JPH03207489A - Method for removing phosphorus in liquid - Google Patents

Method for removing phosphorus in liquid

Info

Publication number
JPH03207489A
JPH03207489A JP100090A JP100090A JPH03207489A JP H03207489 A JPH03207489 A JP H03207489A JP 100090 A JP100090 A JP 100090A JP 100090 A JP100090 A JP 100090A JP H03207489 A JPH03207489 A JP H03207489A
Authority
JP
Japan
Prior art keywords
liq
phosphorus
added
electrical conductivity
stage
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
JP100090A
Other languages
Japanese (ja)
Other versions
JPH0675708B2 (en
Inventor
Takeshi Minami
南 武
Yoshiaki Suzuki
義明 鈴木
Izumi Hirasawa
泉 平沢
Hiroshi Nakamura
弘志 中村
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.)
Ebara Corp
Tokyo Metropolitan Government
Original Assignee
Ebara Infilco Co Ltd
Tokyo Metropolitan Government
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 Ebara Infilco Co Ltd, Tokyo Metropolitan Government filed Critical Ebara Infilco Co Ltd
Priority to JP100090A priority Critical patent/JPH0675708B2/en
Publication of JPH03207489A publication Critical patent/JPH03207489A/en
Publication of JPH0675708B2 publication Critical patent/JPH0675708B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Removal Of Specific Substances (AREA)

Abstract

PURPOSE:To highly remove phosphorus in a liq. by very simple operation by regulating the electrical conductivity of the liq. to a certain value or above with a soln. of salts and carrying out catalytic dephosphorization. CONSTITUTION:A liq. contg. phosphorus, e.g. waste water from an industrial or living waste water such as sewerage or night soil is introduced into a pretreating stage 2, where a mineral acid is added, air is blown and carbonates is the liq. are removed. Slaked lime and Ca salt are added to regulated the concn. of Ca and the pH of the liq. and a soln. 7 of salts such as NaCl is further added to regulate the electrical conductivity of the liq. flowing in a subsequent dephosphorizing stage 4 to >=2000muV/cm. Suspended solids in the liq. are then removed in a sand filtering stage 3 and the liq. is sent to the stage 4 packed with granules having phosphorus removing ability. By such very simple operation, phosphorus removing performance is considerably enhanced.

Description

【発明の詳細な説明】 C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。
DETAILED DESCRIPTION OF THE INVENTION C. Industrial Application Field The present invention relates to a method for removing phosphorus contained in domestic wastewater such as sewage and human waste, industrial wastewater, and the like.

〔従来の技術〕[Conventional technology]

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。
When removing phosphorus from a liquid, a phosphorus-containing liquid is treated with granules having phosphorus removal ability in the presence of calcium ions,
For example, the method of contacting with phosphate rock, bone coal, MgO, slag, etc. is a well-known method established as a catalytic dephosphorization method. In this catalytic dephosphorization method, in order to promote the phosphorus removal reaction, it is known that carbonic acid substances that inhibit the phosphorus removal reaction are removed or F ions are added as a promoter.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかしながら、下水二次処理水(通常リンとして1〜2
■/1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0.2〜0.4■/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, secondary treated sewage water (usually 1 to 2 phosphorus)
■ When the catalytic dephosphorization method is applied to water (containing /1), the phosphorus concentration in the treated water is constantly 0.2 to 0.4 even after decarboxylation (removal of carbonated substances in the liquid). If this treated water is reused as landscaping water, algae will grow in the waterways.

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0.2〜0.4■/I!にするのが限度であり、多
量に添加するとCaF tの沈殿を生し、汚泥の発生量
を高めるという問題があった。
Moreover, even if F ions are added, the phosphorus concentration of the treated water can be reduced to 0.2 to 0.4 ■/I! However, if a large amount is added, CaFt will precipitate and the amount of sludge generated will increase.

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違
或しうる方法を提供することを目的とするものである. 〔諜題を解決するための手段〕 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2,000μIJ / 
cs以上に調整したのち接触脱リンすることを特徴とす
る戒中のリン除去方法である。
The object of the present invention is to solve the above-mentioned conventional problems in the catalytic dephosphorization method and to provide a method that can achieve high phosphorus removal performance with extremely simple operations. [Means for Solving the Problem] The present invention provides a catalytic dephosphorization method in which phosphorus is removed by bringing a phosphorus-containing liquid into contact with particulate matter having a phosphorus removal ability in the presence of calcium ions. Add a salt solution to the liquid to increase the electrical conductivity of the liquid to 2,000μIJ/
This method of removing phosphorus in the prefecture is characterized by carrying out contact dephosphorization after adjusting the phosphorus to a level higher than cs.

[作 用] 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#)シ、その後消石灰やCa塩を添加し、脱リン反応
に必要なCaf74度やp}lが調整される。さら乙こ
、この前処理工程2で塩類熔Wi.1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2,000
μ1J/cIn以上乙こ調整する。例えば、通常の下水
には、500〜1 , 500μび/clI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, 000μV/CS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
11 / an以上の値に維持することも好ましい。
[Function] To explain the function of the present invention based on drawings showing embodiments, in FIG. Introduce. In pre-treatment step 2, mineral acid is added to the secondary sewage treatment water and air is blown in to remove carbonated substances from the liquid (decarburization #), and then slaked lime and Ca salt are added to carry out the dephosphorization reaction. The Caf74 degree and p}l required for this are adjusted. In this pre-treatment step 2, salt melt Wi. 1 to increase the electrical conductivity of the liquid flowing into the subsequent dephosphorization step 4 to 2,000.
Adjust by more than μ1J/cIn. For example, normal sewage has an electrical conductivity of 500 to 1,500μV/clI, but it can be increased to 2,000μV/CS or more by adding salt solution 7 in proportion to the flow rate, or by using a pretreatment process. An electrical conductivity meter is installed in 2 or in the flow path to the dephosphorization process 4, and is linked to the saline solution injection pump.
It is also preferable to maintain a value of 11/an or more.

電気伝導度を高める塩類溶液としては、NaCI門gc
l., BaCl2, CaC]z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。
As a salt solution that increases electrical conductivity, NaCI gc
l. , BaCl2, CaC]z, or seawater can be used, but seawater is more preferable.

次いで、電気伝導度を2, 000μv/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
定床弐でも流動床弐でも良い。リン除去能力を有する粒
状物としては、リン鉱石,骨炭,軽焼マグ不シア転炉ス
ラグなどが使用できる。
Next, the liquid whose electrical conductivity has been adjusted to 2,000 μv/cm or more is subjected to sand filtration step 3 to remove suspended matter in the liquid.
It is transferred to a dephosphorization step 4 filled with granules having phosphorus removal ability. In the dephosphorization step 4, calcium phosphate is crystallized on granules having phosphorus removal ability, phosphorus in the liquid is removed, and dephosphorized water can be obtained. The dephosphorization step 4 may be of an upward flow type or a downward flow type, and may be a fixed bed or a fluidized bed. As the granular material having phosphorus removal ability, phosphate rock, bone charcoal, light burnt mag inertia 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。
Note that the salt solution 7 may be added not only in the pretreatment step 2 but also anywhere before the dephosphorization step 4, but when seawater is used as the salt solution, it may be added from the sand filtration step 3 as in the illustrated example. If added beforehand, it can also remove turbidity and phosphorus from the seawater, helping to purify the 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層を形威さ
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。
Figure 2 is an example of using sand filtration/dephosphorization process 6, which integrates sand filtration process 3 and dephosphorization process 4 in Figure 1, with a sand layer at the bottom and a granular material layer with phosphorus removal ability at the top. The effluent water from the pretreatment step 2 is passed through it.

[実施例〕 リンを2■/l含有する下水二次処理水に硫酸を添加し
、p}14.5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CaCI.溶液(Caとして20
,000*/ +! )を添加してCaを60〜70■
/lに調整し、さらにNaOH溶液を添加してpH9.
0とした。
[Example] Sulfuric acid was added to secondary treated sewage water containing 2 μ/l of phosphorus to adjust it to p}14.5, and seawater was added to adjust the electrical conductivity to various predetermined values. Prepare each of them, and further add CaCI. Solution (20 as Ca
,000*/+! ) to increase Ca to 60-70■
/l, and further added NaOH solution to pH 9.
It was set to 0.

一方、リンを2■/l含有する純水に、CaCI.溶液
を添加してCaを60〜70■/1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NaOH溶液を添加してpH9.0とし
た。
On the other hand, CaCI. A solution was added to adjust Ca to 60 to 70 /1, and seawater was added to adjust the electrical conductivity to various predetermined values.
Furthermore, a NaOH solution was added to each to adjust the pH to 9.0.

これらの各液1lをビーカーにとり、リン鉱石を1,0
00■/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
ぴ/cs以上になると上澄水のリン濃度が著しく低下し
た。
Take 1 liter of each of these solutions in a beaker and add 1.0 liters of phosphate rock.
The phosphorus concentration of the supernatant water was measured after 1 hour of reaction after adding 00 μ/l, and the influence of electrical conductivity was examined. The results of these experiments are shown in Figure 3, and the electrical conductivity was 2,000μ.
The phosphorus concentration of the supernatant water decreased significantly when the temperature exceeded p/cs.

また、電気伝導度を調整するために、一海水に代えNa
C]溶液を使用した結果も第3図に併記したが、NaC
l溶液より海水の方がリン除去性能が良好であった。
In addition, in order to adjust the electrical conductivity, Na
The results using NaC] solution are also shown in Figure 3.
The seawater had better phosphorus removal performance than the l solution.

〔発明の効果〕〔Effect of the invention〕

以上述べたように、本発明は、接触脱リン法において、
被処理液中の電気伝導度を、塩類溶液を添加することに
よって2,000μ1J/cIl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, in the catalytic dephosphorization method, the present invention provides
Phosphorus removal performance can be significantly improved by an extremely simple operation of adjusting the electrical conductivity in the liquid to be treated to 2,000 μl J/cIl or more by adding a salt solution.

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

第1図及び第2図はそれぞれ本発明の実施Li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
FIGS. 1 and 2 are system explanatory diagrams showing examples of implementation Li of the present invention, respectively, and FIG. 3 is a diagram showing the relationship between supernatant water phosphorus concentration and electrical conductivity in experimental results. 1...Secondary sewage treatment water, 2...Pre-treatment process, 3...
- Sand filtration process, 4... Dephosphorization process, 5... Dephosphorization treated water, 6... Sand filtration/dephosphorization process, 7... Salt solution.

Claims (1)

【特許請求の範囲】[Claims] (1)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。
(1) In the catalytic dephosphorization method, in which phosphorus is removed by contacting a phosphorus-containing liquid with particulate matter having a phosphorus-removing ability in the presence of calcium ions, a salt solution is added to the phosphorus-containing liquid to remove phosphorus. A method for removing phosphorus from a liquid, characterized by carrying out catalytic dephosphorization after adjusting the electrical conductivity to 2,000μ/cm or more.
JP100090A 1990-01-09 1990-01-09 Method for removing phosphorus from liquid Expired - Lifetime JPH0675708B2 (en)

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 true JPH03207489A (en) 1991-09-10
JPH0675708B2 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)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0647209A1 (en) * 1992-06-23 1995-04-12 Water Board Process for the removal of phosphorous
KR19990083819A (en) * 1999-08-13 1999-12-06 김기준 Inorganic chemical treatment of waste water
US20120228217A1 (en) * 2009-12-01 2012-09-13 Jinmin Li Method and apparatus for sluge treatment and use thereof in sewage biotreatment

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0647209A1 (en) * 1992-06-23 1995-04-12 Water Board Process for the removal of phosphorous
EP0647209A4 (en) * 1992-06-23 1995-05-31 Water Board Process for the removal of phosphorous.
KR19990083819A (en) * 1999-08-13 1999-12-06 김기준 Inorganic chemical treatment of waste water
US20120228217A1 (en) * 2009-12-01 2012-09-13 Jinmin Li Method and apparatus for sluge treatment and use thereof in sewage biotreatment
US8932466B2 (en) * 2009-12-01 2015-01-13 Jinmin Li Method and apparatus for sluge treatment and use thereof in sewage biotreatment

Also Published As

Publication number Publication date
JPH0675708B2 (en) 1994-09-28

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