JPH0230296B2 - RINJOKYOZAI - Google Patents
RINJOKYOZAIInfo
- Publication number
- JPH0230296B2 JPH0230296B2 JP6607885A JP6607885A JPH0230296B2 JP H0230296 B2 JPH0230296 B2 JP H0230296B2 JP 6607885 A JP6607885 A JP 6607885A JP 6607885 A JP6607885 A JP 6607885A JP H0230296 B2 JPH0230296 B2 JP H0230296B2
- Authority
- JP
- Japan
- Prior art keywords
- phosphorus
- present
- removing agent
- agent
- heat treatment
- 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 - Lifetime
Links
- 229910052698 phosphorus Inorganic materials 0.000 claims description 40
- 239000011574 phosphorus Substances 0.000 claims description 40
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 38
- 239000003795 chemical substances by application Substances 0.000 claims description 17
- 238000010438 heat treatment Methods 0.000 claims description 6
- 239000002075 main ingredient Substances 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 239000004058 oil shale Substances 0.000 description 6
- 239000002699 waste material Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 4
- 239000010842 industrial wastewater Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 1
- BNIILDVGGAEEIG-UHFFFAOYSA-L disodium hydrogen phosphate Chemical compound [Na+].[Na+].OP([O-])([O-])=O BNIILDVGGAEEIG-UHFFFAOYSA-L 0.000 description 1
- 229910000397 disodium phosphate Inorganic materials 0.000 description 1
- 235000019800 disodium phosphate Nutrition 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 238000012851 eutrophication Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 150000003017 phosphorus Chemical class 0.000 description 1
- -1 phosphorus compound Chemical class 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Removal Of Specific Substances (AREA)
- Water Treatment By Sorption (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Fertilizers (AREA)
Description
〔技術分野〕
本発明は新規なリン除去剤に関するものであ
る。
〔従来技術〕
リンは、水質の富栄養化現象をもたらす原因物
質となることから、工業排水はもちろん、下水生
活排水、産業排水、その他の汚染水からリンを除
去することが必要である。
従来、排水中からのリンを除去する方法として
は種々の方法が知られているが、いずれもコスト
的に未だ満足し得るものはなく、安価なリン除去
剤の開発が望まれている。
〔目 的〕
本発明は安価なリン除去剤を提供することを目
的とする。
〔構 成〕
本発明によれば、オイルシエールの熱処理残渣
を主剤とするリン除去剤が提供される。
本発明のリン除去剤は、オイルシエールの熱処
理残渣を主剤とする。この場合、オイルシエール
の熱処理は、温度400〜1000℃、好ましくは500〜
800℃である。本発明のリン除去剤としては、一
般の廃オイルシエールをそのまま用いることがで
きるし、好ましくはこれをさらに熱処理して用い
ることができ、非常に安価に得ることがきる。こ
のリン除去剤は、微粉末状又は顆粒状等の種々の
形状で用いることができる。
本発明のリン除去剤を用いて水中に溶解するリ
ンを除去するには、本発明のリン除去剤に対し、
リンを含む水を接触させればよい。この場合、リ
ン除去剤とリン含有水との接触方式としては、リ
ン含有水中にリン除去剤を投入する方式の他、リ
ン除去剤を充填したカラムにリン含有水を流通さ
せる方式等がある。リン含有水にリン除去剤を投
入してリンの除去を行う場合、リン含有水に対す
るリン除去剤の使用割合は、通常0.1〜10重量%、
好ましくは0.5〜5重量%である。処理時間は、
通常30分〜3時間程度である。
〔効 果〕
本発明のリン除去剤は、リンを含む種々の排水
からのリンの除去に適用される。この場合、リン
を吸着したリン除去剤は、吸着したリン成分がク
溶性のものであるため、リン肥料として有効利用
することができる。
〔実施例〕
次に本発明を実施例によりさらに詳細に説明す
る。
実施例 1
リン除去剤として、米国コロラド産のオイルシ
エールを500〜600℃で乾留した下記表−1に示す
組成の廃オイルシエール及びその熱処理残渣を用
いた。
[Technical Field] The present invention relates to a novel phosphorus removal agent. [Prior Art] Since phosphorus is a causative substance that causes eutrophication of water quality, it is necessary to remove phosphorus from not only industrial wastewater, but also sewage domestic wastewater, industrial wastewater, and other contaminated water. Conventionally, various methods have been known for removing phosphorus from wastewater, but none of them are yet satisfactory in terms of cost, and there is a desire to develop an inexpensive phosphorus removal agent. [Purpose] The purpose of the present invention is to provide an inexpensive phosphorus removal agent. [Structure] According to the present invention, there is provided a phosphorus removal agent containing a heat-treated residue of oil shale as a main ingredient. The phosphorus removing agent of the present invention has a heat-treated residue of oil shale as a main ingredient. In this case, the oil sierre heat treatment is performed at a temperature of 400-1000℃, preferably 500-1000℃.
The temperature is 800℃. As the phosphorus removing agent of the present invention, general waste oil shale can be used as it is, or preferably it can be further heat-treated before use, and can be obtained at a very low cost. This phosphorus removing agent can be used in various forms such as fine powder or granules. In order to remove phosphorus dissolved in water using the phosphorus remover of the present invention, for the phosphorus remover of the present invention,
All you have to do is bring it into contact with water containing phosphorus. In this case, methods for bringing the phosphorus removing agent into contact with the phosphorus-containing water include a method in which the phosphorus removing agent is introduced into the phosphorus-containing water, and a method in which the phosphorus-containing water is passed through a column filled with the phosphorus removing agent. When removing phosphorus by adding a phosphorus remover to phosphorus-containing water, the ratio of the phosphorus remover to the phosphorus-containing water is usually 0.1 to 10% by weight.
Preferably it is 0.5 to 5% by weight. The processing time is
It usually takes about 30 minutes to 3 hours. [Effects] The phosphorus removal agent of the present invention is applicable to the removal of phosphorus from various wastewaters containing phosphorus. In this case, the phosphorus remover that has adsorbed phosphorus can be effectively used as a phosphorus fertilizer because the adsorbed phosphorus component is soluble. [Example] Next, the present invention will be explained in more detail with reference to Examples. Example 1 As a phosphorus removal agent, waste oil shale from Colorado, USA, which was carbonized at 500 to 600°C and whose composition is shown in Table 1 below, and its heat-treated residue were used.
【表】
前記廃オイルシエールの熱処理は、電気炉中
で、200〜1000℃で、2時間行つた。
次に、前記の廃オイルシエール及びその熱処理
残渣を、リン除去剤として用い、これをリン化合
物としてリン酸水素ナトリウム(Na2HPO4)
0.001モルを水100mlに溶解した水溶液に添加し、
25℃で2時間撹拌混合した後、リン除去剤を濾過
し、濾液中の残留PO4 3を測定し、その測定結果
に基づいてリン除去率を算出した。その結果を次
表に示す。
なお、表−2において、熱処理温度が0のリン
除去剤は、廃オイルシエールそれ自体を意味す
る。[Table] The heat treatment of the waste oil siel was carried out in an electric furnace at 200 to 1000°C for 2 hours. Next, the above-mentioned waste oil shale and its heat treatment residue were used as a phosphorus removing agent, and this was converted into sodium hydrogen phosphate (Na 2 HPO 4 ) as a phosphorus compound.
Add 0.001 mol to an aqueous solution of 100 ml of water,
After stirring and mixing at 25° C. for 2 hours, the phosphorus removing agent was filtered, and the residual PO 4 3 in the filtrate was measured, and the phosphorus removal rate was calculated based on the measurement results. The results are shown in the table below. In addition, in Table 2, the phosphorus removing agent whose heat treatment temperature is 0 means waste oil siel itself.
【表】
実施例 2
実施例1において、廃オイルシエールの代り
に、未熱処理のオイルシエールを用いた以外は同
様にして実験を行つた。その結果を表−3に示
す。
なお、表−3において、熱処理温度が0のリン
除去剤は、未熱処理のオイルシエールそれ自体を
意味する。[Table] Example 2 An experiment was carried out in the same manner as in Example 1, except that unheated oil sheer was used instead of waste oil sheer. The results are shown in Table-3. In addition, in Table 3, the phosphorus removing agent whose heat treatment temperature is 0 means unheat-treated oil shale itself.
【表】【table】
Claims (1)
ン除去剤。1. A phosphorus removal agent whose main ingredient is oil siel heat treatment residue.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6607885A JPH0230296B2 (en) | 1985-03-29 | 1985-03-29 | RINJOKYOZAI |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6607885A JPH0230296B2 (en) | 1985-03-29 | 1985-03-29 | RINJOKYOZAI |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61222535A JPS61222535A (en) | 1986-10-03 |
JPH0230296B2 true JPH0230296B2 (en) | 1990-07-05 |
Family
ID=13305453
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6607885A Expired - Lifetime JPH0230296B2 (en) | 1985-03-29 | 1985-03-29 | RINJOKYOZAI |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0230296B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0464994U (en) * | 1990-10-09 | 1992-06-04 |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19859443A1 (en) * | 1998-12-22 | 2000-06-29 | Rohrbach Zement Gmbh & Co Kg | Absorbent and / or adsorbent to reduce pollutant levels in polluted media |
JP5564680B2 (en) * | 2009-07-21 | 2014-07-30 | 地方独立行政法人東京都立産業技術研究センター | Glass foam, phosphoric acid adsorbent containing glass foam, plant growth medium containing glass foam, and method for producing glass foam |
-
1985
- 1985-03-29 JP JP6607885A patent/JPH0230296B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0464994U (en) * | 1990-10-09 | 1992-06-04 |
Also Published As
Publication number | Publication date |
---|---|
JPS61222535A (en) | 1986-10-03 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4479924A (en) | Process for the separation of heavy metal compounds from phosphoric acid | |
JP4470216B2 (en) | Treatment method for fluorine-containing solid waste | |
ES2705166T3 (en) | Method to remove heavy metals from silicate sources during the manufacture of a silicate | |
JPH0230296B2 (en) | RINJOKYOZAI | |
KR100239916B1 (en) | Immobilization of metal contaminants from a liquid to a solid medium | |
US4071546A (en) | Silicon-containing chelating composition and method therefor | |
JPS6177614A (en) | Purification of phosphoric acid | |
JPH02233503A (en) | Purification of hydrochloric acid | |
DE2619421A1 (en) | PROCESS FOR THE REGENERATION OF DIALYSIS FLUIDS IN HAEMODIALYSIS SYSTEMS | |
JPS6340575B2 (en) | ||
JP2001129562A (en) | Phosphorus removing method | |
JPS6319211B2 (en) | ||
JPH03505542A (en) | Filtration media for technical filters | |
JP3728807B2 (en) | Processing method for heavy metal-containing ash | |
CN113274977B (en) | Mercury removal adsorbent for removing Hg (II) in water and preparation method and application thereof | |
RU2146403C1 (en) | Method for water cleaning from radionuclides | |
CN112897668B (en) | Defluorination medicament and preparation method and application thereof | |
JPS583639A (en) | Fluorine disposing agent | |
JP4840846B2 (en) | Phosphorus recovery material, production method thereof, and fertilizer using phosphorus recovery material | |
JP2005239438A (en) | Method for recovering ammonia and/or ammonium ion in waste water or exhaust gas | |
JPS57192252A (en) | Method of regenerating electroless copper plating solution | |
JP3318860B2 (en) | How to clean mercury contaminated soil | |
KR20210052674A (en) | Method for preparing ion exchange resin with reduced metal impurity content | |
SU1407915A1 (en) | Method of purifying waste water of fluosilicic acid | |
SU1344402A1 (en) | Method of producing carbon-containing sorbent |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
EXPY | Cancellation because of completion of term |