CN102943280B - A kind of method of electrochemical production Two-step purifying body - Google Patents

A kind of method of electrochemical production Two-step purifying body Download PDF

Info

Publication number
CN102943280B
CN102943280B CN201210397654.3A CN201210397654A CN102943280B CN 102943280 B CN102943280 B CN 102943280B CN 201210397654 A CN201210397654 A CN 201210397654A CN 102943280 B CN102943280 B CN 102943280B
Authority
CN
China
Prior art keywords
preparation
aluminium
electrolytic solution
purifying
high purity
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.)
Active
Application number
CN201210397654.3A
Other languages
Chinese (zh)
Other versions
CN102943280A (en
Inventor
黄克宙
李声泽
李旻
岳永刚
何明利
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.)
CHENGDU HUAZE CRYSTAL MATERIAL Co Ltd
Original Assignee
CHENGDU HUAZE CRYSTAL MATERIAL Co 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 CHENGDU HUAZE CRYSTAL MATERIAL Co Ltd filed Critical CHENGDU HUAZE CRYSTAL MATERIAL Co Ltd
Priority to CN201210397654.3A priority Critical patent/CN102943280B/en
Publication of CN102943280A publication Critical patent/CN102943280A/en
Application granted granted Critical
Publication of CN102943280B publication Critical patent/CN102943280B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

The invention discloses a kind of method of electrochemical production Two-step purifying body, the method adopts high-purity aluminium sheet in the electrolyte solution of purifying after electrolysis, its electrolysate is obtained Two-step purifying body through high purity water washing, hydrothermal treatment consists, washing, drying, and its purity range is 99.9% ~ 99.999%.The inventive method gained has the Two-step purifying body of good dispersion, and its preparation technology is simple, and productive rate is high, and product stability is good; Environmentally safe, is easy to large-scale production.Two-step purifying body prepared by the present invention is widely used in multiple fields such as chemical industry, coating, building, traffic and electrical equipment.

Description

A kind of method of electrochemical production Two-step purifying body
Technical field
The present invention relates to a kind of method of electrochemical production Two-step purifying body.
Background technology
High purity aluminium hydroxide is the ultrafine powder product that a kind of added value is very high, and its purity is 99.9% ~ 99.999%.It can as the whitening agent of papermaking filler, paper and optical brightener, the flocculation agent etc. of the fire-retardant filler such as rubber, resin, Urban water supply can also be applied to, be widely used in multiple fields such as chemical industry, coating, building, traffic and electrical equipment as a kind of new function material and structured material at present.High purity aluminium hydroxide is as inorganic combustion inhibitor in recent years, and its application makes substantial progress, and has become the fire retardant kind that application quantity is maximum in the world at present.But the technology of preparing relative progress of high purity aluminium hydroxide is slow, still there is numerous technical barrier, cause product performance unstable, the control of product purity is more difficult.
Through finding the literature search of prior art, the method preparing high purity aluminium hydroxide at present has multiple, as existing patent and literature procedure are mainly kind of a point-score, carbon method and sluggish precipitation etc.These methods respectively have feature, and aforesaid method all exists that control that is as too high in raw material preparation cost, particle size is more difficult, complex operation, have the problem demanding prompt solutions such as pollution to environment.As a kind of high pure and ultra-fine material of functionalization, the industrialized difficulty of preparation technology of high purity aluminium hydroxide is comparatively large, only has minority overseas enterprise can large-scale production at present.In view of this, special proposition the present invention.
Summary of the invention
In order to overcome the shortcoming that above-mentioned prior art exists, the invention provides that a kind of cost is low, experiment condition is simple, environmentally safe, being easy to the preparation method of the high purity aluminium hydroxide of suitability for industrialized production.
The technical scheme that technical solution problem of the present invention is taked is as follows: described preparation method be using surface treatment after high-purity aluminium sheet in negative electrode and anode electrolytic solution after purification, carry out electrolytic reaction simultaneously, gained electrolysate is obtained Two-step purifying body after washing, hydrothermal treatment consists, washing, drying.
In the technical scheme of above-mentioned preparation method: described raw material aluminium adopts high-purity aluminium sheet, purity is 99.99% ~ 99.999%.
In the technical scheme of above-mentioned preparation method: described surface treatment is: high-purity surface of aluminum plate first utilizes caustic dip, and then utilize lower concentration mineral acid washes.Wherein, described mineral acid is selected from the one in hydrochloric acid, nitric acid and sulfuric acid, and its concentration range is 0.05 ~ 0.5mol/L; Alkali lye is selected from the one in sodium hydroxide, potassium hydroxide, and its concentration range is 0.5 ~ 2.5g/L.
In preparation method of the present invention, effective constituent in the electrolytic solution that described electrolytic reaction adopts is the cats product of carbon atom number 5 ~ 25, and described tensio-active agent is any one in choline chloride 60, benzyl trimethyl ammonium chloride, Beta-methyl choline chloride 60, benzyltriethylammoinium chloride, benzyl dimethyl four decyl ammonium chloride.
In preparation method of the present invention, the purification process of described electrolytic solution is: with the electrolyte solution of high purity water preparation 50 ~ 500g/L, surface treated high-purity aluminium sheet is that anode and cathode carries out electrolysis and by electrolysate filtering separation, filtrate is for subsequent use as the electrolytic solution after purifying.
In preparation method of the present invention, described electrolytic reaction adopts power supply to be direct supply.
In preparation method of the present invention, described electrolysis in pH6 ~ 10, current density 1 ~ 5A/dm 2, temperature 30 ~ 90 DEG C, mechanical stirring or pneumatic blending gas pushing quantity are carry out under the condition of 100 ~ 3000L/min.
In electrolytic reaction of the present invention, when the content of electrolysate in electrolytic solution and white aluminium hydroxide powder is 3% ~ 30%, be separated by electrolyte filtering, as passed through dynamic separation aluminium hydroxide powder, namely filtrate use as the circulation of elecrolyte of purifying of the present invention.In this step, the separation method that the separation of electrolysate adopts those skilled in the art usual.
In preparation method of the present invention, described hydrothermal treatment consists is: electrolysate is put into high pressure vessel, and add high purity water, crystal seed and organic anion, be 100 ~ 300 DEG C in temperature, pressure is that under the condition of 1 ~ 87kg, constant temperature 1 ~ 48h carries out hydrothermal treatment consists; Wherein, the consumption of high purity water is 1 ~ 8 times of aluminium hydrate powder body weight; The consumption of organic anion is 0.5 ‰ ~ 10% of aluminium hydrate powder body weight.
In above-mentioned hydrothermal treatment consists, described crystal seed is the Two-step purifying body of particle diameter 5 ~ 100nm, and its injected volume is aluminium hydrate powder body weight 1 ‰ ~ 10%.
In preparation method of the present invention, described organic anion is the one in tartrate or citric acid.
In preparation method of the present invention, described washing, refer to that the aluminium hydroxide powder high purity water after by hydrothermal treatment consists washs, this bath water can recycle after treatment.
In preparation method of the present invention, the electrical resistivity range of described high purity water is 10 ~ 18.3M Ω .cm.
As a kind of preferred forms of the present invention, the present invention preferably adopts following preparation method: high-purity aluminium sheet is carried out surface treatment, and is the purifying electrolytic solution of 400g/L containing benzyl trimethyl ammonium chloride amount.High-purity aluminium sheet after surface treatment is placed in the electrolytic solution after purifying, in pH8 ~ 10 as negative electrode and anode simultaneously; Current density 1A/dm 2, temperature is 50 DEG C, and pneumatic blending gas pushing quantity is electrolysis aluminium sheet under the condition of 100L/min.When powder content reaches 25% in electrolytic solution, after filtering tank liquor, obtain aluminium hydroxide powder; By aluminium hydroxide powder after high purity water washing, putting into high pressure vessel, and add the tartrate of high purity water, crystal seed and aluminium hydrate powder body weight 5%, is 150 DEG C in temperature, and pressure is constant temperature 1h under the condition of 30kg.Take out aluminium hydroxide powder through washing, after drying, Two-step purifying body can be obtained.
Adopt technique scheme, the purity range of high purity aluminium hydroxide prepared by the present invention is 99.99% ~ 99.999%, and yield is 40% ~ 90%.
Compared to existing technology, the present invention has following beneficial effect:
1. the Two-step purifying body of preparation, its purity range is 99.9% ~ 99.999%, and yield is 40% ~ 90%.
2. in Two-step purifying production procedure, agents useful for same is the organic composition that volatility is little, not containing inorganic additive, also can not introduce impurity element simultaneously, highly beneficial to preparing high purity product.
3. in Two-step purifying production procedure, high purity water used can be recycled, without a large amount of waste residue, waste gas and discharge of wastewater, extremely beneficial to environment protection, belongs to environment-friendly type technique.
4. preparation technology of the present invention is simple, and production cost is lower, and scale and benefit are strong, easy to utilize.
Embodiment
Embodiment 1
The preparation method of the high purity aluminium hydroxide of present embodiment carries out in accordance with the following steps: high-purity aluminium sheet is carried out surface treatment, and purifying chloride containing choline amount is the electrolytic solution of 200g/L.High-purity aluminium sheet after surface treatment is placed in the electrolytic solution after purifying as negative electrode and anode simultaneously, and be 7 ~ 8 at pH, current density is 3A/dm 2, temperature is 60 DEG C, and mechanical stirring gas pushing quantity is electrolysis aluminium sheet under the condition of 800L/min.When levels of precipitate reaches 28% in electrolytic solution, after filtering tank liquor, obtain aluminium hydroxide powder; By aluminium hydroxide powder after washing, put into high pressure vessel, and add the citric acid of high purity water, crystal seed and filter cake weight 5%; Temperature be 200 DEG C, pressure be the condition of 12kg under constant temperature 6h carry out hydrothermal treatment consists; Wherein the consumption of high purity water is 4 times of aluminium hydrate powder body weight; Described crystal seed is the nano-aluminum hydroxide powder of particle diameter 50nm, and its injected volume is aluminium hydrate powder body weight 5%; Tartaric consumption is 6% of aluminium hydrate powder body weight.Take out after hydrothermal treatment consists through washing, after drying, Two-step purifying body can be obtained.
Through above-mentioned preparation process, the purity of the Two-step purifying body finally obtained is 99.95%, and yield is 70%.
Embodiment 2
The preparation method of the high purity aluminium hydroxide of present embodiment carries out in accordance with the following steps:
High-purity aluminium sheet is carried out surface treatment, and purifying is the electrolytic solution of 400g/L containing benzyl trimethyl ammonium chloride amount.High-purity aluminium sheet after surface treatment is placed in the electrolytic solution after purifying, in pH8 ~ 10 as negative electrode and anode simultaneously; Current density 1A/dm 2, temperature is 40 DEG C, and mechanical stirring gas pushing quantity is electrolysis aluminium sheet under the condition of 100L/min.When levels of precipitate reaches 15% in electrolytic solution, after filtering tank liquor, obtain aluminium hydroxide powder; By aluminium hydroxide powder after washing, putting into high pressure vessel, and add the citric acid of high purity water, crystal seed and aluminium hydrate powder body weight 5%, is 100 DEG C in temperature, and pressure is that under the condition of 10kg, constant temperature 1h carries out hydrothermal treatment consists; Wherein the consumption of high purity water is 3 times of aluminium hydrate powder body weight; Described crystal seed is the nano-aluminum hydroxide powder of particle diameter 5nm, and its injected volume is aluminium hydrate powder body weight 1 ‰; The consumption of citric acid is 6% of aluminium hydrate powder body weight.Take out after hydrothermal treatment consists through washing, after drying, Two-step purifying body can be obtained.
The purity of Two-step purifying body prepared by the present embodiment is 99.99%, and yield is 80%.
Embodiment 3
The preparation method of the high purity aluminium hydroxide of present embodiment carries out in accordance with the following steps:
High-purity aluminium sheet is carried out surface treatment, and purifying is the electrolytic solution of 400g/L containing benzyltriethylammoinium chloride amount.High-purity aluminium sheet after surface treatment is placed in the electrolytic solution after purifying, in pH8 ~ 10 as negative electrode and anode simultaneously; Current density 5A/dm 2; Temperature is 90 DEG C; Pneumatic blending gas pushing quantity is electrolysis aluminium sheet under the condition of 1000L/min.When aluminium hydrate powder body burden reaches 30% in electrolytic solution, after being filtered by tank liquor, obtain aluminium hydroxide powder; After being washed by aluminium hydroxide powder, putting into high pressure vessel, and add the tartrate of high purity water, crystal seed and aluminium hydrate powder body weight 10%, is 300 DEG C in temperature; Pressure is that under the condition of 87kg, constant temperature 30h carries out hydrothermal treatment consists; Wherein the consumption of high purity water is 5 times of aluminium hydrate powder body weight; Described crystal seed is the nano-aluminum hydroxide powder of particle diameter 100nm, and its injected volume is aluminium hydrate powder body weight 10%; Tartaric consumption is 2% of aluminium hydrate powder body weight.Take out after hydrothermal treatment consists through high purity water washing, after drying, Two-step purifying body can be obtained.
The purity of Two-step purifying body prepared by the present embodiment is 99.995%, and yield is 75%.
Embodiment 4
The preparation method of the high purity aluminium hydroxide of present embodiment carries out in accordance with the following steps:
High-purity aluminium sheet is carried out surface treatment, and purifying chloride containing choline amount is the electrolytic solution of 50g/L.High-purity aluminium sheet after surface treatment is placed in the electrolytic solution after purifying as negative electrode and anode simultaneously, in pH7 ~ 8, current density 3A/dm 2, temperature is 60 DEG C, and pneumatic blending gas pushing quantity is electrolysis aluminium sheet under the condition of 3000L/min.When levels of precipitate reaches 3% in electrolytic solution, after filtering tank liquor, obtain aluminium hydroxide powder; By aluminium hydroxide powder after washing, putting into high pressure vessel, and add high purity water, crystal seed and tartrate, is 200 DEG C in temperature, and pressure is that under the condition of 32kg, constant temperature 24h carries out hydrothermal treatment consists; Wherein, the consumption of high purity water is 8 times of aluminium hydrate powder body weight; Described crystal seed is the nano-aluminum hydroxide powder of particle diameter 20nm, and its injected volume is aluminium hydrate powder body weight 5%; Tartaric consumption is 0.5 ‰ of aluminium hydrate powder body weight.Take out after hydrothermal treatment consists, through high purity water washing, after drying, Two-step purifying body can be obtained.
The purity of Two-step purifying body prepared by the present embodiment is 99.995%, and yield is 70%.
Embodiment 5
The preparation method of the high purity aluminium hydroxide of present embodiment carries out in accordance with the following steps:
High-purity aluminium sheet is carried out surface treatment, and purifying is the electrolytic solution of 500g/L containing benzyl dimethyl four decyl ammonium chloride amount.High-purity aluminium sheet after surface treatment is placed in the electrolytic solution after purifying as negative electrode and anode simultaneously, in pH6 ~ 7, current density 5A/dm 2, temperature is 30 DEG C, and mechanical stirring gas pushing quantity is electrolysis aluminium sheet under the condition of 2000L/min.When levels of precipitate reaches 10% in electrolytic solution, after filtering tank liquor, obtain aluminium hydroxide powder; By aluminium hydroxide powder after washing, putting into high pressure vessel, and add high purity water, crystal seed and citric acid, is 150 DEG C in temperature, and pressure is that under the condition of 7kg, constant temperature 48h carries out hydrothermal treatment consists; Wherein, the consumption of high purity water is 1 times of aluminium hydrate powder body weight; Described crystal seed is the nano-aluminum hydroxide powder of particle diameter 30nm, and its injected volume is aluminium hydrate powder body weight 1%; The consumption of citric acid is 5% of aluminium hydrate powder body weight.Take out after hydrothermal treatment consists, through high purity water washing, after drying, Two-step purifying body can be obtained.
The purity of Two-step purifying body prepared by the present embodiment is 99.95%, and yield is 40%.
Embodiment 6
The preparation method of the high purity aluminium hydroxide of present embodiment carries out in accordance with the following steps:
High-purity aluminium sheet is carried out surface treatment, and purifying is the electrolytic solution of 400g/L containing Beta-methyl choline chloride 60.High-purity aluminium sheet after surface treatment is placed in the electrolytic solution after purifying as negative electrode and anode simultaneously, in pH8 ~ 10, current density 5A/dm 2, temperature is 30 DEG C, and mechanical stirring gas pushing quantity is electrolysis aluminium sheet under the condition of 100L/min.When levels of precipitate reaches 20% in electrolytic solution, after filtering tank liquor, obtain aluminium hydroxide powder; By aluminium hydroxide powder after washing, putting into high pressure vessel, and add high purity water, crystal seed and tartrate, is 100 DEG C in temperature, and pressure is that under the condition of 37kg, constant temperature 48h carries out hydrothermal treatment consists; Wherein, the consumption of high purity water is 2 times of aluminium hydrate powder body weight; Described crystal seed is the nano-aluminum hydroxide powder of particle diameter 60nm, and its injected volume is aluminium hydrate powder body weight 7%; Tartaric consumption is 10% of aluminium hydrate powder body weight.Take out after hydrothermal treatment consists, through high purity water washing, after drying, Two-step purifying body can be obtained.
The purity of Two-step purifying body prepared by the present embodiment is 99.99%, and yield is 75%.
Embodiment in above-described embodiment can combine further or replace; and embodiment is only be described the preferred embodiments of the present invention; not the spirit and scope of the present invention are limited; under the prerequisite not departing from design philosophy of the present invention; the various changes and modifications that in this area, professional and technical personnel makes technical scheme of the present invention, all belong to protection scope of the present invention.

Claims (7)

1. the preparation method of a high purity aluminium hydroxide, it is characterized in that, described preparation method be using surface treatment after high-purity aluminium sheet in the electrolytic solution of purifying, carry out electrolytic reaction as negative electrode and anode simultaneously, gained electrolysate is obtained Two-step purifying body after washing, hydrothermal treatment consists, washing, drying; The effective constituent of described electrolytic solution is the cats product of carbon atom number 5 ~ 25, and described tensio-active agent is any one in choline chloride 60, benzyl trimethyl ammonium chloride, Beta-methyl choline chloride 60, benzyltriethylammoinium chloride, benzyl dimethyl four decyl ammonium chloride; Described hydrothermal treatment consists is: put into high pressure vessel after being filtered by electrolysate aluminium hydroxide powder, and add high purity water, crystal seed and organic anion, be 100 ~ 300 DEG C in temperature, pressure is that under the condition of 1 ~ 87kg, constant temperature 1 ~ 48h carries out hydrothermal treatment consists; Wherein, described organic anion is the one in tartrate or citric acid, and the consumption of high purity water is 1 ~ 8 times of aluminium hydrate powder body weight; The consumption of organic anion is 0.5 ‰ ~ 10% of aluminium hydrate powder body weight; Described crystal seed is the nano-aluminum hydroxide powder of particle diameter 5 ~ 100nm, and the injected volume of crystal seed is 1 ‰ ~ 10% of aluminium hydrate powder body weight.
2. preparation method according to claim 1, it is characterized in that, the preparation method of electrolyte of described purifying is as follows: with the electrolyte solution of high purity water preparation 50 ~ 500g/L, surface treated high-purity aluminium sheet is that anode and cathode carries out electrolysis and by electrolysate filtering separation, filtrate is for subsequent use as the electrolytic solution after purifying.
3. preparation method according to claim 1, is characterized in that, described electrolytic reaction adopts power supply to be direct supply.
4. preparation method according to claim 1, is characterized in that, described electrolytic reaction in pH6 ~ 10, current density 1 ~ 5A/dm 2, temperature is 30 ~ 90 DEG C, and mechanical stirring or pneumatic blending gas pushing quantity are carry out under the condition of 100 ~ 3000L/min.
5. preparation method according to claim 1, is characterized in that, when in electrolytic solution, the content of electrolysate white aluminium hydroxide powder is 3% ~ 30%, be separated by electrolyte filtering, filtrate is for subsequent use as the electrolytic solution after purifying.
6. preparation method according to claim 1, is characterized in that, the electrical resistivity range of described high purity water is 10 ~ 18.3M Ω cm.
7. preparation method according to claim 1, it is characterized in that, described preparation method is: high-purity aluminium sheet is carried out surface treatment, and contain the purifying electrolytic solution that benzyl trimethyl ammonium chloride amount is 400g/L, high-purity aluminium sheet after surface treatment is placed in the electrolytic solution after purifying, in pH8 ~ 10 as negative electrode and anode simultaneously; Current density 1A/dm 2, temperature is 30 DEG C, and pneumatic blending gas pushing quantity is electrolysis aluminium sheet under the condition of 100L/min, when solids content reaches 25% in electrolytic solution, obtains aluminium hydroxide powder after filtering tank liquor; By aluminium hydroxide powder after washing, putting into high pressure vessel, and add the tartrate of high purity water, crystal seed and aluminium hydrate powder body weight 5%, is 100 DEG C in temperature, and pressure is constant temperature 1h under the condition of 30kg; Take out through high purity water washing, after drying, Two-step purifying body can be obtained.
CN201210397654.3A 2012-10-18 2012-10-18 A kind of method of electrochemical production Two-step purifying body Active CN102943280B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210397654.3A CN102943280B (en) 2012-10-18 2012-10-18 A kind of method of electrochemical production Two-step purifying body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210397654.3A CN102943280B (en) 2012-10-18 2012-10-18 A kind of method of electrochemical production Two-step purifying body

Publications (2)

Publication Number Publication Date
CN102943280A CN102943280A (en) 2013-02-27
CN102943280B true CN102943280B (en) 2016-01-06

Family

ID=47726262

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210397654.3A Active CN102943280B (en) 2012-10-18 2012-10-18 A kind of method of electrochemical production Two-step purifying body

Country Status (1)

Country Link
CN (1) CN102943280B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104047015B (en) * 2014-06-19 2017-02-01 郑州昆研新材料科技有限公司 Method for preparing high-purity alumina powder by alternating current electrolysis
CN108217705A (en) * 2016-12-10 2018-06-29 中国科学院大连化学物理研究所 A kind of preparation method of alumina in Nano level

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2833707A (en) * 1951-01-29 1958-05-06 Guareschi Pietro Electrolytic production of alumina
JPS61284590A (en) * 1985-06-10 1986-12-15 Mitsubishi Heavy Ind Ltd Production of alumina particle
CN1417880A (en) * 2002-11-22 2003-05-14 天津大学 Electrochemical aluminium-water hydrogen storing and producing method and equipment
CN1556250A (en) * 2003-12-31 2004-12-22 �Ϻ���ͨ��ѧ Electrolysis preparation method of nano cuprous oxide
CN1792801A (en) * 2006-01-10 2006-06-28 中国铝业股份有限公司 Process for producing aluminium hydroxide
CN101659547A (en) * 2009-07-03 2010-03-03 江苏海迅实业集团股份有限公司 Preparation method of high-purity super fine alumina
CN102320638A (en) * 2011-08-04 2012-01-18 中国铝业股份有限公司 Preparation method of low-sodium fine grain alumina
CN102560521A (en) * 2012-01-14 2012-07-11 新疆哥兰德新能源有限公司 Method for electrochemically preparing high-purity aluminum oxide

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2833707A (en) * 1951-01-29 1958-05-06 Guareschi Pietro Electrolytic production of alumina
JPS61284590A (en) * 1985-06-10 1986-12-15 Mitsubishi Heavy Ind Ltd Production of alumina particle
CN1417880A (en) * 2002-11-22 2003-05-14 天津大学 Electrochemical aluminium-water hydrogen storing and producing method and equipment
CN1556250A (en) * 2003-12-31 2004-12-22 �Ϻ���ͨ��ѧ Electrolysis preparation method of nano cuprous oxide
CN1792801A (en) * 2006-01-10 2006-06-28 中国铝业股份有限公司 Process for producing aluminium hydroxide
CN101659547A (en) * 2009-07-03 2010-03-03 江苏海迅实业集团股份有限公司 Preparation method of high-purity super fine alumina
CN102320638A (en) * 2011-08-04 2012-01-18 中国铝业股份有限公司 Preparation method of low-sodium fine grain alumina
CN102560521A (en) * 2012-01-14 2012-07-11 新疆哥兰德新能源有限公司 Method for electrochemically preparing high-purity aluminum oxide

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
水热处理对氢氧化铝微观形貌的改性;王晶等;《大连交通大学学报》;20091015;第30卷(第05期);第27-30页 *
纳米氧化铝的电化学制备和表征;徐淑丽等;《科学技术与工程》;20060731;第6卷(第13期);第1798-1800页 *

Also Published As

Publication number Publication date
CN102943280A (en) 2013-02-27

Similar Documents

Publication Publication Date Title
CN102515223B (en) Method for efficient and comprehensive utilization of high-iron bauxite
CN101988210B (en) Ionic liquid indium chloride/n-butyl pyridine chloride system electroplating solution
CN110656343B (en) Method for preparing double-alkali co-production high-purity gypsum from mirabilite and limestone by utilizing PCET reaction
CN102677062B (en) Method for electrolyzing and regenerating alkaline etching liquid
CN105483707A (en) Method for extracting copper for reuse from alkaline copper chloride etching waste liquid
CN111635994A (en) Method for recovering copper from acidic copper-containing etching solution and preparing cuprous oxide
CN102689999A (en) Resourceful treatment method for silica gel waste water
CN110395749A (en) A method of lithium chloride is prepared using the displacement reaction electrodialysis of four compartments
CN102634817A (en) Ionic liquid low-temperature aluminum electrolysis method with glassy carbon as inert anode
CN102689956A (en) Silicon removing method for silicone waste water
CN105036159A (en) Method for preparing lithium carbonate with high-lithium salt lake bittern
CN102925914B (en) A kind of method of electrochemical production nano-aluminum hydroxide powder
CN102943280B (en) A kind of method of electrochemical production Two-step purifying body
CN101275240A (en) Processing method for anode liquor for electrowinning cobalt
CN106011929A (en) Method for recycling copper extracted from alkaline copper chloride etching waste liquid
CN106894037B (en) A method of electrolysis method produces high concentration ferrate step by step
CN101659438B (en) Iron extracting and removing method of aluminum sulfate solution
CN105502854A (en) Treatment method of denim printing and dyeing wastewater
CN102602946A (en) Method for preparing high-specific-surface white carbon black by circularly utilizing waste water including sodium sulfate
CN105063654A (en) Method for preparing methanesulfonic acid and sodium hydroxide by utilizing sodium methanesulfonate
CN101560677A (en) Method for preparing solution of tin methane sulfonate
CN103774178B (en) A kind of additive for electrolytic manganese from manganese sulfate electrolyte system and application method thereof
CN103663563B (en) Preparation method of potassium ferrate
CN105543887A (en) Electrolytic oxidation preparation method of sulfenamide accelerator
CN102051635B (en) Method for producing metal cobalt by adopting high-current density sulfuric acid electrolyte

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant