JPS5932404B2 - Method for producing basic aluminum solution - Google Patents

Method for producing basic aluminum solution

Info

Publication number
JPS5932404B2
JPS5932404B2 JP51037045A JP3704576A JPS5932404B2 JP S5932404 B2 JPS5932404 B2 JP S5932404B2 JP 51037045 A JP51037045 A JP 51037045A JP 3704576 A JP3704576 A JP 3704576A JP S5932404 B2 JPS5932404 B2 JP S5932404B2
Authority
JP
Japan
Prior art keywords
acid
basic aluminum
aluminum
solution
mixture
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
Application number
JP51037045A
Other languages
Japanese (ja)
Other versions
JPS51128694A (en
Inventor
デビツド・ベリー
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.)
Evonik LIL Ltd
Original Assignee
Laporte Industries Ltd
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 Laporte Industries Ltd filed Critical Laporte Industries Ltd
Publication of JPS51128694A publication Critical patent/JPS51128694A/en
Publication of JPS5932404B2 publication Critical patent/JPS5932404B2/en
Expired legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • C02F1/5245Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F7/00Compounds of aluminium
    • C01F7/78Compounds containing aluminium and two or more other elements, with the exception of oxygen and hydrogen
    • C01F7/786Compounds containing aluminium and two or more other elements, with the exception of oxygen and hydrogen containing, besides aluminium, only anions, e.g. Al[OH]xCly[SO4]z

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Geology (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 本発明は塩基性アルミニウム含有溶液の製造方法及び水
処理、より具体的にいえば飲用水、下水または下水スラ
ッジの処理に於けるこの溶液の製造方法に関するもので
ある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a process for the preparation of basic aluminum-containing solutions and for the treatment of water, more particularly in the treatment of drinking water, sewage or sewage sludge.

従来は、塩基性アルミニウム含有溶液の製造について各
種の方法が述べられていて、その溶液中では、巨大分子
が形成されその分子中に於てアルミニウム原子は硫酸塩
のような多価アニオンによって架橋されている。
Previously, various methods have been described for the production of basic aluminum-containing solutions, in which macromolecules are formed in which aluminum atoms are crosslinked by polyvalent anions such as sulfates. ing.

例えば、英国特許明細書第1222561号に於ては、
適切量の多価アニオンを塩基性塩化アルミニウム溶液へ
添加して混合物を好ましくは熟成する方法が記載されて
いる。
For example, in British Patent Specification No. 1222561,
A method is described in which a suitable amount of polyvalent anion is added to a basic aluminum chloride solution and the mixture is preferably aged.

しかし、硫酸塩アニオンを使用するときには得られる溶
液は塩基性塩化アルミニウム溶液を多価アニオン添加な
しで用いるよりも、飲用水、下水、あるいは下水スラッ
ジの処理に於てさほど効果が大きくないことを我々は発
見したのである。
However, we have found that when using sulfate anions, the resulting solutions are no more effective in treating drinking water, sewage, or sewage sludge than basic aluminum chloride solutions without the addition of polyvalent anions. was discovered.

このことは恐らくは、硫酸塩アニオンが与えられた条件
下で溶液中の塩基性塩化アルミニウムを攻撃し得ず、そ
の結果、溶液中に残る塩基性アルミニウムがはじめと同
じ分子量のものである傾向をもつためと、信じられる。
This probably means that the sulfate anion cannot attack the basic aluminum chloride in solution under the given conditions, so that the basic aluminum remaining in solution tends to be of the same molecular weight as the original. I can believe it.

驚くべきことには、上記方法に於て硫酸と燐酸の混合物
を使用すると、硫酸塩のみを含む比較溶液よりもスラッ
ジ脱水及び水処理に於てより有効である溶液が生じ得る
ことを、我々はここに発見したのである。
Surprisingly, we have found that the use of a mixture of sulfuric and phosphoric acids in the above process can result in a solution that is more effective in sludge dewatering and water treatment than a comparative solution containing only sulfate. I discovered it here.

本発明によれば、塩基性塩化アルミニウム溶液を、燐酸
と硫酸のモル比が2:1〜1:2の範囲にあり、しかも
各酸の量が塩基性塩化アルミニウム中のアルミニウム1
モル当り少なくとも0.05モルかつ全酸量がアルミニ
ウム1モル当り0.3モル以下となるよう混合した燐酸
と硫酸との混合物と混合し、この混合物を熟成する、塩
基性アルミニウム溶液の製造方法が提供される。
According to the present invention, a basic aluminum chloride solution is prepared in which the molar ratio of phosphoric acid and sulfuric acid is in the range of 2:1 to 1:2, and the amount of each acid is 1 % aluminum in the basic aluminum chloride.
A method for producing a basic aluminum solution, which comprises mixing with a mixture of phosphoric acid and sulfuric acid mixed such that the total acid amount is at least 0.05 mole per mole and not more than 0.3 mole per mole of aluminum, and aging this mixture. provided.

一般的には燐酸対硫酸のモル比は広範囲に変り得るが、
このモル比が2:1乃至1:2の範囲にあることが便利
である。
In general, the molar ratio of phosphoric acid to sulfuric acid can vary over a wide range;
Conveniently, this molar ratio is in the range 2:1 to 1:2.

理論的には、塩基性塩化アルミニウム溶液は極めて少量
の燐酸及び硫酸ででも処理し得るが、アルミニウム1モ
ルあたす少くとも0.05モルの各酸で以て処理するこ
とが好ましい。
In theory, basic aluminum chloride solutions can be treated with very small amounts of phosphoric acid and sulfuric acid, but it is preferred to treat them with at least 0.05 mole of each acid per mole of aluminum.

一般的には、酸の合計モル対アルミニウムのモル比が0
.3:1より多くなく、しばしば0.1:1乃至0.2
:1の範囲に入ることが望ましい。
Generally, the total moles of acid to molar ratio of aluminum is 0.
.. No more than 3:1, often 0.1:1 to 0.2
: It is desirable to fall within the range of 1.

塩基性塩化アルミニウム溶液をこのような量の酸で処理
することによって、水性媒体を効果的に処理するために
使用できる生成物が得られる。
Treatment of basic aluminum chloride solution with such amounts of acid provides a product that can be used to effectively treat aqueous media.

熟成を昇温で実施することが好ましい。Preferably, the aging is carried out at elevated temperatures.

一般には、所望の結果を達成するための熟成期間は熟成
が行なわれる温度とともに変る。
Generally, the period of ripening to achieve the desired result will vary with the temperature at which the ripening is carried out.

一般的にいえば、スラッジ脱水及び水処理の改善された
能力は長時間の熟成工程を採用することによって得られ
るが、実際的には、得られる改善度はすべて昇温下での
熟成によるコスト増と鈎合わねばならない。
Generally speaking, improved capabilities of sludge dewatering and water treatment can be obtained by adopting a longer aging process, but in practice, the improvements obtained are entirely due to the cost of aging at elevated temperatures. You have to match the increase.

実質的に還流加熱温度で約1時間乃至約6時間続けるこ
とが好ましく、特に約2乃至3時間力樋当である。
Preferably, the heating is continued at substantially reflux temperature for about 1 hour to about 6 hours, especially about 2 to 3 hours.

より低い温度での熟成はより長時間を必要とし、従って
実質上周辺温度での熟成は商業的に可能性がないことが
理解されるべきである。
It should be understood that aging at lower temperatures requires longer times and therefore aging at substantially ambient temperatures is not commercially viable.

塩基性塩化アルミニウム溶液は33%乃至83%の範囲
の塩基性をもつことができる。
The basic aluminum chloride solution can have a basicity ranging from 33% to 83%.

この溶液中の硫酸塩及び燐酸塩イオンを導入することの
効果はこの塩基性を下げるものである。
The effect of introducing sulfate and phosphate ions in this solution is to reduce its basicity.

ことが理解されるであろう。That will be understood.

塩基性塩化アルミニウム溶液の塩基性と使用される燐酸
及び硫酸の量は、最終溶液の塩基性が40乃至75%の
範囲、特に60乃至75%の範囲内に入るよう選ぶこと
が、実際的には好ましい。
It is practical to choose the basicity of the basic aluminum chloride solution and the amounts of phosphoric acid and sulfuric acid used such that the basicity of the final solution is in the range 40 to 75%, especially in the range 60 to 75%. is preferable.

一般的には、本発明による塩基性アルミニウム含有溶液
は貯蔵及び処理のために好ましくはAl2O3で表現し
て5乃至20%アルミニウム濃度をもつ。
Generally, the basic aluminum-containing solutions according to the invention preferably have an aluminum concentration of 5 to 20%, expressed as Al2O3, for storage and processing.

このような範囲内では、溶液は、安定すなわち数ケ月の
期間にわたってアルミニウム塩の沈澱を生ずることがな
いものを得ることができる。
Within such a range, a solution can be obtained that is stable, ie, without precipitation of aluminum salts over a period of several months.

このような溶液はまた安定性を損うことなくA1203
1乃至2%の程度のアルミニウム濃度へ稀釈することも
できる。
Such solutions also allow A1203 without loss of stability.
It can also be diluted to aluminum concentrations on the order of 1-2%.

本発明による溶液は飲用水供給または下水の処理または
調節に使用することができ、特に下水スラッジの調節に
特に向けられる。
The solution according to the invention can be used for the treatment or conditioning of potable water supplies or sewage, and is particularly directed in particular to the conditioning of sewage sludge.

このようにして処理された飲用水はしばしば貯槽に貯え
られ、スラッジから抽出された水は下水処理工場内に再
循環され、そこからの溢流水は近くの川または運河へ通
常はすてられる。
Potable water treated in this way is often stored in storage tanks, the water extracted from the sludge is recycled into the sewage treatment plant, and the overflow from there is usually dumped into a nearby river or canal.

溶液中の燐酸塩イオンは富栄養化をもたらし、すなわち
植物物質の成長を刺戟し、これは静水路または自由流動
水路の閉塞をもたらし得る。
Phosphate ions in solution lead to eutrophication, ie, stimulate the growth of plant matter, which can lead to blockage of static or free-flowing waterways.

従って、燐酸塩を含む水の処理はすべて富栄養化問題を
もたらし得ることが予想される。
Therefore, it is expected that any treatment of water containing phosphates may result in eutrophication problems.

しかし、一般には燐酸塩は水処理中に形成されるフロッ
クの中に保留され、かくして給水中へは実質的な程度に
は放出されない。
However, phosphates are generally retained in the flocs formed during water treatment and thus are not released to a substantial extent into the water supply.

事実、本発明による塩基性アルミニウム溶液での処理は
一般的には処理された水の中の燐酸塩水準の低下につな
がることを我々は発見したのである。
In fact, we have discovered that treatment with basic aluminum solutions according to the present invention generally leads to a reduction in phosphate levels in the treated water.

本発明によるいくつかの具体化は参考用のみの目的で、
ここにさらに詳しく次に説明する。
Some embodiments according to the invention are for reference purposes only:
This will be explained in more detail below.

実施例 1 本実施例に於ては、塩基性塩化アルミニウム溶液を硫酸
塩対燐酸塩対アルミニウム(Alとして表現)のモル比
が0.1 : 0.2 : 1.0のモル比で硫酸及び
燐酸と混合した。
Example 1 In this example, a basic aluminum chloride solution was treated with sulfuric acid and sulfuric acid at a molar ratio of sulfate to phosphate to aluminum (expressed as Al) of 0.1:0.2:1.0. Mixed with phosphoric acid.

混合物を1時間還流加熱し次いで冷却させる。The mixture is heated to reflux for 1 hour and then allowed to cool.

生成物は12.8重量%のアルミニウム含量(A120
3として表現)と45.2%の塩基性をもっていた。
The product has an aluminum content of 12.8% by weight (A120
3) and had a basicity of 45.2%.

安定性試験は生成物は少くとも5ケ月間安定であること
を示した。
Stability testing showed that the product was stable for at least 5 months.

実施例 2 本実施例に於ては、上記と同じ手順を実施したが但し、
硫酸塩対燐酸塩対アルミニウムのモル比はo、i:o、
1:1であり、混合物は2時間還流加熱し、そして生成
物は13.2%のアルミナ含有量と48.6%の塩基性
をもっていた。
Example 2 In this example, the same procedure as above was carried out, but
The molar ratio of sulfate to phosphate to aluminum is o, i:o,
1:1, the mixture was heated to reflux for 2 hours, and the product had an alumina content of 13.2% and a basicity of 48.6%.

生成物はまた少くとも5ケ月間安定であった。The product was also stable for at least 5 months.

実施例 3 本実施例に於ては、実施例2と同じ手順を実施したが、
但し混合物は6時間還流加熱し、最終生成物は14.8
%のアルミナ含量と47.7%の塩基性をもっていた。
Example 3 In this example, the same procedure as in Example 2 was carried out, but
However, the mixture was heated under reflux for 6 hours, and the final product was 14.8
% alumina content and basicity of 47.7%.

この生成物はまた少くとも5ケ月間安定でもあった。This product was also stable for at least 5 months.

実施例 4 本実施例に於ては、下水スラッジ脱水に於ける実施例1
乃至3の生成物の有効性がジョンズ濾過テストによって
測定された。
Example 4 In this example, Example 1 in sewage sludge dewatering
The effectiveness of products 3 to 3 was determined by John's filtration test.

A乃至Eのスラッジは家庭及び工業混合下水を各処理す
る下水処理場から得たものである。
Sludges A through E were obtained from sewage treatment plants that treat mixed domestic and industrial sewage.

スラッジA及びBは同じ処理場から採取されたものであ
るが異なる時期に得た試料であった。
Sludge A and B were samples taken from the same treatment plant but at different times.

スラッジのP液の比抵抗(SR)をそれぞれ4.OX
1012m/kg及び3.OX1012m/kgへ減ら
すのに要する製品の投入量は、第1表及び第2表に於て
、下水スラッジ乾燥固体含量に対するアルミナ添加重量
%に関して示されている投入量が少ないほど、その製品
が脱水時に於てより有効である。
The specific resistance (SR) of the P liquid in the sludge is 4. OX
1012m/kg and 3. The product input required to reduce OX to 1012 m/kg is indicated in Tables 1 and 2 in terms of weight % alumina addition to sewage sludge dry solids content.The lower the input, the more dehydrated the product is. Sometimes it is more effective.

Fはその製品を用いるときにSRが到達し得なかったこ
とを示している。
F indicates that SR could not be reached when using that product.

同じスラッジA乃至Eは比較用製品CI及びC2を用い
て脱水された。
The same sludges A through E were dewatered using comparative products CI and C2.

C1は約60%の塩基性をもつ塩基性塩化アルミニウム
の商業的に入手できる溶液であり、C2はアルミナを1
0.2重量%含み50%の塩基性をもつポリ塩化アルミ
ニウム溶液で日本で多木製肥所■から販売されている。
C1 is a commercially available solution of basic aluminum chloride with a basicity of about 60% and C2 is a solution of alumina
It is a polyaluminum chloride solution containing 0.2% by weight and having a basicity of 50% and is sold in Japan by Taki Hijo ■.

結果はまた第1表及び第2表に総括されている。The results are also summarized in Tables 1 and 2.

第1表及び第2表から、一般には、実施例1乃至3の製
品は比較用製品CIより実質上よい成積を示すことが見
られる。
It can be seen from Tables 1 and 2 that, in general, the products of Examples 1-3 exhibit substantially better performance than the comparative product CI.

さらに、多くの場合に、特に、実施例2及び3の製品は
ジョンズp過テストに於て比較用製品C2よりすぐれて
いるか、あるいは誤差範囲内で実質上同じであったこと
が見られる。
Furthermore, in many cases, particularly, the products of Examples 2 and 3 were found to outperform comparative product C2 in the John's p-pass test, or were substantially the same within error.

Claims (1)

【特許請求の範囲】 1 塩基性塩化アルミニウム溶液を、多価アニオン酸の
酸前駆体と混合し、この混合物を熟成する工程を含む、
水処理あるいは下水処理に適した、Al2O3として表
わして1〜20重量%のアルミニウム及び多価アニオン
を含有する塩基性アルミニウム溶液の製造方法において
、燐酸と硫酸とのモル比が2:1〜1:2の範囲にあり
、しかも各酸の量が塩基性塩化アルミニウム中のアルミ
ニウム1モル当り少なくとも0205モルかつ全酸量が
アルミニウム1モル当り0.3モル以下となるよう混合
した燐酸と硫酸さの混合物を前記酸前駆体きして使用す
ることを特徴とする、上記塩基性アルミニウム溶液の製
造方法。 2 塩基性塩化アルミニウム溶液をアルミニウム1モル
当りO11〜0.2モルの酸で処理する、特許請求の範
囲第1項記載の方法。 3 混合物を実質的に還流温度で熟成する、特許請求の
範囲第1項または第2項に記載の方法。 4 混合物を2〜3時間熟成する、特許請求の範囲第3
項に記載の方法。 5 塩基性アルミニウム溶液の塩基度および燐酸と硫酸
の使用量を、得られる生成物が40〜75%の塩基度と
なるように選択する、特許請求の範囲第1項〜第4項の
いずれか1項に記載の方法。
[Claims] 1. A method comprising the steps of: 1 mixing a basic aluminum chloride solution with an acid precursor of a polyanionic acid; and aging this mixture;
In a method for producing a basic aluminum solution containing 1 to 20% by weight of aluminum expressed as Al2O3 and polyvalent anions, suitable for water treatment or sewage treatment, the molar ratio of phosphoric acid to sulfuric acid is 2:1 to 1: 2, and the amount of each acid is at least 0.205 moles per mole of aluminum in basic aluminum chloride and the total amount of acid is not more than 0.3 mole per mole of aluminum. The above-mentioned method for producing a basic aluminum solution, characterized in that the acid precursor is used as the acid precursor. 2. Process according to claim 1, characterized in that the basic aluminum chloride solution is treated with an acid containing from 11 to 0.2 moles of O per mole of aluminum. 3. A method according to claim 1 or 2, wherein the mixture is aged at substantially reflux temperature. 4. Claim 3, wherein the mixture is aged for 2 to 3 hours.
The method described in section. 5. Any one of claims 1 to 4, wherein the basicity of the basic aluminum solution and the amounts of phosphoric acid and sulfuric acid used are selected such that the resulting product has a basicity of 40 to 75%. The method described in Section 1.
JP51037045A 1975-04-05 1976-04-02 Method for producing basic aluminum solution Expired JPS5932404B2 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB14044/75A GB1531411A (en) 1975-04-05 1975-04-05 Preparations of solutions of a basic aluminium compound and their use in water treatment

Publications (2)

Publication Number Publication Date
JPS51128694A JPS51128694A (en) 1976-11-09
JPS5932404B2 true JPS5932404B2 (en) 1984-08-08

Family

ID=10033986

Family Applications (1)

Application Number Title Priority Date Filing Date
JP51037045A Expired JPS5932404B2 (en) 1975-04-05 1976-04-02 Method for producing basic aluminum solution

Country Status (6)

Country Link
JP (1) JPS5932404B2 (en)
AU (1) AU504727B2 (en)
DE (1) DE2612503C2 (en)
FR (1) FR2306170A1 (en)
GB (1) GB1531411A (en)
IT (1) IT1058036B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4036116A1 (en) * 1990-11-13 1992-05-14 Beiersdorf Ag Purifying waste water using flocculating agent system - comprises adding aluminium chloride, poly:aluminium chloride or poly:aluminium sulphate and aluminate to waste water

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3544476A (en) * 1967-05-09 1970-12-01 Taki Fertilizer Mfg Co Ltd Coagulant and method for treating aqueous medium comprising a basic metal salt and a multivalent anion

Also Published As

Publication number Publication date
GB1531411A (en) 1978-11-08
DE2612503C2 (en) 1984-12-20
JPS51128694A (en) 1976-11-09
AU1215076A (en) 1977-09-22
AU504727B2 (en) 1979-10-25
FR2306170A1 (en) 1976-10-29
FR2306170B1 (en) 1980-02-29
DE2612503A1 (en) 1976-10-21
IT1058036B (en) 1982-04-10

Similar Documents

Publication Publication Date Title
US3544476A (en) Coagulant and method for treating aqueous medium comprising a basic metal salt and a multivalent anion
US4051028A (en) Process for purifying water
JPH04227900A (en) Method for improving dehydration of waste water sludge produced by bacteriological digestion
KR0142224B1 (en) Flocculant for water treatment and method for producing it
US4131545A (en) Water treatment
JPS5839775B2 (en) Enkisei Aluminum Enno Yoekino Seizouhouhou
US2744866A (en) Iron retention in aqueous solution
JPS5932404B2 (en) Method for producing basic aluminum solution
JPS62288104A (en) Solid-shaped basic metallic hydroxy sulfate complex and manufacture thereof
CA1077798A (en) Inorganic flocculating composition and method for its preparation
US4038181A (en) Process for dewatering sewage sludge
JPS62155994A (en) Method for preventing bulking of activated sludge
JPH0122840B2 (en)
SU1724570A1 (en) Method of producing porous iron phosphate
JPS58126827A (en) Preparation of glycerol in high purity
JPS60241998A (en) Treatment of sewage and other waste water
US3259458A (en) Process for preparing wet process phosphoric acid stabilized against iron and aluminum precipitation
US1870404A (en) Method of treating water
JPS59449B2 (en) Method for producing basic aluminum solution
JP4246648B2 (en) Method for producing zeolitic modified soil
KR100192872B1 (en) Poly aluminum calcium chloride and process for preparation thereof
RU2107027C1 (en) Method of processing of aluminosilicate raw material
JPS6125699A (en) Dehydrating method of organic sludge
JPH04175220A (en) Method for separating salt from naturally occurring salt
JPS6312645B2 (en)