CN1948259A - Production method of ferrous oxalate special for ferrous lithium phosphate - Google Patents
Production method of ferrous oxalate special for ferrous lithium phosphate Download PDFInfo
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- CN1948259A CN1948259A CN 200610097170 CN200610097170A CN1948259A CN 1948259 A CN1948259 A CN 1948259A CN 200610097170 CN200610097170 CN 200610097170 CN 200610097170 A CN200610097170 A CN 200610097170A CN 1948259 A CN1948259 A CN 1948259A
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- oxalic acid
- inhibitor
- ferrous
- ferrous sulfate
- ferrox
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Abstract
The present invention relates to a method for preparing ferrous oxalate. Said method uses ferrous sulfate and oxalic acid as raw material, and includes the following steps: pretreatment of ferrous sulfate, said pretreatment includes: water-washing ferrous sulfate and inhibiting hydrolysis of its aqueous solution; mixing the pretreated ferrous sulfate with ammonium oxalate and oxalic acid according to the mole ratio of 3:7-8:2 to obtain their mixed solution; making said mixed solution produce reaction for 10-20 min at 65-95 deg.C, then standing still for 2-4 h, separating, washing and drying so as to obtain the invented product ferrous oxalate.
Description
One, technical field
The present invention relates to a kind of preparation method of known fine chemicals, the production method of the special-purpose Ferrox of specifically a kind of phosphoric acid (Asia) iron lithium.
Two, background technology
Its chemical name of Ferrox is oxalic acid ferrous (fouerr oxalate), and current is preparation novel lithium battery positive electrode material--one of main raw material of phosphoric acid (Asia) iron lithium.
The known preparation method of Ferrox joins ferrous sulfate in the oxalic acid solution exactly and reacts, and the Ferrox precipitation of generation is separated out, and promptly packing is dispatched from the factory after separating, washing drying.The yield of this method only about 80%, product purity 98～99%.
Can not satisfy the requirement of novel lithium battery positive electrode material with the Ferrox of known method preparation, not only purity not Enough, particle diameter big (35～45 μ m), particularly crystalline form are unstable and not single, be oblique side, monocline and triclinic mixing crystalline form.
Three, summary of the invention
The present invention is intended to provide qualified raw material for the novel lithium battery positive electrode material.Technical problem to be solved is to improve the single Ferrox of prepared crystalline form.
This preparation method and prior art something in common are: be raw material with ferrous sulfate and oxalic acid equally, that technological process comprises is synthetic, separate, washing and dry.Improvements over the prior art are: 1, carry out pre-treatment and be used to then synthesize raw material sulphuric acid is ferrous; Use oxalic acid and ammonium oxalate mixing solutions when 2, synthesizing.
Described pre-treatment comprises the Fe that removes in the ferrous sulfate
+ 3Wait the hydrolysis of other impurity and inhibition copperas solution, Here it is fully washes to slough Fe
+ 3Deng, be dissolved in the pure water then and suppress its hydrolysis.The technical scheme that suppresses hydrolysis had preferably both been controlled pH3～4 for controlling pH value of solution 3～4 or/and add the inhibitor of 0.5～3wt% (weight percent), added inhibitor again.
Described inhibitor is selected from one or two or more inhibitor in polysaccharide or glucose or sucrose or the polyvalent alcohol, and preferred glucose is or/and sucrose.
Described synthetic be copperas solution and oxalic acid and ammonium oxalate mixing solutions (hereinafter to be referred as mixed solution) stirring reaction 10～20 minutes under 65～95 ℃ of conditions, stop then stirring and left standstill 2～4 hours, allow the Ferrox crystallization separate out, separate then, wash, final drying.
Mol ratio (hereinafter to be referred as ammonium acid ratio) at mixed solution mesoxalic acid ammonium and oxalic acid is 3: 7～8: 2.
Experiment showed, that the Ferrox that crystallization is separated out is a rhomboidal crystal when temperature of reaction≤72 ℃, ammonium acid lower (such as below 4: 6).When temperature of reaction＞85 ℃, ammonium acid during than higher (such as more than 7: 3), the Ferrox that crystallization is separated out is a monoclinic crystal.When temperature of reaction is 73～85 ℃, ammonium acid during than moderate (such as 5: 5～6: 4), the Ferrox that crystallization is separated out is an anorthic crystal.Lower or the higher mole number that is meant mixed solution mesoxalic acid ammonium of so-called ammonium acid.
Mixed solution can be by being used to synthesize after oxalic acid, ammonium oxalate and the water preparation.In view of ammonium oxalate is to be generated by oxalic acid and ammonia react, the neutralization reaction of a heat release of this foot, and synthesis of oxalic acid needs heating when ferrous, for making full use of this neutralization heat, also can lead to ammonia on-site preparation mixed solution when synthetic in oxalic acid solution.Ammonium acid in the mixed solution is than determining by chemical analysis.Because the variation and the temperature correlation of ammonium acid this moment ratio are so also can be determined by experience after the skilled operation.It should be noted that temperature in the kettle is relevant with envrionment temperature, and the envrionment temperature four seasons are different, so ammonium acid ratio is different with the corresponding relation of temperature in the kettle in the four seasons.
Thereby present method prepares the Ferrox product of different single crystalline forms by the condition of control building-up reactions.Product cut size 10～20 μ m, purity 〉=99.5%, yield (in oxalic acid) 〉=93.3%.Because particle diameter is little, crystalline form is single, be used for that its packing density of positive electrode material is big, charging capacity is many, and membrane smoothly.
Four, description of drawings
Fig. 1: the X diffractogram of monocline Ferrox.
Fig. 2: the X diffractogram of oblique side's Ferrox.
Circle is depicted as the difference place of two kinds of crystalline forms among the figure.
Five, embodiment
1, ferrous sulfate pre-treatment
Ferrous sulfate is dropped in the stainless steel washing still, add pure water (distilled water) agitator treating 2～3 times, after the filtering separation, ferrous sulfate after the washing is added in the enamel dissolution kettle, add the pure water stirring and dissolving, transfer pH to 3 with sulfuric acid, leave standstill, clarify after adding 2% sucrose stirring and dissolving simultaneously, it is standby after the filtering separation ferrous sulfate clear liquor to be pumped into storage tank.
2, the monocline Ferrox is synthetic
In the enamel synthesis reactor that band stirs, add oxalic acid and pure water stirring and dissolving control concentration of oxalic acid 35～50wt% (weight percent).Stir slowly logical down ammonia, at this moment temperature in the kettle rises, when rising to 85～95 ℃, temperature stops to lead to ammonia when (at this moment ammonium acid than being about about 7.5～3.5), (this is an equimolar building-up reactions in theory to add copperas solution under stirring simultaneously, but ferrous sulfate should be more excessive slightly in the actually operating, down together).Stopped in 15 minutes stirring in 86～95 ℃ of following stirring reactions, left standstill 3 hours, after the Ferrox precipitation is complete, take out supernatant liquid, reclaim(ed) sulfuric acid hydrogen ammonium adds pure water and stirs washing in 5 minutes, left standstill 3 hours, filtering separation is washed to the sulfate radical-free ion simultaneously, and final drying promptly gets the Ferrox of monoclinic form.Its X diffractogram is seen Fig. 1.
3, oblique side's Ferrox is synthetic:
The oxalic acid solution preparation is with embodiment 2.Logical ammonia, (ammonium acid at this moment is than being about about 3.5:4.5) stops logical ammonia when temperature rises to 70～80 ℃, stirs down the adding copperas solution simultaneously in 65～72 ℃ of following stirring reactions 15 minutes, stop to stir, left standstill 3 hours, later operation obtains iris shape Ferrox with embodiment 2.Its X diffractogram is seen Fig. 2.
4, three oblique Ferroxs is synthetic
The oxalic acid solution preparation is with embodiment 2.Logical ammonia, (ammonium acid at this moment is than being about about 5.5:4.5) stops logical ammonia when temperature rises to 80～90 ℃, stir adding copperas solution down simultaneously, under 73～85 ℃, stir reaction down 15 minutes, stop stirring, left standstill 3 hours, later operation is with embodiment 2.Obtain three oblique crystalline form Ferroxs.
Claims (3)
1, the production method of the special-purpose Ferrox of a kind of phosphoric acid (Asia) iron lithium, with ferrous sulfate and oxalic acid is raw material, comprise synthetic, separate, washing and dry, it is characterized in that: ferrous sulfate is carried out after the pre-treatment and oxalic acid and the synthetic preparation of ammonium oxalate mixing solutions Ferrox; Described pre-treatment is exactly to wash ferrous sulfate and its solution is transferred pH3～4 or/and add the inhibitor of 0.5～3wt%, and described inhibitor is selected from one or more inhibitor in polysaccharide or glucose or sucrose or the polyvalent alcohol; Described synthetic be copperas solution and oxalic acid and ammonium oxalate mixing solutions stirring reaction 10～20 minutes under 65～95 ℃ of conditions, left standstill then 2～4 hours, the mol ratio of mixing solutions mesoxalic acid ammonium and oxalic acid is 3: 7～8: 2.
2, production method according to claim 1, it is characterized in that: transfer pH3～4 to add the inhibitor of 0.5～3wt% simultaneously to copperas solution, described inhibitor is selected from one or more inhibitor in polysaccharide or glucose or sucrose or the polyvalent alcohol.
3, production method according to claim 1 and 2 is characterized in that: described inhibitor is that glucose is or/and sucrose.
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| CN1948259A true CN1948259A (en) | 2007-04-18 |
| CN100488937C CN100488937C (en) | 2009-05-20 |
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2009124431A1 (en) | 2008-04-07 | 2009-10-15 | Byd Company Limited | A method for preparing iron source used for preparing lithium ferrous phosphate, and a method for preparing lithium ferrous phosphate |
| CN101811952A (en) * | 2010-03-31 | 2010-08-25 | 朱辰 | Production method of doped ferrous oxalate |
| CN101311156B (en) * | 2007-05-22 | 2011-05-25 | 比亚迪股份有限公司 | Method for preparing ferrous oxalate |
| CN102225890A (en) * | 2011-04-30 | 2011-10-26 | 湖北浩元材料科技有限公司 | Method for preparing battery-level ferrous oxalate for production of lithium iron phosphate material |
| CN101417941B (en) * | 2007-10-26 | 2012-01-25 | 比亚迪股份有限公司 | Method for preparing ferrous oxalate hydrous salt crystal |
| CN102336646A (en) * | 2010-07-21 | 2012-02-01 | 宁波杉杉新材料科技有限公司 | Preparation method of ferrous oxalate |
| CN102344356A (en) * | 2010-08-05 | 2012-02-08 | 中国科学院宁波材料技术与工程研究所 | Battery grade nano ferrous oxalate, its preparation method and application |
| CN101386575B (en) * | 2008-07-04 | 2012-06-20 | 合肥国轩高科动力能源有限公司 | Method for preparing iron oxalate |
| CN101580464B (en) * | 2009-07-07 | 2012-07-25 | 中南大学 | Method for producing battery-grade ferrous oxalate by using ferrous sulfate as titanium pigment byproduct |
| CN101462944B (en) * | 2007-12-17 | 2012-12-12 | 比亚迪股份有限公司 | Iron oxalate crystal and preparation thereof |
| CN103408417A (en) * | 2013-07-18 | 2013-11-27 | 合肥亚龙化工有限责任公司 | Preparation method for nanoscale ferrous oxalate |
-
2006
- 2006-10-28 CN CNB2006100971701A patent/CN100488937C/en not_active Expired - Fee Related
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101311156B (en) * | 2007-05-22 | 2011-05-25 | 比亚迪股份有限公司 | Method for preparing ferrous oxalate |
| CN101417941B (en) * | 2007-10-26 | 2012-01-25 | 比亚迪股份有限公司 | Method for preparing ferrous oxalate hydrous salt crystal |
| CN101462944B (en) * | 2007-12-17 | 2012-12-12 | 比亚迪股份有限公司 | Iron oxalate crystal and preparation thereof |
| WO2009124431A1 (en) | 2008-04-07 | 2009-10-15 | Byd Company Limited | A method for preparing iron source used for preparing lithium ferrous phosphate, and a method for preparing lithium ferrous phosphate |
| CN101386575B (en) * | 2008-07-04 | 2012-06-20 | 合肥国轩高科动力能源有限公司 | Method for preparing iron oxalate |
| CN101580464B (en) * | 2009-07-07 | 2012-07-25 | 中南大学 | Method for producing battery-grade ferrous oxalate by using ferrous sulfate as titanium pigment byproduct |
| CN101811952A (en) * | 2010-03-31 | 2010-08-25 | 朱辰 | Production method of doped ferrous oxalate |
| CN102336646A (en) * | 2010-07-21 | 2012-02-01 | 宁波杉杉新材料科技有限公司 | Preparation method of ferrous oxalate |
| CN102344356A (en) * | 2010-08-05 | 2012-02-08 | 中国科学院宁波材料技术与工程研究所 | Battery grade nano ferrous oxalate, its preparation method and application |
| CN102225890A (en) * | 2011-04-30 | 2011-10-26 | 湖北浩元材料科技有限公司 | Method for preparing battery-level ferrous oxalate for production of lithium iron phosphate material |
| CN102225890B (en) * | 2011-04-30 | 2013-11-20 | 湖北浩元材料科技有限公司 | Method for preparing battery-level ferrous oxalate for production of lithium iron phosphate material |
| CN103408417A (en) * | 2013-07-18 | 2013-11-27 | 合肥亚龙化工有限责任公司 | Preparation method for nanoscale ferrous oxalate |
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Application publication date: 20070418 Assignee: Hefei Asialon Chemical Co., Ltd. Assignor: Li Chuanyou Contract record no.: 2010340000038 Denomination of invention: Production method of ferrous oxalate special for ferrous lithium phosphate Granted publication date: 20090520 License type: Exclusive License Record date: 20100408 |
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Effective date of registration: 20160614 Address after: 230000 No. 8, Grand Avenue, circular economy demonstration park, Anhui, Hefei Patentee after: Hefei Asialon Chemical Co., Ltd. Address before: 230011 No. 596, Yu Jie Road, Hefei, Anhui Patentee before: Li Chuanyou |
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