TWI450947B - Method for producing β-sialon - Google Patents

Method for producing β-sialon Download PDF

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TWI450947B
TWI450947B TW100132375A TW100132375A TWI450947B TW I450947 B TWI450947 B TW I450947B TW 100132375 A TW100132375 A TW 100132375A TW 100132375 A TW100132375 A TW 100132375A TW I450947 B TWI450947 B TW I450947B
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acid
mixed
aluminum oxynitride
solution
heating step
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TW201217495A (en
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Shintaro Watanabe
Mitsuaki Saitoh
Hideyuki Emoto
Suzuya Yamada
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Denki Kagaku Kogyo Kk
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    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
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    • C09K11/00Luminescent, e.g. electroluminescent, chemiluminescent materials
    • C09K11/08Luminescent, e.g. electroluminescent, chemiluminescent materials containing inorganic luminescent materials
    • C09K11/0883Arsenides; Nitrides; Phosphides
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    • C09K11/00Luminescent, e.g. electroluminescent, chemiluminescent materials
    • C09K11/08Luminescent, e.g. electroluminescent, chemiluminescent materials containing inorganic luminescent materials
    • C09K11/77Luminescent, e.g. electroluminescent, chemiluminescent materials containing inorganic luminescent materials containing rare earth metals
    • C09K11/7728Luminescent, e.g. electroluminescent, chemiluminescent materials containing inorganic luminescent materials containing rare earth metals containing europium
    • C09K11/77348Silicon Aluminium Nitrides or Silicon Aluminium Oxynitrides

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Description

β型矽鋁氮氧化物之製造方法Method for producing β-type lanthanum aluminum oxynitride

本發明係關於將銪(Eu)固溶的β型矽鋁氮氧化物之製造方法。The present invention relates to a method for producing a β-type lanthanum aluminum oxynitride which solid-solves lanthanum (Eu).

在專利文獻1中係記載有以將Eu固溶的β型矽鋁氮氧化物之製造方法而言,藉由使用氫氟酸與硝酸的混酸溶液的酸處理,來使固溶有Eu的β型矽鋁氮氧化物的發光強度提升的技術內容。但是,在專利文獻1中亦記載有若混酸溶液的濃度較高時,螢光體會溶解,及若溫度為60℃以上時,螢光體會溶解的技術內容。Patent Document 1 describes a method for producing a β-type lanthanum aluminum oxynitride in which Eu is dissolved, and an acid-treated solution of hydrofluoric acid and nitric acid is used to chemically dissolve β of Eu. The technical content of the luminescence intensity improvement of the bismuth aluminum oxynitride. However, Patent Document 1 also discloses a technique in which a phosphor dissolves when the concentration of the mixed acid solution is high, and when the temperature is 60 ° C or higher, the phosphor dissolves.

在專利文獻2中係揭示出為了使固溶有Eu的β型矽鋁氮氧化物的發光強度提升,將經粉碎的燒成物在氮氣以外的惰性氣體中在1300℃~1600℃下進行再加熱後,使用50%氫氟酸與70%硝酸的混酸溶液來進行酸處理的技術。Patent Document 2 discloses that in order to increase the luminescence intensity of β-type lanthanum aluminum oxynitride in which Eu is dissolved, the pulverized fired product is further dried at 1300 ° C to 1600 ° C in an inert gas other than nitrogen. After heating, a technique of acid treatment using a mixed acid solution of 50% hydrofluoric acid and 70% nitric acid is used.

[先前技術文獻][Previous Technical Literature] [專利文獻][Patent Literature]

[專利文獻1]日本特開2005-255885號公報[Patent Document 1] Japanese Patent Laid-Open Publication No. 2005-255885

[專利文獻2]國際公開第2008/062781號小冊子[Patent Document 2] International Publication No. 2008/062781

本發明之目的在提供一種可重現性佳地實現更高發光效率之固溶有Eu的β型矽鋁氮氧化物之製造方法。SUMMARY OF THE INVENTION An object of the present invention is to provide a method for producing a β-type lanthanum aluminum oxynitride which is solid-solubilized with Eu which is reproducible in achieving higher luminous efficiency.

本發明係基於在酸處理步驟中在使用氫氟酸與硝酸的混酸溶液的情形下,若降低混酸溶液濃度,所得螢光體的發光強度會變低,但是在較高溫度下,發光強度會變高的新穎見解而得者。該見解係與專利文獻1所記載之「若混酸溶液的濃度較高,固溶有Eu的β型矽鋁氮氧化物會溶解,故較不理想」及「混酸處理溫度較低為佳」的揭示呈相反的結果。The present invention is based on the use of a mixed acid solution of hydrofluoric acid and nitric acid in the acid treatment step, if the concentration of the mixed acid solution is lowered, the luminous intensity of the obtained phosphor will become low, but at a higher temperature, the luminous intensity will be The new insights that have become higher. This knowledge is described in Patent Document 1 "If the concentration of the mixed acid solution is high, the β-type lanthanum aluminum oxynitride in which Eu is dissolved is dissolved, so it is less desirable" and the "mixed acid treatment temperature is lower". Reveal the opposite result.

本發明係一種β型矽鋁氮氧化物之製造方法,係在以通式:Si6-z Alz Oz N8-z (0<z≦4.2)所示之β型矽鋁氮氧化物上固溶Eu的β型矽鋁氮氧化物之製造方法,其具有:將含有Si、Al、Eu的原料混合粉末在氮氣環境中進行燒成的第一加熱步驟;將所得的燒成物在惰性氣體環境中或真空中進行熱處理的第二加熱步驟;及在第二加熱步驟後,在氫氟酸與硝酸的混酸溶液中,以超過60℃、100℃以下的溫度範圍進行酸處理的步驟。The present invention relates to a method for producing a β-type lanthanum aluminum oxynitride, which is a β-type lanthanum aluminum oxynitride represented by the general formula: Si 6-z Al z O z N 8-z (0<z≦4.2). A method for producing a solid solution of Eu-type β-alumina aluminum oxynitride, comprising: a first heating step of firing a raw material mixed powder containing Si, Al, and Eu in a nitrogen atmosphere; and the obtained fired product is a second heating step of performing heat treatment in an inert gas atmosphere or in a vacuum; and a step of performing acid treatment in a mixed acid solution of hydrofluoric acid and nitric acid at a temperature range exceeding 60 ° C and 100 ° C or less after the second heating step .

藉由本發明之方法,可重現性佳地製造具有高發光效率之將Eu固溶的β型矽鋁氮氧化物。By the method of the present invention, ?-type lanthanum aluminum oxynitride which is solid-solved with Eu having high luminous efficiency can be produced with good reproducibility.

[用以實施發明之形態][Formation for implementing the invention]

本發明係一種將Eu固溶的β型矽鋁氮氧化物之製造方法,其係包含:將含有Si、Al、Eu的原料混合粉末在氮氣環境中進行燒成的第一加熱步驟;將所得的燒成物在惰性氣體環境中或真空中進行熱處理的第二加熱步驟;及在第二加熱步驟後,在氫氟酸與硝酸的混酸溶液中,以超過60℃、100℃以下的溫度範圍進行酸處理的步驟。The present invention relates to a method for producing a β-type lanthanum aluminum oxynitride which dissolves Eu, which comprises: a first heating step of firing a raw material mixed powder containing Si, Al, and Eu in a nitrogen atmosphere; a second heating step of heat-treating the material in an inert gas atmosphere or in a vacuum; and, after the second heating step, in a mixed acid solution of hydrofluoric acid and nitric acid at a temperature exceeding 60 ° C and below 100 ° C The step of acid treatment is carried out.

含有Si、Al、Eu的原料混合粉末係指將氧化矽及/或氧化鋁、氮化矽、氮化鋁、選自銪的金屬、氧化物、碳酸鹽、氮化物或氮氧化物的銪化合物加以混合的粉末。The raw material mixed powder containing Si, Al, and Eu refers to a cerium compound containing cerium oxide and/or aluminum oxide, cerium nitride, aluminum nitride, a metal selected from cerium, an oxide, a carbonate, a nitride, or an oxynitride. The powder to be mixed.

含有Si、Al的原料係以滿足通式:Si6-z Alz Oz N8-z (0<z≦4.2)的方式來進行摻合。The raw material containing Si and Al is blended so as to satisfy the general formula: Si 6-z Al z O z N 8-z (0 < z ≦ 4.2).

Eu含量係以0.1質量%以上3質量%以下的範圍為佳。若Eu含量在上述範圍內,可充分獲得發光亮度。The Eu content is preferably in the range of 0.1% by mass or more and 3% by mass or less. If the Eu content is within the above range, the luminance of the light can be sufficiently obtained.

若將含有Si、Al、Eu的原料混合時,係有進行乾式混合的方法;在與原料各成分不會實質上起反應的惰性溶媒中進行濕式混合後,將溶媒去除的方法等,在本發明中亦可適用任何方法。以混合裝置而言,係可使用V型混合機、搖擺式混合機(Rocking Mixer)、球磨機、振動磨機等。When a raw material containing Si, Al, or Eu is mixed, a method of performing dry mixing is carried out, and a method of removing the solvent after performing wet mixing in an inert solvent that does not substantially react with each component of the raw material is Any method can also be applied in the present invention. As the mixing device, a V-type mixer, a rocking mixer, a ball mill, a vibration mill, or the like can be used.

將原料混合粉末視需要乾燥後,填充在至少將該原料所相接的面形成為氮化硼的坩堝等容器內,在氮氣環境中加熱。The raw material mixed powder is dried as needed, and then filled in a container such as a crucible in which at least the surface on which the raw material is in contact is formed into boron nitride, and heated in a nitrogen atmosphere.

將經混合的原料混合粉末在氮氣環境下,在1820℃以上2200℃以下,較佳為在1850℃以上2050℃以下的溫度範圍下加熱來進行燒成(以下稱為第一加熱步驟)。若加熱溫度較低,Eu無法進入至β型矽鋁氮氧化物結晶中,若將加熱溫度加高至所需以上,則必須施加較高的氮氣壓力來抑制Eu固溶β型矽鋁氮氧化物的分解。燒成中的壓力條件係以0.5MPa以上10MPa以下為佳。加熱時間一般為10小時~20小時。The mixed raw material mixed powder is heated in a nitrogen atmosphere at a temperature of from 1820 ° C to 2200 ° C, preferably from 1850 ° C to 2050 ° C (hereinafter referred to as a first heating step). If the heating temperature is low, Eu can not enter the β-type yttrium aluminum oxynitride crystal. If the heating temperature is increased above the required temperature, a higher nitrogen pressure must be applied to suppress the Eu-solution β-type lanthanum aluminum oxynitride. Decomposition of matter. The pressure condition in the firing is preferably 0.5 MPa or more and 10 MPa or less. The heating time is generally from 10 hours to 20 hours.

以原料混合粉末而言,亦可為含有Si的金屬粉末來取代使用氮化矽。此時,必須將含有Si的金屬粉末在第一加熱步驟之前進行氮化處理。含有Si的金屬粉末的氮化反應係在1400℃以上1600℃的溫度下進行,因此在第一加熱步驟之前將含有Si的金屬粉末在氮氣環境下,在上述溫度範圍下加熱而將Si轉換為Si3 N4In the case of the raw material mixed powder, it is also possible to use a metal powder containing Si instead of using tantalum nitride. At this time, the metal powder containing Si must be subjected to nitriding treatment before the first heating step. The nitridation reaction of the Si-containing metal powder is performed at a temperature of 1400 ° C to 1600 ° C. Therefore, the Si-containing metal powder is heated under the above-mentioned temperature range to convert Si into a nitrogen atmosphere before the first heating step. Si 3 N 4 .

接著,在第一加熱步驟之後,另外將所得的燒成物在真空中或氮氣以外的氣體環境中加熱(以下稱為第二加熱步驟)。該第二加熱步驟係用以使殘留在燒成物中的低結晶性部分更加不安定的處理。因第二加熱步驟處理而變得不安定的低結晶相係藉由後述的混酸溶液處理予以去除。Next, after the first heating step, the obtained fired product is additionally heated in a vacuum or a gas atmosphere other than nitrogen (hereinafter referred to as a second heating step). This second heating step serves to make the low crystalline portion remaining in the fired material more unstable. The low crystal phase which becomes unstable due to the second heating step treatment is removed by the mixed acid solution treatment described later.

為了使低結晶性部分不安定化,較佳為在儘量不含有屬於構成低結晶性部分的元素的氮與氧的氣體環境中將燒成物進行加熱處理。若將第二加熱步驟在氮氣以外的氣體環境中進行時,在排氣步驟後,在加熱爐內填充惰性氣體(以下稱為導入步驟)。惰性氣體係選自氦、氖、氬、氪、氙、氡、氫的氣體,較佳為氬、氫。In order to make the low crystalline portion unstable, it is preferred to heat-treat the fired product in a gas atmosphere in which nitrogen and oxygen belonging to the element constituting the low crystalline portion are not contained as much as possible. When the second heating step is performed in a gas atmosphere other than nitrogen, after the exhausting step, the heating furnace is filled with an inert gas (hereinafter referred to as an introduction step). The inert gas system is selected from the group consisting of helium, neon, argon, xenon, krypton, xenon, and hydrogen, preferably argon or hydrogen.

在第二加熱步驟中,燒成物係在真空中在1200℃以上1550℃以下的溫度範圍、或惰性氣體環境中在1300℃以上1550℃以下的溫度範圍予以加熱。若加熱溫度在該溫度範圍內,可抑制Eu固溶β型矽鋁氮氧化物的分解。In the second heating step, the fired product is heated in a temperature range of 1200 ° C to 1550 ° C or less in a vacuum or in a temperature range of 1300 ° C to 1550 ° C in an inert gas atmosphere. If the heating temperature is within this temperature range, the decomposition of Eu-solution β-type lanthanum aluminum oxynitride can be suppressed.

在第二加熱步驟後進至酸處理步驟。在該酸處理步驟中,係將藉由第二加熱步驟所得的燒成物進行粉碎,使粉碎燒成物分散在氫氟酸與硝酸的混酸溶液中,在超過60℃的溫度範圍下進行攪拌。酸處理步驟係藉由浸漬在酸性液體中,來去除呈不安定化的低結晶性部分的步驟。After the second heating step, the acid treatment step is advanced. In the acid treatment step, the fired product obtained by the second heating step is pulverized, and the pulverized fired product is dispersed in a mixed acid solution of hydrofluoric acid and nitric acid, and stirred at a temperature exceeding 60 ° C. . The acid treatment step is a step of removing the unstabilized low crystalline portion by immersion in an acidic liquid.

酸處理的溫度係超過60℃、100℃以下的溫度範圍。若為過度低溫,Eu固溶的β型矽鋁氮氧化物的發光強度會降低。The temperature of the acid treatment exceeds a temperature range of 60 ° C or lower. If it is excessively low in temperature, the luminescence intensity of the Eu-soluble β-type lanthanum aluminum oxynitride is lowered.

氫氟酸與硝酸的混合溶液亦可為將約50%濃度的氫氟酸與約70%濃度的硝酸加以混合者(以下稱為混合原液)或將該混合原液加以稀釋者(以下將混合原液經稀釋者稱為混酸溶液)。將混合原液稀釋後的溶液的濃度係以25%以上、未達100%為佳,更佳為25%以上50%。亦可非為將高濃度的氫氟酸及硝酸的混合溶液加以稀釋,而是將經稀釋的低濃度的氫氟酸及硝酸加以混合。The mixed solution of hydrofluoric acid and nitric acid may be a mixture of hydrofluoric acid of about 50% concentration and nitric acid of about 70% concentration (hereinafter referred to as mixed stock solution) or diluted with the mixed stock solution (the following mixed liquid solution) Diluted is called mixed acid solution). The concentration of the solution diluted with the mixed stock solution is preferably 25% or more and less than 100%, more preferably 25% or more and 50%. Instead of diluting a high concentration of a mixed solution of hydrofluoric acid and nitric acid, a diluted low concentration of hydrofluoric acid and nitric acid may be mixed.

氫氟酸與硝酸的混合比若為將約50%濃度的氫氟酸與約70%濃度的硝酸加以混合的情形,係以1~9:9~1的比率為佳,特佳為3~7:7~3。When the mixing ratio of hydrofluoric acid and nitric acid is mixed with hydrofluoric acid having a concentration of about 50% and nitric acid having a concentration of about 70%, a ratio of from 1 to 9:9 to 1 is preferred, and particularly preferably from 3 to 3. 7:7~3.

前述混合溶液係以將濃氫氟酸及濃硝酸混合者為佳。濃氫氟酸係指其濃度為40%以上60%以下,濃硝酸係指其濃度為55%以上75%以下者。The mixed solution is preferably a mixture of concentrated hydrofluoric acid and concentrated nitric acid. Concentrated hydrofluoric acid means that the concentration is 40% or more and 60% or less, and concentrated nitric acid means a concentration of 55% or more and 75% or less.

[實施例1][Example 1]

以下關於本發明之實施例,一面參照表1,一面詳加說明。表1係顯示後述實施例1~7及比較例1、2的處理條件與發光特性者。Hereinafter, an embodiment of the present invention will be described in detail with reference to Table 1. Table 1 shows the processing conditions and light-emitting characteristics of Examples 1 to 7 and Comparative Examples 1 and 2 described later.

摻合α型氮化矽粉末(宇部興產公司製SN-E 10級,氧含量1.1質量%、β相含量4.5質量%)95.4質量%、氮化鋁粉末(Tokuyama公司製F級,氧含量0.8質量%)3.0質量%、氧化鋁粉末(大明化學公司製TM-DAR級)0.74質量%、氧化銪粉末(信越化學工業公司製RU級)0.71質量%,而得原料混合物600g。Blending α-type tantalum nitride powder (SN-E grade 10 made by Ube Industries, Ltd., oxygen content 1.1% by mass, β phase content 4.5% by mass) 95.4% by mass, aluminum nitride powder (F grade, Tokuyama company, oxygen content) 0.8% by mass of 3.0% by mass, alumina powder (TM-DAR grade manufactured by Daming Chemical Co., Ltd.), 0.74% by mass, and cerium oxide powder (RU grade manufactured by Shin-Etsu Chemical Co., Ltd.) were 0.71% by mass, and 600 g of a raw material mixture was obtained.

藉由搖擺式混合機(愛知電機公司製RM-10),以60分鐘乾式混合所得的原料混合物,另外全部通過篩孔150μm的不銹鋼製篩,而得原料粉末。The obtained raw material mixture was dry-mixed for 60 minutes by a rocking mixer (RM-10 manufactured by Aichi Electric Co., Ltd.), and all of them were passed through a stainless steel sieve having a mesh opening of 150 μm to obtain a raw material powder.

將所得的原料粉末填充170g在以內寸計為直徑10cm×高度9cm×厚度0.5cm之附蓋的圓筒型氮化硼製容器(電氣化學工業公司製N-1級),在碳加熱器的電氣爐,作為第一加熱步驟而在0.9MPa的加壓氮氣環境中,在1950℃下進行15小時的燒成。將所得的燒成物裂解,通過篩孔45μm的篩而得粉末。The obtained raw material powder was filled with 170 g of a cylindrical boron nitride container (N-1 grade, manufactured by Denki Kagaku Co., Ltd.) having a diameter of 10 cm, a height of 9 cm, and a thickness of 0.5 cm, in a carbon heater. The electric furnace was fired at 1950 ° C for 15 hours in a pressurized nitrogen atmosphere of 0.9 MPa as a first heating step. The obtained calcined product was cleaved and passed through a sieve having a mesh size of 45 μm to obtain a powder.

將所得粉末填充20g在以內寸計為直徑6cm×高度3.5cm×厚度0.5cm之附蓋的圓筒型氮化硼製容器(電氣化學工業公司製N-1級),以碳加熱器的電氣爐,作為第二加熱步驟而在真空中,在1400℃下進行8小時的加熱處理。The obtained powder was filled with 20 g of a cylindrical boron nitride container (N-1 grade, manufactured by Denki Kagaku Co., Ltd.) having a diameter of 6 cm, a height of 3.5 cm, and a thickness of 0.5 cm. The furnace was subjected to heat treatment at 1400 ° C for 8 hours in a vacuum as a second heating step.

將50%濃度的氫氟酸(HF)25ml及70%濃度的硝酸(HNO3 )25ml混合而形成為混合原液。在混合原液中添加蒸餾水150ml,將混合原液的濃度稀釋成25%,來調整HF+HNO3 水溶液200ml。投入第二加熱步驟後的粉末5g,一面將HF+HNO3 水溶液保持在70℃,一面進行1小時的酸處理。25 ml of 50% hydrofluoric acid (HF) and 25 ml of 70% nitric acid (HNO 3 ) were mixed to form a mixed stock solution. 150 ml of distilled water was added to the mixed stock solution, and the concentration of the mixed stock solution was diluted to 25% to adjust 200 ml of the HF + HNO 3 aqueous solution. 5 g of the powder after the second heating step was charged, and the HF + HNO 3 aqueous solution was maintained at 70 ° C for one hour of acid treatment.

酸處理後的粉末係以蒸餾水將酸充分地沖洗過濾,使其乾燥後,通過篩孔45μm的篩而得實施例1的螢光體粉末。The powder after the acid treatment was sufficiently washed with distilled water to filter the acid, dried, and passed through a sieve having a mesh opening of 45 μm to obtain a phosphor powder of Example 1.

接著,對實施例1的螢光體粉末,使用積分球來進行全光束發光光譜測定(參考文獻:照明學會誌,第83卷,第2號,平成11年(2000年),p87-93、NBS標準螢光體之量子效率的測定,大久保和明等著)。激發光係使用經分光的氙燈光源。Next, the full-beam luminescence spectrum was measured using the integrating sphere for the phosphor powder of Example 1 (Reference: Lighting Society, Vol. 83, No. 2, Heisei 11 (2000), p87-93, Determination of the quantum efficiency of NBS standard phosphors, Okubo and Akira). The excitation light system uses a split xenon light source.

所製造的β型矽鋁氮氧化物的評估係如表1所示,以光吸收率、內部量子效率、外部量子效率的發光特性來進行。The evaluation of the produced β-type lanthanum aluminum oxynitride was carried out as shown in Table 1, and was carried out by the light-absorption characteristics, the internal quantum efficiency, and the external quantum efficiency.

在進行該評估時,在試料部安置反射率為99%的標準反射板(Labsphere公司,Spectralon(註冊商標))來測定激發光的光譜,若激發波長為455nm時,由450~465nm的波長範圍的光譜來計算出激發光光子數(Qex),接著,在試料部安置螢光體,由所得的光譜數據來計算出激發反射光光子數(Qref)及螢光光子數(Qem),由所得的三種光子數,來求出光吸收率(=(Qex-Qref)×100)、內部量子效率(=Qem/(Qex-Qref)×100)及外部量子效率(=Qem/Qex×100)。激發反射光光子數係在與激發光光子數相同的波長範圍內,螢光光子數係若激發光為455nm時,在465~800nm的範圍內計算出。At the time of this evaluation, a standard reflection plate (Labsphere, Spectralon (registered trademark)) having a reflectance of 99% was placed in the sample portion to measure the spectrum of the excitation light, and when the excitation wavelength was 455 nm, the wavelength range was from 450 to 465 nm. The spectrum is used to calculate the number of excitation photons (Qex). Then, the phosphor is placed in the sample portion, and the obtained spectral data is used to calculate the number of photons (Qref) and the number of photons (Qem) of the excited reflected light. The three kinds of photons are used to obtain the light absorption rate (=(Qex-Qref)×100), the internal quantum efficiency (=Qem/(Qex-Qref)×100), and the external quantum efficiency (=Qem/Qex×100). The number of photons of the excitation reflection light is in the same wavelength range as the number of photons of the excitation light, and the number of fluorescence photons is calculated in the range of 465 to 800 nm when the excitation light is 455 nm.

實施例1中的發光特性係光吸收率72.5%、內部量子效率69.9%、外部量子效率50.7%。The luminescent properties in Example 1 were 72.5% for light absorption, 69.9% for internal quantum efficiency, and 50.7% for external quantum efficiency.

[實施例2][Embodiment 2]

實施例2的β型矽鋁氮氧化物之製造方法係除了將酸處理的溫度設為80℃以外,係與實施例1為相同的條件,光吸收率71.8%、內部量子效率71.4%、外部量子51.2%。The method for producing β-type lanthanum aluminum oxynitride of Example 2 is the same as in Example 1 except that the temperature of the acid treatment is 80° C., the light absorptivity is 71.8%, the internal quantum efficiency is 71.4%, and the external method. Quantum 51.2%.

[實施例3][Example 3]

實施例3的β型矽鋁氮氧化物之製造方法係除了將酸處理的溫度設為90℃以外,係與實施例1為相同的條件,光吸收率71.2%、內部量子效率72.0%、外部量子51.3%。The method for producing β-type lanthanum aluminum oxynitride of Example 3 was the same as in Example 1 except that the temperature of the acid treatment was 90° C., and the light absorptance was 71.2%, the internal quantum efficiency was 72.0%, and the external method was used. Quantum 51.3%.

[實施例4][Example 4]

實施例4係將酸處理步驟,以將50%濃度的氫氟酸(HF)15ml及70%濃度的硝酸(HNO3 )35ml混合而形成為混合原液,在混合原液中添加蒸餾水150ml,將混合原液稀釋而使濃度成為25%的方式調整HF+HNO3 水溶液200ml。除了投入第二加熱步驟後的粉末5g,一面將HF+HNO3 水溶液保持在80℃一面進行1小時的酸處理以外,係與實施例1同樣地進行。若為實施例4的情形,光吸收率71.6%、內部量子效率70.9%、外部量子效率50.8%。In the fourth embodiment, an acid treatment step is carried out to mix 15 ml of hydrofluoric acid (HF) and 50 ml of 70% strength nitric acid (HNO 3 ) to form a mixed stock solution, and 150 ml of distilled water is added to the mixed stock solution to mix. 200 ml of an aqueous solution of HF+HNO 3 was adjusted so that the stock solution was diluted and the concentration was 25%. In the same manner as in Example 1, except that 5 g of the powder after the second heating step was placed, the HF + HNO 3 aqueous solution was maintained at 80 ° C for 1 hour. In the case of Example 4, the light absorption rate was 71.6%, the internal quantum efficiency was 70.9%, and the external quantum efficiency was 50.8%.

[實施例5][Example 5]

實施例5係將50%濃度的氫氟酸35ml及70%濃度的硝酸15ml混合而形成為混合原液以外,係與實施例4為相同條件之製造方法。若為實施例5的情形,光吸收率71.7%、內部量子效率71.3%、外部量子效率51.1%。Example 5 is a production method in which the same conditions as in Example 4 are carried out except that 35 ml of hydrofluoric acid (50%) and 15 ml of 70% hydrochloric acid are mixed to form a mixed stock solution. In the case of Example 5, the light absorption rate was 71.7%, the internal quantum efficiency was 71.3%, and the external quantum efficiency was 51.1%.

[實施例6][Embodiment 6]

實施例6係將50%濃度的氫氟酸50ml及70%濃度的硝酸50ml混合而形成為混合原液。在混合原液中添加蒸餾水100ml,將混合原液稀釋,調整濃度成為50%的HF+HNO3 水溶液200ml。除了投入第二加熱步驟後的粉末5g,一面將HF+HNO3 水溶液保持在80℃,一面進行1小時的酸處理以外,係為相同者。若為實施例6的情形,光吸收率74.7%、內部量子效率70.0%、外部量子效率52.3%。In Example 6, 50 ml of 50% hydrofluoric acid and 50 ml of 70% nitric acid were mixed to form a mixed stock solution. 100 ml of distilled water was added to the mixed stock solution, and the mixed stock solution was diluted to adjust 200 ml of an aqueous solution of HF + HNO 3 having a concentration of 50%. The same was carried out except that the HF+HNO 3 aqueous solution was kept at 80 ° C while the acid treatment was carried out for 1 hour, except that 5 g of the powder after the second heating step was placed. In the case of Example 6, the light absorption rate was 74.7%, the internal quantum efficiency was 70.0%, and the external quantum efficiency was 52.3%.

[實施例7][Embodiment 7]

實施例7係未在實施例6的酸處理中的酸使用蒸餾水,除了使用100ml的原液濃度100%者以外,係與實施例6同樣地進行。在實施例7中,光吸收率72.9%、內部量子效率72.6%、外部量子效率52.9%。Example 7 was carried out in the same manner as in Example 6 except that distilled water was not used as the acid in the acid treatment of Example 6, except that 100% of the stock solution concentration of 100 ml was used. In Example 7, the light absorption rate was 72.9%, the internal quantum efficiency was 72.6%, and the external quantum efficiency was 52.9%.

(比較例1)(Comparative Example 1)

比較例1除了將酸處理溫度設為60℃以外,係設成與實施例1相同條件。光吸收率為72.0%、內部量子效率為69.2%、外部量子效率為49.8%。Comparative Example 1 was set to the same conditions as in Example 1 except that the acid treatment temperature was changed to 60 °C. The light absorption rate was 72.0%, the internal quantum efficiency was 69.2%, and the external quantum efficiency was 49.8%.

(比較例2)(Comparative Example 2)

比較例2係除了將酸處理溫度設為35℃以外,以與實施例6相同的條件進行。若為比較例2的情形,光吸收率為73.6%、內部量子效率為68.8%、外部量子效率為50.6%。Comparative Example 2 was carried out under the same conditions as in Example 6 except that the acid treatment temperature was 35 °C. In the case of Comparative Example 2, the light absorptance was 73.6%, the internal quantum efficiency was 68.8%, and the external quantum efficiency was 50.6%.

由實施例1、2、3與比較例1可知,藉由提升酸處理的溫度,光吸收率、內部量子效率以及外部量子效率均會提升。處理溫度若為超過60℃、100℃以下即可,以70℃以上90℃以下為佳。From Examples 1, 2, and 3 and Comparative Example 1, it is understood that the light absorption rate, the internal quantum efficiency, and the external quantum efficiency are improved by increasing the temperature of the acid treatment. The treatment temperature may be more than 60 ° C and 100 ° C or less, and preferably 70 ° C or more and 90 ° C or less.

由實施例1~5與比較例2可知,即使酸處理步驟中的混酸溶液的濃度較稀,尤其將混合原液稀釋而使濃度為25%以上50%的範圍內,相較於作為習知例的比較例2,其光吸收率、內部量子效率、外部量子效率的任一者均提升。由比較例1及2可知,若使混酸溶液濃度變稀時,發光特性會降低。It is understood from Examples 1 to 5 and Comparative Example 2 that even if the concentration of the mixed acid solution in the acid treatment step is relatively thin, in particular, the mixed stock solution is diluted to have a concentration of 25% or more and 50%, as compared with the conventional example. In Comparative Example 2, any of the light absorptivity, the internal quantum efficiency, and the external quantum efficiency was improved. As is apparent from Comparative Examples 1 and 2, when the concentration of the mixed acid solution was diluted, the light-emitting characteristics were lowered.

[實施例8][Embodiment 8]

雖在表中未顯示,製作出將摻合有在實施例及比較例中所使用的β型矽鋁氮氧化物的矽酮密封樹脂層積在LED的發光面的發光裝置。若使用實施例1~7的β型矽鋁氮氧化物,在使其發光之後,即使以80℃×濕度40%的高溫放置2小時後,亦未發現發光特性降低。相對於此,在使用比較例1及2的β型矽鋁氮氧化物的發光裝置中,發現發光特性降低。Although not shown in the table, a light-emitting device in which an anthrone sealing resin containing β-type lanthanum aluminum oxynitride used in the examples and the comparative examples was laminated on the light-emitting surface of the LED was produced. When the β-type lanthanum aluminum oxynitrides of Examples 1 to 7 were used, after the light was emitted, even after being left at a high temperature of 80 ° C × humidity of 40% for 2 hours, no decrease in luminescent properties was observed. On the other hand, in the light-emitting device using the β-type lanthanum aluminum oxynitride of Comparative Examples 1 and 2, it was found that the light-emitting characteristics were lowered.

[產業上可利用性][Industrial availability]

本發明之β型矽鋁氮氧化物若作為螢光體加以使用時,以紫外至藍色光的範圍寬廣的波長予以激發,而呈現高亮度的綠色發光,因此可適於使用作為以藍色或紫外光為光源的白色LED的螢光體,而可適於使用在照明器具、圖像顯示裝置等。When the β-type lanthanum aluminum oxynitride of the present invention is used as a phosphor, it is excited by a wide wavelength range of ultraviolet to blue light, and exhibits high-luminance green light, so that it can be suitably used as blue or The ultraviolet light is a phosphor of a white LED of a light source, and can be suitably used for a lighting fixture, an image display device, or the like.

Claims (2)

一種β型矽鋁氮氧化物之製造方法,係在以通式:Si6-z Alz Oz N8-z (0<z≦4.2)所示之β型矽鋁氮氧化物上固溶Eu的β型矽鋁氮氧化物之製造方法,其包含:將含有Si、Al、Eu的原料混合粉末在氮氣環境中進行燒成的第一加熱步驟;將所得的燒成物在惰性氣體環境中或真空中進行熱處理的第二加熱步驟;及在第二加熱步驟後,在氫氟酸與硝酸的混酸溶液中,以超過60℃、100℃以下的溫度範圍進行酸處理的步驟,該混酸溶液係以體積比(50%濃度的氫氟酸/70%濃度的硝酸)1~9/9~1的比率,將50%濃度的氫氟酸與70%濃度的硝酸混合而得。A method for producing β-type lanthanum aluminum oxynitride, which is dissolved on β-type lanthanum aluminum oxynitride represented by the general formula: Si 6-z Al z O z N 8-z (0<z≦4.2) A method for producing a β-type lanthanum aluminum oxynitride of Eu, comprising: a first heating step of firing a raw material mixed powder containing Si, Al, and Eu in a nitrogen atmosphere; and the obtained fired material in an inert gas atmosphere a second heating step of heat treatment in a medium or vacuum; and a step of acid treatment in a mixed acid solution of hydrofluoric acid and nitric acid at a temperature range exceeding 60 ° C and 100 ° C or less after the second heating step, the mixed acid The solution was obtained by mixing 50% hydrofluoric acid and 70% nitric acid in a volume ratio (50% hydrofluoric acid/70% nitric acid) at a ratio of 1 to 9/9 to 1. 如申請專利範圍第1項之β型矽鋁氮氧化物之製造方法,其中前述混酸溶液係將濃氫氟酸及濃硝酸混合而加以稀釋者,稀釋率為25%以上。The method for producing a β-type lanthanum aluminum oxynitride according to the first aspect of the invention, wherein the mixed acid solution is prepared by mixing concentrated hydrofluoric acid and concentrated nitric acid, and the dilution ratio is 25% or more.
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