CN1148830C - 锂二次电池用有机碳酸酯类溶剂的制备方法 - Google Patents
锂二次电池用有机碳酸酯类溶剂的制备方法 Download PDFInfo
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- CN1148830C CN1148830C CNB011414391A CN01141439A CN1148830C CN 1148830 C CN1148830 C CN 1148830C CN B011414391 A CNB011414391 A CN B011414391A CN 01141439 A CN01141439 A CN 01141439A CN 1148830 C CN1148830 C CN 1148830C
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- organic carbonate
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- 239000002904 solvent Substances 0.000 title claims abstract description 27
- 150000005677 organic carbonates Chemical class 0.000 title claims abstract description 19
- 229910052744 lithium Inorganic materials 0.000 title claims abstract description 14
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical group [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 title claims abstract description 9
- 238000004519 manufacturing process Methods 0.000 title abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 8
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 claims abstract description 8
- 238000001035 drying Methods 0.000 claims abstract description 6
- 239000002808 molecular sieve Substances 0.000 claims abstract description 6
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims abstract description 6
- KEAYESYHFKHZAL-UHFFFAOYSA-N Sodium Chemical compound [Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 claims abstract description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 4
- 229910052799 carbon Inorganic materials 0.000 claims abstract description 4
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims abstract description 3
- 229910001628 calcium chloride Inorganic materials 0.000 claims abstract description 3
- 239000001110 calcium chloride Substances 0.000 claims abstract description 3
- 230000018044 dehydration Effects 0.000 claims description 5
- 238000006297 dehydration reaction Methods 0.000 claims description 5
- 238000004821 distillation Methods 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 5
- 150000004649 carbonic acid derivatives Chemical class 0.000 claims description 3
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 2
- 229940072033 potash Drugs 0.000 claims description 2
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 2
- 235000015320 potassium carbonate Nutrition 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 8
- HBBGRARXTFLTSG-UHFFFAOYSA-N Lithium ion Chemical compound [Li+] HBBGRARXTFLTSG-UHFFFAOYSA-N 0.000 abstract description 4
- 229910001416 lithium ion Inorganic materials 0.000 abstract description 4
- 239000002274 desiccant Substances 0.000 abstract 2
- 239000000126 substance Substances 0.000 abstract 2
- XGZVUEUWXADBQD-UHFFFAOYSA-L lithium carbonate Chemical compound [Li+].[Li+].[O-]C([O-])=O XGZVUEUWXADBQD-UHFFFAOYSA-L 0.000 abstract 1
- 229910052808 lithium carbonate Inorganic materials 0.000 abstract 1
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 description 7
- JBTWLSYIZRCDFO-UHFFFAOYSA-N ethyl methyl carbonate Chemical compound CCOC(=O)OC JBTWLSYIZRCDFO-UHFFFAOYSA-N 0.000 description 7
- IEJIGPNLZYLLBP-UHFFFAOYSA-N dimethyl carbonate Chemical compound COC(=O)OC IEJIGPNLZYLLBP-UHFFFAOYSA-N 0.000 description 6
- OIFBSDVPJOWBCH-UHFFFAOYSA-N Diethyl carbonate Chemical compound CCOC(=O)OCC OIFBSDVPJOWBCH-UHFFFAOYSA-N 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 3
- 239000008151 electrolyte solution Substances 0.000 description 2
- -1 propylene carbonate ester Chemical class 0.000 description 2
- QGHDLJAZIIFENW-UHFFFAOYSA-N 4-[1,1,1,3,3,3-hexafluoro-2-(4-hydroxy-3-prop-2-enylphenyl)propan-2-yl]-2-prop-2-enylphenol Chemical group C1=C(CC=C)C(O)=CC=C1C(C(F)(F)F)(C(F)(F)F)C1=CC=C(O)C(CC=C)=C1 QGHDLJAZIIFENW-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- SIXOAUAWLZKQKX-UHFFFAOYSA-N carbonic acid;prop-1-ene Chemical compound CC=C.OC(O)=O SIXOAUAWLZKQKX-UHFFFAOYSA-N 0.000 description 1
- QGBSISYHAICWAH-UHFFFAOYSA-N dicyandiamide Chemical compound NC(N)=NC#N QGBSISYHAICWAH-UHFFFAOYSA-N 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- RUOJZAUFBMNUDX-UHFFFAOYSA-N propylene carbonate Chemical compound CC1COC(=O)O1 RUOJZAUFBMNUDX-UHFFFAOYSA-N 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Classifications
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
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Abstract
本发明公开了锂二次电池用有机碳酸酯类溶剂的制备方法,涉及锂离子电池制造技术领域。本发明将有机碳酸酯流经一干燥柱,干燥剂用金属锂、金属钠、硫酸钙、氯化钙、碳酸钾、活性氧化铝、分子筛、活性炭中的一种或几种干燥剂,干燥除去水分;然后将除水后的溶剂进入蒸馏塔,在50-200℃、-0.05~-0.1MPa条件下进行蒸馏,分离出馏前和馏后物。本发明所得有机碳酸酯类溶剂纯度达99.99%以上,水份含量小于5ppm。
Description
技术领域
本发明涉及锂离子电池制造技术领域,具体地是有机碳酸酯类溶剂的制备方法。
背景技术
目前,锂二次电池普遍作为驱动小型电子设备的电源,该类电池包括:正极、非水电解液以及负极。其中非水电解液的溶剂体系即为有机碳酸酯类,主要包括碳酸丙烯酯(PC)、碳酸乙烯酯(EC)、碳酸二乙酯(DEC)、碳酸二甲酯(DMC)、碳酸甲乙酯(EMC)。为降低电池的内阻、提高电池的容量、延长其循环使用寿命,要求该类溶剂纯度达99.99%以上,水份含量小于5ppm。一般工业提供的有机碳酸酯优级品主含量93~98.5%,水份含量在0.1~0.3%,根据不同的生产方法产品中还含有其它少量杂质。若直接采用满足不了电池行业的需要,必须对工业品进行脱水、精制,以达到电池行业的要求。
发明内容
为解决上述技术存在的问题和不足,本发明提供了一种精制有机碳酸酯溶剂的脱水、蒸馏方法,制备出的有机碳酸酯溶剂满足锂离子电池行业的需要。
本发明提供的方法可使有机碳酸酯类溶剂的含水量小于5ppm。本发明选用干燥剂对碳酸酯类溶剂进行干燥,所用干燥剂包括金属锂、金属钠、CaSO4、CaCl2、K2CO3、活性氧化铝、分子筛、活性炭。
本发明是提供另一种方法,使有机碳酸酯类溶剂纯度达99.99%以上。本发明所用方法为蒸馏方法,分离出馏前和馏后物使产品达到99.99%以上。
以下为本发明的详细说明:
将干燥剂(金属锂、金属钠、活性氧化铝、分子筛等)填充在干燥柱内,溶剂流经干燥柱进行干燥,使水份达到5ppm以下,再将处理过的溶剂进行提馏,分离出轻组分,然后进行精馏,制备出纯度达99.99%以上的产品。
本发明采用如下技术措施:
锂二次电池用有机碳酸酯类溶剂的制备方法,包括将溶剂脱水、蒸馏,其工艺过程包括:1、脱水:有机碳酸酯类溶剂流经一装填有金属锂、金属钠、硫酸钙、氯化钙、碳酸钾、活性氧化铝、分子筛、活性炭中的一种或几种干燥剂的充填柱,干燥除去水份;2、蒸馏:除水后的溶剂进入蒸馏塔,在100-200℃、-0.05~-0.1MPa条件下进行蒸馏,所得水份含量小于5ppm。
本发明的优点和积极效果:本发明提供的锂二次电池用有机碳酸酯类溶剂的制备方法,其工艺过程简单、操作控制方便,生产成本低廉,生产效率高,而且有效地降低了产品中的水分,水份含量小于5ppm,有机碳酸酯类溶剂纯度达99.99%以上。
具体实施方式
下面结合实施例对本工艺进一步说明,但本发明并不仅限于本
实施例。
实施例1
碳酸丙烯酯溶剂50Kg,流经一充填无水CaCl2颗粒的干燥柱,然后进入蒸馏塔内,在200℃下进行蒸馏,得产品42Kg。分析产品碳酸丙烯酯含量为99.998%、水份含量为4.5ppm。
实施例2
碳酸乙烯酯溶剂50Kg,加热溶解后,流经一充填金属锂片的干燥柱,然后进入蒸馏塔内,在190℃下进行蒸馏得产品45Kg。分析产品,碳酸乙烯酯含量为99.991%、水份含量为5ppm。
实施例3
碳酸二甲酯溶剂50Kg,流经一充填活性氧化铝的干燥柱,然后进入蒸馏塔内,在120℃下进行蒸馏,得产品43Kg。分析产品,碳酸二甲酯含量为99.991%、水份含量为4.7ppm。
实施例4
碳酸二乙酯溶剂50Kg,流经一充填硫酸钙的干燥柱,然后进入蒸馏塔,在140℃下进行蒸馏,得产品46Kg。分析产品,碳酸二乙酯含量为99.998%、水份含量为4.2ppm。
实施例5
碳酸甲乙酯溶剂50Kg,流经一充填分子筛的干燥柱,然后进入蒸馏塔,在90℃下进行蒸馏,得产品44Kg。分析产品,碳酸甲乙酯含量为99.995%、水份含量为4.8ppm。
上述蒸馏后的碳酸酯类溶剂分别按EC/DMC=1∶1、EC/DEC/DMC=1∶1∶1、EC/DMC/EMC=1∶1∶1的比例配制1摩尔/升六氟磷酸锂电解液,注入18650型锂离子电池中,分别测定电池容量及循环寿命,结果如表一:
Claims (1)
1.锂二次电池用有机碳酸酯类溶剂的制备方法,包括将溶剂脱水、蒸馏,其特征在于:
脱水:有机碳酸酯类溶剂流经一装填有金属锂、金属钠、硫酸钙、氯化钙、碳酸钾、活性氧化铝、分子筛、活性炭中的一种或几种干燥剂的充填柱,干燥除去水份;
蒸馏:除水后的溶剂进入蒸馏塔,在100-200℃、-0.05~-0.01Mpa条件下进行蒸馏,所得碳酸酯类溶剂纯度99.99%以上,水份含量小于5ppm。
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| CNB011414391A CN1148830C (zh) | 2001-09-25 | 2001-09-25 | 锂二次电池用有机碳酸酯类溶剂的制备方法 |
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| CNB011414391A CN1148830C (zh) | 2001-09-25 | 2001-09-25 | 锂二次电池用有机碳酸酯类溶剂的制备方法 |
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| CN1338789A CN1338789A (zh) | 2002-03-06 |
| CN1148830C true CN1148830C (zh) | 2004-05-05 |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| WO2014050877A1 (ja) * | 2012-09-28 | 2014-04-03 | ダイキン工業株式会社 | 非水電解液、電気化学デバイス、リチウムイオン二次電池、及び、モジュール |
| WO2015004236A1 (en) | 2013-07-11 | 2015-01-15 | Basf Se | Drying of electrolyte mixtures containing acids with molecular sieves |
| US10230131B2 (en) | 2013-07-11 | 2019-03-12 | Gotion Inc. | Method for producing a dehydrated liquid organic carbonate mixture |
| CN105541782A (zh) * | 2015-12-18 | 2016-05-04 | 苏州华一新能源科技有限公司 | 一种碳酸亚乙烯酯的纯化方法 |
| CN117550977A (zh) * | 2023-08-08 | 2024-02-13 | 上海宸硕半导体材料有限公司 | 一种电池级碳酸二甲酯的制备方法 |
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