JPS583968B2 - aluminum gun - Google Patents
aluminum gunInfo
- Publication number
- JPS583968B2 JPS583968B2 JP50116968A JP11696875A JPS583968B2 JP S583968 B2 JPS583968 B2 JP S583968B2 JP 50116968 A JP50116968 A JP 50116968A JP 11696875 A JP11696875 A JP 11696875A JP S583968 B2 JPS583968 B2 JP S583968B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- aluminum
- containing waste
- precipitate
- membrane
- 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
Links
Landscapes
- Removal Of Specific Substances (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
Description
【発明の詳細な説明】
本発明は、アルミニウム含有廃液中の有機物その他の不
純物を除去し、アルミニウム含有液を精製する方法に関
するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for purifying an aluminum-containing liquid by removing organic substances and other impurities from the aluminum-containing waste liquid.
アルミニウム含有廃液の例としては、金属表面処
理廃水、上水汚泥の酸処理による回収ばん土液などがあ
る。Examples of aluminum-containing waste liquids include metal surface treatment waste water and soil liquid recovered from acid treatment of tap water sludge.
金属表面処理廃水には、酸性廃水とアルカリ性廃水があ
り、酸性廃水には濃度の高い更新廃水と濃度は低いが排
水量の多い洗浄廃水とがあり、また、アルカリ性廃水に
も濃度の高い更新廃水と濃度が低い洗浄廃水とがある。There are two types of metal surface treatment wastewater: acidic wastewater and alkaline wastewater. Acidic wastewater includes high-concentration renewal wastewater and cleaning wastewater, which has a low concentration but a large amount of drainage. Alkaline wastewater also includes high-concentration renewal wastewater and high-concentration renewal wastewater. There is cleaning wastewater with low concentration.
これらの廃水を回収しようとする際に、問題となるのが
共存する汚染物、例えば懸濁性物質、油、グリース、鉄
イオン,その他の有機物等であり、これらを除去する必
要がある。When attempting to recover these wastewaters, problems arise from coexisting contaminants such as suspended solids, oil, grease, iron ions, and other organic substances, which must be removed.
また、上水汚泥中にはアルミニウム水酸化物が含有され
、この汚泥の脱水処理に当っては、予じめ汚泥中のアル
ミニウム水酸化物を硫酸によって溶離して脱水性を向上
させ、溶離された液を回収ばん土として再利用する例が
あるが、この回収ばん土液中にはかなりの着色性有機物
、鉄イオンが含有され、赤茶色に着色されているため、
この着色性有機物を除去することは再利用にとって必要
である。In addition, aluminum hydroxide is contained in clean water sludge, and when dewatering this sludge, the aluminum hydroxide in the sludge is eluted with sulfuric acid in advance to improve dewatering properties, and the eluted aluminum hydroxide is There is an example of reusing the collected soil as recovered soil, but this recovered soil contains a considerable amount of colored organic matter and iron ions, giving it a reddish-brown color.
Removal of this colored organic matter is necessary for reuse.
本発明は、各種アルミニウム含有廃液中の不純物を効果
的に除去することによってアルミニウム含有廃液を精製
し、もって再利用に便ならしめることを目的とするもの
である。The object of the present invention is to purify aluminum-containing waste liquids by effectively removing impurities in various aluminum-containing waste liquids, thereby making them convenient for reuse.
本発明は、アルミニウム含有廃液中の遊離の酸またはア
ルカリを予じめ実質的に除去したのち、アルミニウム沈
殿生成剤を添加して、該液中の一部のアルミニウムを沈
殿にかえ、沈殿物を分離除去することを特徴とし、この
際、もし液中に鉄イオンが存在するときは、曝気するこ
とによって第2鉄イオンの大部分を生殿させてアルミニ
ウム沈殿と共に分離除去するものである。In the present invention, after substantially removing free acid or alkali in aluminum-containing waste liquid, an aluminum precipitant is added to convert some aluminum in the liquid into precipitate, and the precipitate is removed. It is characterized by separation and removal, and at this time, if iron ions are present in the liquid, most of the ferric ions are precipitated by aeration and separated and removed together with the aluminum precipitate.
本発明における液中の遊離の酸またはアルカリを除去す
る方法としては、薬剤中和、イオン交換膜法、イオン交
換樹脂法などがあり、このようにして酸またはアルカリ
を除去したのちに添加するアルミニウム沈殿生成剤とし
ては、該液が酸性の場合にはアルカリ剤、アルカリ性の
場合には酸剤を用いる。Methods for removing free acid or alkali in the liquid in the present invention include chemical neutralization, ion exchange membrane method, ion exchange resin method, etc. After removing acid or alkali in this way, aluminum is added. As the precipitating agent, an alkaline agent is used when the liquid is acidic, and an acidic agent is used when the liquid is alkaline.
また、アルミニウム沈殿生成に当っては、アルミニウム
含有液の精製といった観点から,該液中に多量に含有さ
れるアルミニウム塩の一部に加水分解をおこさせて生殿
するにとどめることが必要であり、この生成沈殿に液中
の懸濁物質、第2鉄イオン、有機性色度などの不純物を
吸着させ、大部分のアルミニウム塩の回収をはかるもの
である。In addition, in producing aluminum precipitate, from the viewpoint of purifying the aluminum-containing liquid, it is necessary to hydrolyze and precipitate only a portion of the aluminum salts contained in large amounts in the liquid. , Impurities such as suspended solids, ferric ions, and organic chromaticity in the liquid are adsorbed to the resulting precipitate to recover most of the aluminum salt.
さらに、液中の不純物を吸着した沈殿を分離除去する方
法としては、沈降、浮上、濾過、遠心分離などがあり、
また、限外濾過膜乃至マイクロポーラス膜、あるいは多
孔性、透水性の支持体に金属水酸化物乃至酸化物、有機
化合物などからなるメディアを形成させたものを用いる
膜分離法も有効に利用することができる。Furthermore, methods for separating and removing precipitates that have adsorbed impurities in the liquid include sedimentation, flotation, filtration, and centrifugation.
In addition, membrane separation methods using ultrafiltration membranes, microporous membranes, or media made of metal hydroxides, oxides, organic compounds, etc. formed on porous, water-permeable supports can also be effectively utilized. be able to.
次に、本発明の実施態様を図面にもとづいて説明する。Next, embodiments of the present invention will be described based on the drawings.
第1図において、硫酸を含有する酸性アルミニウム含有
廃液1を陰イオン交換膜電気透析装置Aへ導入し、ここ
で硫酸2を分離し系外へ排出し、かくて実質的に遊離の
酸が除去された液3は限外濾過膜を装着したセルBに圧
力1〜5kgf/cm2にて送液されるが、途中で苛性
ソーダ液4を注入して液中のアルミニウムの一部を水酸
化物に転換させて液中の不純物を吸着させるが、必要に
よってさらに高分子電解質などの凝集助剤を添加して凝
集体を発生させる。In FIG. 1, an acidic aluminum-containing waste liquid 1 containing sulfuric acid is introduced into an anion exchange membrane electrodialyzer A, where sulfuric acid 2 is separated and discharged from the system, thus substantially removing free acid. The resulting liquid 3 is sent to cell B equipped with an ultrafiltration membrane at a pressure of 1 to 5 kgf/cm2, but midway through, a caustic soda solution 4 is injected to convert some of the aluminum in the liquid into hydroxide. The liquid is converted to adsorb impurities in the liquid, and if necessary, a coagulation aid such as a polymer electrolyte is further added to generate aggregates.
かくて限外濾過膜装着セルBで濃縮された沈殿含有スラ
リ5と、膜透過した精製液6はそれぞれ系外へ排出され
る。The precipitate-containing slurry 5 concentrated in the cell B equipped with the ultrafiltration membrane and the purified liquid 6 that has passed through the membrane are each discharged to the outside of the system.
また第2図示例は、上水汚泥の酸処理による回収ばん土
液の精製に関する実施態様であって、回収されたばん土
液7に苛性ソーダ液4を注入することによって、遊離酸
の実質的除去ならびに液中の一部のアルミニウムを加水
分解させて沈殿を発生させ、次いで液中に鉄イオンや易
分解性有機物が含有されるときは、曝気装置Cに導入し
、圧送される空気8等の酸化ガスによって所要時間曝気
し、液中の第1鉄イオンを酸化して第2鉄の沈殿を発生
させ、また有機物の分解を行ない、一部生成されたアル
ミニウム水酸化物沈殿に液中の不純物、第2鉄沈殿等を
吸着させながら、液9は必要によって凝集助剤10が添
加され、圧力1〜5kpf/cm2で多孔性透水支持体
を装着したセルDへ圧送される。The second illustrated example is an embodiment related to the purification of recovered sand sludge through acid treatment of clean water sludge, in which free acid is substantially removed by injecting caustic soda solution 4 into the collected sand sludge 7. In addition, some aluminum in the liquid is hydrolyzed to generate a precipitate, and then when the liquid contains iron ions or easily decomposable organic substances, it is introduced into the aeration device C and the air 8 etc. Aerating with oxidizing gas for a required period of time oxidizes ferrous ions in the liquid to generate ferric precipitates, and also decomposes organic matter to partially form aluminum hydroxide precipitates and impurities in the liquid. While adsorbing ferric precipitates and the like, the liquid 9 is added with a coagulation aid 10 if necessary, and is fed under pressure to a cell D equipped with a porous water-permeable support at a pressure of 1 to 5 kpf/cm2.
セルDは0.1〜数μ程度の多孔性透水支持体面上に液
中の沈殿物が付着して、一種の濾過膜が形成されたもの
で、ここで圧送される液中の沈殿物、不純物を除去し、
濃縮液5と膜透過精製液6はそれぞれ系外へ排出される
。In Cell D, precipitates in the liquid adhere to the surface of a porous water-permeable support with a size of about 0.1 to several microns, forming a kind of filtration membrane. remove impurities,
The concentrated liquid 5 and the membrane-permeated purified liquid 6 are each discharged to the outside of the system.
なお、アルミニウム含有廃液がアルカリを含有するとき
は、第1図示例では陰イオン交換膜電気透析装置Aに代
えて陽イオン交換膜電気透析装置を使用すればよく、ま
た各図示例において注入される苛性ソーダ液4に代えて
酸剤を使用するとよいO
また、上記実施態様において最終的に得られたアルミニ
ウム含有精製液6は、さらに逆浸透膜によって濃縮して
もよい。Note that when the aluminum-containing waste liquid contains alkali, a cation exchange membrane electrodialysis device may be used in place of the anion exchange membrane electrodialysis device A in the first illustrated example, and in each illustrated example, a cation exchange membrane electrodialysis device may be used. It is preferable to use an acid agent instead of the caustic soda solution 4. In addition, the aluminum-containing purified liquid 6 finally obtained in the above embodiment may be further concentrated using a reverse osmosis membrane.
以上述べたように本発明によれば、アルミニウム含有廃
液中の不純物を極めて効果的に除去して精製することが
でき、その再利用をはかり、さらに精製液の爾後の濃縮
処理操作も効率よく進めることができる。As described above, according to the present invention, impurities in the aluminum-containing waste liquid can be extremely effectively removed and purified, the waste liquid can be reused, and the subsequent concentration treatment of the purified liquid can be efficiently carried out. be able to.
次に本発明の実施例を示す。Next, examples of the present invention will be shown.
導電率14300μV/cm、pH1.45/25℃、
懸濁固形物1.4g/l,A[として1820m9/l
、色度2400度、全Fe410m9/l、Mn47■
/lを含有するアルミニウム含有廃液に、10%苛性ソ
ーダ液を添加してpH2.5に調整し、1.5時間曝気
してAl(OH)3、Fe(OH)3を生殿させ、これ
を0,25μのポリエステル系のマイクロポーラス膜を
装着したセルに圧力1. 5 kgf/am2で通液し
たところ、導電率11500μv/cm,pH2.55
/25℃、懸濁固形物28〜30〜/l、Al1710
mg/l、色度120度、第IFeとして210mg/
l、Mn 35mg/lの膜透過液を得た。Electrical conductivity 14300 μV/cm, pH 1.45/25°C,
Suspended solids 1.4 g/l, A [as 1820 m9/l
, chromaticity 2400 degrees, total Fe410m9/l, Mn47■
A 10% caustic soda solution was added to the aluminum-containing waste solution containing /l to adjust the pH to 2.5, and the mixture was aerated for 1.5 hours to precipitate Al(OH)3 and Fe(OH)3. A pressure of 1. When the liquid was passed through at 5 kgf/am2, the conductivity was 11,500 μv/cm, and the pH was 2.55.
/25℃, suspended solids 28-30~/l, Al1710
mg/l, chromaticity 120 degrees, 210 mg/l as No. IFe
A membrane permeate containing 35 mg/l and Mn was obtained.
この場合の膜透過水量は、圧力1.5kgf/cm2で
27001/m2・dであり、懸濁固形物の除去率は9
8%であった。In this case, the amount of water permeated through the membrane is 27001/m2・d at a pressure of 1.5 kgf/cm2, and the removal rate of suspended solids is 9
It was 8%.
第1図および第2図は、それぞれ本発明の実施態様を示
す系統説明図である。
1・・・・・・酸性アルミニウム含有廃液、4・・・・
・・苛性ソーダ液、6・・・・・・精製液、7・・・・
・・回収ばん土液、A・・・・・・陰イオン交換膜電気
透析装置、B・・・・・・限外濾過膜装着セル、C・・
・・・・曝気装置、D・・・・・・多孔性透水支持体装
着セル。FIG. 1 and FIG. 2 are system explanatory diagrams showing embodiments of the present invention, respectively. 1...Acidic aluminum-containing waste liquid, 4...
... Caustic soda solution, 6 ... Purified liquid, 7 ...
...Recovered soil liquid, A... Anion exchange membrane electrodialysis device, B... Cell equipped with ultrafiltration membrane, C...
...Aeration device, D...Cell equipped with a porous water-permeable support.
Claims (1)
を実質的に除去したるのち、アルミニウム沈殿生成剤を
添加し、該液中のアルミニウム水酸化物の生成を一部に
とどめ、沈殿物を分離除去することを特徴とするアルミ
ニウム含有廃液の精製方法。1 After substantially removing free acid or alkali in the aluminum-containing waste liquid, add an aluminum precipitation agent to limit the formation of aluminum hydroxide in the liquid to a portion and separate and remove the precipitate. A method for purifying aluminum-containing waste liquid, characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50116968A JPS583968B2 (en) | 1975-09-26 | 1975-09-26 | aluminum gun |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50116968A JPS583968B2 (en) | 1975-09-26 | 1975-09-26 | aluminum gun |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5240492A JPS5240492A (en) | 1977-03-29 |
| JPS583968B2 true JPS583968B2 (en) | 1983-01-24 |
Family
ID=14700201
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP50116968A Expired JPS583968B2 (en) | 1975-09-26 | 1975-09-26 | aluminum gun |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS583968B2 (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS54131717U (en) * | 1978-03-06 | 1979-09-12 | ||
| JP2753441B2 (en) * | 1993-11-16 | 1998-05-20 | 大同鋼板株式会社 | Ceiling support structure |
| JP2753442B2 (en) * | 1993-12-08 | 1998-05-20 | 大同鋼板株式会社 | Ceiling support structure |
| TWI693888B (en) * | 2018-05-08 | 2020-05-21 | 國立中正大學 | Automatic water quality adjustment system and method |
-
1975
- 1975-09-26 JP JP50116968A patent/JPS583968B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5240492A (en) | 1977-03-29 |
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