., Ltd. (72) Hiroshi Nakamura 1-6-27 Konan, Minato-ku, Tokyo Ebara Within Infilco Corporation
Claims (1)
で、リン除去能力を有する粒状物と接触させてリンを除
去する接触脱リン法において、前記リンを含む液に塩類
溶液を添加して液の電気伝導度を2,000μ/cm以上に調
整したのち接触脱リンすることを特徴とする液中のリン
除去方法。1. In a catalytic dephosphorization method of removing phosphorus by contacting a liquid containing phosphorus with a granular material having a phosphorus removing ability in the presence of calcium ions, a salt solution is added to the liquid containing phosphorus. A method for removing phosphorus from a liquid, which comprises performing catalytic dephosphorization after adjusting the electrical conductivity of the liquid to 2,000 μ / cm or more.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP100090A JPH0675708B2 (en) | 1990-01-09 | 1990-01-09 | Method for removing phosphorus from liquid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP100090A JPH0675708B2 (en) | 1990-01-09 | 1990-01-09 | Method for removing phosphorus from liquid |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03207489A JPH03207489A (en) | 1991-09-10 |
| JPH0675708B2 true JPH0675708B2 (en) | 1994-09-28 |
Family
ID=11489319
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP100090A Expired - Lifetime JPH0675708B2 (en) | 1990-01-09 | 1990-01-09 | Method for removing phosphorus from liquid |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0675708B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| HUT75444A (en) * | 1992-06-23 | 1997-05-28 | Water Board | Process for the remoual of phosphorous |
| KR19990083819A (en) * | 1999-08-13 | 1999-12-06 | 김기준 | Inorganic chemical treatment of waste water |
| CN102149645B (en) * | 2009-12-01 | 2011-11-16 | 李进民 | Sludge treatment method and apparatus thereof and application to wastewater bio-treatment |
-
1990
- 1990-01-09 JP JP100090A patent/JPH0675708B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03207489A (en) | 1991-09-10 |
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