CN113481383A - Preparation method of metal potassium - Google Patents
Preparation method of metal potassium Download PDFInfo
- Publication number
- CN113481383A CN113481383A CN202110828864.2A CN202110828864A CN113481383A CN 113481383 A CN113481383 A CN 113481383A CN 202110828864 A CN202110828864 A CN 202110828864A CN 113481383 A CN113481383 A CN 113481383A
- Authority
- CN
- China
- Prior art keywords
- potassium
- metal
- under
- lithium hydride
- vertical tube
- 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.)
- Granted
Links
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B26/00—Obtaining alkali, alkaline earth metals or magnesium
- C22B26/10—Obtaining alkali metals
Abstract
A preparation method of metal potassium relates to the technical field of metal simple substance synthesis, and comprises the steps of taking lithium hydride and potassium salt as raw materials, mixing the lithium hydride and the potassium salt according to a molar ratio of 1: 0.1-10 under the protection of inert atmosphere, placing the mixture in a vertical tube furnace, heating the mixture to 200-700 ℃ under a vacuum condition, and preserving heat for 0.5-24 hours. And after the reaction is finished and the reaction product is cooled, taking out a product at the upper end of the vertical tube furnace under the protection of inert atmosphere, namely the metal potassium simple substance. The invention utilizes the reaction of lithium hydride and potassium salt under the heating condition to generate the potassium simple substance, thereby greatly reducing the synthesis temperature of potassium. The method is simple and easy to control, green and environment-friendly, low in cost and easy to realize industrial production. The prepared metal potassium can be applied to the fields of potassium-sodium alloy and potassium ion batteries, and the prepared batteries have excellent electrochemical performance.
Description
Technical Field
The invention relates to the technical field of metal simple substance synthesis, in particular to a preparation method of metal potassium.
Background
The metal potassium is used as an active alkali metal and is widely applied to the fields of material chemical industry, biological medicine, potassium-sodium alloy, electronic information, potassium ion batteries and the like. The currently industrially predominant preparation process is to react sodium metal with potassium chloride at 850 ℃ (Na + KCl → NaCl + K) and to obtain potassium metal by one-step refining by fractional distillation. The reaction utilizes the difference of melting points between potassium (760 ℃) and sodium (883 ℃) to realize the preparation of potassium.
However, there are two major problems in this preparation process: 1. the prepared potassium contains a large amount of sodium, and the potassium with higher purity can be obtained by further fractionation; 2. the preparation process is usually carried out at 850 ℃, and the energy consumption is high. Therefore, the development of a novel, efficient, low-cost and low-energy-consumption preparation method of the metal potassium is of great significance.
Disclosure of Invention
The invention aims to provide a novel, efficient, low-cost, low-energy-consumption and easy-industrialized-production method for preparing the metal potassium.
In order to achieve the purpose, the technical scheme adopted by the invention is as follows: a preparation method of metal potassium utilizes lithium hydride and potassium salt to react under heating condition to generate the metal potassium, and specifically comprises the following steps:
(1) mixing lithium hydride and potassium salt according to the molar ratio of 1: 0.1-10 under the protection of inert atmosphere, and placing the mixture in a vertical tubular furnace;
(2) heating the mixture in the vertical tube furnace to 200-700 ℃ under a vacuum condition, and preserving heat for 0.5-24 h;
(3) and after the reaction is finished and the reaction product is cooled, taking out the product at the upper end of the vertical tube furnace under the protection of inert atmosphere, thus obtaining the metal potassium.
As a preferred technical scheme of the invention, the preparation method comprises the following steps:
the inert gas mentioned in the step (1) means a gas which does not react with lithium hydride, potassium salt and potassium.
The potassium salt in the step (1) is at least one of potassium chloride, potassium oxide and potassium peroxide.
The heating rate of the heating process in the step (2) is 0.1-50 ℃/min.
The inert gas in the step (3) is a gas which does not react with the potassium metal.
Compared with the prior art, the invention has the beneficial effects that:
(1) the invention utilizes the reaction of lithium hydride and potassium salt under the heating condition to generate the metal potassium, and fills up the blank of the technology of preparing the metal potassium at lower temperature.
(2) The method is simple and easy to control, green and environment-friendly, low in cost and easy to realize industrial production.
(3) The metal potassium prepared by the method can be applied to the fields of potassium-sodium alloy and potassium ion batteries, and the prepared batteries have excellent electrochemical properties.
Drawings
FIG. 1 is an X-ray diffraction pattern of the product prepared in example 1.
FIG. 2 shows the preparation of potassium metal and FeSe by example 12And assembling the battery into a cycle performance diagram.
FIG. 3 shows the preparation of potassium metal and FeSe by example 12And assembling into a rate performance graph of the battery.
FIG. 4 shows potassium metal and FeSe prepared by example 12And assembling the first three charge-discharge curves of the battery.
Detailed Description
Example 1
0.1031g of lithium hydride and 0.9426g of potassium chloride were introduced into a vertical tube furnace under an argon atmosphere, sealed and evacuated. The mixture was raised to 550 ℃ at a rate of 10 ℃/min and held for 2 h. After the reaction is finished and the reaction product is cooled, collecting gas in the vertical tubular furnace, and taking out the solid product from the upper end of the vertical tubular furnace (the temperature of the upper end of the vertical tubular furnace is lower, and the metal potassium is preferentially deposited at the upper end) under the protection of argon atmosphere to obtain the metal potassium.
FIG. 1 is an X-ray diffraction pattern of the product prepared in example 1, and it can be seen from FIG. 1 that the positions of diffraction peaks of the sample completely correspond to the PDF # -01-0500 cards of potassium, indicating that the invention successfully synthesizes metallic potassium.
With FeSe2As a positive electrode, the metal potassium synthesized in the example 1 is used as a negative electrode, glass fiber is used as a diaphragm, and 3M KFSI solute is dissolved in an EC/DEC solvent to assemble a battery for electrochemical performance test.
FIG. 2 shows the preparation of potassium metal and FeSe by example 12Cycle performance diagram of assembled battery, which is 0.1A g-1The first discharge capacity of the lithium ion battery reaches up to 660mAh g-1After 60 times of circulation, the product still keeps up to 200mAh g-1The reversible capacity of (a).
FIG. 3 shows the preparation of potassium metal and FeSe by example 12Rate performance diagram of assembled battery, which is 0.1A g-1、0.3A g-1、0.5A g-1、1.0A g-1、2.0A g-1Respectively shows 360mAh g at a current density of-1、300mAh g-1、280mAh g-1、180mAh g-1、150mAh g-1And when the current density returns to 0.1A g again-1Then, the capacity was maintained at 320mAh g-1Showing that it possesses excellent rate capability.
FIG. 4 shows potassium metal and FeSe prepared by example 12The first three times of charging and discharging curve chart of the assembled battery has unobvious discharging platform and conforms to FeSe2The second and third charge-discharge curves of the compound are basically coincident, and the excellent stability of the compound is proved.
Example 2
0.1031g of lithium hydride and 0.5g of potassium chloride were charged into a vertical tube furnace under a nitrogen atmosphere, sealed and evacuated. The mixture was raised to 600 ℃ at a rate of 5 ℃/min and held for 6 h. After the reaction is finished and the reaction product is cooled, collecting gas in the vertical tube furnace, and taking out the solid product from the upper end of the vertical tube furnace under the protection of helium atmosphere to obtain the metal potassium.
Example 3
Under a nitrogen/argon mixed atmosphere, 1g of lithium hydride and 8g of potassium chloride were charged into a vertical tube furnace, sealed and evacuated. The mixture was heated to 450 ℃ at a heating rate of 6 ℃/min and held for 10 h. And after the reaction is finished and the reaction product is cooled, collecting the gas in the vertical tube furnace, and taking out the solid product from the upper end of the vertical tube furnace under the protection of helium/argon mixed atmosphere to obtain the metal potassium.
Example 4
Under a helium atmosphere, 0.5g of lithium hydride and 2g of potassium chloride were charged into a vertical tube furnace, sealed and evacuated. The mixture was warmed to 620 ℃ at a rate of 3 ℃/min and held for 0.5 h. After the reaction is finished and the reaction product is cooled, collecting gas in the vertical tube furnace, and taking out the solid product from the upper end of the vertical tube furnace under the protection of helium atmosphere to obtain the metal potassium.
Example 5
Under an argon atmosphere, 2g of lithium hydride and 8g of potassium chloride were charged into a vertical tube furnace, sealed and evacuated. The mixture was raised to 650 ℃ at a temperature rise rate of 15 ℃/min and held for 0.2 h. And after the reaction is finished and the reaction product is cooled, collecting the gas in the vertical tube furnace, and taking out the solid product from the upper end of the vertical tube furnace under the protection of the nitrogen/argon mixed atmosphere to obtain the metal potassium.
Example 6
Under a helium/argon mixed atmosphere, 3g of lithium hydride and 9g of potassium peroxide were charged into a vertical tube furnace, sealed and evacuated. The mixture was raised to 700 ℃ at a rate of 9 ℃/min and held for 1 h. And after the reaction is finished and the reaction product is cooled, collecting the gas in the vertical tube furnace, and taking out the solid product from the upper end of the vertical tube furnace under the protection of a helium/argon mixed atmosphere to obtain the metal potassium.
Example 7
Under a helium/argon mixed atmosphere, 3g of lithium hydride and 9g of potassium oxide were charged into a vertical tube furnace, sealed and evacuated. The mixture was raised to 680 ℃ at a rate of 20 ℃/min and held for 1.5 h. And after the reaction is finished and the reaction product is cooled, collecting the gas in the vertical tube furnace, and taking out the solid product from the upper end of the vertical tube furnace under the protection of the nitrogen/argon mixed atmosphere to obtain the metal potassium.
The foregoing is merely exemplary and illustrative of the principles of the present invention and various modifications, additions and substitutions of the specific embodiments described herein may be made by those skilled in the art without departing from the principles of the present invention or exceeding the scope of the claims set forth herein.
Claims (5)
1. The preparation method of the metal potassium is characterized in that lithium hydride and potassium salt are reacted under the heating condition to generate the metal potassium, and the preparation method specifically comprises the following steps:
(1) mixing lithium hydride and potassium salt according to the molar ratio of 1: 0.1-10 under the protection of inert atmosphere, and placing the mixture in a vertical tubular furnace;
(2) heating the mixture in the vertical tube furnace to 200-700 ℃ under a vacuum condition, and preserving heat for 0.5-24 h;
(3) and after the reaction is finished and the reaction product is cooled, taking out the product at the upper end of the vertical tube furnace under the protection of inert atmosphere, thus obtaining the metal potassium.
2. The method of claim 1, wherein: the inert gas mentioned in the step (1) means a gas which does not react with lithium hydride, potassium salt and potassium.
3. The method of claim 1, wherein: the potassium salt in the step (1) is at least one of potassium chloride, potassium oxide and potassium peroxide.
4. The method of claim 1, wherein: the heating rate of the heating process in the step (2) is 0.1-50 ℃/min.
5. The method of claim 1, wherein: the inert gas in the step (3) is a gas which does not react with the potassium metal.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110828864.2A CN113481383B (en) | 2021-07-21 | 2021-07-21 | Preparation method of metal potassium |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110828864.2A CN113481383B (en) | 2021-07-21 | 2021-07-21 | Preparation method of metal potassium |
Publications (2)
Publication Number | Publication Date |
---|---|
CN113481383A true CN113481383A (en) | 2021-10-08 |
CN113481383B CN113481383B (en) | 2022-07-19 |
Family
ID=77942926
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110828864.2A Active CN113481383B (en) | 2021-07-21 | 2021-07-21 | Preparation method of metal potassium |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN113481383B (en) |
Citations (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB961565A (en) * | 1960-07-21 | 1964-06-24 | Montedison Spa | Process of and device for preparing metallic potassium |
US4499063A (en) * | 1982-09-30 | 1985-02-12 | Rhone-Poulenc Specialities Chimiques | Preparation of silane, SiH4 |
CN1036687A (en) * | 1988-04-07 | 1989-11-01 | 国际壳牌研究有限公司 | Triazine herbicides |
JPH08130011A (en) * | 1994-09-05 | 1996-05-21 | Fuji Photo Film Co Ltd | Nonaqueous secondary battery |
US5886229A (en) * | 1998-05-29 | 1999-03-23 | Mine Safety Appliances Company | Method of synthesis of alkali metal trisubstituted borohydride reagents |
WO2000043400A1 (en) * | 1999-01-19 | 2000-07-27 | Mine Safety Appliances Company | Synthesis of alkali metal substituted borohydride reagents |
CN101463429A (en) * | 2009-01-05 | 2009-06-24 | 复旦大学 | Preparation of alloy |
CN101914699A (en) * | 2010-07-26 | 2010-12-15 | 中国科学院长春应用化学研究所 | Fused salt electrosynthesis method of hydrogen storage alloy containing magnesium, lithium, sodium and potassium |
CN102765723A (en) * | 2012-07-23 | 2012-11-07 | 复旦大学 | Method for synthesizing KSi hydrogen storage alloy |
CN105271238A (en) * | 2015-11-18 | 2016-01-27 | 浙江工业大学 | Method for preparing silica powder through mechanical chemical method |
CN106976854A (en) * | 2017-05-24 | 2017-07-25 | 浙江工业大学 | A kind of method for preparing carbon material |
WO2017179369A1 (en) * | 2016-04-11 | 2017-10-19 | 日本曹達株式会社 | Method for producing organic polysilane |
CN108649267A (en) * | 2018-05-11 | 2018-10-12 | 深圳市清新电源研究院 | A kind of potassium ion conductor and its preparation method and application |
CN111349001A (en) * | 2018-12-20 | 2020-06-30 | 深圳先进技术研究院 | Crystal material, preparation method and application thereof, battery positive electrode active material, battery positive electrode material, battery and electric equipment |
JP2020196682A (en) * | 2019-06-03 | 2020-12-10 | 国立大学法人東海国立大学機構 | Curved aromatic compound and method for producing the same |
-
2021
- 2021-07-21 CN CN202110828864.2A patent/CN113481383B/en active Active
Patent Citations (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB961565A (en) * | 1960-07-21 | 1964-06-24 | Montedison Spa | Process of and device for preparing metallic potassium |
US4499063A (en) * | 1982-09-30 | 1985-02-12 | Rhone-Poulenc Specialities Chimiques | Preparation of silane, SiH4 |
CN1036687A (en) * | 1988-04-07 | 1989-11-01 | 国际壳牌研究有限公司 | Triazine herbicides |
JPH08130011A (en) * | 1994-09-05 | 1996-05-21 | Fuji Photo Film Co Ltd | Nonaqueous secondary battery |
US5886229A (en) * | 1998-05-29 | 1999-03-23 | Mine Safety Appliances Company | Method of synthesis of alkali metal trisubstituted borohydride reagents |
WO2000043400A1 (en) * | 1999-01-19 | 2000-07-27 | Mine Safety Appliances Company | Synthesis of alkali metal substituted borohydride reagents |
CN101463429A (en) * | 2009-01-05 | 2009-06-24 | 复旦大学 | Preparation of alloy |
CN101914699A (en) * | 2010-07-26 | 2010-12-15 | 中国科学院长春应用化学研究所 | Fused salt electrosynthesis method of hydrogen storage alloy containing magnesium, lithium, sodium and potassium |
CN102765723A (en) * | 2012-07-23 | 2012-11-07 | 复旦大学 | Method for synthesizing KSi hydrogen storage alloy |
CN105271238A (en) * | 2015-11-18 | 2016-01-27 | 浙江工业大学 | Method for preparing silica powder through mechanical chemical method |
WO2017179369A1 (en) * | 2016-04-11 | 2017-10-19 | 日本曹達株式会社 | Method for producing organic polysilane |
CN106976854A (en) * | 2017-05-24 | 2017-07-25 | 浙江工业大学 | A kind of method for preparing carbon material |
CN108649267A (en) * | 2018-05-11 | 2018-10-12 | 深圳市清新电源研究院 | A kind of potassium ion conductor and its preparation method and application |
CN111349001A (en) * | 2018-12-20 | 2020-06-30 | 深圳先进技术研究院 | Crystal material, preparation method and application thereof, battery positive electrode active material, battery positive electrode material, battery and electric equipment |
JP2020196682A (en) * | 2019-06-03 | 2020-12-10 | 国立大学法人東海国立大学機構 | Curved aromatic compound and method for producing the same |
Also Published As
Publication number | Publication date |
---|---|
CN113481383B (en) | 2022-07-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101643481B (en) | Synthesis technique for obtaining difluoro oxalate lithium borate and di-oxalate lithium borate | |
CN107845796B (en) | Carbon-doped sodium vanadium phosphate cathode material and preparation method and application thereof | |
KR20110132311A (en) | Preparation of lithium sulfide | |
CN108640096B (en) | Preparation method of difluorophosphoric acid and difluorolithium phosphate | |
CN109437339A (en) | Nickelic quaternary positive electrode material precursor and nickelic quaternary positive electrode, preparation method and purposes | |
CN103872287A (en) | Composite positive electrode material of graphene and lithium iron phosphate battery and preparation method thereof | |
JP4188685B2 (en) | Synthesis of transition metal lithium sulfide | |
CN114361579B (en) | Method for preparing sulfide solid electrolyte with low cost and high efficiency | |
CN101070149B (en) | Lithium iron carbonate material prepared by vacuum carbon reduction and method | |
CN107585776A (en) | A kind of method of Rheological Phase Method synthesis LiBF4 | |
CN102763248A (en) | Aluminum-based hydride anodes and galvanic elements containing aluminum-based hydride anodes | |
KR102212995B1 (en) | Preparation method and application of high-purity and proportional-mixed lithium salt | |
CN112687947B (en) | High-pressure-resistant and decomposition-resistant electrolyte for thermal battery and preparation method thereof | |
CN105186014B (en) | A kind of method that one-step method prepares the electrolyte for lithium-ferrous disulfide battery | |
CN112520763B (en) | Method for preparing lithium sulfide by using lithium sulfate | |
GB2351075A (en) | Producing lithiated transition metal sulphides | |
CN113481383B (en) | Preparation method of metal potassium | |
CN110311107B (en) | Metal lithium alloy and preparation method and application thereof | |
CN111446447A (en) | Method for preparing sulfur stannide/carbon composite material by supercritical carbon dioxide fluid and application | |
CN109360979A (en) | A kind of poriferous titanium dioxide that phosphate radical is modified and its application in sodium-ion battery | |
CN108666569A (en) | A kind of spongy carbon material and its preparation method and application | |
CN114447318B (en) | Preparation method for synthesizing ferric trifluoride carbon anode material by gas phase fluorination | |
CN110459754B (en) | High-performance lithium ion battery C3N4Preparation method of/carbon composite negative electrode material | |
CN107244693B (en) | Li0.5TiO2Method for preparing powder material | |
KR20230092272A (en) | Manufacturing method of lithium sulfide with high-yield and high-purity and Crystallization of Lithium sulfide using the method |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |