TW201307605A - Vapor-phase deposition method for modifying powder surface, manufacturing method of electrode and electrode - Google Patents

Vapor-phase deposition method for modifying powder surface, manufacturing method of electrode and electrode Download PDF

Info

Publication number
TW201307605A
TW201307605A TW100127243A TW100127243A TW201307605A TW 201307605 A TW201307605 A TW 201307605A TW 100127243 A TW100127243 A TW 100127243A TW 100127243 A TW100127243 A TW 100127243A TW 201307605 A TW201307605 A TW 201307605A
Authority
TW
Taiwan
Prior art keywords
powder
reactor
electrode
carbon
gas phase
Prior art date
Application number
TW100127243A
Other languages
Chinese (zh)
Other versions
TWI453298B (en
Inventor
Chien-Te Hsieh
Jung-Pin Wang
Wei-Yu Chen
Chia-Yi Lin
Chia-Chen Chen
Yung-Ying Liu
Chi-Yuan Lin
Bi-Sheng Chang
I-Ling Chen
Original Assignee
Chien-Te Hsieh
Jung-Pin Wang
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 Chien-Te Hsieh, Jung-Pin Wang filed Critical Chien-Te Hsieh
Priority to TW100127243A priority Critical patent/TWI453298B/en
Publication of TW201307605A publication Critical patent/TW201307605A/en
Application granted granted Critical
Publication of TWI453298B publication Critical patent/TWI453298B/en

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/10Energy storage using batteries

Abstract

A vapor-phase deposition method for modifying powder surfaces is applied to coat nano conductive layer on powder surfaces. Therefore, the conductive property and the stability of powder can be improved. The modified powder can be used to manufacture the electrode of Li-battery so as to improve the charging/discharging rate.

Description

粉體改質之氣相沈積方法、電極製作方法及其電極Vapor deposition method for powder upgrading, electrode manufacturing method and electrode thereof

本發明係有關於一種粉體改質方法、電極製作方法及其電極,尤指一種以氣相沈積方式進行粉體改質之方法、電極製作方法及其電極。The invention relates to a powder upgrading method, an electrode manufacturing method and an electrode thereof, in particular to a method for performing powder reforming by vapor deposition, an electrode manufacturing method and an electrode thereof.

鋰離子電池目前主要應用在可攜式的消費性電子產品部份,以手機、筆記型電腦、數位相機等為主,鋰離子電池依正極材料的不同又可以區分成鋰鈷、鋰錳、鋰鎳鈷、磷酸鋰鐵電池等,其中以鋰鈷電池為主流,佔比重達九成以上(一般所稱的鋰電池即是指鋰鈷電池)但鋰鈷電池因為具有安全性問題及缺貨問題,近來各電池大廠已開始尋找新替代性的正極材料,如鋰錳電池,但鋰錳、鋰鎳鈷電池相較於磷酸鋰鐵電池仍具有安全性問題,故未來鋰電池將逐漸朝完全沒有安全性問題的磷酸鋰鐵電池發展。Lithium-ion batteries are mainly used in portable consumer electronic products, mainly mobile phones, notebook computers, digital cameras, etc. Lithium-ion batteries can be distinguished into lithium cobalt, lithium manganese, and lithium depending on the cathode material. Nickel-cobalt, lithium iron phosphate battery, etc., of which lithium-cobalt battery is the mainstream, accounting for more than 90% (generally referred to as lithium-ion battery refers to lithium-cobalt battery), but lithium-cobalt battery has safety problems and out of stock problems Recently, various battery manufacturers have begun to look for new alternative cathode materials, such as lithium manganese batteries, but lithium manganese and lithium nickel cobalt batteries still have safety problems compared with lithium iron phosphate batteries, so lithium batteries will gradually become more complete in the future. The development of lithium iron phosphate batteries without safety issues.

磷酸鋰鐵電池正極材料分子間具有「強共價鏈」,結構穩定沒有安全性問題,較無燃燒爆炸的安全問題;相較於安全性頻傳的鋰鈷電池,相當具有優勢。磷酸鋰鐵電池純以材料成本而言,磷酸鋰鐵電池為所有鋰離子電池中最低者(15~28 USD/kg,鋰鈷26~50 USD/kg),未來隨技術提升良率提高,產品逐漸普及後,售價可望逐漸下降。又因環保意識抬頭影響,油電混合車備受市場注意,未來市場成長潛力佳。油電混合動力車因為兼採內燃機(引擎)及電動馬達之優點,彌補各自之缺點,能有效減少油耗及污染。目前油電混合車均以鎳氫電池為主,未來將有2/3會採用鋰離子電池,完全無爆炸且大電流的磷酸鋰鐵將為明日之星。假設1台油電混合車所使用的電池約需新台幣20萬元,預估2007年油電混合車電池市場達新台幣1,200億元,2010年將成長至4,200億元。The lithium iron phosphate battery cathode material has a "strong covalent chain" between molecules, and the structure is stable without safety problems, and has no safety problem of combustion and explosion; it is quite advantageous compared with the safety of lithium-cobalt batteries. Lithium iron phosphate battery purely in terms of material cost, lithium iron phosphate battery is the lowest of all lithium-ion batteries (15~28 USD/kg, lithium cobalt 26~50 USD/kg), and the future will increase with the technology to improve the yield. After gradually becoming popular, the price is expected to gradually decline. Due to the impact of environmental awareness, the hybrid electric vehicle has received much attention from the market and has a good market growth potential in the future. Because of the advantages of internal combustion engine (engine) and electric motor, the hybrid electric vehicle can make up for its shortcomings and effectively reduce fuel consumption and pollution. At present, the hybrid electric vehicles are mainly nickel-hydrogen batteries. In the future, 2/3 will use lithium-ion batteries, and lithium iron phosphate with no explosion and high current will be the star of tomorrow. Assume that the battery used in a hybrid electric vehicle requires about NT$200,000. It is estimated that the fuel-electric hybrid battery market will reach NT$120 billion in 2007 and will grow to RMB420 billion in 2010.

磷酸鐵鋰的橄欖型晶體結構使其晶格形變(crystal lattice deformation)比其他電池結構來得小,並改善放電過程;其循環週期因此特別長,也能抵抗氧化、抗酸蝕,讓電池能有更多的電解質選擇,其性能也獲得最佳化。在電池不使用的時候,磷酸鐵鋰的保存期限也更長。另一個磷酸鐵鋰的優點,是被認為是較安全的電池技術;該種電池芯架構在攝氏300~500度的高溫環境下仍能維持穩定,最高甚至可耐受攝氏700度。而在相同的溫度條件下,那些使用鈷、鎳、錳等材料的鋰電池就會開始解體,甚至有爆炸的可能。惟該材料仍有體積能量密度較低及材料導電性差等缺點;換言之,電極的體積能量密度低將限制該電池在手攜式產品之應用,無法適用於高放電率之電動機具應用,因此,磷酸鐵鋰電極之導電性則需仰賴製程技術來改善。The olive-type crystal structure of lithium iron phosphate makes its crystal lattice deformation smaller than other battery structures and improves the discharge process; its cycle period is therefore extremely long, and it can also resist oxidation and acid corrosion, so that the battery can have More electrolyte choices and their performance are also optimized. Lithium iron phosphate has a longer shelf life when the battery is not in use. Another advantage of lithium iron phosphate is that it is considered to be a safer battery technology; the cell structure can remain stable at temperatures as high as 300 to 500 degrees Celsius, and can withstand up to 700 degrees Celsius. Under the same temperature conditions, lithium batteries using materials such as cobalt, nickel, manganese, etc. will begin to disintegrate and even have the possibility of explosion. However, the material still has disadvantages such as low volume energy density and poor conductivity of the material; in other words, the low volume energy density of the electrode will limit the application of the battery in the hand-held product, and cannot be applied to the motor device with high discharge rate. The conductivity of the lithium iron phosphate electrode is dependent on process technology to improve.

又,一種傳統技術係利用液相方式進行磷酸鐵鋰電極粉體的改質,然液相改質需選用長鏈的化合物,其製程複雜且有廢液問題,故需加以改進。Moreover, a conventional technique uses a liquid phase method to reform a lithium iron phosphate electrode powder, and a liquid phase modification requires a long-chain compound, which has a complicated process and a waste liquid problem, and therefore needs to be improved.

本發明之目的之一,在於提供一種粉體改質之氣相沈積方法,以達到低成本且有效提升粉體特性的目的。One of the objects of the present invention is to provide a powder reforming method for powder modification to achieve the purpose of low cost and effective improvement of powder characteristics.

本發明實施例係提供一種粉體改質之氣相沈積方法,包含以下步驟:將粉體置於一反應器,並使所述之粉體均勻地分散於該反應器;通入至少一種導體之氣相前驅物進入該反應器;以及調整該反應器之參數,使該導體之氣相前驅物轉化為固相導體層,並使該固相導體層沈積於所述之粉體之表面。Embodiments of the present invention provide a powder reforming method for powder upgrading, comprising the steps of: placing a powder in a reactor and uniformly dispersing the powder in the reactor; and introducing at least one conductor a gas phase precursor enters the reactor; and adjusting parameters of the reactor to convert the gas phase precursor of the conductor into a solid phase conductor layer and depositing the solid phase conductor layer on the surface of the powder.

本發明實施例係提供一種電極製作方法,包含以下步驟:將電極粉體置於一反應器,並使所述之電極粉體均勻地分散於該反應器;通入至少一種導體之氣相前驅物進入該反應器;調整該反應器之參數,使該導體之氣相前驅物轉化為固相導體層,並使該固相導體層沈積於所述之電極粉體的表面以形成改質電極粉體;以及將所述之改質電極粉體製作成一電極。Embodiments of the present invention provide a method for fabricating an electrode, comprising the steps of: placing an electrode powder in a reactor, and uniformly dispersing the electrode powder in the reactor; and introducing a gas phase precursor of at least one conductor Entering the reactor; adjusting the parameters of the reactor to convert the gas phase precursor of the conductor into a solid phase conductor layer, and depositing the solid phase conductor layer on the surface of the electrode powder to form a modified electrode a powder; and the modified electrode powder is formed into an electrode.

本發明實施例更提供一種電極,其係由電極粉體所製作成型,其中所述之電極粉體的表面具有一固相導體層,該固相導體層係提供一第一路徑及一第二路徑,藉以使電子可沿著該第一路徑傳輸,而離子可沿著該第二路徑傳輸。The embodiment of the present invention further provides an electrode formed by the electrode powder, wherein the surface of the electrode powder has a solid phase conductor layer, and the solid phase conductor layer provides a first path and a second a path by which electrons can be transmitted along the first path and ions can be transported along the second path.

本發明具有以下有益的效果:本發明主要利用氣相方式將導電層沈積於粉體之表面,有利於均勻熱傳及質傳,且可縮短反應時間,故整體製程簡單、成本較低;而本發明之改質方法可應用於電極粉體,以於電子粉體的表面及粉體之間的介面建構成良好的電子導通路徑與離子傳導路徑,進而大幅提升電池電極之高充放電率。The invention has the following beneficial effects: the invention mainly uses a gas phase method to deposit a conductive layer on the surface of the powder, which is favorable for uniform heat transfer and mass transfer, and can shorten the reaction time, so the overall process is simple and the cost is low; The modification method of the invention can be applied to the electrode powder to form a good electron conduction path and an ion conduction path on the surface of the electronic powder and the interface between the powders, thereby greatly increasing the high charge and discharge rate of the battery electrode.

為使能更進一步瞭解本發明之特徵及技術內容,請參閱以下有關本發明之詳細說明與附圖,然而所附圖式僅提供參考與說明用,並非用來對本發明加以限制者。For a better understanding of the features and technical aspects of the present invention, reference should be made to the accompanying drawings.

本發明提出一種粉體改質之氣相沈積方法,其係利用氣相轉化為固相的方式將導電層披覆於粉體上,以達到改質粉體的目的,而本發明更將電極粉體以上述方法進行改質,使所製作出的電池電極具有較佳的電子傳遞效果,進而提升電池本身的特性。The invention provides a powder reforming method for powder modification, which uses a gas phase to convert into a solid phase to coat a conductive layer on a powder to achieve the purpose of modifying the powder, and the invention further comprises an electrode The powder is modified by the above method, so that the produced battery electrode has a better electron transfer effect, thereby improving the characteristics of the battery itself.

請配合圖1A至圖3;本發明所提出的粉體改質之氣相沈積方法至少包括以下步驟:步驟一:提供一反應器20(如圖3所示),並將粉體10置於反應器20中,使粉體10均勻地分散於該反應器20;而為了達到粉體10之均勻分佈,在本步驟中更包括通入一惰性氣體於該反應器20的步驟,並控制該惰性氣體的流量以將所述之粉體10均勻地分散於該反應器20。具體而言,本發明係以鋰電池所使用之商業級磷酸鐵鋰粉體進行表面改質之說明,但並非用於限制本發明;例如鋰電池正極材料粉體:鈷酸鋰粉體、錳酸鋰粉體、鎳鈷酸鋰粉體、鎳鈷錳酸鋰粉體,或其他如碳材粉體、陶瓷粉體、半導體材料粉體、金屬粉體、合金粉體及高分子粉體等等均可適用於本發明。另外,反應器20更包括一連接反應器20之出口端202的冷凝裝置(cold trap system)23以回收廢氣及部分被抽出之粉體。Please refer to FIG. 1A to FIG. 3; the powder reforming method for powder upgrading proposed by the present invention comprises at least the following steps: Step 1: providing a reactor 20 (as shown in FIG. 3) and placing the powder 10 thereon. In the reactor 20, the powder 10 is uniformly dispersed in the reactor 20; and in order to achieve uniform distribution of the powder 10, in this step, a step of introducing an inert gas into the reactor 20 is further included, and the step is controlled. The flow rate of the inert gas is to uniformly disperse the powder 10 in the reactor 20. Specifically, the present invention is a description of the surface modification of a commercial grade lithium iron phosphate powder used in a lithium battery, but is not intended to limit the present invention; for example, a lithium battery positive electrode material powder: lithium cobalt oxide powder, manganese Lithium acid powder, lithium nickel cobalt oxide powder, lithium nickel cobalt manganese oxide powder, or other materials such as carbon powder, ceramic powder, semiconductor material powder, metal powder, alloy powder, and polymer powder The same can be applied to the present invention. In addition, the reactor 20 further includes a cold trap system 23 connected to the outlet end 202 of the reactor 20 to recover the exhaust gas and a portion of the extracted powder.

在本具體實施例中,將磷酸鐵鋰粉體靜置於反應器20中,且經氣閥21C由反應器20之入口端201通入氮氣(即惰性氣體),藉由氣體流量單元21(如質子流量計)準確控制流量,並調整流量,以達到粉體10之流體化,藉以將粉體10均勻地分散於該反應器20。值得說明的是,惰性氣體的流量必須配合反應器20之管徑加以控制,流量太小將無法使粉體10均勻分散,反之,過大的流量會使粉體10由出口端202衝出。在一具體的實施例中,反應器20的管徑為5公分,而惰性氣體的流量較佳地控制於200至1000 cc/min,但不以此為限。In the present embodiment, the lithium iron phosphate powder is placed in the reactor 20, and nitrogen gas (i.e., inert gas) is introduced from the inlet end 201 of the reactor 20 through the gas valve 21C, by the gas flow unit 21 ( For example, the proton flow meter accurately controls the flow rate and adjusts the flow rate to achieve fluidization of the powder 10, thereby uniformly dispersing the powder 10 in the reactor 20. It should be noted that the flow rate of the inert gas must be controlled in accordance with the diameter of the reactor 20. If the flow rate is too small, the powder 10 will not be uniformly dispersed. Conversely, an excessive flow rate will cause the powder 10 to be flushed out from the outlet end 202. In a specific embodiment, the diameter of the reactor 20 is 5 cm, and the flow rate of the inert gas is preferably controlled to 200 to 1000 cc/min, but not limited thereto.

步驟二:通入至少一種導體之氣相前驅物進入該反應器20;步驟三即為調整反應器20之參數,使該導體之氣相前驅物轉化為固相導體層11、11′(如圖1A、圖1B),並使固相導體層11、11′沈積於粉體10的表面。在一實施例中,係選用碳之氣相前驅物,並將其通入反應器20,例如含一個碳至四個碳的氣相化合物,如炔類、烯類、醇類、烷類以及各式含碳之氣相前趨物;接著在步驟三中以加熱裝置22(包含加熱器221及溫控裝置222)使反應器20達到一預定反應溫度,並控制反應時間,使該固相導體層11、11′沈積形成一預定厚度於粉體10的表面。Step 2: introducing a gas phase precursor of at least one conductor into the reactor 20; step 3 is to adjust the parameters of the reactor 20 to convert the gas phase precursor of the conductor into the solid phase conductor layer 11, 11' (eg 1A and 1B), the solid phase conductor layers 11, 11' are deposited on the surface of the powder 10. In one embodiment, a gaseous precursor of carbon is selected and passed to reactor 20, such as a gas phase compound containing one carbon to four carbons, such as alkynes, alkenes, alcohols, alkanes, and Various carbon-containing gas phase precursors; then in step three, the heating device 22 (including the heater 221 and the temperature control device 222) is used to bring the reactor 20 to a predetermined reaction temperature, and the reaction time is controlled to make the solid phase The conductor layers 11, 11' are deposited to form a predetermined thickness on the surface of the powder 10.

在一具體實施例中,經過氣閥21A通入乙炔為碳之氣相前驅物並配合由氣閥21B所通入之氫氣,在反應溫度介於500至900℃之間,反應時間則設定於30至120分鐘之間,即可均勻沈積奈米碳層(即圖1A所示之固相導體層11)於磷酸鐵鋰粉體表面,其碳層厚度介於5至30奈米之間。根據SEM分析,原始磷酸鐵鋰粉體尺寸介於5到10微米之間(如附件一(a)、(b)所示),而經由本技術改質後之磷酸鐵鋰粉體外觀並無顯著差異;請參考XRD分析(如圖4),原始磷酸鐵鋰粉體具有高結晶度,經由本發明之氣相沈積方法改質之後,該粉體仍具有相當高之結晶性顯示(如圖5之(b)),亦即經改質後並未改變其原有結晶度。此外,由圖中顯示,改質時間120分鐘並無發現碳層的存在,主要是由於奈米碳層含量低(低於5%)所致。In a specific embodiment, a gas phase precursor of acetylene is introduced into the gas phase through the gas valve 21A and the hydrogen gas is supplied through the gas valve 21B. The reaction temperature is set between 500 and 900 ° C, and the reaction time is set at Between 30 and 120 minutes, the nanocarbon layer (i.e., the solid phase conductor layer 11 shown in Fig. 1A) can be uniformly deposited on the surface of the lithium iron phosphate powder, and the carbon layer thickness is between 5 and 30 nm. According to SEM analysis, the original lithium iron phosphate powder has a size between 5 and 10 microns (as shown in Annexes (a) and (b)), and the lithium iron phosphate powder modified by the present technology has no appearance. Significant difference; please refer to XRD analysis (Fig. 4), the original lithium iron phosphate powder has high crystallinity, and after upgrading by the vapor deposition method of the present invention, the powder still has a relatively high crystallinity display (as shown in the figure). 5 (b)), that is, it has not changed its original crystallinity after upgrading. In addition, as shown in the figure, the presence of the carbon layer was not found in the modification time of 120 minutes, mainly due to the low content of the nanocarbon layer (less than 5%).

另外,請參考TEM分析(如附件二(a)、(b)所示)經由30分鐘之氣相沈積後磷酸鐵鋰粉體表面具有約5奈米厚度之奈米碳層,而經由120分鐘流體化改質後磷酸鐵鋰粉體表面具有約30奈米厚度之奈米碳層,由以上觀察顯示,本發明之氣相沈積方法可將奈米碳層(即固相導體層11)批覆於粉體10的表面。In addition, please refer to the TEM analysis (as shown in Annex II (a), (b)) after 30 minutes of vapor deposition, the surface of the lithium iron phosphate powder has a nanocarbon layer of about 5 nm thickness, and 120 minutes through 120 minutes. After the fluidized modification, the surface of the lithium iron phosphate powder has a nano carbon layer having a thickness of about 30 nm. From the above observation, the vapor deposition method of the present invention can laminate the nano carbon layer (ie, the solid phase conductor layer 11). On the surface of the powder 10.

本發明更利用一電極製作方法將改質後的磷酸鐵鋰粉體(即電極粉體)以燒結或鍛燒製作電極,並將其組裝成電池後與傳統鋰電池進行充放電的特性比較。請參考圖5(a)所示,原始磷酸鐵鋰粉體所組裝之鈕扣型鋰離子半電池充放電行為,在低充放電率時(0.1 C),該電池具有120 mAh/g之可逆電容量,但其無法適用於高充放電率(如10 C)下進行充放電。反之,如圖5(b)所示,經由120分鐘之反應時間後之電極粉體所製作之電池的充放電行為有明顯改善,不僅能夠維持低充放電時之可逆電容量,亦可於10 C下進行充放電,例如保持50 mAh/g之可逆電容量。In the invention, the modified lithium iron phosphate powder (ie, the electrode powder) is sintered or calcined to form an electrode, and the battery is assembled into a battery and compared with a conventional lithium battery for charging and discharging. Referring to Figure 5(a), the charge-discharge behavior of the button-type lithium-ion half-cell assembled with the original lithium iron phosphate powder has a reversible power of 120 mAh/g at a low charge-discharge rate (0.1 C). Capacity, but it cannot be applied to charge and discharge at high charge and discharge rates (such as 10 C). On the other hand, as shown in FIG. 5(b), the charge and discharge behavior of the battery prepared by the electrode powder after the reaction time of 120 minutes is remarkably improved, and the reversible capacity at the time of low charge and discharge can be maintained, and 10 Charge and discharge are performed under C, for example, maintaining a reversible capacity of 50 mAh/g.

如圖6所示,經由30分鐘之反應時間的改質後,相較於0.1 C下,該電池仍可在3 C充放電速率下維持66%之電容量;經由120分鐘反應時間的改質後,相較於0.1 C下,該電池仍可在10 C充放電速率下維持50%之電容量;反之,傳統電池在3C充放電速率下就無法儲存電量。As shown in Figure 6, after 30 minutes of reaction time modification, the battery can still maintain 66% of the capacitance at 3 C charge and discharge rate compared to 0.1 C; the modification of the reaction time via 120 minutes After that, the battery can maintain 50% of the capacity at 10 C charge and discharge rate compared to 0.1 C; conversely, the conventional battery cannot store power at the 3 C charge and discharge rate.

在另一實施例中,同樣以乙炔為碳之氣相前驅物,但在將乙炔通入之前,更於粉體10的表面製作觸媒層,如被覆金屬鈷於粉體10的表面,而在反應溫度介於500至900℃之間,反應時間則設定於30至120分鐘之間,即可均勻沈積奈米碳管(即圖1B所示之固相導體層11′具有奈米碳管)於磷酸鐵鋰粉體表面,其碳層厚度介於5至30奈米之間。In another embodiment, a gas phase precursor of acetylene is also used as the carbon, but before the acetylene is introduced, a catalyst layer is formed on the surface of the powder 10, such as coating the metal cobalt on the surface of the powder 10. The reaction temperature is between 500 and 900 ° C, and the reaction time is set between 30 and 120 minutes, so that the carbon nanotubes can be uniformly deposited (that is, the solid phase conductor layer 11' shown in FIG. 1B has a carbon nanotube On the surface of the lithium iron phosphate powder, the thickness of the carbon layer is between 5 and 30 nm.

由SEM分析(如附件三(a)、(b)所示),原始磷酸鐵鋰粉體尺寸介於5到10微米之間,而經由本發明之氣相沈積方法改質後,可發現大量捲曲之奈米碳管均勻接枝於粉體表面,奈米碳管直徑約為20至50奈米,長度約為數微米,換言之,本發明可將奈米碳管接枝於電極粉體的表面。By SEM analysis (as shown in Annexes III (a), (b)), the original lithium iron phosphate powder has a size between 5 and 10 microns, and after upgrading by the vapor deposition method of the present invention, a large amount can be found. The crimped carbon nanotubes are evenly grafted onto the surface of the powder. The carbon nanotubes have a diameter of about 20 to 50 nanometers and a length of about several micrometers. In other words, the present invention can graft the carbon nanotubes onto the surface of the electrode powder. .

由圖8所示,經奈米碳管接枝後,電池性能已有明顯之改善,尤其在高充放電時,電池仍具有良好之充放電性能,例如該電池仍可在3 C充放電速率下維持約75%之電容量;反之,傳統電池在3C充放電速率下就無法儲存電量。As shown in Fig. 8, after grafting through the carbon nanotubes, the battery performance has been significantly improved, especially in the case of high charge and discharge, the battery still has good charge and discharge performance, for example, the battery can still be charged and discharged at a rate of 3 C. The battery capacity is maintained at about 75%; on the contrary, the conventional battery cannot store power at the 3C charge and discharge rate.

因此,本發明提出一種利用氣相沈積技術,將導電層(如碳層、碳管等)包覆於微米級或次微米級粉體之表面,當應用於電極粉體時,不僅提升該粉體之導電特性,並能引導離子擴散,減少離子擴散阻力,如圖2所示,電極粉體表面之導電層可提供一第一路徑P1及一第二路徑P2,藉以使電子可沿著該第一路徑P1傳輸,而離子可沿著該第二路徑P2傳輸,具體而言,因奈米碳層或碳管係均勻包覆磷酸鐵鋰粉體的表面,故可於粉體的表面及粉體之間的介面建構成良好的電子導通路徑(即第一路徑P1);由於奈米碳層為非晶相碳層,故其對鋰離子擴散阻力低,若磷酸鐵鋰表面成長奈米碳管,鋰離子亦容易於粉體的表面擴散,且電子可經由奈米碳管進行一維傳遞,可大幅減少離子擴散阻力,且具有增進電子導通之功效,故可改善原有粉體之傳輸電子與離子的能力,且可有效抑制粉體之間之凝聚作用。Therefore, the present invention proposes a method of coating a conductive layer (such as a carbon layer, a carbon tube, etc.) on the surface of a micron or submicron powder by a vapor deposition technique, and when applied to an electrode powder, not only the powder is lifted. The conductive property of the body can guide the ion diffusion and reduce the ion diffusion resistance. As shown in FIG. 2, the conductive layer on the surface of the electrode powder can provide a first path P1 and a second path P2, so that electrons can be along the The first path P1 is transmitted, and the ions can be transported along the second path P2. Specifically, since the surface of the lithium iron phosphate powder is uniformly coated by the nano carbon layer or the carbon tube system, the surface of the powder can be The interface between the powders constitutes a good electron conduction path (ie, the first path P1); since the nanocarbon layer is an amorphous carbon layer, the diffusion resistance to lithium ions is low, and if the surface of the lithium iron phosphate grows nanometer Carbon tube, lithium ion is also easy to diffuse on the surface of the powder, and electrons can be transported one-dimensionally through the carbon nanotubes, which can greatly reduce the ion diffusion resistance and improve the effect of electron conduction, so that the original powder can be improved. The ability to transport electrons and ions, and The aggregation inhibiting effect acting between the powder.

另一方面,本發明並不限制固相導體層11的材質,例如以金屬之有機化合物作為氣相前驅物,如錫、鋅、銅等氣相前驅物通入反應器20,並控制反應溫度,即可生成前述金屬的固相導體層11於粉體10的表面,亦可達成提升粉體之導電特性的效果。On the other hand, the present invention does not limit the material of the solid phase conductor layer 11, for example, a metal organic compound is used as a gas phase precursor, and a gas phase precursor such as tin, zinc, copper or the like is introduced into the reactor 20, and the reaction temperature is controlled. The solid phase conductor layer 11 of the above metal can be formed on the surface of the powder 10, and the effect of improving the electrical conductivity of the powder can be achieved.

綜上所述,本發明至少具有以下優點:In summary, the present invention has at least the following advantages:

1、本發明利用流體方式使粉體均勻分佈,並以氣相前驅物的反應進行粉體的改質,在應用上可大幅提升磷酸鐵鋰之電池電極之高充放電率,相較於液相粉體改質方法,本發明的製程簡單,更可改善電池性能,亦可降低其製作成本。1. The invention utilizes a fluid method to uniformly distribute the powder, and the powder is modified by the reaction of the gas phase precursor, and the high charge and discharge rate of the battery electrode of the lithium iron phosphate can be greatly improved in application, compared with the liquid. The phase powder upgrading method has simple process, can improve battery performance, and can reduce the manufacturing cost thereof.

2、本發明所製作之改質後磷酸鐵鋰粉體,表面具有均勻奈米碳層,大幅增加產品的克電容量,且在製作電極時無需再添加大量的導電添加劑;換言之,可降低導電添加材的使用量以降低成本,且不需複雜的機台或製程,故符合商業規模的要求。2. The modified lithium iron phosphate powder prepared by the invention has a uniform nano carbon layer on the surface, which greatly increases the gram capacity of the product, and does not need to add a large amount of conductive additive when manufacturing the electrode; in other words, the conductive can be reduced. The amount of added material is used to reduce costs and does not require complicated machines or processes, so it meets the requirements of commercial scale.

3、本發明亦可將不同載體上沈積奈米塗層,即可製作出披覆有導電層之物件,例如,觸媒、奈米材料、陶瓷粉體、半導體封裝等等;因此,本發明具有有效提升各式粉體導電性、避免粉體聚集與變質、使粉體更易於儲存之特性。3. The present invention can also deposit a nano-coating on different carriers to fabricate an article coated with a conductive layer, such as a catalyst, a nanomaterial, a ceramic powder, a semiconductor package, etc.; therefore, the present invention It has the characteristics of effectively improving the conductivity of various powders, avoiding powder aggregation and deterioration, and making the powder easier to store.

4、本發明可節省能源消耗與處理時間、具有高質傳速率,且欲改質之粉體在氣相中可與前趨物氣體分子接觸,於適當的溫度下進行氣固反應,以達到奈米導電層均勻塗佈的目的。4. The invention can save energy consumption and processing time, has high mass transfer rate, and the powder to be modified can be in contact with the precursor gas molecules in the gas phase, and the gas-solid reaction is carried out at an appropriate temperature to achieve The purpose of uniform coating of the nano conductive layer.

以上所述僅為本發明之較佳可行實施例,非因此侷限本發明之專利範圍,故舉凡運用本發明說明書及圖示內容所為之等效技術變化,均包含於本發明之範圍內。The above description is only a preferred embodiment of the present invention, and is not intended to limit the scope of the present invention, and the equivalents of the present invention are intended to be included within the scope of the present invention.

10...粉體10. . . Powder

11、11′...固相導體層11, 11'. . . Solid conductor layer

20...反應器20. . . reactor

201...入口端201. . . Entrance end

202...出口端202. . . Exit end

21...氣體流量單元twenty one. . . Gas flow unit

21A、21B、21C...氣閥21A, 21B, 21C. . . Air valve

22...加熱裝置twenty two. . . heating equipment

221...加熱器221. . . Heater

222...溫控裝置222. . . Temperature control device

23...冷凝裝置twenty three. . . Condensing device

P1...第一路徑P1. . . First path

P2...第二路徑P2. . . Second path

圖1A係顯示本發明之方法將粉體進行改質後的示意圖。Fig. 1A is a schematic view showing the modification of the powder by the method of the present invention.

圖1B係顯示本發明之方法將粉體進行改質後的另一態樣示意圖。Figure 1B is a schematic view showing another aspect of the method of the present invention after upgrading the powder.

圖2係顯示本發明之改質後粉體形成電極之電子與離子的路徑示意圖。Fig. 2 is a schematic view showing the paths of electrons and ions of the modified powder forming electrode of the present invention.

圖3係顯示進行本發明之氣相沈積方法的機台示意圖。Fig. 3 is a schematic view showing a machine for carrying out the vapor deposition method of the present invention.

圖4係顯示改質前後粉體的XRD分析圖。Figure 4 is a graph showing the XRD analysis of the powder before and after the modification.

圖5A係顯示使用改質前之電極的電池之充放電特性圖。Fig. 5A is a graph showing charge and discharge characteristics of a battery using an electrode before modification.

圖5B係顯示使用以碳層改質後之電極的電池之充放電特性圖。Fig. 5B is a graph showing the charge and discharge characteristics of a battery using an electrode modified with a carbon layer.

圖6係顯示使用改質前與以碳層改質後後之電極的電池之充放電特性比較圖。Fig. 6 is a graph showing comparison of charge and discharge characteristics of a battery using an electrode after modification and modification with a carbon layer.

圖7係顯示使用以奈米碳管改質後之電極的電池之充放電特性圖。Fig. 7 is a graph showing the charge and discharge characteristics of a battery using an electrode modified with a carbon nanotube.

圖8係顯示使用改質前與以奈米碳管改質後之電極的電池之充放電特性比較圖。Fig. 8 is a graph showing comparison of charge and discharge characteristics of a battery using an electrode modified with a carbon nanotube before modification.

10...粉體10. . . Powder

P1...第一路徑P1. . . First path

P2...第二路徑P2. . . Second path

Claims (13)

一種粉體改質之氣相沈積方法,包含以下步驟:將粉體置於一反應器,並使所述之粉體均勻地分散於該反應器;通入至少一種導體之氣相前驅物進入該反應器;以及調整該反應器之參數,使該導體之氣相前驅物轉化為固相導體層,並使該固相導體層沈積於所述之粉體之表面。A powder reforming method for powder upgrading comprises the steps of: placing a powder in a reactor and uniformly dispersing the powder in the reactor; introducing a gas phase precursor of at least one conductor into the reactor The reactor; and adjusting the parameters of the reactor to convert the gas phase precursor of the conductor into a solid phase conductor layer and depositing the solid phase conductor layer on the surface of the powder. 如申請專利範圍第1項所述之粉體改質之氣相沈積方法,其中在將粉體置於一反應器的步驟中,更包括通入一惰性氣體於該反應器的步驟,並控制該惰性氣體的流量以將所述之粉體均勻地分散於該反應器。The method for vapor-depositing a powder modified according to claim 1, wherein in the step of placing the powder in a reactor, the step of introducing an inert gas into the reactor is further controlled. The flow rate of the inert gas is to uniformly disperse the powder in the reactor. 如申請專利範圍第1項所述之粉體改質之氣相沈積方法,其中在通入至少一種導體之氣相前驅物進入該反應器的步驟中,係將碳之氣相前驅物通入該反應器。The method for vapor-depositing a powder modified according to claim 1, wherein in the step of introducing a gas phase precursor of at least one conductor into the reactor, a gas phase precursor of carbon is introduced. The reactor. 如申請專利範圍第3項所述之粉體改質之氣相沈積方法,其中前述碳之氣相前驅物係為含一個碳至四個碳的氣相化合物;而在使該導體之氣相前驅物轉化為固相導體層的步驟中,該固相導體層係為一非均質的碳層。The method for vapor-depositing a powder modified according to claim 3, wherein the gas phase precursor of the carbon is a gas phase compound containing one carbon to four carbons; and the gas phase of the conductor is made In the step of converting the precursor into a solid phase conductor layer, the solid phase conductor layer is a heterogeneous carbon layer. 如申請專利範圍第3項所述之粉體改質之氣相沈積方法,其中在將碳之氣相前驅物通入該反應器的步驟之前,更包括一於所述之粉體的表面製作觸媒層的步驟;其中前述碳之氣相前驅物係為含一個碳至四個碳的氣相化合物,在使該導體之氣相前驅物轉化為固相導體層的步驟中,該固相導體層係具有奈米碳管。The method for vapor-depositing a powder modified according to claim 3, wherein before the step of introducing a gaseous precursor of carbon into the reactor, the method further comprises: forming a surface of the powder a step of contacting the catalyst layer; wherein the gas phase precursor of the carbon is a gas phase compound containing one carbon to four carbons, and the solid phase is in the step of converting the gas phase precursor of the conductor into a solid phase conductor layer The conductor layer has a carbon nanotube. 如申請專利範圍第4或5項所述之粉體改質之氣相沈積方法,其中在調整該反應器之參數的步驟中更包括以下步驟:提供一加熱裝置,以使該反應器達到一預定反應溫度;以及控制反應時間,使該固相導體層沈積形成一預定厚度於所述之粉體的表面。The method for vapor reforming the powder modified according to claim 4 or 5, wherein the step of adjusting the parameters of the reactor further comprises the step of: providing a heating device to bring the reactor to a The reaction temperature is predetermined; and the reaction time is controlled such that the solid phase conductor layer is deposited to form a predetermined thickness on the surface of the powder. 一種電極製作方法,包含以下步驟:將電極粉體置於一反應器,並使所述之電極粉體均勻地分散於該反應器;通入至少一種導體之氣相前驅物進入該反應器;調整該反應器之參數,使該導體之氣相前驅物轉化為固相導體層,並使該固相導體層沈積於所述之電極粉體的表面以形成改質電極粉體;以及將所述之改質電極粉體製作成一電極。An electrode manufacturing method comprising the steps of: placing an electrode powder in a reactor, and uniformly dispersing the electrode powder in the reactor; and introducing a gas phase precursor of at least one conductor into the reactor; Adjusting the parameters of the reactor, converting the gas phase precursor of the conductor into a solid phase conductor layer, and depositing the solid phase conductor layer on the surface of the electrode powder to form a modified electrode powder; The modified electrode powder is fabricated into an electrode. 如申請專利範圍第7項所述之電極製作方法,其中在將電極粉體置於一反應器的步驟中,更包括通入一惰性氣體於該反應器的步驟,並控制該惰性氣體的流量以將所述之電極粉體均勻地分散於該反應器。The method for fabricating an electrode according to claim 7, wherein the step of placing the electrode powder in a reactor further comprises the step of introducing an inert gas into the reactor, and controlling the flow rate of the inert gas. The electrode powder is uniformly dispersed in the reactor. 如申請專利範圍第7項所述之電極製作方法,其中在通入至少一種導體之氣相前驅物進入該反應器的步驟中,係將碳之氣相前驅物通入該反應器。The method of fabricating an electrode according to claim 7, wherein in the step of introducing a vapor phase precursor of at least one conductor into the reactor, a gas phase precursor of carbon is introduced into the reactor. 如申請專利範圍第9項所述之電極製作方法,其中前述碳之氣相前驅物係為含一個碳至四個碳的氣相化合物;而在使該導體之氣相前驅物轉化為固相導體層的步驟中,該固相導體層係為一非均質的碳層。The method for fabricating an electrode according to claim 9, wherein the gas phase precursor of the carbon is a gas phase compound containing one carbon to four carbons; and the gas phase precursor of the conductor is converted into a solid phase. In the step of conducting the conductor layer, the solid phase conductor layer is a heterogeneous carbon layer. 如申請專利範圍第9項所述之電極製作方法,其中在將碳之氣相前驅物通入該反應器的步驟之前,更包括一於所述之電極粉體的表面製作觸媒層的步驟;其中前述碳之氣相前驅物係為含一個碳至四個碳的氣相化合物,在使該導體之氣相前驅物轉化為固相導體層的步驟中,該固相導體層係具有奈米碳管。The electrode manufacturing method according to claim 9, wherein the step of forming a catalyst layer on the surface of the electrode powder before the step of introducing a gas phase precursor of carbon into the reactor Wherein the gas phase precursor of the carbon is a gas phase compound containing one carbon to four carbons, and in the step of converting the gas phase precursor of the conductor into a solid phase conductor layer, the solid phase conductor layer has a naphthalene Carbon tube. 如申請專利範圍第10或11項所述之電極製作方法,其中在調整該反應器之參數的步驟中更包括以下步驟:提供一加熱裝置,以使該反應器達到一預定反應溫度;以及控制反應時間,使該固相導體層沈積形成一預定厚度於所述之粉體的表面。The electrode preparation method according to claim 10 or 11, wherein the step of adjusting the parameters of the reactor further comprises the steps of: providing a heating device to bring the reactor to a predetermined reaction temperature; and controlling The reaction time is such that the solid phase conductor layer is deposited to form a predetermined thickness on the surface of the powder. 一種電極,其係由電極粉體所製作成型,其中所述之電極粉體的表面具有一固相導體層,該固相導體層係提供一第一路徑及一第二路徑,藉以使電子可沿著該第一路徑傳輸,而離子可沿著該第二路徑傳輸。An electrode formed by an electrode powder, wherein the surface of the electrode powder has a solid phase conductor layer, the solid phase conductor layer providing a first path and a second path, so that the electron can be Transmitted along the first path, and ions can be transported along the second path.
TW100127243A 2011-08-01 2011-08-01 Vapor-phase deposition method for modifying powder surface, manufacturing method of electrode and electrode TWI453298B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW100127243A TWI453298B (en) 2011-08-01 2011-08-01 Vapor-phase deposition method for modifying powder surface, manufacturing method of electrode and electrode

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW100127243A TWI453298B (en) 2011-08-01 2011-08-01 Vapor-phase deposition method for modifying powder surface, manufacturing method of electrode and electrode

Publications (2)

Publication Number Publication Date
TW201307605A true TW201307605A (en) 2013-02-16
TWI453298B TWI453298B (en) 2014-09-21

Family

ID=48169670

Family Applications (1)

Application Number Title Priority Date Filing Date
TW100127243A TWI453298B (en) 2011-08-01 2011-08-01 Vapor-phase deposition method for modifying powder surface, manufacturing method of electrode and electrode

Country Status (1)

Country Link
TW (1) TWI453298B (en)

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TW200533779A (en) * 2004-04-13 2005-10-16 China Synthetic Rubber Corp Produce carbon nanotubes by chemical catalytic deposited method
KR101406013B1 (en) * 2008-03-17 2014-06-11 신에쓰 가가꾸 고교 가부시끼가이샤 Non-aqueous electrolyte secondary battery, negative electrode material, and making method
US20110104576A1 (en) * 2009-10-29 2011-05-05 Uchicago Argonne, Llc Lithium-oxygen electrochemical cells and batteries

Also Published As

Publication number Publication date
TWI453298B (en) 2014-09-21

Similar Documents

Publication Publication Date Title
Zhang et al. Structural Engineering of Hierarchical Micro‐nanostructured Ge–C Framework by Controlling the Nucleation for Ultralong‐Life Li Storage
JP7133914B2 (en) Porous silicon composite clusters, carbon composites using the same, and electrodes, lithium batteries, field emission devices, biosensors, semiconductor devices and thermoelectric devices containing the same
CN108899507B (en) Preparation method of double-layer carbon-coated metal sulfide composite electrode material with core-shell structure
Jo et al. Continuous-flow synthesis of carbon-coated silicon/iron silicide secondary particles for Li-ion batteries
Deng et al. One-step ultrasonic spray route for rapid preparation of hollow Fe3O4/C microspheres anode for lithium-ion batteries
CN106544640B (en) Carbon coating method of nanoparticles and carbon-coated nanoparticles manufactured thereby
US9774033B2 (en) Process for producing silicon nanowires directly from silicon particles
Yang et al. Regulating the Li2S deposition by grain boundaries in metal nitrides for stable lithium-sulfur batteries
CN108807862A (en) A kind of silicon based composite material and preparation method thereof, negative material and lithium battery
You et al. Design strategies of Si/C composite anode for lithium‐ion batteries
CN1889290A (en) Olivine carbon bobbles composite material and use thereof
WO2019019410A1 (en) Modified lithium-free anode, method for preparing same, and lithium-ion battery comprising same
CN112397706A (en) Lithium ion battery cathode material structure, preparation method thereof and lithium ion battery
CN100540456C (en) A kind of silicon nanowire/carbon composite and its production and use
Du et al. Large-scale synthesis of silicon arrays of nanowire on titanium substrate as high-performance anode of Li-ion batteries
Hong et al. Novel synthesis of Silicon/Carbon nanotubes microspheres as anode additives through chemical vapor deposition in fluidized bed reactors
CN100369809C (en) Carbon wool ball material and its preparation method and uses
Ou et al. Carbon coated Si nanoparticles anchored to graphene sheets with excellent cycle performance and rate capability for Lithium-ion battery anodes
Qiu et al. Tailored chemically bonded metal phosphide@ carbon nanowire arrays on foam metal as an all-in-one anode for ultrahigh-area-capacity sodium-ion batteries
Chang et al. Solution-grown phosphorus-hyperdoped silicon nanowires/carbon nanotube bilayer fabric as a high-performance lithium-ion battery anode
Wu et al. Reviving of silicon waste with N-doped carbon core-shell structure prepared by vapor deposition polymerization of polypyrrole applied in lithium-ion battery
CN110247028A (en) A kind of nano wire/three-dimensional graphene composite material
Huang et al. Silicon/carbon composites based on natural microcrystalline graphite as anode for lithium-ion batteries
KR101653962B1 (en) Method of doped carbon coating on nanoparticle, method of doped carbon nano structure, doped carbon coated nano particle, doped carbon nanoscale structure produced by the same, and use thereof
Wang et al. High-performance anode of lithium ion batteries with plasma-prepared silicon nanoparticles and a three-component binder

Legal Events

Date Code Title Description
MM4A Annulment or lapse of patent due to non-payment of fees