CN1136535A - Products of poly aluminium-ferrous chloride and polymerized aluminium-ferrous sulfate and technology - Google Patents

Products of poly aluminium-ferrous chloride and polymerized aluminium-ferrous sulfate and technology Download PDF

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Publication number
CN1136535A
CN1136535A CN95105833A CN95105833A CN1136535A CN 1136535 A CN1136535 A CN 1136535A CN 95105833 A CN95105833 A CN 95105833A CN 95105833 A CN95105833 A CN 95105833A CN 1136535 A CN1136535 A CN 1136535A
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CN
China
Prior art keywords
aluminium
technology
water
poly aluminium
bauxite
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.)
Pending
Application number
CN95105833A
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Chinese (zh)
Inventor
陈世国
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.)
HAINAN PROV TIMBER CO
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HAINAN PROV TIMBER CO
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 HAINAN PROV TIMBER CO filed Critical HAINAN PROV TIMBER CO
Priority to CN95105833A priority Critical patent/CN1136535A/en
Publication of CN1136535A publication Critical patent/CN1136535A/en
Pending legal-status Critical Current

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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Abstract

The characteristic lies in that the crushed bauxite is put in the reaction still to react with hydrochloric acid or sulfuric acid. The recation temp. is 80-100 deg.C, the reaction pressure is 3-5 atmospheric pressure. Then the reacted mixture is poured in the stirred pool and the high aluminium lime and water are added in at temp. of 60-75 deg.C, then they are stirred for 2-5 hr, and it is obtained after precipitation. The water purifier of poly aluminium-ferrous chloride and polymerized aluminium-ferrous sulfate produced by said method features good result for purifying water, simple productive process, quick speed for purifying water and non corrosiveness.

Description

Poly aluminium chloride iron and polyaluminium sulfate iron product and technology
The present invention belongs to the natural terrain water of field of environment protection to purify the water purification agent of handling usefulness with industry, civil sewage.
The at present domestic water purification agent of generally producing mostly is single aluminium salt and single molysite greatly, for example Tai-Ace S 150, aluminium chlorohydroxide, polymerize aluminum chloride, iron trichloride, ferrous sulfate, bodied ferric sulfate etc., the shortcoming of its product mainly is the production cost height, cleaning water is low, water purification speed is slow: great majority have the different corrodibility of degree.
The object of the invention provides that production cost is low, cleaning water is high, the fireballing water purification agent of water purification.
The present invention is achieved in that
The technology of poly aluminium chloride iron is: bauxite → pulverizing → hydrochloric acid acid is molten → and alkaline substance polymerization → precipitation → separation → product
Bauxite is through pulverizing, in reactor with hydrochloric acid at temperature 80-100 ℃, pressure is under 3-5 the normal atmosphere, after reaction in 2-5 hour, pour in the agitated pool, add water and stir, when heating, add the high alumina ash to 60-75 ℃, the reaction times is 1.5-4 hour precipitation, separate product.
Proportioning raw materials is:
Bauxite 12-18%, high alumina ash 8-10%
Hydrochloric acid (concentration is 30%) 35-42%, water 30-45%
The production technique of PAFS:
Bauxite → pulverizing → sulfuric acid solution → modification → precipitation → product (chemical formula [(AL 2O 3) 2(Fe 2O 3) b (SO 3) O (rho) d] bauxite is through pulverizing, add in the reactor, adding sulfuric acid again is 80-100 ℃ in temperature, down reaction 2-5 hour of an air pressure 3-5 normal atmosphere, with its reactant people to going in the agitated pool, adding entry stirs, when heating to 60-75 ℃, add the high alumina ash, the reaction times is 1.5-4 hour, the precipitation, separate product.
Proportioning raw materials is:
Bauxite 14-18, sulfuric acid (concentration 90%) 20-35%, high alumina ash 0.25-0.5%, water 46.5-65.7%.
Poly aluminium chloride iron of the present invention, the PAFS cost is low, and purifying water effect is good, and cohesive force is strong in water purification, and sedimentation speed is fast, and filterableness is good, has no side effect, and is easy to use, simple to operate, and can not increase corrosion to equipment, pipeline.
The poly aluminium chloride iron (20 ° of B é) of producing 1 ton is after 150kg bauxite is pulverized, join in the reactor, with 30% hydrochloric acid of 390kg be through 2 little reactions under 4 normal atmosphere at 95 ℃ of temperature, pressure, then mixture is put into agitated pool, in temperature is under 75 ℃, add 90kg high alumina ash and 470kg water, stirred 2 hours, post precipitation gets product.
Producing 1 ton of PAFS is after the bauxite of 160kg is pulverized, join in the reactor, with 90 sulfuric acid of 300kg be that 100 ℃, pressure are just then the mixture in the reactor to be put into agitated pool through 2.5 hours anti-under 4 normal atmosphere in temperature, in temperature is under 70 ℃, add 4kg high alumina ash and 636kg water, stirred 2 hours, the precipitation and product.

Claims (3)

1, poly aluminium chloride iron, polyaluminium sulfate iron product and technology is characterized in that: its technology is being pulverized bauxite.After, in adding reactor, add hydrochloric acid or sulfuric acid then, in temperature is that 80-10 ℃, pressure are to react under 3-5 the normal atmosphere, carry out its mixture should being poured in the agitated pool of reaction in 2-5 hour, when temperature is 60-75 ℃, add entry and high alumina ash, churning time is 1.5-4 hour, precipitates, separates and get.
2, poly aluminium chloride iron according to claim 1, polyaluminium sulfate iron product and technology, it is characterized in that: the proportioning raw materials of poly aluminium chloride iron is:
Bauxite 12-18%, high alumina ash 8-10%
30% hydrochloric acid 35-42%, water 30-45%
3, poly aluminium chloride iron according to claim 1, polyaluminium sulfate iron product and technology is characterized in that:
The proportioning raw materials of PAFS is:
Bauxite 14-18% high alumina ash 0.25-5%
90% sulfuric acid 20-35% water 46.5-65.7%
CN95105833A 1995-05-22 1995-05-22 Products of poly aluminium-ferrous chloride and polymerized aluminium-ferrous sulfate and technology Pending CN1136535A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN95105833A CN1136535A (en) 1995-05-22 1995-05-22 Products of poly aluminium-ferrous chloride and polymerized aluminium-ferrous sulfate and technology

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN95105833A CN1136535A (en) 1995-05-22 1995-05-22 Products of poly aluminium-ferrous chloride and polymerized aluminium-ferrous sulfate and technology

Publications (1)

Publication Number Publication Date
CN1136535A true CN1136535A (en) 1996-11-27

Family

ID=5075598

Family Applications (1)

Application Number Title Priority Date Filing Date
CN95105833A Pending CN1136535A (en) 1995-05-22 1995-05-22 Products of poly aluminium-ferrous chloride and polymerized aluminium-ferrous sulfate and technology

Country Status (1)

Country Link
CN (1) CN1136535A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100221977B1 (en) * 1997-06-16 1999-09-15 김명호 Method for producing cohesive of inorganic polymer
CZ301421B6 (en) * 1998-04-01 2010-02-24 Alcan International Limited Water treatment method
CN101973586A (en) * 2010-10-14 2011-02-16 广西天工冶金科技有限公司 Method for preparing polymeric aluminum ferric sulfate by using aluminium ore washing gangue
CN102815735A (en) * 2012-08-14 2012-12-12 衡阳市建衡实业有限公司 New process for directly producing poly aluminum chloride by using bauxite

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100221977B1 (en) * 1997-06-16 1999-09-15 김명호 Method for producing cohesive of inorganic polymer
CZ301421B6 (en) * 1998-04-01 2010-02-24 Alcan International Limited Water treatment method
CN101973586A (en) * 2010-10-14 2011-02-16 广西天工冶金科技有限公司 Method for preparing polymeric aluminum ferric sulfate by using aluminium ore washing gangue
CN101973586B (en) * 2010-10-14 2012-08-15 广西天工冶金科技有限公司 Method for preparing polymeric aluminum ferric sulfate by using aluminium ore washing gangue
CN102815735A (en) * 2012-08-14 2012-12-12 衡阳市建衡实业有限公司 New process for directly producing poly aluminum chloride by using bauxite

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