CN105668538A - Crystallization method of lithium hexafluorophosphate - Google Patents
Crystallization method of lithium hexafluorophosphate Download PDFInfo
- Publication number
- CN105668538A CN105668538A CN201610024302.1A CN201610024302A CN105668538A CN 105668538 A CN105668538 A CN 105668538A CN 201610024302 A CN201610024302 A CN 201610024302A CN 105668538 A CN105668538 A CN 105668538A
- Authority
- CN
- China
- Prior art keywords
- crystallization
- crystallization kettle
- lithium hexafluorophosphate
- kettle
- mother liquor
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D15/00—Lithium compounds
- C01D15/005—Lithium hexafluorophosphate
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Battery Electrode And Active Subsutance (AREA)
- Secondary Cells (AREA)
Abstract
The invention discloses a crystallization method of lithium hexafluorophosphate. The method comprises the following steps: 1) putting mother liquor containing lithium hexafluorophosphate into a sealed crystallization kettle; 2) pumping out the mother liquor in the crystallization kettle by a circulating pump, letting the mother liquor pass a liquid phase circulating tube and finally return to the crystallization kettle; 3) cooling the environment in the crystallization kettle within the cooling range of minus 20- minus 60 DEG C while circulating the mother liquor; and 4) carrying out liquid-solid separation in the crystallization kettle after the above steps so as to obtain a lithium hexafluorophosphate solid. The invention provides a crystallization method of lithium hexafluorophosphate. According to the method, advantages of static crystallization and agitated crystallization are combined, and crystallization efficiency is raised.
Description
Technical field
The present invention relates to method for crystallising, especially relate to the method for crystallising of a kind of lithium hexafluoro phosphate.
Background technology
Lithium hexafluoro phosphate method for crystallising conventional at present mainly has stationary crystallization and two kinds of methods of stirred crystallization, and two kinds of methods are respectively arranged with merits and demerits. The advantage of stationary crystallization includes: 1, fluohydric acid gas remains static relatively, and stability is better, and safety is higher; 2, crystal speed of separating out is slow, and product and impurity can separate precipitation because of different dissolubility in crystal solution, are beneficial to purity and the quality of finished product. The shortcoming of stationary crystallization includes: 1, need of a sufficiently low temperature, requires higher to freezing, and crystallization time is longer, causes energy resource consumption very big, is unfavorable for cost; 2, the granule that crystallization produces is bigger, it is necessary to physical method is pulverized again, causes that product particle is irregular uniformly, and mobility is poor. The advantage of stirred crystallization includes: 1, stirred crystallization granule is uniform, and product quality is relatively stable; 2, crystallization time is short, and temperature requirement compares that stationary crystallization requirement is low, and energy consumption is less, with short production cycle can be effectively improved production efficiency; The shortcoming of stirred crystallization includes: 1, Fluohydric acid. stirred crystallization, and volatility increases, and can cause that fluohydric acid gas material loss increases; 2, stirred crystallization crystal speed of separating out is very fast, it is possible to can cause that the impurity composition in mother solution precipitates out together, causes that in product, impurity composition is higher. 3, Mixing Machine seals and easily corrodes leakage, maintenance inconvenience, causes that product quality is abnormal.
Summary of the invention
It is an object of the invention to change the defect in tradition lithium hexafluoro phosphate method for crystallising, it is provided that the method for crystallising of a kind of lithium hexafluoro phosphate, the method combines the advantage of stationary crystallization and stirred crystallization, improves crystalline rate.
To achieve these goals, the technical scheme is that the method for crystallising designing a kind of lithium hexafluoro phosphate, it is characterised in that comprise the steps:
1) mother solution containing lithium hexafluoro phosphate is loaded in the crystallization kettle sealed;
2) adopt circulating pump by liquor abstraction in crystallization kettle, and make mother solution pass through liquid phase circulation pipe, finally turn again in crystallization kettle;
3) while circulating mother liquor, crystallization kettle environment being lowered the temperature, cooling scope is at-20 ~-60 DEG C;
4) by above-mentioned steps, produce liquid-solid phase in crystallization kettle and separate, thus obtaining lithium hexafluoro phosphate solid.
Advantages of the present invention and having the beneficial effects that: provide the method for crystallising of a kind of lithium hexafluoro phosphate, the advantage that the method combines stationary crystallization and stirred crystallization, utilize the method for crystallising that liquid self circulation flows, namely equipment remains stationary as, crystal solution self-loopa is allowed by the conveying of pump, whole system is in air-proof condition, it is possible to avoid the volatilizing loss of liquid self circulation process Raw; Flowed by the self-loopa of liquid and can effectively improve heat exchange efficiency, shorten crystallization time, improve production efficiency. Adopt the method that crystal solution method of self-loopa in airtight crystallization kettle instead of tradition stirred crystallization, avoid the material loss caused because of the volatilization of Fluohydric acid. in whipping process, and a large amount of impurity caused because of stirred crystallization precipitate out jointly and the problem such as the corrosion of Mixing Machine. Meanwhile, also solve crystallization time in stationary crystallization long, the problem such as crystal solution poor fluidity.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the present invention.
Wherein, crystallization kettle 1, crystal solution liquid phase 2, crystal solution solid phase 3, liquid phase circulation pipe 4, circulating pump 5.
Detailed description of the invention
Below in conjunction with drawings and Examples, the specific embodiment of the present invention is further described. Following example are only for clearly illustrating technical scheme, and can not limit the scope of the invention with this.
Embodiment:
The method for crystallising of a kind of lithium hexafluoro phosphate, it is characterised in that comprise the steps:
1) mother solution containing lithium hexafluoro phosphate is loaded in the crystallization kettle 1 sealed;
2) adopt circulating pump 5 by liquor abstraction in crystallization kettle 1, and make mother solution pass through liquid phase circulation pipe 4, finally turn again in crystallization kettle 1;
3) while circulating mother liquor, crystallization kettle 1 environment being lowered the temperature, cooling scope is at-30 DEG C;
4) by above-mentioned steps, producing liquid-solid phase and separate in crystallization kettle 1, respectively crystal solution liquid phase 2 and crystal solution solid phase 3, thus obtaining lithium hexafluoro phosphate solid.
The above is only the preferred embodiment of the present invention; it should be pointed out that, for those skilled in the art, under the premise without departing from the know-why of the present invention; can also making some improvements and modifications, these improvements and modifications also should be regarded as protection scope of the present invention.
Claims (1)
1. the method for crystallising of a lithium hexafluoro phosphate, it is characterised in that comprise the steps:
1) mother solution containing lithium hexafluoro phosphate is loaded in the crystallization kettle sealed;
2) adopt circulating pump by liquor abstraction in crystallization kettle, and make mother solution pass through liquid phase circulation pipe, finally turn again in crystallization kettle;
3) while circulating mother liquor, crystallization kettle environment being lowered the temperature, cooling scope is at-20 ~-60 DEG C;
4) by above-mentioned steps, produce liquid-solid phase in crystallization kettle and separate, thus obtaining lithium hexafluoro phosphate solid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610024302.1A CN105668538A (en) | 2016-01-15 | 2016-01-15 | Crystallization method of lithium hexafluorophosphate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610024302.1A CN105668538A (en) | 2016-01-15 | 2016-01-15 | Crystallization method of lithium hexafluorophosphate |
Publications (1)
Publication Number | Publication Date |
---|---|
CN105668538A true CN105668538A (en) | 2016-06-15 |
Family
ID=56300710
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610024302.1A Pending CN105668538A (en) | 2016-01-15 | 2016-01-15 | Crystallization method of lithium hexafluorophosphate |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105668538A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110182828A (en) * | 2019-06-14 | 2019-08-30 | 江苏新泰材料科技有限公司 | A kind of lithium hexafluoro phosphate dynamic crystallization device and method for crystallising |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102320588A (en) * | 2011-09-05 | 2012-01-18 | 贵州省化工研究院 | Lithium hexafluorophosphate synthesizer |
CN102874790A (en) * | 2012-09-29 | 2013-01-16 | 谭云东 | Preparation method of crystal lithium hexafluorophosphate |
-
2016
- 2016-01-15 CN CN201610024302.1A patent/CN105668538A/en active Pending
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102320588A (en) * | 2011-09-05 | 2012-01-18 | 贵州省化工研究院 | Lithium hexafluorophosphate synthesizer |
CN102874790A (en) * | 2012-09-29 | 2013-01-16 | 谭云东 | Preparation method of crystal lithium hexafluorophosphate |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110182828A (en) * | 2019-06-14 | 2019-08-30 | 江苏新泰材料科技有限公司 | A kind of lithium hexafluoro phosphate dynamic crystallization device and method for crystallising |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105600809A (en) | Method and device for preparing lithium hexafluorophosphate through dynamic crystallization | |
CN106496159A (en) | A kind of production technology of the big granularity crystal of acesulfame potassium | |
CN104292181A (en) | Method for concentrating acesulfame potassium mother liquor by adopting MVR system | |
CN110054196B (en) | Method for preparing high-purity spherical instant boric acid by organic molecule induction | |
CN106995402B (en) | Equipment for producing fine-carbody and process for producing fine-carbody by utilizing static melting crystallization method | |
CN112142080B (en) | Method for preparing battery-grade lithium carbonate by freezing, circulating and recycling lithium precipitation concentrated mother solution | |
CN104030261B (en) | A kind of production method of high purity electron-level phosphoric acid | |
CN104003428B (en) | The method of lithium hydroxide is produced in a kind of triphane pipeline reactor stripping | |
CN103570523B (en) | A kind of production method of 95% sodium formiate | |
CN109593071A (en) | A kind of continuous controllable acesulfame potassium recrystallization centrifugal device and method | |
CN104478693A (en) | Preparation method of refined oxalic acid | |
CN105668538A (en) | Crystallization method of lithium hexafluorophosphate | |
CN104525064A (en) | Alkaline silica sol and preparation method thereof | |
CN103524390A (en) | Preparation method of tellurium diethyl dithiocarbamate | |
CN102674405B (en) | Method for preparing potassium sulfate by using picromerite | |
CN102367234A (en) | Crystallization method of dicumyl peroxide | |
CN108147386B (en) | Preparation method of dynamic crystalline lithium hexafluorophosphate | |
CN106565815A (en) | Monoammonium glycyrrhizinate purification method | |
CN103265072B (en) | A kind of basic zirconium chloride method for crystallising | |
CN102391322B (en) | Method for recovering glucosamine hydrochloride from hydrolytic mother liquid of glucosamine hydrochloride | |
CN202315388U (en) | Device for crystallizing dicumyl peroxide | |
CN102120609B (en) | Dynamic crystallization technological method and device for stannous chloride solution | |
CN103613497A (en) | Method for producing chloroacetic acid by use of large crystallization kettle | |
CN108992965B (en) | Continuous cooling crystallization preparation process and device for large particles of uniform sodium hypophosphite monohydrate | |
CN110182828A (en) | A kind of lithium hexafluoro phosphate dynamic crystallization device and method for crystallising |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination |