JPS58163491A - Removal of phosphorus dissolved in water - Google Patents
Removal of phosphorus dissolved in waterInfo
- Publication number
- JPS58163491A JPS58163491A JP4454082A JP4454082A JPS58163491A JP S58163491 A JPS58163491 A JP S58163491A JP 4454082 A JP4454082 A JP 4454082A JP 4454082 A JP4454082 A JP 4454082A JP S58163491 A JPS58163491 A JP S58163491A
- Authority
- JP
- Japan
- Prior art keywords
- filtering
- raw water
- dissolved
- phosphorus
- pipe
- 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
Links
Landscapes
- Removal Of Specific Substances (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は、水中に溶存する燐の除去方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for removing phosphorus dissolved in water.
一般に水中に溶存する燐は、窒素と共に水の高栄養化の
一端をにない公害発生源として太き(問題化されている
。そして、燐を除去する手段として石灰又は金属塩によ
る凝集、燐鉱石による方法等が採用されているが、前者
す°なわち石灰又は金属塩による方法では汚泥の発生が
問題となり、また、後者すなわち燐鉱石による方法につ
いては充分なr速が得られないなどの問題があり、その
改良が望まれているのが現状である。In general, phosphorus dissolved in water, together with nitrogen, is a major source of pollution that contributes to the high nutrient content of water. However, the former method, i.e., the method using lime or metal salts, has the problem of generating sludge, and the latter method, i.e., the method using phosphate rock, has problems such as not being able to obtain sufficient r-speed. Currently, there is a need for improvement.
この発明は、上記事情に鑑みなされたもので、凝集操作
を行うことなくr過操作のみで、しかも、従来のものよ
り速いf速によって脱燐を行うことを特徴とする水中に
溶存する燐の除去方法を提供しようとするものである。This invention has been made in view of the above circumstances, and is characterized in that it dephosphorizes phosphorus dissolved in water by only r-over-operation without performing a coagulation operation, and at an f-speed faster than conventional methods. The purpose is to provide a removal method.
以下にこの発明の実施例を添付図面をもって詳細に説明
する。Embodiments of the present invention will be described in detail below with reference to the accompanying drawings.
まず、図面に示すように、接触触媒r材2を配した密閉
濾過タンク1を用意して、原水中の溶存酸素の増加に有
利なようにする。この場合、r材2には例えば酸化鉄接
触触媒f材を用い、その−例として、オイルカーボンに
乾燥粘土を混合し、これに酸化鉄を加えて透粒し、これ
を850℃程度の温度で酸素の存在のない状態で30分
〜1時間焼成した後、篩分けしてr材2とする。なお、
このr材2の成分の分析比は以下の表のようになる。First, as shown in the drawings, a closed filtration tank 1 in which a contact catalyst material 2 is arranged is prepared so as to be advantageous for increasing dissolved oxygen in raw water. In this case, for example, an iron oxide contact catalyst F material is used as the R material 2. For example, oil carbon is mixed with dry clay, iron oxide is added thereto, the mixture is granulated, and the mixture is heated to a temperature of about 850°C. After firing for 30 minutes to 1 hour in the absence of oxygen, the material is sieved to obtain R material 2. In addition,
The analysis ratio of the components of this r material 2 is as shown in the table below.
なお、上記分析方法は、JIS R,−5202ポルト
ランドセメント分析法の準用である。Note that the above analysis method is a mutatis mutandis application of JIS R, -5202 Portland cement analysis method.
上記のように形成されるr材2を1層厚で濾過タンク1
のf床3の上に積層して1層を構成する。そして、濾過
に際しては、原水流入管4に図示しないコンプレッサに
接続する加圧空気を送入して燐溶存の原水に対し充分な
溶存酸素を存在せしめ、次に原水流入管4に接続する接
続管5から原水に硫酸第一鉄溶液を注入して原水を濾過
タンク1内において、LV= 12.5〜MSV= 1
2.51/Hの条件下で濾過する。なお、濾過に際し、
原水中の余剰空気は、濾過タンク1の上部に設けた安全
弁6により排出され、r層中には気泡が発生しないよう
にしである。なお7は処理水取出し管である。A filtration tank 1 is made of R material 2 formed as described above with one layer thickness.
It is laminated on top of the f-floor 3 to form one layer. During filtration, pressurized air connected to a compressor (not shown) is fed into the raw water inflow pipe 4 to make sufficient dissolved oxygen exist in the raw water containing dissolved phosphorus, and then the connecting pipe connected to the raw water inflow pipe 4 is 5, inject the ferrous sulfate solution into the raw water and place the raw water in the filtration tank 1, LV = 12.5 ~ MSV = 1
Filter under conditions of 2.51/H. In addition, when filtering,
Excess air in the raw water is discharged by a safety valve 6 provided at the top of the filtration tank 1 to prevent air bubbles from forming in the r layer. Note that 7 is a treated water outlet pipe.
上記のようにして行った実験の結果、燐の除去状況は下
表のようになりto
なおこの場合、燐酸と硫酸第一鉄の反応は次のようにな
る。すなわち、
3Fe+ 2PO4→Fea(PO4)2ここで、Fe
5(po4 )2 は酸素雰囲気状態ではFePO4
に変化する。そして、r材表面でのこの反応が進行し、
f材表面にこの生成分が付着し肥厚してゆくが、触媒機
能の劣化は見られず、一定時間経過後は1層の逆洗を実
施し、濾過機能の回復を図ることができる。As a result of the experiment conducted as described above, the phosphorus removal status is as shown in the table below. In this case, the reaction between phosphoric acid and ferrous sulfate is as follows. That is, 3Fe+ 2PO4→Fea(PO4)2 where, Fe
5(po4)2 is FePO4 in an oxygen atmosphere
Changes to Then, this reaction progresses on the surface of the r material,
Although this product adheres to the surface of the f-material and becomes thick, no deterioration of the catalyst function is observed, and after a certain period of time, one layer of backwashing can be carried out to restore the filtration function.
なお、上記実施例では接触触媒濾過が酸化鉄接触触媒の
場合を示したが、必ずしもこの酸化鉄に限定されるもの
ではなく、第一鉄を第二鉄に酸化できるものであればよ
い。In the above embodiments, the case where the catalytic catalyst filtration is an iron oxide catalytic catalyst is shown, but it is not necessarily limited to this iron oxide, and any catalyst that can oxidize ferrous iron to ferric iron may be used.
以上に説明したようK、この発明の燐の除去方法によれ
ば、凝集操作を行うことなく濾過操作のみで、しかも、
従来の燐鉱石を用いる方法よりも速いf速、例えば3倍
程のr速力冑能となるため、設置面積を小さくして能率
良く脱燐操作を行うことができるなどの優れた効果が得
られ、その利用価値は顕著である。As explained above, according to the method for removing phosphorus of the present invention, only a filtration operation is required without performing a flocculation operation, and
Since the f-speed is faster than the conventional method using phosphate rock, for example, the r-speed is about three times faster, excellent effects such as the ability to reduce the installation area and perform the dephosphorization operation efficiently can be obtained. , its utility value is remarkable.
図面はこの発明の方法の一例を示す説明図である。
図において、
l 密閉r過タンク 2 接触触媒r材3F 床
4 原水流入管5 接続管 6
安全弁
7 処理水取出し管
である。
特許出願人 水道機工株式会社The drawings are explanatory diagrams showing an example of the method of the present invention. In the figure: 1 Sealed filtration tank 2 Catalyst catalyst material 3F Floor
4 Raw water inflow pipe 5 Connection pipe 6
Safety valve 7 This is a pipe for taking out treated water. Patent applicant Suido Kiko Co., Ltd.
Claims (1)
た接触触媒r材を用意し、この沢材で燐を溶存する原水
を充分な溶存酸素と第一鉄イオンの存在のもとにr遇す
ることにより、接触触媒の介在で両者の反応を図り、燐
を不溶解物質に変じて除去することを特徴とする水中に
溶存する燐の除去方法。A catalytic catalyst material with a catalytic interface made of an oxidized metal such as iron is prepared on the particle surface of the material, and this material is used to catalyze raw water containing dissolved phosphorus in the presence of sufficient dissolved oxygen and ferrous ions. 1. A method for removing phosphorus dissolved in water, which is characterized by converting phosphorus into an insoluble substance and removing it by causing a reaction between the two through the intervention of a contact catalyst.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4454082A JPS58163491A (en) | 1982-03-23 | 1982-03-23 | Removal of phosphorus dissolved in water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4454082A JPS58163491A (en) | 1982-03-23 | 1982-03-23 | Removal of phosphorus dissolved in water |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58163491A true JPS58163491A (en) | 1983-09-28 |
JPS618758B2 JPS618758B2 (en) | 1986-03-17 |
Family
ID=12694338
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4454082A Granted JPS58163491A (en) | 1982-03-23 | 1982-03-23 | Removal of phosphorus dissolved in water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58163491A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007268338A (en) * | 2006-03-30 | 2007-10-18 | Green Japan:Kk | Method for removing phosphorus included underwater |
CN115321713A (en) * | 2022-09-02 | 2022-11-11 | 江西师范大学 | Solid-liquid separation and recycling method for pig raising wastewater |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61252429A (en) * | 1985-04-30 | 1986-11-10 | Toyotomi Kogyo Co Ltd | Safety device for petroleum burner |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4983256A (en) * | 1972-12-18 | 1974-08-10 |
-
1982
- 1982-03-23 JP JP4454082A patent/JPS58163491A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4983256A (en) * | 1972-12-18 | 1974-08-10 |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2007268338A (en) * | 2006-03-30 | 2007-10-18 | Green Japan:Kk | Method for removing phosphorus included underwater |
CN115321713A (en) * | 2022-09-02 | 2022-11-11 | 江西师范大学 | Solid-liquid separation and recycling method for pig raising wastewater |
Also Published As
Publication number | Publication date |
---|---|
JPS618758B2 (en) | 1986-03-17 |
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