Method for preparing manganese-doped red phosphor, product, device, and backlight module

Abstract

Disclosed are a preparation method for manganese-doped red phosphor, a device and a backlight module including the product. The method includes: 1) mixing A2BF6 polycrystalline particles with mill balls; 2) mixing A2BF6 powder obtained after ball-milling with a hydrofluoric acid for secondary crystallization; 3) filtering out solid particles in A2BF6 and hydrofluoric acid solution after the secondary crystallization; 4) performing ion exchange between A2BF6 particles and A2BF6; and 5) filtering out solid particles to obtain a filter cake, and performing drying treatment to obtain manganese-doped red phosphor.

Description

CROSS REFERENCE TO RELATED APPLICATIONS

This application is a national application of CN201811006339.7, filed on Aug. 30, 2018. The contents of CN201811006339.7 are all hereby incorporated by reference.

TECHNICAL FIELD

The disclosure relates to a preparation method, a product and an application of phosphor, and in particular to a preparation method for manganese-doped red phosphor, a product, a device and a backlight module.

BACKGROUND

With the development of a display technology, new-type display technologies are developed endlessly, such as Organic Light-Emitting Diode (OLED) curved flexible display, a quantum dot display technology, virtual and augmented reality display. However, mainstream displays that are widely used at present are still a liquid crystal display technology that uses Light-Emitting Diode (LED) as a backlight source. Because liquid crystal display is light-emitting passively, an external light source must be used for image display. Therefore, the luminous quality of the backlight source often determines the quality of a liquid crystal display image.

LED has the advantages of high energy efficiency, low energy consumption, high reliability, long service life, small size and the like. LED is a very excellent backlight source for liquid crystal displays, and the white light LED used for the display backlight source mainly uses a blue light chip to excite a fluorescence conversion-type LED device packaged by red and green phosphor. A color picture of a liquid crystal display is realized through R, G, B color filters. In order to improve a color gamut range and a color saturation of the liquid crystal display, red, green, and blue spectral ranges of the backlight source should be matched with a range of the corresponding display filter. Therefore, the development of wide color gamut and high color saturation display requires the development of a narrow-band LED fluorescent material which is matched with the display filter, especially red and green narrow-band fluorescent materials suitable for blue chip excitation.

Compared with the parity-allowed f-d transition of Eu²⁺ or Ce³⁺, d-d transition emission of Me which is parity-forbidden has a narrower spectral range. Therefore, the use of red emission of the Mn⁴⁺ is expected to broaden the color gamut. Furthermore, phonon energy of a fluoride system is low, so the fluoride system activated by the Mn⁴⁺ is expected to produce high-efficiency luminescence. The fluoride activated by the Me is good red phosphor for the display backlight source. However, the fluoride red phosphor currently used in the display backlight source mainly includes K₂SiF₆:Mn⁴⁺ and K₂GeF₆:Mn⁴⁺ two systems.

K₂TiF₆:Mn⁴⁺ also emits light under the excitation of 450 nm to 460 nm of blue light, but due to the low external quantum efficiency of K₂TiF₆:Mn⁴⁺, the K₂TiF₆:Mn⁴⁺ red phosphor is not commercialized all the time. A document (Nature Communications, 2014, 5:4312) and a patent with a patent document number CN103980896A disclose that while the Mn concentration is 1.40%, the internal quantum efficiency of K₂TiF₆:Mn⁴⁺ reaches 98% maximally and the absorption rate is only 36% (the corresponding external quantum efficiency is 35.28%); and while the Me concentration is 6.50%, the absorption rate reaches 60% but the internal quantum efficiency is only 78% (the corresponding external quantum efficiency is 46.8%). It is reported by a document (Optical Materials Express, 2018, 8(1): 73) that the internal quantum efficiency of K₂TiF₆:Mn⁴⁺ synthesized by ball-milling at 100 RPMs for 15 minutes is 62.5%, and the maximum external quantum efficiency is 47% (namely, the absorption rate is 75.2%). It is reported by a document (Optical Materials Express, 2018, 8(1): 73) that the maximum internal quantum efficiency of K₂TiF₆:Mn⁴⁺ synthesized by ball-milling at 100 RPMs for 5 minutes is 65.9%, and the external quantum efficiency is 42.8%. It is reported by a document (J. Mater. Chem. C, 2015, 3, 1935) that the internal quantum efficiency of K₂TiF₆:Mn⁴⁺ red powder is 98%, but a diffuse reflectance spectrum in FIG. 5 of the document shows that the absorption rate of the phosphor thereof is only about 20% (namely, the external quantum efficiency is about 19.6%). It is reported by a document (J. Mater. Sci: Mater. Electron. 2018, 29:12536) that the internal quantum efficiency of K₂TiF₆:Mn⁴⁺@NaF is 99.19%±0.03%, but the external quantum efficiency is unknown. It is reported by a document (Journal of Materials Science Materials in Electronics, 2017, 28(16):11878) that the internal quantum efficiency of K₂TiF₆:Mn⁴⁺ reaches 94.04%, and the external quantum efficiency is unknown. It is reported by a document (Materials Research Bulletin, 2016, 83:316) that the internal quantum efficiency of K₂TiF₆:Mn⁴⁺ reaches 99%, and the external quantum efficiency is unknown. It is reported by a document (J. Lumin. 2017, 188:307) that the internal quantum efficiency of K₂TiF₆.BaF(HF):Mn⁴⁺ is 60.75%±0.03%, and the external quantum efficiency is unknown. It is reported by a document (ECS J. Solid State Sci. Tech. 2018, 7: R3006) that the internal quantum efficiency of K₂TiF₆:Mn⁴⁺ is 62%, and the external quantum efficiency is unknown. A patent with a patent document number CN106221694A discloses that the internal quantum efficiency of K_1.8Ba_0.1Ti_0.95F₆:0.05Mn⁴⁺ is at most 98%, and the external quantum efficiency is unknown. A patent with a patent document number CN106479485A discloses that the internal quantum efficiency of K_1.8Cu_0.1Ti_0.95F₆:0.05Mn⁴⁺ is at most 98%, and the external quantum efficiency is unknown. A patent with a patent document number CN106318373A discloses a synthesis method suitable for K₂SiF₆:Mn⁴⁺, K₂GeF₆:Mn⁴⁺ and K₂TiF₆:Mn⁴⁺ red phosphor, but the patent does not provide internal and external quantum efficiency parameters, it is judged from FIG. 9 in Embodiments 1 to 3 that the internal quantum efficiency of the K₂TiF₆:Mn⁴⁺ red phosphor synthesized by using this method of the patent is far lower than that of K₂SiF₆:Mn⁴⁺ and K₂GeF₆:Mn⁴⁺.

Although there are many documents and patents for the research of the synthesis and luminescence properties of the K₂TiF₆:Mn⁴⁺ red phosphor, the external quantum efficiency of the manganese-doped red phosphor prepared in the prior art is generally 47% or less, therefore, the prior art has a technical problem that the external quantum efficiency of the manganese-doped red phosphor is lower.

SUMMARY

A technical problem to be solved by the disclosure is to provide a preparation method for manganese-doped red phosphor, a product, a device and a backlight module, so as to solve the technical problem in the prior art that the external quantum efficiency of the manganese-doped red phosphor is lower.

The disclosure solves the above technical problem through the following technical schemes.

An embodiment of the disclosure provides a preparation method for manganese-doped red phosphor, and the method includes:

• • 1) A₂BF₆ polycrystalline particles are mixed with grinding balls, herein the mass ratio of the A₂BF₆ polycrystalline particles to the grinding balls is 1:1 to 1:2.5, and then ball-milling is performed for 30 minutes to 120 minutes, herein A is a monovalent cation, and B is a tetravalent cation;
  • 2) A₂BF₆ powder obtained after ball-milling is mixed with a hydrofluoric acid, a mass fraction of the hydrofluoric acid is 30% to 59%, herein the mass ratio of the A₂BF₆ powder obtained after ball-milling to the hydrofluoric acid is 1:1 to 2.5:1, and then at a revolving speed of 1 RPM to 1200 RPMs, stirring is performed for 12 hours to 72 hours for secondary crystallization treatment;
  • 3) solid particles in A₂BF₆ and hydrofluoric acid solution after the secondary crystallization are filtered out, to obtain A₂BF₆ particles after the secondary crystallization;
  • 4) according to the molar ratio of A₂BF₆ and A₂MnF₆ which is 93:7 to 90:10, the A₂BF₆ particles after the secondary crystallization and A₂MnF₆ are weighed, and then firstly A₂MnF₆ is dissolved in the hydrofluoric acid by mass fraction, the mass fraction of the hydrofluoric acid is 30% to 59%, and then the A₂BF₆ is added to a solution comprising A₂MnF₆ and hydrofluoric acid, and the stirring is continuously performed for 10 minutes to 360 minutes for ion exchange, herein a ratio of the total mass of A₂BF₆ and A₂MnF₆ to the mass of the hydrofluoric acid is 1:1 to 4:1; and
  • 5) the solid particles in solution after the ion exchange are filtered out, to obtain a filter cake, and then the filter cake is dried to obtain the manganese-doped red phosphor.

Optionally, a secondary crystallization treatment process in the step 2) is performed in a sealed reactor.

Optionally, the step 3) includes:

• • under conditions of a vacuum degree of 60 Pa to 200 Pa and a flow rate of 60 L/min to 100 L/min, vacuum suction filtration treatment is performed on the A₂BF₆ and hydrofluoric acid solution after the secondary crystallization, to obtain the A₂BF₆ particles after the secondary crystallization.

Optionally, a preparation method for A₂MnF₆ in the step 4) includes:

• • A: potassium hydrogen fluoride is dissolved in a hydrofluoric acid, the mass fraction of the hydrofluoric acid is 30% to 59%, herein a mass ratio of the potassium hydrogen fluoride to the hydrofluoric acid is 2:10 to 4:10; and at a revolving speed of 10 RPMs to 1000 RPMs, stirring is performed for 15 minutes to 40 minutes;
  • B: potassium permanganate is added while stirring, herein a mass ratio of the potassium permanganate to the potassium hydrogen fluoride is 1:5 to 2:5;
  • C: a hydrogen peroxide is used to titrate solution after adding the potassium permanganate to be golden yellow, the mass fraction of the hydrogen is 25% to 40%;
  • D: the titrated solution together with a reactor is put into an ice-water mixture at 0° C. to 5° C. and standing is performed for 15 minutes to 40 minutes, a precipitate is filtered out, and then acetone is used to repeatedly wash the precipitate to be neutral; and
  • E: the washed precipitate is dried for 1 hour to 4 hours under conditions of a temperature of 60° C. to 90° C. and a vacuum degree of 90 Pa to 500 Pa, to obtain A₂MnF₆.

Optionally, the step 5) includes:

• • under conditions of a vacuum degree of 60 Pa to 200 Pa and a flow rate of 60 L/min to 100 L/min, vacuum suction filtration treatment is performed on the solution after ion exchange, to obtain a filter cake, and then acetone is used to repeatedly wash the filter cake to be neutral, and then the filter cake is dried for 1 hour to 4 hours under conditions of a temperature of 60° C. to 90° C. and a vacuum of 90 Pa to 500 Pa, to obtain the manganese-doped red phosphor.

Optionally, the monovalent cation A includes one or a combination of a group consist of a hydrogen ion, a lithium ion, a sodium ion and a cesium ion; and

• • the tetravalent cation B includes one or a combination of a group consist of a silicon ion, a germanium ion, a tin ion, and a zirconium ion.

An embodiment of the disclosure further provides a product prepared by any one of the above preparation methods for the manganese-doped red phosphor.

An embodiment of the disclosure further provides a device packaged by a product prepared by any one of the above preparation methods for the manganese-doped red phosphor, the device includes: an excitation source, phosphor, an electrode, a packaging material, and a support, herein,

• • the electrode is connected with the excitation source;
  • the phosphor is distributed in the packaging material, and arranged around the excitation source; and
  • the support carries the excitation source, the electrode, and the packaging material.

An embodiment of the disclosure further provides a backlight module packaged by a product prepared by any one of the above preparation methods for the manganese-doped red phosphor.

Compared with the prior art, the disclosure has the following advantages:

• • 1). The embodiment of the disclosure is applied, through pulverizing the A₂BF₆ polycrystalline particles for the secondary crystallization, and adding A₂BF₆ to the hydrogen fluoride solution in which A₂MnF₆ is dissolved for the ion exchange, the external quantum efficiency of the manganese-doped red phosphor can be improved to 69.09%.
  • 2). The embodiment of the disclosure is applied, the external quantum efficiency of the manganese-doped red phosphor is improved, and less phosphor can be used to achieve the same brightness, and the amount of the phosphor is saved.
  • 3). The embodiment of the disclosure is applied, and a use cost is reduced under a condition that it is similar to a wavelength peak value of the existing K₂GeF₆:Mn⁴⁺.
  • 4). The particle size of the phosphor prepared after ball-milling and secondary crystallization treatment is highly dispersed, which can further save the amount of the phosphor.

BRIEF DESCRIPTION OF THE DRAWINGS

FIG. 1 is a structure schematic diagram of a device packaged by manganese-doped red phosphor provided by an embodiment of the disclosure.

FIG. 2 is a test result of the emission intensity of products prepared in Embodiments 1 to 4 provided by an embodiment of the disclosure.

FIG. 3 is a test result of the emission intensity of products prepared in Embodiments 5 to 8 provided by an embodiment of the disclosure.

FIG. 4 is a test result of the emission intensity of products prepared in Embodiments 9 to 12 provided by an embodiment of the disclosure.

FIG. 5 is a test result of the emission intensity of products prepared in Embodiments 13 to 16 provided by an embodiment of the disclosure.

FIG. 6 is a test result of the emission intensity of products prepared in Embodiments 17 to 19 provided by an embodiment of the disclosure.

FIG. 7 is a schematic diagram of an emission spectrum of a material prepared in the embodiment of the disclosure and a contrast example provided by an embodiment of the disclosure.

DETAILED DESCRIPTION OF THE EMBODIMENTS

Embodiments of the disclosure are described in detail below. The embodiments are implemented on the premise of technical schemes of the disclosure, and detailed implementation modes and specific operation processes are provided, but a scope of protection of the disclosure is not limited to the following embodiments.

The embodiments of the disclosure provide a preparation method for manganese-doped red phosphor, a product, a device and a backlight module, and the preparation method for the manganese-doped red phosphor provided by the embodiment of the disclosure are firstly introduced below.

An embodiment of the disclosure provides a preparation method for manganese-doped red phosphor, the method includes:

• • 1) K₂TiF₆ polycrystalline particles purchased from Aladdin Reagent Network with an article number P112424 were mixed with grinding balls, and the mass ratio of the K₂TiF₆ polycrystalline particles to the grinding balls was 1:1. A mixture of the K₂TiF₆ polycrystalline particles and the grinding balls was loaded into a polytetrafluoroethylene reactor, and ball-milling was performed for 30 min in a MSK-SFM-3-type high-speed vibration ball mill produced by Hefei Kejing Material Technology Co., Ltd.
  • 2) In the polytetrafluoroethylene reactor, K₂TiF₆ powder obtained after ball-milling was mixed with a hydrofluoric acid, the mass fraction of the hydrofluoric acid was 30%, herein the mass ratio of the K₂TiF₆ powder obtained after ball-milling to the hydrofluoric acid was 1:1, and the hydrofluoric acid was an analytical pure hydrofluoric acid produced by Tianjin Hengxing Chemical Reagent Manufacture Co., Ltd. Then, the polytetrafluoroethylene reactor was sealed, and an HJ-4A-type digital display temperature controlled magnetic stirrer produced by Changzhou Guoyu Instrument Manufacture Co., Ltd. was used to treat the mixture of the hydrofluoric acid and the K₂TiF₆ powder obtained after ball-milling, at a revolving speed of 1 RPM to 1200 RPMs stirring was performed for 12 hours to 72 hours for secondary crystallization treatment.
  • 3) An SHZ-BD(III) polytetrafluoroethylene vacuum filter produced by Yangshen Technology Instrument (Shanghai) Co., Ltd., under conditions of a vacuum degree of 60 Pa to 200 Pa and a flow rate of 60 L/min to 100 L/min, was used to perform vacuum suction filtration treatment on K₂TiF₆ and hydrofluoric acid solution after the secondary crystallization, to obtain K₂TiF₆ particles after the secondary crystallization.
  • 4) Firstly, K₂MnF₆ was prepared according to the following method: A: In a polytetrafluoroethylene beaker, according to the mass ratio of analytical pure potassium hydrogen fluoride produced by Shanghai Sansi Zhuoyue Chemical Co., Ltd. to the hydrofluoric acid which was 2:10 to 4:10, the potassium hydrogen fluoride was dissolved in the hydrofluoric acid, the mass fraction of hydrofluoric acid was 30% to 59%, and at a revolving speed of 10 RPMs to 1000 RPMs, an HJ-4A digital display temperature controlled magnetic stirrer produced by Changzhou Guoyu Instrument Manufacture Co., Ltd. was used to stir for 30 minutes. B: While stirring, analytical pure potassium permanganate produced by Sinopharm Group Chemical Reagent Co., Ltd. (National Pharmaceutical Code 10017308) was added, herein the mass ratio of the potassium permanganate to the potassium hydrogen fluoride was 1:5 to 2:5. C: Analytical pure hydrogen peroxide produced by Sinopharm Group Chemical Reagent Co., Ltd. (National Pharmaceutical Code 10011208) with a mass fraction of 25% to 40% was used to titrate solution after adding the potassium permanganate to be golden yellow, until the color of the solution was not changed along with dropping of the hydrogen peroxide. D: The titrated solution together with a reactor was put into ice-water mixed solution at 0° C. to 5° C. and standing was performed for 15 minutes to 40 minutes, a precipitate is filtered out, and then analytical pure acetone (National Pharmaceutical Code 10000418) produced by Sinopharm Group Chemical Reagent Co., Ltd. was used to repeatedly wash the precipitate to be neutral. E: Then, a DZF-6020 vacuum dryer produced by Shanghai Boxun Industrial Co., Ltd. was used to dry the washed precipitate under conditions of a temperature of 60° C. to 90° C. and a vacuum degree of 90 Pa to 500 Pa for 1 hour to 4 hours, to obtain K₂MnF₆.
  • 5) According to the molar ratio of K₂TiF₆ to K₂MnF₆ which was 93:7 to 90:10, the K₂TiF₆ particles after the secondary crystallization and K₂MnF₆ were weighed, and then firstly K₂MnF₆ was dissolved in the hydrofluoric acid, the mass fraction of the hydrofluoric acid was 30% to 59% and K₂TiF₆ was added to solution of K₂MnF₆ and hydrofluoric acid, and the stirring was continuously performed for 10 minutes to 360 minutes for ion exchange, herein a ratio of the total mass of K₂TiF₆ and K₂MnF₆ to the mass of the hydrofluoric acid was 1:1 to 4:1.
  • 6) Under conditions of a vacuum degree 60 Pa to 200 Pa and a flow rate 60 L/min to 100 L/min, vacuum suction filtration treatment was performed on the solution after the ion exchange, to obtain a filter cake, and then the analytical pure acetone (National Pharmaceutical Code 10000418) produced by Sinopharm Group Chemical Reagent Co., Ltd. was used to repeatedly wash the filter cake to be neutral, and then the DZF-6020 vacuum dryer produced by Shanghai Boxun Industrial Co., Ltd., under conditions of a temperature of 60° C. to 90° C. and a vacuum degree of 90 Pa to 500 Pa, was used to dry the filter cake for 1 hour to 4 hours, to obtain the manganese-doped red phosphor, namely K₂TiF₆:Mn⁴⁺.

An embodiment of the disclosure further provides a product prepared according to the above method.

An embodiment of the disclosure further provides a device packaged by a product prepared according to the above method, and FIG. 1 is a structure schematic diagram of a device packaged by manganese-doped red phosphor provided by an embodiment of the disclosure, as shown in FIG. 1, the device 100 includes: an excitation source 101, phosphor 103, an electrode 105, a packaging material 107 and a support 109, herein,

• • the electrode 105 is connected with the excitation source 101; specifically, the excitation source 101 can be an LED chip;
  • the phosphor 103 is distributed in the packaging material 107, and arranged around the excitation source 101; specifically, the packaging material 107 can be a transparent silica gel; and
  • the support 109 carries the excitation source 101, the electrode 105, and the packaging material 107.

An embodiment of the disclosure further provides a backlight module packaged by a product prepared according to the above method.

Technical schemes in the embodiments of the disclosure are clearly and completely described below, herein Table 1 is a table of process parameters used in Embodiments 1 to 9 of the disclosure; and Table 2 is a table of process parameters used in Embodiments 10 to 19 of the disclosure; as shown in Table 1 and Table 2.

TABLE 1
	Embodiment
	number	1	2	3	4	5	6	7	8	9
Step	Ball to material	1:1	1:1	1:1	1:1	1.5:1	1.5:1	1.5:1	1.5:1	2:1
1	ratio
	Ball-milling time	30	60	90	120	30	60	90	120	30
	length (min)
Step	Hydrofluoric acid	30	35	40	45	50	55	59	30	35
2	mass fraction (%)
	Mass ratio of	1:1	1:1.5	1:2	1:2.5	1:2.5	1:2	1:1.5	1:1	1:1.5
	potassium
	fluorotitanate to
	hydrofluoric acid
	Stirring speed	400	600	800	1200	800	1200	400	600	12000
	(RPM)
	Crystallization	24	36	48	60	36	24	60	48	48
	time length (h)
Step	Suction filtration	60	70	80	90	100	110	120	130	140
3	vacuum degree
	(Pa)
	Suction filtration	60	65	70	75	80	85	90	95	100
	flow rate (L/min)
Step	Mass ratio of	2:10	2.5:10	3:10	3.5:10	4:10	2:10	2.5:10	3:10	3.5:10
4	potassium
	hydrogen fluoride
	to hydrofluoric
	acid
	Hydrofluoric acid	30	35	40	45	50	55	59	30	35
	mass fraction (%)
	Stirring speed	10	20	40	60	80	100	200	300	400
	(RPM)
	Stirring time	15	17	20	22	25	27	30	15	17
	length (min)
	Mass ratio of	1:5	1.2:5	1.5:5	1.7:5	2:5	1:5	1.2:5	1.5:5	1.7:5
	potassium
	permanganate to
	potassium
	hydrogen fluoride
	Hydrogen	25	27	30	32	35	37	40	25	27
	peroxide mass
	fraction (%)
	Ice-water mixture	0	1	2	3	4	5	0	1	2
	temperature (° C.)
	Standing time	15	17	20	22	25	27	30	32	35
	length (min)
	Drying	60	65	70	75	80	85	90	60	65
	temperature (° C.)/
	Drying vacuum	90	120	150	180	200	240	280	320	360
	degree (Pa)
	Drying time length	1	1.2	1.4	1.6	1.8	2	2.2	2.4	2.6
	(h)
Step	Molar ratio of	90:10	91:9	92:8	93:7	90:10	91:9	92:8	93:7	90:10
5	potassium
	fluorotitanate to
	potassium
	fluoromanganate
	Hydrofluoric acid	30	35	40	45	50	55	59	30	35
	mass fraction (%)
	Stirring time	10	20	40	60	80	100	120	140	160
	length (min)
	Ratio of total	1:1	1.5:1	2:1	2.5:1	3:1	3.5:1	4:1	1:1	1.5:1
	mass of
	potassium
	fluorotitanate and
	potassium
	fluoromanganate
	to mass of
	hydrofluoric acid
Step6	Suction filtration	60	70	80	90	100	110	120	130	140
	vacuum degree
	(Pa)
	Suction filtration	60	65	70	75	80	85	90	95	100
	flow rate (L/min)
	Drying	60	65	70	75	80	85	90	60	65
	temperature (° C.)
	Drying vacuum	90	120	150	180	210	240	270	300	330
	degree (Pa)
	Drying time length	1	1.5	2	2.5	3	3.5	4	1	1.5
	(h)

TABLE 2
	Embodiment
	number	10	11	12	13	14	15	16	17	18	19
Step	Ball to material	2:1	2:1	2:1	2.5:1	2.5:1	2.5:1	2.5:1	2:1	2:1	2:1
1	ratio
	Ball-milling time	60	90	120	30	60	90	120	90	90	90
	length (min)
Step2	Hydrofluoric	40	45	50	55	59	30	35	40	40	40
	acid mass
	fraction (%)
	Mass ratio of	1:1	1:2.5	1:2	1:2	1:2	1:1.5	1:1.5	1:1.5	1:1.5	1:1.5
	potassium
	fluorotitanate to
	hydrofluoric
	acid
	Stirring speed	800	600	400	600	400	1200	800	400	400	400
	(RPM)
	Crystallization	60	24	36	60	48	36	24	36	48	60
	time length (h)
Step	Suction filtration	150	160	170	180	190	200	190	180	180	180
3	vacuum degree
	(Pa)
	Suction filtration	60	65	70	75	80	85	90	95	95	95
	flow rate (L/min)
Step4	Mass ratio of	4:10	2:10	2.5:10	3:10	3.5:10	4:10	2:10	2.5:10	2.5:10	2.5:10
	potassium
	permanganate
	to potassium
	hydrogen
	fluoride
	Hydrofluoric	40	45	50	55	59	30	35	40	40	40
	acid mass
	fraction (%)
	Stirring speed	500	600	700	800	900	1000	900	800	800	800
	(RPM)
	Stirring time	20	22	25	27	30	15	17	20	30	30
	length (min)
	Mass ratio of	2:5	1:5	1.2:5	1.5:5	1.7:5	2:5	1:5	1.2:5	1.2:5	1.2:5
	potassium
	permanganate
	to potassium
	hydrogen
	fluoride
	Hydrogen	30	32	35	37	40	25	27	30	30	30
	peroxide mass
	fraction (%)
	Ice-water	3	4	5	0	1	2	3	4	4	4
	mixture
	temperature
	(° C.)
	Standing time	37	40	15	17	20	22	25	27
	length (min)
	Drying	70	75	80	85	90	60	65	70	70	70
	temperature
	(° C.)
	Drying vacuum	400	420	440	480	500	90	120	150	150	150
	degree (Pa)
	Drying time	2.8	3	3.2	3.4	3.6	3.8	4	1	3	3
	length (h)
Step	Molar ratio of	91:9	92:8	93:7	90:10	91:9	92:8	93:7	90:10	92:8	92:8
5	potassium
	fluorotitanate to
	potassium
	fluoromanganate
	Hydrofluoric	40	45	50	55	59	30	35	40	40	40
	acid mass
	fraction (%)
	Stirring speed	500	600	700	800	900	1000	900	800	400	400
	(RPM)
	Stirring time	180	200	220	240	260	280	300	320	340	360
	length (min)
	Ratio of total	2:1	2.5:1	3:1	3.5:1	4:1	1:1	1.5:1	2:1	4:1	4:1
	mass of
	potassium
	fluorotitanate
	and potassium
	fluoromanganate
	to mass of
	hydrofluoric
	acid
Step	Suction filtration	150	160	170	180	190	200	190	180	180	180
6	vacuum degree
	(Pa)
	Suction filtration	60	65	70	75	80	85	90	95	95	95
	flow rate (L/min)
	Drying	70	75	80	85	90	60	65	70	70	70
	temperature
	(° C.)
	Drying vacuum	360	390	420	450	480	500	470	440	440	440
	degree (Pa)
	Drying time	2	2.5	3	3.5	4	1	1.5	4	4	4
	length (h)

Relative Light Intensity Test

An F4600 fluorescence spectrometer produced by Hitachi Manufacture Co., Ltd. is used to test the products prepared in Embodiments 1 to 19, and test results are shown in Table 3.

Table 3 is the test results of luminous intensities, color coordinates, color temperatures and color rendering indexes of the products prepared in Embodiments 1 to 19 provided by the embodiments of the disclosure, herein the relative intensity is obtained by integrating an emission spectrum within a range of 580 nm to 680 nm; and the color coordinates, correlated color temperatures, and color rendering indexes are calculated by using “CIE13_3w.exe” software.

TABLE 3
			Correlated
			color	Color
	Relative	Color	temperature	rendering
	intensity	coordinate (x, y)	(K)	index Ra
Embodiment 1	55.94242	(0.6877, 0.3121)	1000	12.03
Embodiment 2	89.87714	(0.6882, 0.3117)	1000	11.63
Embodiment 3	84.27215	(0.6880, 0.3119)	1000	11.36
Embodiment 4	50.64414	(0.6879, 0.3120)	1000	11.24
Embodiment 5	80.00677	(0.6882, 0.3116)	1000	11.64
Embodiment 6	67.25242	(0.6880, 0.3119)	1000	11.67
Embodiment 7	94.9639	(0.6884, 0.3114)	1000	11.13
Embodiment 8	57.37577	(0.6881, 0.3118)	1000	10.47
Embodiment 9	82.79778	(0.6883, 0.3115)	1000	11.36
Embodiment	100	(0.6883, 0.3116)	1000	11.15
10
Embodiment	92.70986	(0.6884, 0.3115)	1000	11.12
11
Embodiment	83.39078	(0.6883, 0.3116)	1000	10.95
12
Embodiment	74.87309	(0.6884, 0.3115)	1000	11.34
13
Embodiment	81.62602	(0.6884, 0.3115)	1000	11.19
14
Embodiment	85.48093	(0.6883, 0.3116)	1000	11.17
15
Embodiment	62.66306	(0.6886, 0.3113)	1000	11.10
16
Embodiment	82.61542	(0.6880, 0.3245)	1000	11.15
17
Embodiment	84.40983	(0.6882, 0.3546)	1000	11.19
18
Embodiment	73.06636	(0.6884, 0.1323)	1000	11.14
19

FIG. 2 is a test result of the emission intensity of products prepared in Embodiments 1 to 4 provided by an embodiment of the disclosure; FIG. 3 is a test result of the emission intensity of products prepared in Embodiments 5 to 8 provided by an embodiment of the disclosure; FIG. 4 is a test result of the emission intensity of products prepared in Embodiments 9 to 12 provided by an embodiment of the disclosure; FIG. 5 is a test result of the emission intensity of products prepared in Embodiments 13 to 16 provided by an embodiment of the disclosure; and FIG. 6 is a test result of the emission intensity of products prepared in Embodiments 17 to 19 provided by an embodiment of the disclosure.

In FIGS. 2 to 5, 1 represents the test result of the product prepared in Embodiment 1, and so on. It can be seen from FIGS. 2 to 5 that the luminous intensity of the products prepared in the embodiment of the disclosure is between 900 to 1300.

A F4600 fluorescence spectrometer produced by Hitachi Manufacture Co., Ltd. is used to perform a relative luminous intensity test according to the above dosage, and FIG. 7 is a schematic diagram of an emission spectrum of a material prepared in the embodiment of the disclosure and a contrast example provided by an embodiment of the disclosure, as shown in FIG. 7, K₂TiF₆:Mn⁴⁺ is an average value of the relative strength of the products prepared by using Embodiments 1 to 19 of the disclosure, and K₂SiF₆:Mn⁴⁺ is KSF red powder (brand name BR-3011C) produced by Mitsubishi Chemical Corporation; K₂GeF₆:Mn⁴⁺ is KGF red powder (brand name 690F-103B) produced by Advanced Material Research Co., Ltd. It is apparent that, through applying the embodiments of the disclosure, the dosage of phosphor can be reduced.

External Quantum Efficiency Comparison Test

A QY-2000-type integrating sphere fluorescence spectrometer produced by Tianjin Dongfang Kejie Technology Co., Ltd. is used to test the products prepared in Embodiments 1 to 19, the KSF (K₂SiF₆:Mn⁴⁺) red powder (brand name BR-301/C) produced by Mitsubishi Chemical Corporation, and the KGF (K₂GeF₆:Mn⁴⁺) red powder (brand name 690F-103B) produced by Grinm Advanced Materials Co., Ltd. Test results are as shown in Table 4.

Table 4 is a result comparison table of testing the products prepared in Embodiments 1 to 19, the KSF (K₂SiF₆:Mn⁴⁺) red powder (brand name BR-301/C) produced by Mitsubishi Chemical Corporation, and the KGF (K₂GeF₆:Mn⁴⁺) red powder (brand name 690F-103B) produced by Grinm Advanced Materials Co., Ltd. according to the embodiments of the disclosure.

	TABLE 4
		External	Absolute	Light
		quantum	quantum	absorption
	Sample	yield (%)	yield (%)	efficiency (%)
	Embodiment 1	69.61%	91.08%	74.24%
	Embodiment 2	69.35%	92.75%	74.69%
	Embodiment 3	69.09%	93.06%	74.24%
	Embodiment 4	69.41%	91.56%	76.58%
	Embodiment 5	69.51%	91.57%	77.34%
	Embodiment 6	69.47%	91.84%	77.34%
	Embodiment 7	69.46%	92.04%	76.53%
	Embodiment 8	69.34%	92.67%	76.84%
	Embodiment 9	69.54%	91.42%	76.28%
	Embodiment 10	69.10%	93.06%	78.68%
	Embodiment 11	69.34%	91.43%	78.24%
	Embodiment 12	69.72%	92.45%	76.58%
	Embodiment 13	69.91%	93.54%	77.34%
	Embodiment 14	69.27%	92.46%	78.54%
	Embodiment 15	69.35%	91.57%	76.35%
	Embodiment 16	69.25%	93.47%	76.82%
	Embodiment 17	69.34%	93.54%	76.24%
	Embodiment 18	69.35%	92.45%	78.24%
	Embodiment 19	69.47%	92.04%	75.28%
	Grinm	66.87%	100%	66.87%
	Advanced
	Materials Co.,
	Ltd.
	Mitsubishi	56.10%	85.57%	65.56%
	Chemical
	Corporation

It can be seen from Table 4 that the external quantum efficiency, absolute quantum efficiency and absorption rate of the products prepared in Embodiments 1 to 19 of the disclosure are all higher than the KSF red powder (brand name BR-301/C) produced by Mitsubishi Chemical Corporation and the KGF (K₂GeF₆:Me) red powder (brand name 690F-103B) produced by Grinm Advanced Materials Co., Ltd.

Phosphor Dosage Comparison Test

The products prepared in Embodiments 1 to 19, the KSF red powder (brand name BR-3011C) produced by Mitsubishi Chemical Corporation, and the KGF red powder (brand name 690F-103B) produced by Grinm Advanced Materials Co., Ltd. are used to be packaged into a white light LED device of a display backlight source, and a weight test is performed. Test results are as shown in Table 5.

Table 5 is a result comparison table of testing the products prepared in Embodiments 1 to 19, the KSF red powder (brand name BR-301/C) produced by Mitsubishi Chemical Corporation, and the KGF red powder (brand name 690F-103B) produced by Grinm Advanced Materials Co., Ltd. according to the embodiments of the disclosure.

TABLE 5
	Dosage	Theron green	Packaging
Number	(g)	powder (g)	glue (g)
Embodiment 1	0.732	0.2874	2.5
Embodiment 2	0.732	0.2874	2.5
Embodiment 3	0.732	0.2874	2.5
Embodiment 4	0.732	0.2874	2.5
Embodiment 5	0.732	0.2874	2.5
Embodiment 6	0.732	0.2874	2.5
Embodiment 7	0.732	0.2874	2.5
Embodiment 8	0.732	0.2874	2.5
Embodiment 9	0.732	0.2874	2.5
Embodiment 10	0.732	0.2874	2.5
Embodiment 11	0.732	0.2874	2.5
Embodiment 12	0.732	0.2874	2.5
Embodiment 13	0.732	0.2874	2.5
Embodiment 14	0.732	0.2874	2.5
Embodiment 15	0.732	0.2874	2.5
Embodiment 16	0.732	0.2874	2.5
Embodiment 17	0.732	0.2874	2.5
Embodiment 18	0.732	0.2874	2.5
Embodiment 19	0.732	0.2874	2.5
Grinm Advanced	0.972	0.2874	2.5
Materials Co., Ltd.
Mitsubishi	0.972	0.2874	2.5
Chemical
Corporation

It can be seen from Table 5 that the amounts of the products prepared in Embodiments 1 to 19 of the disclosure are all less than that of the KSF red powder (brand name BR-301/C) produced by Mitsubishi Chemical Corporation, and the KGF red powder (brand name 690F-103B) produced by Grinm Advanced Materials Co., Ltd.

The above are only the preferred embodiments of the disclosure, and are not intended to limit the disclosure. Any modifications, equivalent replacements and improvements and the like made within the spirit and principle of the disclosure shall be included in a scope of protection of the disclosure.

Claims

1. A preparation method for manganese-doped red phosphor, wherein the method comprises: 1) mixing A2BF6 polycrystalline particles with grinding balls, wherein a mass ratio of the A2BF6 polycrystalline particles to the grinding balls is 1:1 to 1:2.5, and then ball-milling for 30 minutes to 120 minutes, wherein A is a monovalent cation, at least one selected from the group consisting of a potassium ion, a hydrogen ion, a lithium ion, a sodium ion and a cesium ion, and B is a tetravalent cation, at least one selected from the group consisting of a titanium ion a silicon ion, a germanium ion, a tin ion, and a zirconium ion;2) secondary crystallization treatment: mixing A2BF6 powder obtained after ball-milling with a hydrofluoric acid, a mass concentration of the hydrofluoric acid is 30% to 59%, wherein a mass ratio of the A2BF6 powder obtained after ball-milling to the hydrofluoric acid is 1:1 to 2.5:1, and then at a revolving speed of 1 RPM to 1200 RPMs, stirring for 12 hours to 72 hours;3) filtering out solid particles in A2BF6 and hydrofluoric acid solution after the secondary crystallization treatment, to obtain secondary crystallization A2BF6 particles;4) according to a molar ratio of A2BF6 and A2MnF6 which is 93:7 to 90:10, weighing the secondary crystallization A2BF6 particles and A2MnF6, and then firstly dissolving A2MnF6 in a hydrofluoric acid, a mass concentration of the hydrofluoric acid is 30% to 59%, and then adding the secondary crystallization A2BF6 particles to a solution comprising the A2MnF6 and the hydrofluoric acid, and continuously stirring for 10 minutes to 360 minutes for ion exchange, wherein a ratio of a total mass of A2BF6 and A2MnF6 to a mass of the hydrofluoric acid is 1:1 to 4:1; and5) filtering out solid particles in solution after the ion exchange, to obtain a filter cake, and then drying the filter cake to obtain the manganese-doped red phosphor.

2. The preparation method for the manganese-doped red phosphor according to claim 1, wherein the secondary crystallization treatment in the step 2) is performed in a sealed reactor.

3. The preparation method for the manganese-doped red phosphor according to claim 1, wherein the step 3) comprises: under conditions of a vacuum degree of 60 Pa to 200 Pa and a flow rate of 60 L/min to 100 L/min, performing vacuum suction filtration treatment on the A2BF6 and hydrofluoric acid solution after the secondary crystallization treatment, to obtain the secondary crystallization A2BF6 particles.

4. The preparation method for the manganese-doped red phosphor according to claim 1, wherein a preparation method for A2MnF6 in the step 4) comprises: A: dissolving potassium hydrogen fluoride in a hydrofluoric acid, a mass concentration of the hydrofluoric acid is 30% to 59%, wherein a mass ratio of the potassium hydrogen fluoride to the hydrofluoric acid is 2:10 to 4:10; and at a revolving speed of 10 RPM to 1000 RPM, stirring for 15 minutes to 40 minutes;B: adding potassium permanganate while stirring, wherein a mass ratio of the potassium permanganate to the potassium hydrogen fluoride is 1:5 to 2:5;C: using a hydrogen peroxide to titrate solution after adding the potassium permanganate to be golden yellow, a mass concentration of the hydrogen peroxide is 25% to 40%;D: putting the titrated solution together with a reactor into an ice-water mixture at 0° C. to 5° C. and standing for 15 minutes to 40 minutes, filtering out a precipitate, and then using acetone to repeatedly wash the precipitate to be neutral; andE: drying the washed precipitate for 1 hour to 4 hours under conditions of a temperature of 60° C. to 90° C. and a vacuum degree of 90 Pa to 500 Pa, to obtain A2MnF6.

5. The preparation method for the manganese-doped red phosphor according to claim 1, wherein the step 5) comprises: under conditions of a vacuum degree of 60 Pa to 200 Pa and a flow rate of 60 L/min to 100 L/min, performing vacuum suction filtration treatment on the solution after ion exchange, to obtain a filter cake, and then using acetone to repeatedly wash the filter cake to be neutral, and then drying the filter cake for 1 hour to 4 hours under conditions of a temperature of 60° C. to 90° C. and a vacuum of 90 Pa to 500 Pa, to obtain the manganese-doped red phosphor.