JP2002038143A - Method for producing rare earth-activated alkaline earth metal fluorohalide-based photostimulable phosphor, rare earth-activated alkaline earth metal fluorohalide-based photostimulable phosphor and radiation image conversion panel - Google Patents

Method for producing rare earth-activated alkaline earth metal fluorohalide-based photostimulable phosphor, rare earth-activated alkaline earth metal fluorohalide-based photostimulable phosphor and radiation image conversion panel

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Publication number
JP2002038143A
JP2002038143A JP2001115073A JP2001115073A JP2002038143A JP 2002038143 A JP2002038143 A JP 2002038143A JP 2001115073 A JP2001115073 A JP 2001115073A JP 2001115073 A JP2001115073 A JP 2001115073A JP 2002038143 A JP2002038143 A JP 2002038143A
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JP
Japan
Prior art keywords
alkaline earth
rare earth
earth metal
activated alkaline
solvent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2001115073A
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Japanese (ja)
Other versions
JP4165029B2 (en
Inventor
Hideaki Wakamatsu
秀明 若松
Hiroto Ito
博人 伊藤
Hiroyuki Nabeta
博之 鍋田
Kanae Tsuchiya
香苗 土屋
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Konica Minolta Inc
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Konica Minolta Inc
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Publication of JP2002038143A publication Critical patent/JP2002038143A/en
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Abstract

PROBLEM TO BE SOLVED: To obtain a finely particulate rare earth-activated alkaline earth metal fluorohalide-based photostimulable phosphor having a uniform particle diameter distribution with a high productivity and to provide a high-sensitivity and high-image quality radiation image conversion panel using the rare earth- activated alkaline earth metal fluorohalide-based photostimulable phosphor. SOLUTION: This method for producing the rare earth-activated alkaline earth metal fluorohalide-based photostimulable phosphor is characterized by removing a solvent from a solution at >=3.3 mol/L barium concentration in a reactional mother liquor and thereby obtaining a photostimulable phosphor precursor in the method for producing the oxygen-introduced rare earth-activated alkaline earth metal fluorohalide-based photostimulable phosphor represented by general formula (I): Ba(1-x)M2(x)FBr(y)I(1-y): aM1, bLn, cO in the liquid phase.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は希土類付活アルカリ
土類金属弗化沃化物系輝尽性蛍光体、該輝尽性蛍光体の
製造方法、及び前記輝尽性蛍光体を用いた放射線画像変
換パネルに関する。
The present invention relates to a rare earth activated alkaline earth metal fluoroiodide-based stimulable phosphor, a method for producing the stimulable phosphor, and a radiation image using the stimulable phosphor. Regarding the conversion panel.

【0002】[0002]

【従来の技術】従来の放射線写真法に代わる有効な診断
手段として、特開昭55−12145号等に記載の輝尽
性蛍光体を用いる放射線画像記録再生方法が知られてい
る。この方法は、輝尽性蛍光体を含有する放射線画像変
換パネル(蓄積性蛍光体シートとも呼ばれる)を利用す
るもので、被写体を透過した、又は被検体から発せられ
た放射線を輝尽性蛍光体に吸収させ、可視光線、紫外線
などの電磁波(励起光と言う)で時系列的に輝尽性蛍光
体を励起して、蓄積されている放射線エネルギーを蛍光
(輝尽発光光と言う)として放射させ、この蛍光を光電
的に読みとって電気信号を得、得られた電気信号に基づ
いて被写体又は被検体の放射線画像を可視画像として再
生するものである。読取り後の変換パネルは、残存画像
の消去が行われ、次の撮影に供される。
2. Description of the Related Art A radiation image recording / reproducing method using a stimulable phosphor described in JP-A-55-12145 or the like is known as an effective diagnostic means which can replace the conventional radiographic method. This method utilizes a radiation image conversion panel (also referred to as a stimulable phosphor sheet) containing a stimulable phosphor, and transmits radiation transmitted through a subject or emitted from a subject to a stimulable phosphor. And stimulates the stimulable phosphor in a time series with electromagnetic waves such as visible light and ultraviolet rays (referred to as excitation light), and radiates the stored radiation energy as fluorescence (referred to as stimulating light). Then, the fluorescence is read photoelectrically to obtain an electric signal, and a radiation image of the subject or the subject is reproduced as a visible image based on the obtained electric signal. After the reading of the conversion panel, the remaining image is erased and used for the next photographing.

【0003】この方法によれば、放射線写真フィルムと
増感紙とを組み合わせて用いる放射線写真法に比して、
遙かに少ない被爆線量で情報量の豊富な放射線画像が得
られる利点がある。又、放射線写真法では撮影毎にフィ
ルムを消費するのに対して、放射線画像変換パネルは繰
り返し使用されるので、資源保護や経済効率の面からも
有利である。
According to this method, compared to a radiographic method using a combination of a radiographic film and an intensifying screen,
There is an advantage that a radiographic image with a large amount of information can be obtained with a much smaller exposure dose. Further, in the radiographic method, the film is consumed for each photographing, whereas the radiographic image conversion panel is used repeatedly, which is advantageous in terms of resource conservation and economic efficiency.

【0004】放射線画像変換パネルは、支持体とその表
面に設けられた輝尽性蛍光体層、又は自己支持性の輝尽
性蛍光体層のみから成り、輝尽性蛍光体層は通常輝尽性
蛍光体とこれを分散支持する結合材から成るものと、蒸
着法や焼結法によって形成される輝尽性蛍光体の凝集体
のみから構成されるものがある。又、該凝集体の間隙に
高分子物質が含浸されているものも知られている。更
に、輝尽性蛍光体層の支持体側とは反対側の表面には、
通常、ポリマーフィルムや無機物の蒸着膜から成る保護
膜が設けられる。
A radiation image conversion panel comprises only a support and a stimulable phosphor layer provided on the surface thereof or a self-supporting stimulable phosphor layer, and the stimulable phosphor layer is usually a stimulable phosphor layer. Some are composed of a stimulable phosphor and a binder for dispersing and supporting the stimulable phosphor, and others are composed only of aggregates of stimulable phosphor formed by a vapor deposition method or a sintering method. In addition, there is also known one in which a polymer substance is impregnated in the gaps of the aggregate. Furthermore, on the surface of the stimulable phosphor layer opposite to the support side,
Usually, a protective film composed of a polymer film or an inorganic vapor-deposited film is provided.

【0005】輝尽性蛍光体としては、通常、400〜9
00nmの範囲にある励起光によって、波長300〜5
00nmの範囲にある輝尽発光を示すものが一般的に利
用され、特開昭55−12145号、同55−1600
78号、同56−74175号、同56−116777
号、同57−23673号、同57−23675号、同
58−206678号、同59−27289号、同59
−27980号、同59−56479号、同59−56
480号等に記載の希土類元素付活アルカリ土類金属弗
化ハロゲン化物系蛍光体;特開昭59−75200号、
同60−84381号、同60−106752号、同6
0−166379号、同60−221483号、同60
−228592号、同60−228593号、同61−
23679号、同61−120882号、同61−12
0883号、同61−120885号、同61−235
486号、同61−235487号等に記載の2価のユ
ーロピウム付活アルカリ土類金属弗化ハロゲン化物系蛍
光体;特開昭55−12144号に記載の希土類元素付
活オキシハライド蛍光体;特開昭58−69281号に
記載のセリウム付活3価金属オキシハライド蛍光体;特
開昭60−70484号に記載のビスマス付活アルカリ
金属ハロゲン化物蛍光体;特開昭60−141783
号、同60−157100号等に記載の2価のユーロピ
ウム付活アルカリ土類金属ハロ燐酸塩蛍光体;特開昭6
0−157099号に記載の2価のユーロピウム付活ア
ルカリ土類金属ハロ硼酸塩蛍光体;特開昭60−217
354号に記載の2価のユーロピウム付活アルカリ土類
金属水素化ハロゲン化物蛍光体;特開昭61−2117
3号、同61−21182号等に記載のセリウム付活希
土類複合ハロゲン化物蛍光体;特開昭61−40390
号に記載のセリウム付活希土類ハロ燐酸塩蛍光体;特開
昭60−78151号に記載の2価のユーロピウム付活
ハロゲン化セリウム・ルビジウム蛍光体;特開昭60−
78151号に記載の2価のユーロピウム付活複合ハロ
ゲン化物蛍光体等が挙げられ、中でも、沃素を含有する
2価のユーロピウム付活アルカリ土類金属弗化ハロゲン
化物蛍光体、沃素を含有する希土類元素付活オキシハロ
ゲン化物蛍光体及び沃素を含有するビスマス付活アルカ
リ金属ハロゲン化物蛍光体等が知られているが、依然、
高輝度の輝尽性蛍光体が要求されている。
As the stimulable phosphor, usually 400 to 9
With excitation light in the range of 00 nm, wavelengths of 300-5
Those exhibiting stimulated emission in the range of 00 nm are generally used, and are disclosed in JP-A-55-12145 and JP-A-55-1600.
No. 78, No. 56-74175, No. 56-116777
No. 57-23673, No. 57-23675, No. 58-206678, No. 59-27289, No. 59
-27980, 59-56479, 59-56
No. 480, etc .; rare earth element-activated alkaline earth metal fluorohalide-based phosphors;
No. 60-84381, No. 60-106752, No. 6
No. 0-166379, No. 60-221483, No. 60
-228592, 60-228593, 61-
No. 23679, No. 61-120882, No. 61-12
No. 0883, No. 61-120885, No. 61-235
Nos. 486, 61-235487, etc .; divalent europium-activated alkaline earth metal fluorohalide-based phosphors; rare earth element-activated oxyhalide phosphors described in JP-A-55-12144; Cerium-activated trivalent metal oxyhalide phosphor described in JP-A-58-69281; Bismuth-activated alkali metal halide phosphor described in JP-A-60-70484;
No. 60-157100, divalent europium-activated alkaline earth metal halophosphate phosphors;
JP-A-60-217, divalent europium-activated alkaline earth metal haloborate phosphor described in JP-A-157099;
No. 354, divalent europium-activated alkaline earth metal hydride halide phosphors;
No. 3, No. 61-21182, etc .; cerium-activated rare earth composite halide phosphors;
Cerium-activated rare earth halophosphate phosphor described in JP-A-60-78151; divalent europium-activated cerium rubidium halide phosphor described in JP-A-60-78151;
No. 78151, such as divalent europium-activated composite halide phosphors described in No. 78151, among which divalent europium-activated alkaline earth metal fluoride halide phosphors containing iodine and rare earth elements containing iodine Activated oxyhalide phosphors and bismuth-activated alkali metal halide phosphors containing iodine are known, but still,
There is a demand for a high-luminance stimulable phosphor.

【0006】又、輝尽性蛍光体を利用する放射線画像変
換方法の利用が進むにつれて、得られる放射線画像の画
質の向上、例えば鮮鋭度の向上や粒状性の向上が更に求
められるようになって来た。
[0006] Further, as the use of a radiation image conversion method using a stimulable phosphor has progressed, it has been required to further improve the image quality of the obtained radiation image, for example, the sharpness and the graininess. Came.

【0007】先に記載の輝尽性蛍光体の製造方法は、固
相法あるいは焼結法と呼ばれる方法で、焼成後の粉砕が
必須であり、感度、画像性能に影響する粒子形状の制御
が困難であるという問題を有する。放射線画像の画質向
上の手段の中で、輝尽性蛍光体の微粒子化と微粒子化さ
れた輝尽性蛍光体の粒径を揃えること、即ち、粒径分布
を狭くすることは有効である。
The method for producing a stimulable phosphor described above is a method called a solid phase method or a sintering method, which requires pulverization after firing, and controls the particle shape which affects sensitivity and image performance. It has the problem of being difficult. Among the means for improving the image quality of a radiation image, it is effective to make the stimulable phosphor finer and to make the particle size of the stimulable phosphor finer, that is, to narrow the particle size distribution.

【0008】特開平7−233369号、同9−291
278号等で開示されている液相からの輝尽性蛍光体の
製造法は、蛍光体原料溶液の濃度を調整して微粒子状の
輝尽性蛍光体前駆体を得る方法であり、粒径分布の揃っ
た輝尽性蛍光体粉末の製造法として有効である。又、放
射線被爆量の低減という観点から、希土類付活アルカリ
土類金属弗化ハロゲン化物系輝尽性蛍光体の内、沃素含
有量が高いものが好ましいことが知られている。これ
は、臭素に比べて沃素がX線吸収率が高いためである。
[0008] JP-A-7-233369, 9-291
No. 278 discloses a method for producing a stimulable phosphor from a liquid phase, which is a method of adjusting the concentration of a phosphor raw material solution to obtain a particulate stimulable phosphor precursor. This is effective as a method for producing a stimulable phosphor powder having a uniform distribution. From the viewpoint of reducing the radiation exposure, it is known that among the rare earth-activated alkaline earth metal fluorohalide-based stimulable phosphors, those having a high iodine content are preferable. This is because iodine has a higher X-ray absorptivity than bromine.

【0009】上記の様に液相で製造されるアルカリ土類
金属弗化沃化物系輝尽性蛍光体は、輝度、粒状性の点で
有利であるが、液相にて前駆体結晶を得る場合、以下の
様な問題を持っている。即ち、特開平10−88125
号、同9−291278号の記載に見られるように、 1)沃化バリウムを水あるいは有機溶媒に溶解し、この
液を攪拌しながら無機弗化物の溶液を添加する、 2)弗化アンモニウムを水に溶解し、この液をを攪拌し
ながら沃化バリウムの溶液を添加する、 方法が有効である。しかし、1)の方法では、溶液中に
過剰の沃化バリウムを存在させておく必要があり、その
ため投入した沃化バリウムと固液分離後に得られる弗化
沃化バリウムの化学量論比は0.4前後と小さい値であ
ることが多い。つまり、投入した沃化バリウムに対し、
アルカリ土類金属弗化沃化物系輝尽性蛍光体の収率は4
0%程度であることが多い。
The alkaline earth metal fluoroiodide-based stimulable phosphor produced in the liquid phase as described above is advantageous in terms of brightness and granularity, but obtains a precursor crystal in the liquid phase. You have the following problems. That is, JP-A-10-88125
No. 9-291278, 1) Barium iodide is dissolved in water or an organic solvent, and an inorganic fluoride solution is added while stirring the solution. 2) Ammonium fluoride is added. A method of dissolving in water and adding a barium iodide solution while stirring the solution is effective. However, in the method 1), an excess of barium iodide needs to be present in the solution. Therefore, the stoichiometric ratio between the charged barium iodide and the barium fluoroiodide obtained after the solid-liquid separation is 0. It is often a small value of about 4. In other words, for the barium iodide
The yield of alkaline earth metal fluoroiodide stimulable phosphor is 4
It is often about 0%.

【0010】又、2)の方法でも、無機弗化物に対して
過剰の沃化バリウムを必要とし、収率が低い。このよう
に、弗化沃化バリウムの液相合成は収率が低く、生産性
が悪いという問題を有している。収率を上げるために母
液中の沃化バリウム濃度を下げると粒子の肥大化を招
き、これは画質特性上好ましくない。
The method 2) also requires an excess of barium iodide with respect to the inorganic fluoride, resulting in a low yield. Thus, the liquid phase synthesis of barium fluoroiodide has a problem that the yield is low and the productivity is poor. If the concentration of barium iodide in the mother liquor is lowered to increase the yield, the particles will be enlarged, which is not preferable in terms of image quality.

【0011】希土類付活アルカリ土類金属弗化ハロゲン
化物系輝尽性蛍光体、特にアルカリ土類金属弗化沃化物
系輝尽性蛍光体の収率を上げる試みとしては、特開平1
1−29324号に、反応母液の濃度と弗素源を添加し
た後、濃縮することにより基本組成式BaFI:xLn
(Ln:Ce、Pr、Sm、Eu、Gd、Tb、Tm及
びYbから選ばれる少なくとも1種の希土類元素、xは
0<x≦0.1の数値を表す)で示される希土類元素含
有角状弗化沃化バリウム結晶を得る方法が開示されてい
る。
An attempt to increase the yield of a rare earth activated alkaline earth metal fluorinated stimulable phosphor, particularly an alkaline earth metal fluorinated iodide stimulable phosphor, is disclosed in Japanese Unexamined Patent Publication No.
No. 1-29324, the concentration of the reaction mother liquor and the fluorine source were added, and the mixture was concentrated to obtain the basic composition formula BaFI: xLn
(Ln: at least one rare earth element selected from Ce, Pr, Sm, Eu, Gd, Tb, Tm, and Yb, and x represents a numerical value of 0 <x ≦ 0.1). A method for obtaining a barium fluoroiodide crystal is disclosed.

【0012】しかし、本発明者らが追試を行った結果、
記載通りBaFI角状結晶は生成したものの、自然蒸発
による濃縮を用いるため著しく生産性が低く、工業的に
は現実的ではないことが判った。又、得られる角状結晶
も粒径が大きく、かつ粒径分布が広いため画像特性が悪
く、実用に供することが出来ないことが判った。
However, as a result of the present inventors' additional tests,
Although BaFI prismatic crystals were formed as described, it was found that the productivity was extremely low due to concentration by spontaneous evaporation, which was not industrially practical. Further, it was found that the obtained square crystals also had a large particle size and a wide particle size distribution, so that the image characteristics were poor and they could not be put to practical use.

【0013】[0013]

【発明が解決しようとする課題】本発明の課題は、ま
ず、粒径分布の揃った希土類付活アルカリ土類金属弗化
ハロゲン化物系輝尽性蛍光体を生産性良く得ることであ
り、更に微粒子化され粒径分布の揃った希土類付活アル
カリ土類金属弗化ハロゲン化物系輝尽性蛍光体を高い生
産性で得ることであり、前記希土類付活アルカリ土類金
属弗化ハロゲン化物系輝尽性蛍光体を用いた高感度・高
画質の放射線画像変換パネルを提供することである。
An object of the present invention is to obtain a rare earth activated alkaline earth metal fluorinated halide stimulable phosphor having a uniform particle size distribution with high productivity. It is an object of the present invention to obtain a rare earth activated alkaline earth metal fluorohalide-based stimulable phosphor having a fine particle size and uniform particle size distribution with high productivity. An object of the present invention is to provide a high-sensitivity, high-quality radiation image conversion panel using a stimulable phosphor.

【0014】[0014]

【課題を解決するための手段】上記本発明の課題は、下
記一般式(I)で示される酸素導入希土類付活アルカリ
土類金属弗化ハロゲン化物系輝尽性蛍光体の液相での製
造方法において、反応母液中のバリウム濃度が3.3m
ol/L以上の溶液から溶媒を除去することにより輝尽
性蛍光体前駆体を得る、希土類付活アルカリ土類金属弗
化ハロゲン化物系輝尽性蛍光体の製造方法によって達成
される。
SUMMARY OF THE INVENTION The object of the present invention is to produce an oxygen-introduced rare earth activated alkaline earth metal fluoride halide stimulable phosphor represented by the following general formula (I) in the liquid phase. In the method, the barium concentration in the reaction mother liquor is 3.3 m.
This is achieved by a method for producing a rare earth-activated alkaline earth metal fluorohalide-based stimulable phosphor, in which a stimulable phosphor precursor is obtained by removing a solvent from a solution of ol / L or more.

【0015】一般式(I) Ba(1-x)2(x)FBr(y)(1-y):aM1,bLn,c
O 式中、M1はLi,Na,K,Rb及びCsから選ばれ
る少なくとも1種のアルカリ金属、M2はBe,Mg,
Sr及びCaから選ばれる少なくとも1種のアルカリ土
類金属、LnはCe,Pr,Sm,Eu,Gd,Tb,
Tm,Dy,Ho,Nd,Er及びYbから選ばれる少
なくとも1種の希土類元素を表し、x,y,a,b及び
cは、それぞれ0≦x≦0.3,0≦y≦0.3,0≦
a≦0.05,0<b≦0.2,0≦c≦0.1であ
る。
[0015] Formula (I) Ba (1-x ) M 2 (x) FBr (y) I (1-y): aM 1, bLn, c
In the formula, M 1 is at least one alkali metal selected from Li, Na, K, Rb and Cs, and M 2 is Be, Mg,
At least one alkaline earth metal selected from Sr and Ca, Ln is Ce, Pr, Sm, Eu, Gd, Tb,
Represents at least one rare earth element selected from Tm, Dy, Ho, Nd, Er and Yb, and x, y, a, b and c represent 0 ≦ x ≦ 0.3 and 0 ≦ y ≦ 0.3, respectively. , 0 ≦
a ≦ 0.05, 0 <b ≦ 0.2, and 0 ≦ c ≦ 0.1.

【0016】尚、上記溶媒の除去後の質量が除去前の質
量に対して0.97以下であることが好ましい。反応溶
媒を除去する方法は、自然乾燥に加えて、除去するため
に反応液を加熱して行う方法、また、これに他の溶媒を
除去する手段を併用することが好ましく、反応溶媒を除
去するために反応容器内を減圧に保つ過程を経ること及
び/又は乾燥気体を通気させる方法及び/又は溶媒除去
の作業中に溶液が濡れ壁を形成すること等が好ましい。
反応母液に予めアルカリ金属のハロゲン塩が0.1〜4
mol/Lの濃度で含有されていることは好ましい。
It is preferable that the mass after the removal of the solvent is 0.97 or less with respect to the mass before the removal. The method of removing the reaction solvent is, in addition to natural drying, a method in which the reaction solution is heated for removal, and it is preferable to use a means for removing another solvent in combination with the method. For this purpose, it is preferable to pass through a process of keeping the inside of the reaction vessel under reduced pressure, and / or a method of passing dry gas and / or forming a wet wall of the solution during the operation of removing the solvent.
The reaction mother liquor is preliminarily containing 0.1 to 4 alkali metal halides.
It is preferable that it is contained at a concentration of mol / L.

【0017】上記の製造方法によって得られた希土類付
活アルカリ土類金属弗化ハロゲン化物系輝尽性蛍光体、
並びに該希土類付活アルカリ土類金属弗化ハロゲン化物
系輝尽性蛍光体を含む蛍光体層を有する放射線画像変換
パネルも、本発明の課題を達成する。
A rare earth-activated alkaline earth metal fluorohalide-based stimulable phosphor obtained by the above method,
A radiation image conversion panel having a phosphor layer containing the rare earth-activated alkaline earth metal fluorohalide-based stimulable phosphor also achieves the object of the present invention.

【0018】[0018]

【発明の実施の形態】本発明の希土類付活アルカリ土類
金属弗化ハロゲン化物系輝尽性蛍光体の製造方法の代表
的な態様を以下に詳しく説明する。
BEST MODE FOR CARRYING OUT THE INVENTION A typical embodiment of the method for producing a rare earth activated alkaline earth metal fluorohalide-based stimulable phosphor of the present invention will be described in detail below.

【0019】液相法による輝尽性蛍光体前駆体製造につ
いては、特開平10−140148号に記載された前駆
体製造方法、特開平10−147778号に記載された
前駆体製造装置が好ましく利用できる。ここで輝尽性蛍
光体前駆体とは、前記一般式(I)の物質が400℃以
上の高温を経ていない状態を示し、輝尽性蛍光体前駆体
は、輝尽発光性や瞬時発光性を殆ど示さない。本発明で
は、液相で一般式(I)で示される輝尽性蛍光体の前駆
体を合成する方法において、該液相は少なくともバリウ
ム成分及び無機フッ化物が存在していることが好まし
く、溶媒の除去の開始時期が該液相中に少なくともバリ
ウム成分と無機フッ化物成分を存在させた直後から行う
ことが好ましい。バリウム成分と無機フッ化物の反応母
液中への添加の順序は特に限定されないが、無機フッ化
物の添加が最後であることが好ましい。また、一般式
(I)で示される輝尽性蛍光体を構成する他の成分の原
材料の投入順序は限定がなく、液相中に添加しても良い
し、焼成時に添加しても良い。
For the production of the stimulable phosphor precursor by the liquid phase method, the precursor production method described in JP-A-10-140148 and the precursor production apparatus described in JP-A-10-147778 are preferably used. it can. Here, the stimulable phosphor precursor refers to a state in which the substance of the general formula (I) has not passed through a high temperature of 400 ° C. or higher, and the stimulable phosphor precursor has a stimulable luminescent property or an instantaneous luminescent property. Is hardly shown. In the present invention, in the method for synthesizing the precursor of the stimulable phosphor represented by the general formula (I) in a liquid phase, it is preferable that the liquid phase contains at least a barium component and an inorganic fluoride. It is preferable to start the removal immediately after at least the barium component and the inorganic fluoride component are present in the liquid phase. The order of adding the barium component and the inorganic fluoride to the reaction mother liquor is not particularly limited, but the addition of the inorganic fluoride is preferably the last. Further, there is no limitation on the order in which the raw materials of the other components constituting the stimulable phosphor represented by the general formula (I) are added, and they may be added in the liquid phase or may be added during firing.

【0020】本発明では以下の液相合成法により前駆体
を得ることが好ましい。前記一般式(I)で示される希
土類付活アルカリ土類金属弗化沃化物系輝尽性蛍光体の
製造は、粒子形状の制御が難しい固相法ではなく、粒径
の制御が容易である液相法により行うことが好ましい。
特に、下記の液相合成法により輝尽性蛍光体を得ること
が好ましい。
In the present invention, it is preferable to obtain a precursor by the following liquid phase synthesis method. The production of the rare earth-activated alkaline earth metal fluoroiodide-based stimulable phosphor represented by the general formula (I) is not a solid phase method in which control of the particle shape is difficult, but the particle size can be easily controlled. It is preferable to carry out by a liquid phase method.
In particular, it is preferable to obtain a stimulable phosphor by the following liquid phase synthesis method.

【0021】(製造法)BaI2とLnのハロゲン化物
を含み、前記一般式(I)のxが0でない場合には、更
にM2のハロゲン化物を、yが0でない場合はBaBr2
を、そしてaが0でない場合、M1のハロゲン化物を含
み、それらが溶解した後、バリウム濃度が3.3mol
/L以上、好ましくは3.5mol/L以上で、上限と
して好ましくは5.0mol/L以下の溶液を調製する
工程;上記溶液を50℃以上、好ましくは100℃以上
の温度に維持しながら、これに濃度5mol/L以上、
好ましくは8mol/L以上、更に好ましくは12mo
l/L以上、上限として好ましくは15mol/L以下
の無機弗化物(弗化アンモニウム又はアルカリ金属の弗
化物)の溶液を添加して、希土類付活アルカリ土類金属
弗化沃化物系輝尽性蛍光体前駆体結晶の沈澱物を得る工
程;上記無機弗化物を添加しつつ、又は添加終了後、反
応液から溶媒を除去する工程;上記前駆体結晶沈澱物を
反応液から分離する工程;そして、分離した前駆体結晶
沈澱物を焼結を避けながら焼成する工程を含む製造方法
である。
[0021] includes (Process) BaI 2 and Ln halide, wherein when x in the general formula (I) is not 0, further halide of M 2, if y is not 0 BaBr 2
And, if a is not 0, contains the halides of M 1 and after their dissolution, the barium concentration is 3.3 mol
/ L or higher, preferably 3.5 mol / L or higher, and preferably 5.0 mol / L or lower as an upper limit; while maintaining the solution at a temperature of 50 ° C or higher, preferably 100 ° C or higher, In addition to this, a concentration of 5 mol / L or more,
Preferably 8 mol / L or more, more preferably 12 mol / L
A solution of an inorganic fluoride (ammonium fluoride or a fluoride of an alkali metal) of not less than 1 / L and preferably not more than 15 mol / L as an upper limit is added, and the rare earth activated alkaline earth metal fluorinated iodide is stimulated. A step of obtaining a precipitate of phosphor precursor crystals; a step of removing a solvent from the reaction solution while adding the inorganic fluoride or after the addition is completed; a step of separating the precursor crystal precipitates from the reaction solution; And baking the separated precursor crystal precipitate while avoiding sintering.

【0022】尚、本発明に係る粒子(前駆体結晶)は、
平均粒径が1〜10μmで、かつ単分散性のものが好ま
しく、平均粒径が1〜5μm、平均粒径の分布(%)が
20%以下のものがより好ましく、特に平均粒径が1〜
3μm、平均粒径の分布が15%以下のものが良い。
The particles (precursor crystals) according to the present invention are:
Those having an average particle diameter of 1 to 10 μm and monodispersity are preferable, those having an average particle diameter of 1 to 5 μm, and a distribution (%) of the average particle diameter of 20% or less are more preferable, and in particular, having an average particle diameter of 1 ~
Those having a size of 3 μm and an average particle size distribution of 15% or less are preferred.

【0023】本発明における平均粒径とは、粒子(結
晶)の電子顕微鏡写真より無作為に粒子200個を選
び、球換算の体積粒子径で平均を求めたものである。
In the present invention, the average particle diameter is obtained by randomly selecting 200 particles from an electron micrograph of particles (crystals) and calculating the average in terms of sphere-equivalent volume particle diameter.

【0024】以下に輝尽性蛍光体の製造法の詳細につい
て説明する。
The details of the method for producing the stimulable phosphor will be described below.

【0025】(前駆体結晶の沈澱物の作製、輝尽性蛍光
体の作製)最初に、水系媒体中を用いて弗素化合物以外
の原料化合物を溶解させる。即ち、BaI2とLnのハ
ロゲン化物、そして必要により更にM2のハロゲン化
物、そして更にM1のハロゲン化物を水系媒体中に入
れ、充分に混合し、溶解させて、それらが溶解した水溶
液を調製する。ただし、BaI2濃度が3.3mol/
L以上、好ましくは3.5mol/L以上となるよう
に、BaI2濃度と水系溶媒との量比を調整しておく。
この時、バリウム濃度が低いと、所望の組成の前駆体が
得られないか、得られても粒子が肥大化する。よって、
バリウム濃度は適切に選択する必要があり、本発明者ら
の検討の結果、3.3mol/L以上で微細な前駆体粒
子を形成することができることが判った。この時、所望
により少量の酸、アンモニア、アルコール、水溶性高分
子ポリマー、水不溶性金属酸化物微粒子粉体などを添加
してもよい。BaI2の溶解度が著しく低下しない範囲
で低級アルコール(メタノール、エタノール等)を適当
量添加しておくのも好ましい態様である。この水溶液
(反応母液)は50℃に、好ましくは80℃以上に、上
限として好ましくは100℃以下に維持される。
(Preparation of Precipitate Crystal Precipitate, Preparation of Stimulable Phosphor) First, a raw material compound other than a fluorine compound is dissolved in an aqueous medium. That is, a halide of BaI 2 and Ln, and if necessary, a halide of M 2 , and further a halide of M 1 are placed in an aqueous medium, thoroughly mixed and dissolved to prepare an aqueous solution in which they are dissolved. I do. However, the BaI 2 concentration was 3.3 mol /
The ratio of the BaI 2 concentration to the aqueous solvent is adjusted so as to be at least L, preferably at least 3.5 mol / L.
At this time, if the barium concentration is low, a precursor having a desired composition cannot be obtained, or even if obtained, the particles are enlarged. Therefore,
It is necessary to appropriately select the barium concentration, and as a result of studies by the present inventors, it has been found that fine precursor particles can be formed at 3.3 mol / L or more. At this time, a small amount of acid, ammonia, alcohol, a water-soluble polymer, a water-insoluble metal oxide fine particle powder or the like may be added as required. It is also a preferred embodiment to add an appropriate amount of a lower alcohol (methanol, ethanol, etc.) as long as the solubility of BaI 2 is not significantly reduced. This aqueous solution (reaction mother liquor) is maintained at 50 ° C., preferably at 80 ° C. or higher, and preferably at 100 ° C. or lower as an upper limit.

【0026】次に、この50℃以上に維持されて、無機
フッ化物水溶液を添加し反応させるが、反応させている
ときの反応液の温度は50℃以上、さらには80℃以上
に保たれていることが好ましい。添加は、撹拌されてい
る水溶液に、無機弗化物(弗化アンモニウム、アルカリ
金属の弗化物など)の水溶液をポンプ付きのパイプ等を
用いて注入する。この注入は、撹拌が特に激しく実施さ
れている領域部分に行うのが好ましい。この無機弗化物
水溶液の反応母液への注入によって、前記一般式(I)
に該当する希土類付活アルカリ土類金属弗化ハロゲン化
物系蛍光体前駆体結晶が沈澱する。
Next, while maintaining the temperature at 50 ° C. or higher, an aqueous solution of inorganic fluoride is added and reacted, the temperature of the reaction solution during the reaction is maintained at 50 ° C. or higher, and more preferably at 80 ° C. or higher. Is preferred. For the addition, an aqueous solution of an inorganic fluoride (ammonium fluoride, alkali metal fluoride, or the like) is injected into the stirred aqueous solution using a pipe with a pump or the like. This injection is preferably carried out in the region where the stirring is particularly violent. By injecting the aqueous solution of inorganic fluoride into the reaction mother liquor, the above-mentioned general formula (I)
Rare earth activated alkaline earth metal fluorohalide-based phosphor precursor crystals corresponding to the above are precipitated.

【0027】次に反応液から溶媒を除去する。本発明の
反応母液から溶媒を除去するとは、自然乾燥で溶媒を蒸
発させるプロセスに加えて、自然乾燥による蒸発速度を
超える速度で溶媒を除去するプロセスを人為的に付与す
ることにより溶媒を除去することを指す。溶媒を除去す
る時期は特に問わないが、無機フッ化物溶液の添加開始
直後から沈殿物(前駆体)を分離するまでの間に行うこ
とが好ましい。ここで添加開始直後とは、添加中及び添
加終了のいずれをも意味する。
Next, the solvent is removed from the reaction solution. To remove the solvent from the reaction mother liquor of the present invention means, in addition to the process of evaporating the solvent by natural drying, removing the solvent by artificially applying a process of removing the solvent at a rate exceeding the evaporation rate by natural drying. Refers to The timing of removing the solvent is not particularly limited, but it is preferably performed immediately after the start of the addition of the inorganic fluoride solution until the precipitate (precursor) is separated. Here, “immediately after the start of the addition” means both during the addition and at the end of the addition.

【0028】溶媒除去は、1回又は複数回に分けて行っ
ても良いし、連続的に行っても良い。例えば、1)無機
フッ化物溶液の添加終了後、溶媒除去を行い、反応母液
を放置する、2)無機フッ化物溶液の添加終了後、第1
回目の溶媒除去を行い、反応母液を放置後、第2回目の
溶媒除去を行い、再び反応母液を放置する、3)無機フ
ッ化物溶液添加終了後、沈殿物を分離するまでの間、連
続的に溶媒除去を行う、などの工程をおこなっても良
い。
The removal of the solvent may be performed once or in a plurality of times, or may be performed continuously. For example, 1) after the addition of the inorganic fluoride solution is completed, the solvent is removed, and the reaction mother liquor is allowed to stand.
After the second solvent removal, the reaction mother liquor is allowed to stand, the second solvent removal is performed, and the reaction mother liquor is left again. 3) After the addition of the inorganic fluoride solution, continuous until the precipitate is separated. , Etc. may be performed.

【0029】溶媒除去の時期は、無機フッ化物溶液の添
加終了後から除去を行うことが好ましく、該有機溶液添
加終了後直ちに除去を開始することが更に好ましい。
It is preferable to remove the solvent after the completion of the addition of the inorganic fluoride solution, and it is more preferable to start the removal immediately after the completion of the addition of the organic solution.

【0030】ここで、本発明に係る溶媒とは、当業者で
認知されている定義と同義であり、溶質を溶かすために
用いた成分である。例えば、本発明では溶質は少なくと
も一般式(I)で表される輝尽性蛍光体を得るために用
いられた原材料や中間体、触媒などが基本的に該当す
る。本発明の溶媒除去工程は、単一の溶媒を除去するだ
けでなく、複数の種類の溶媒が母液に含まれる場合は、
それら全てが溶媒除去の対象となるが、除去の対象は限
定されない。
Here, the solvent according to the present invention has the same definition as that recognized by those skilled in the art, and is a component used for dissolving a solute. For example, in the present invention, the solute basically corresponds to at least a raw material, an intermediate, a catalyst, and the like used for obtaining the stimulable phosphor represented by the general formula (I). The solvent removal step of the present invention not only removes a single solvent, but also when a plurality of types of solvents are contained in the mother liquor,
All of them are targets for solvent removal, but the targets for removal are not limited.

【0031】溶媒の除去量は、除去前と除去後の質量比
で3%以上が好ましい。これ以下では結晶が好ましい組
成に成りきらない場合がある。そのため除去量は3%以
上が好ましく、5%以上がより好ましい。又、除去し過
ぎても、反応溶液の粘度が過剰に上昇するなど、ハンド
リングの面で不都合が生じる場合がある。そのため、溶
媒の除去量は、除去前と除去後の質量比で50%以下が
好ましく、30%以下がより好ましく、更には20%以
下がより好ましい。ここで、溶媒除去後とは、全ての溶
媒除去工程を終えた後を指す。
The amount of solvent removed is preferably 3% or more by mass ratio before and after removal. Below this, the crystal may not have a desirable composition. Therefore, the removal amount is preferably 3% or more, more preferably 5% or more. In addition, even if it is removed too much, there may be a problem in handling, such as an excessive increase in the viscosity of the reaction solution. Therefore, the removal amount of the solvent is preferably 50% or less, more preferably 30% or less, and even more preferably 20% or less in terms of mass ratio before and after the removal. Here, “after removing the solvent” refers to after finishing all the solvent removing steps.

【0032】溶媒の除去に要する時間は、生産性に大き
く影響するばかりでなく、粒子の形状、粒径分布も溶媒
の除去方法に影響されるので、除去方法は適切に選択す
る必要がある。溶媒の除去は単位面積当たり2.0Kg
/m2・hr以上20.0Kg/m2・hr以下の速度で
行うことが好ましく、更には3.0Kg/m2・hr以
上10.0Kg/m2・hr以下の速度がより好まし
い。ここで、単位面積とは、反応母液の大気とが接触し
ている面積を指す。一般的に、溶媒の除去に際しては、
溶液を加熱し、溶媒を蒸発する方法が選択される。本発
明においても、この方法は有用である。溶媒の除去によ
り、意図した組成の前駆体を得ることができる。ここ
で、溶液を加熱しとは、溶媒除去工程の反応母液温度を
溶媒除去工程時にも維持する又はそれ以上の温度に上げ
る事を指す。反応母液を50℃以上、80℃以上に保つ
ように加熱することが好ましい。
The time required for removing the solvent not only greatly affects the productivity, but also the shape and particle size distribution of the particles are affected by the method for removing the solvent. Therefore, it is necessary to appropriately select a removing method. 2.0 kg of solvent removal per unit area
/ M is preferably carried out at 2 · hr or more 20.0 kg / m 2 · hr or less speed, even 3.0 Kg / m 2 · hr or more 10.0 kg / m 2 · hr or less speed is more preferable. Here, the unit area refers to the area of the reaction mother liquor in contact with the atmosphere. Generally, when removing the solvent,
The method of heating the solution and evaporating the solvent is selected. This method is also useful in the present invention. By removing the solvent, a precursor having an intended composition can be obtained. Here, "heating the solution" means to maintain or raise the temperature of the reaction mother liquor in the solvent removing step even during the solvent removing step. It is preferable to heat the reaction mother liquor so as to keep it at 50 ° C. or higher and 80 ° C. or higher.

【0033】更に、生産性を上げるため、又、粒子形状
を適切に保つため、他の溶媒除去方法を併用することが
好ましい。併用する溶媒の除去方法は特に問わない。本
発明では生産性の面から、以下の除去方法を選択するこ
とが好ましい。
Further, in order to increase the productivity and maintain the particle shape appropriately, it is preferable to use another solvent removing method in combination. The method for removing the solvent used in combination is not particularly limited. In the present invention, it is preferable to select the following removal method from the viewpoint of productivity.

【0034】1.乾燥気体を通気 反応容器を密閉型とし、少なくとも2箇所以上の気体が
通過できる孔を設け、そこから乾燥気体を通気する。気
体の種類は任意に選ぶことができる。安全性の面から、
空気、窒素が好ましい。通気する気体の飽和水蒸気量に
依存して溶媒が気体に同伴、除去される。反応容器の空
隙部分に通気する方法の他、液相中に気体を気泡として
噴出させ、気泡中に溶媒を吸収させる方法も、又、有効
である。
1. Ventilation of dry gas The reaction vessel is made to be a closed type, provided with holes through which at least two or more gases can pass, and the dry gas is ventilated therefrom. The type of gas can be arbitrarily selected. In terms of safety,
Air and nitrogen are preferred. The solvent is entrained and removed from the gas depending on the saturated water vapor amount of the gas to be passed. In addition to the method of ventilating the void portion of the reaction vessel, a method of ejecting gas as bubbles into the liquid phase and absorbing the solvent into the bubbles is also effective.

【0035】2.減圧 よく知られるように、減圧にすることで溶媒の蒸気圧は
低下する。蒸気圧降下により効率的に溶媒を除去するこ
とができる。減圧度としては溶媒の種類により適宜選択
することができる。溶媒が水の場合、86,450Pa
以下が好ましい。
2. Depressurization As is well known, reducing the pressure reduces the vapor pressure of the solvent. The solvent can be efficiently removed by the vapor pressure drop. The degree of reduced pressure can be appropriately selected depending on the type of the solvent. 86,450 Pa when the solvent is water
The following is preferred.

【0036】3.液膜 蒸発面積を拡大することにより溶媒の除去を効率的に行
うことができる。本発明のように、一定容積の反応容器
を用いて加熱、攪拌し、反応を行わせる場合、加熱方法
としては、加熱手段を液体中に浸漬するか、容器の外側
に加熱手段を装着する方法が一般的である。該方法によ
ると、伝熱面積は液体と加熱手段が接触する部分に限定
され、溶媒除去に伴い伝熱面積が減少し、よって、溶媒
除去に要する時間が長くなる。これを防ぐため、ポンプ
又は攪拌機を用いて反応容器の壁面に散布し、伝熱面積
を増大させる方法が有効である。
3. The solvent can be removed efficiently by enlarging the liquid film evaporation area. As in the present invention, when heating and stirring using a reaction vessel having a fixed volume to carry out the reaction, the heating method is a method of immersing the heating means in a liquid or attaching the heating means to the outside of the vessel. Is common. According to this method, the heat transfer area is limited to a portion where the liquid and the heating means come into contact, and the heat transfer area decreases with the removal of the solvent, and thus the time required for the solvent removal becomes longer. In order to prevent this, it is effective to use a pump or a stirrer to spray the solution on the wall surface of the reaction vessel to increase the heat transfer area.

【0037】このように反応容器壁面に液体を散布し、
液膜を形成する方法は“濡れ壁”として知られている。
濡れ壁の形成方法としては、ポンプを用いる方法の他、
特開平6−335627号、同11−235522号に
記載の攪拌機を用いる方法が挙げられる。
Thus, the liquid is sprayed on the wall surface of the reaction vessel,
The method of forming a liquid film is known as "wet wall".
As a method of forming a wet wall, in addition to a method using a pump,
Examples thereof include a method using a stirrer described in JP-A-6-335627 and JP-A-11-235522.

【0038】これらの方法は単独のみならず、組み合わ
せて用いても構わない。液膜を形成する方法と容器内を
減圧にする方法の組合せ、液膜を形成する方法と乾燥気
体を通気する方法の組合せ等が有効である。特に前者が
好ましく、特開平6−335627号に記載の方法が好
ましく用いられる。
These methods may be used alone or in combination. A combination of a method of forming a liquid film and a method of reducing the pressure in the container, a combination of a method of forming a liquid film and a method of aerating a dry gas, and the like are effective. The former is particularly preferred, and the method described in JP-A-6-335627 is preferably used.

【0039】次に、上記の蛍光体前駆体結晶を、濾過、
遠心分離などにより溶液から分離し、メタノール等で充
分に洗浄し、乾燥する。この乾燥蛍光体前駆体結晶に、
アルミナ微粉末、シリカ微粉末などの焼結防止剤を添
加、混合し、結晶表面に焼結防止剤微粉末を均一に付着
させる。尚、焼成条件を選ぶことにより焼結防止剤の添
加を省略することも可能である。
Next, the above phosphor precursor crystals are filtered,
Separate from the solution by centrifugation or the like, sufficiently wash with methanol or the like, and dry. In this dried phosphor precursor crystal,
A sintering inhibitor such as alumina fine powder and silica fine powder is added and mixed to uniformly adhere the sintering inhibitor fine powder to the crystal surface. Note that the addition of the sintering inhibitor can be omitted by selecting the firing conditions.

【0040】次に、蛍光体前駆体の結晶を、石英ポー
ト、アルミナ坩堝、石英坩堝などの耐熱性容器に充填
し、電気炉の炉心に入れて焼結を避けながら焼成を行
う。焼成温度は400〜1,300℃の範囲が適当であ
り、500〜1,000℃の範囲が好ましい。焼成時間
は、蛍光体原料混合物の充填量、焼成温度及び炉からの
取出し温度などによっても異なるが、一般には0.5〜
12時間が適当である。
Next, the crystal of the phosphor precursor is filled in a heat-resistant container such as a quartz port, an alumina crucible, or a quartz crucible, and placed in a furnace of an electric furnace to perform sintering while avoiding sintering. The firing temperature is suitably in the range of 400 to 1,300 ° C, and preferably in the range of 500 to 1,000 ° C. The firing time varies depending on the filling amount of the phosphor raw material mixture, the firing temperature, the temperature of taking out from the furnace, and the like.
12 hours is appropriate.

【0041】焼成雰囲気としては、窒素ガス雰囲気、ア
ルゴンガス雰囲気等の中性雰囲気、あるいは少量の水素
ガスを含有する窒素ガス雰囲気、一酸化炭素を含有する
二酸化炭素雰囲気などの弱還元性雰囲気、あるいは微量
酸素導入雰囲気が利用される。焼成方法については、特
開2000−8034号に記載の方法が好ましく用いら
れる。
The firing atmosphere may be a neutral atmosphere such as a nitrogen gas atmosphere, an argon gas atmosphere, a weakly reducing atmosphere such as a nitrogen gas atmosphere containing a small amount of hydrogen gas, a carbon dioxide atmosphere containing carbon monoxide, or the like. A trace oxygen introduction atmosphere is used. As the firing method, a method described in JP-A-2000-8034 is preferably used.

【0042】上記の焼成によって目的の希土類付活アル
カリ土類金属弗化ハロゲン化物系輝尽性蛍光体が得られ
る。
By the above calcination, the desired rare earth-activated alkaline earth metal fluorohalide-based stimulable phosphor is obtained.

【0043】(放射線画像変換パネルの作製)本発明の
放射線画像変換パネルに用いられる支持体としては、各
種高分子材料、ガラス、金属等が用いられる。特に情報
記録材料としての取扱い上、可撓性のあるシート又はウ
ェブに加工できるものが好適であり、この点から言えば
セルロースアセテート、ポリエステル、ポリエチレンテ
レフタレート、ポリアミド、ポリイミド、トリアセテー
ト、ポリカーボネートフィルム等のプラスチックフィル
ム;アルミニウム、鉄、銅、クロム等の金属シート又は
該金属酸化物の被覆層を有する金属シート等が好まし
い。
(Preparation of Radiation Image Conversion Panel) As the support used in the radiation image conversion panel of the present invention, various polymer materials, glass, metal and the like are used. Particularly, in terms of handling as an information recording material, a material that can be processed into a flexible sheet or web is preferable. In this regard, plastics such as cellulose acetate, polyester, polyethylene terephthalate, polyamide, polyimide, triacetate, and polycarbonate film are preferable. Film; a metal sheet of aluminum, iron, copper, chromium, or the like, or a metal sheet having a coating layer of the metal oxide is preferable.

【0044】これら支持体の層厚は、用いる支持体の材
質等によって異なるが、一般的には10〜1000μm
であり、取扱い上の点から、更に好ましくは10〜50
0μmである。
The layer thickness of the support varies depending on the material of the support to be used and the like.
From the viewpoint of handling, more preferably 10 to 50
0 μm.

【0045】これら支持体の表面は滑面であってもよい
し、輝尽性蛍光体層との接着性を向上させる目的でマッ
ト面としてもよい。更に、輝尽性蛍光体層との接着性を
向上させる目的で、輝尽性蛍光体層が設けられる面に下
引層を設けてもよい。
The surface of the support may be a smooth surface or a mat surface for the purpose of improving the adhesion to the stimulable phosphor layer. Furthermore, an undercoat layer may be provided on the surface on which the stimulable phosphor layer is provided, for the purpose of improving the adhesiveness with the stimulable phosphor layer.

【0046】輝尽性蛍光体層に用いられる結合剤の例と
しては、ゼラチン等の蛋白質、デキストラン等のポリサ
ッカライド、又はアラビアゴムのような天然高分子物
質;ポリビニルブチラール、ポリ酢酸ビニル、ニトロセ
ルロース、エチルセルロース、塩化ビニリデン・塩化ビ
ニルコポリマー、ポリアルキル(メタ)アクリレート、
塩化ビニル・酢酸ビニルコポリマー、ポリウレタン、セ
ルロースアセテートブチレート、ポリビニルアルコー
ル、線状ポリエステル等のような合成高分子物質などに
より代表される結合剤を挙げることができる。これらの
中で特に好ましいものは、ニトロセルロース、線状ポリ
エステル、ポリアルキル(メタ)アクリレート、ニトロ
セルロースと線状ポリエステルとの混合物、ニトロセル
ロースとポリアルキル(メタ)アクリレートとの混合物
及びポリウレタンとポリビニルブチラールとの混合物で
ある。尚、これらの結合剤は、架橋剤によって架橋され
たものでもよい。
Examples of the binder used in the stimulable phosphor layer include proteins such as gelatin, polysaccharides such as dextran, and natural high molecular substances such as gum arabic; polyvinyl butyral, polyvinyl acetate, nitrocellulose , Ethylcellulose, vinylidene chloride-vinyl chloride copolymer, polyalkyl (meth) acrylate,
Examples of the binder include synthetic polymer substances such as vinyl chloride / vinyl acetate copolymer, polyurethane, cellulose acetate butyrate, polyvinyl alcohol, and linear polyester. Particularly preferred among these are nitrocellulose, linear polyester, polyalkyl (meth) acrylate, a mixture of nitrocellulose and linear polyester, a mixture of nitrocellulose and polyalkyl (meth) acrylate, and polyurethane and polyvinyl butyral. Is a mixture with In addition, these binders may be crosslinked with a crosslinking agent.

【0047】輝尽性蛍光体層は、例えば次のような方法
により下塗層上に形成することができる。
The stimulable phosphor layer can be formed on the undercoat layer by the following method, for example.

【0048】まず、沃素含有輝尽性蛍光体、黄変防止の
ための亜燐酸エステル等の化合物及び結合剤を適当な溶
剤に添加し、これらを充分に混合して結合剤溶液中に蛍
光体粒子及び該化合物の粒子が均一に分散した塗布液を
調製する。
First, an iodine-containing stimulable phosphor, a compound such as a phosphite for preventing yellowing, and a binder are added to an appropriate solvent, and these are mixed well and the phosphor is added to the binder solution. A coating solution in which particles and particles of the compound are uniformly dispersed is prepared.

【0049】本発明に用いられる結着剤としては、例え
ばゼラチンの如き蛋白質、デキストランの如きポリサッ
カライド又はアラビアゴム、ポリビニルブチラール、ポ
リ酢酸ビニル、ニトロセルロース、エチルセルロース、
塩化ビニルデン・塩化ビニルコポリマー、ポリメチルメ
タクリレート、塩化ビニル・酢酸ビニルコポリマー、ポ
リウレタン、セルロースアセテートブチレート、ポリビ
ニルアルコール等のような、通常、層構成に用いられる
造膜性の結着剤が使用される。
Examples of the binder used in the present invention include proteins such as gelatin, polysaccharides or gum arabic such as dextran, polyvinyl butyral, polyvinyl acetate, nitrocellulose, ethyl cellulose, and the like.
A film-forming binder usually used for the layer constitution such as vinyldene chloride / vinyl chloride copolymer, polymethyl methacrylate, vinyl chloride / vinyl acetate copolymer, polyurethane, cellulose acetate butyrate, polyvinyl alcohol, etc. is used. .

【0050】一般に、結着剤は輝尽性蛍光体1質量部に
対して0.01〜1質量部の範囲で使用される。しかし
ながら、得られる放射線画像変換パネルの感度と鮮鋭性
の点では結着剤は少ない方が好ましく、塗布の容易さと
の兼合いから0.03〜0.2質量部の範囲がより好ま
しい。
In general, the binder is used in an amount of 0.01 to 1 part by mass per 1 part by mass of the stimulable phosphor. However, from the viewpoint of the sensitivity and sharpness of the obtained radiation image conversion panel, it is preferable that the amount of the binder is small, and the range of 0.03 to 0.2 part by mass is more preferable in consideration of the ease of application.

【0051】塗布液における結合剤と輝尽性蛍光体との
混合比(ただし、結合剤全部がエポキシ基含有化合物で
ある場合には、該化合物と蛍光体との比率に等しい)
は、目的とする放射線画像変換パネルの特性、蛍光体の
種類、エポキシ基含有化合物の添加量などによって異な
るが、一般には、結合塗布液調製用の溶剤例として、メ
タノール、エノタール、1−プロパノール、2−プロパ
ノール、ブタノール等の低級アルコール;メチレンクロ
ライド、エチレンクロライド等の塩素原子含有炭化水
素;アセトン、メチルエチルケトン、メチルイソブチル
ケトン等のケトン;酢酸メチル、酢酸エチル、酢酸ブチ
ル等の低級脂肪酸と低級アルコールとのエステル;ジオ
キサン、エチレングリコールエチルエーテル、エチレン
グリコールモノメチルエーテル等のエーテル;トルエ
ン;そして、それらの混合物を挙げることができる。
Mixing ratio of the binder and the stimulable phosphor in the coating solution (however, when the entire binder is an epoxy group-containing compound, it is equal to the ratio of the compound to the phosphor)
The target varies depending on the characteristics of the radiation image conversion panel, the type of phosphor, the amount of the epoxy group-containing compound added, etc., but, in general, examples of solvents for preparing a binding coating solution include methanol, enotal, 1-propanol, Lower alcohols such as 2-propanol and butanol; hydrocarbons containing chlorine atoms such as methylene chloride and ethylene chloride; ketones such as acetone, methyl ethyl ketone and methyl isobutyl ketone; lower fatty acids such as methyl acetate, ethyl acetate and butyl acetate and lower alcohols; Esters of dioxane, ethylene glycol ethyl ether, ethylene glycol monomethyl ether and the like; toluene; and mixtures thereof.

【0052】輝尽性蛍光体層用塗布液の調製に用いられ
る溶剤例としては、メタノール、エタノール、1−プロ
パノール、ブタノール等の低級アルコール;アセトン、
メチルエチルケトン、メチルイソブチルケトン、シクロ
ヘキサノン等のケトン;酢酸メチル、酢酸エチル、酢酸
ブチル等の低級脂肪酸と低級アルコールとのエステル;
ジオキサン、エチレングリコールモノエチルエーテル、
エチレングリコールモノメチルエーテル等のエーテル;
トリオール、キシロール等の芳香族化合物;メチレンク
ロライド、エチレンクロライド等のハロゲン化炭化水素
及びそれらの混合物などが挙げられる。
Examples of solvents used for preparing the coating solution for the stimulable phosphor layer include lower alcohols such as methanol, ethanol, 1-propanol and butanol; acetone,
Ketones such as methyl ethyl ketone, methyl isobutyl ketone and cyclohexanone; esters of lower fatty acids such as methyl acetate, ethyl acetate and butyl acetate with lower alcohols;
Dioxane, ethylene glycol monoethyl ether,
Ethers such as ethylene glycol monomethyl ether;
Aromatic compounds such as triol and xylol; halogenated hydrocarbons such as methylene chloride and ethylene chloride, and mixtures thereof.

【0053】尚、塗布液には、該塗布液中における蛍光
体の分散性を向上させるための分散剤、又、形成後の輝
尽性蛍光体層中における結合剤と蛍光体との結合力を向
上させるための可塑剤など、種々の添加剤が混合されて
もよい。そのような目的に用いられる分散剤の例として
は、フタル酸、ステアリン酸、カプロン酸、親油性界面
活性剤などを挙げることができる。又、可塑剤の例とし
ては、燐酸トリフェニル、燐酸トリクレジル、燐酸ジフ
ェニルなどの燐酸エステル;フタル酸ジエチル、フタル
酸ジメトキシエチル等のフタル酸エステル;グリコール
酸エチルフタリルエチル、グリコール酸ブチルフタリル
ブチルなどのグリコール酸エステル;トリエチレングリ
コールとアジピン酸とのポリエステル、ジエチレングリ
コールとコハク酸とのポリエステル等のポリエチレング
リコールと脂肪族二塩基酸とのポリエステル等を挙げる
ことができる。
The coating solution contains a dispersant for improving the dispersibility of the phosphor in the coating solution, and a binding force between the binder and the phosphor in the stimulable phosphor layer after formation. Various additives such as a plasticizer for improving the viscosity may be mixed. Examples of dispersants used for such purposes include phthalic acid, stearic acid, caproic acid, and lipophilic surfactants. Examples of the plasticizer include phosphoric esters such as triphenyl phosphate, tricresyl phosphate and diphenyl phosphate; phthalic esters such as diethyl phthalate and dimethoxyethyl phthalate; ethyl phthalyl ethyl glycolate and butyl phthalyl butyl glycolate And polyesters of aliphatic dibasic acid such as polyesters of triethylene glycol and adipic acid, polyesters of diethylene glycol and succinic acid, and the like.

【0054】上記のように調製した塗布液を、下塗層の
表面に均一に塗布することにより塗布液の塗膜を形成す
る。この塗布操作は通常の塗布手段、例えばドクターブ
レード、ロールコーター、ナイフコーター等を用いて行
うことができる。次いで、形成された塗膜を徐々に加熱
することにより乾燥し、下塗層上への輝尽性蛍光体層の
形成を完了する。
The coating solution prepared as described above is uniformly applied to the surface of the undercoat layer to form a coating film of the coating solution. This coating operation can be performed using a usual coating means, for example, a doctor blade, a roll coater, a knife coater or the like. Next, the formed coating film is dried by gradually heating to complete the formation of the stimulable phosphor layer on the undercoat layer.

【0055】輝尽性蛍光体層用塗布液の調製は、ボール
ミル、サンドミル、アトライター、三本ロールミル、高
速インペラー分散機、Kadyミル、及び超音波分散機
などの分散装置を用いて行われる。調製された塗布液を
ドクターブレード、ロールコーター、ナイフコーター等
の塗布装置を用いて支持体上に塗布し、乾燥することに
より輝尽性蛍光体層が形成される。前記塗布液を保護層
上に塗布・乾燥した後に輝尽性蛍光体層と支持体とを接
着してもよい。
The preparation of the coating solution for the stimulable phosphor layer is carried out using a dispersing device such as a ball mill, a sand mill, an attritor, a three-roll mill, a high-speed impeller disperser, a Kady mill, and an ultrasonic disperser. The prepared coating solution is coated on a support using a coating device such as a doctor blade, a roll coater, or a knife coater, and dried to form a stimulable phosphor layer. After coating and drying the coating solution on the protective layer, the stimulable phosphor layer and the support may be bonded.

【0056】放射線画像変換パネルの輝尽性蛍光体層の
膜厚は、目的とする放射線画像変換パネルの特性、輝尽
性蛍光体の種類、結着剤と輝尽性蛍光体との混合比等に
よって異なるが、10〜1,000μmの範囲から選ば
れるのが好ましく、10〜500μmの範囲から選ばれ
るのがより好ましい。
The thickness of the stimulable phosphor layer of the radiation image conversion panel depends on the desired properties of the radiation image conversion panel, the type of stimulable phosphor, and the mixing ratio between the binder and the stimulable phosphor. Although it depends on the like, it is preferably selected from the range of 10 to 1,000 μm, more preferably from the range of 10 to 500 μm.

【0057】以上、ユーロピウム付活弗化沃化バリウム
等の輝尽性蛍光体の例について主に説明したが、ユーロ
ピウム付活弗化臭化バリウム、その他の前記一般式
(I)で表される輝尽性蛍光体についても、上記を参照
して製造することが出来る。
While the examples of the stimulable phosphor such as europium-activated barium fluoroiodide have been mainly described above, europium-activated barium fluorobromide and other compounds represented by the above general formula (I) can be used. The stimulable phosphor can also be produced with reference to the above.

【0058】[0058]

【実施例】以下、実施例を挙げて本発明を例証する。The present invention will now be illustrated by way of examples.

【0059】実施例1 ユーロピウム付活弗化沃化バリウムの輝尽性蛍光体前駆
体を合成するため、二つの孔を有する耐圧容器にBaI
2水溶液(4mol/L濃度)2500mlとEuI3
溶液(0.2mol/L濃度)26.5mlを入れた。
更に、水溶液中に沃化カリウム992gを添加した。
Example 1 In order to synthesize a stimulable phosphor precursor of europium-activated barium fluoroiodide, BaI was placed in a pressure-resistant container having two holes.
2500 ml of 2 aqueous solution (4 mol / L concentration) and 26.5 ml of EuI 3 aqueous solution (0.2 mol / L concentration) were added.
Further, 992 g of potassium iodide was added to the aqueous solution.

【0060】この反応器中の反応母液を撹拌しながら8
3℃で保温した。弗化アンモニウム水溶液(10mol
/L濃度)600mlを、反応母液中にローラーポンプ
を用いて注入し、沈澱物を生成させた。注入終了後、乾
燥空気を10L/minの割合で20分間通気した。通
気前後の溶液の質量比は0.94であった。反応容器を
密封しそのままの温度で90分間攪拌した。90分攪拌
した後、濾過しエタノール2,000mlで洗浄した。
While stirring the reaction mother liquor in this reactor, 8
The temperature was kept at 3 ° C. Ammonium fluoride aqueous solution (10mol
/ L concentration) was injected into the reaction mother liquor using a roller pump to produce a precipitate. After completion of the injection, dry air was blown at a rate of 10 L / min for 20 minutes. The mass ratio of the solution before and after aeration was 0.94. The reaction vessel was sealed and stirred at that temperature for 90 minutes. After stirring for 90 minutes, the mixture was filtered and washed with 2,000 ml of ethanol.

【0061】回収した前駆体の質量を計測し、投入した
Ba量から求めた理論収量と比較することで収率を求め
た。又、得られた沈殿物についてX線回折測定(Cu−
Kα線を使用)を行った。次いで、沈殿物の平均粒径も
測定した。
The yield was determined by measuring the mass of the recovered precursor and comparing it with the theoretical yield determined from the amount of Ba charged. The obtained precipitate was subjected to X-ray diffraction measurement (Cu-
Kα radiation). Next, the average particle size of the precipitate was also measured.

【0062】実施例2 弗化アンモニウムの添加終了後、循環アスピレーターを
用いて反応容器内の圧力を74,480Paとし、溶媒
の減圧濃縮を行った。15分間濃縮を行った。濃縮前後
の反応溶液の質量比は0.92であった。
Example 2 After the addition of ammonium fluoride was completed, the pressure inside the reaction vessel was set to 74,480 Pa using a circulating aspirator, and the solvent was concentrated under reduced pressure. Concentration was performed for 15 minutes. The mass ratio of the reaction solution before and after concentration was 0.92.

【0063】これ以外は実施例1と同様の操作を行い、
沈殿物を得た。実施例1と同様に収率を計算し、沈殿物
のX線回折、平均粒径測定を行った。
Except for this, the same operation as in the first embodiment is performed.
A precipitate was obtained. The yield was calculated in the same manner as in Example 1, and the precipitate was subjected to X-ray diffraction and average particle size measurement.

【0064】実施例3 弗化アンモニウムの添加終了後、ポンプを用いて反応容
器壁面に反応液を散布し、液膜を形成させつつ溶媒を蒸
発させた。この操作を15分間行った。濃縮前後の反応
溶液の質量比は0.94であった。
Example 3 After the addition of ammonium fluoride was completed, the reaction solution was sprayed on the wall surface of the reaction vessel using a pump to evaporate the solvent while forming a liquid film. This operation was performed for 15 minutes. The mass ratio of the reaction solution before and after concentration was 0.94.

【0065】これ以外は実施例1と同様の操作を行い、
沈殿物を得た。実施例1と同様に収率を計算し、沈殿物
のX線回折、平均粒径測定を行った。
Otherwise, the same operation as in Example 1 was performed,
A precipitate was obtained. The yield was calculated in the same manner as in Example 1, and the precipitate was subjected to X-ray diffraction and average particle size measurement.

【0066】比較例1 ユーロピウム付活弗化沃化バリウムの輝尽性蛍光体前駆
体を合成するために、BaI2水溶液(4mol/L濃
度)2,500mlとEuI3水溶液(0.2mol/
L濃度)26.5mlを反応器に入れた。更に、水溶液
中に沃化カリウム332gを添加した。この反応母液を
撹拌しながら83℃で保温した。弗化アンモニウム水溶
液(10mol/L濃度)250mlを反応母液中にロ
ーラーポンプを用いて注入し、沈澱物を生成させた。注
入終了後、そのままの温度で90分間攪拌した。90分
攪拌した後、濾過しエタノール2,000mlで洗浄し
た。実施例1と同様に収率を計算し、沈殿物のX線回
折、平均粒径測定を行った。
Comparative Example 1 In order to synthesize a stimulable phosphor precursor of europium-activated barium fluoroiodide, 2,500 ml of an aqueous BaI 2 solution (4 mol / L concentration) and an aqueous solution of EuI 3 (0.2 mol / L) were used.
(L concentration) 26.5 ml was charged into the reactor. Further, 332 g of potassium iodide was added to the aqueous solution. The reaction mother liquor was kept at 83 ° C. while stirring. 250 ml of an ammonium fluoride aqueous solution (10 mol / L concentration) was injected into the reaction mother liquor by using a roller pump to form a precipitate. After completion of the injection, the mixture was stirred at the same temperature for 90 minutes. After stirring for 90 minutes, the mixture was filtered and washed with 2,000 ml of ethanol. The yield was calculated in the same manner as in Example 1, and the precipitate was subjected to X-ray diffraction and average particle size measurement.

【0067】比較例2 反応母液に注入する弗化アンモニウム水溶液の量を60
0mlとした以外は比較例1と同様にして沈殿物を得
た。実施例1と同様に収率を計算し、沈殿物のX線回
折、平均粒径測定を行った。
Comparative Example 2 The amount of the aqueous ammonium fluoride solution to be injected into the reaction mother liquor was 60
A precipitate was obtained in the same manner as in Comparative Example 1 except that the amount was 0 ml. The yield was calculated in the same manner as in Example 1, and the precipitate was subjected to X-ray diffraction and average particle size measurement.

【0068】比較例3 反応母液に注入する弗化アンモニウム水溶液の量を60
0mlとし、弗化アンモニウム溶液を注入した後、15
時間、自然蒸発により溶液を濃縮した。濃縮前後の反応
溶液の質量比は0.89であった。
Comparative Example 3 The amount of the aqueous ammonium fluoride solution injected into the reaction mother liquor was 60
0 ml, and after injecting ammonium fluoride solution, 15
Over time, the solution was concentrated by spontaneous evaporation. The mass ratio of the reaction solution before and after concentration was 0.89.

【0069】これ以外は比較例1と同様にして沈殿物を
得た。実施例1と同様に収率を計算し、沈殿物のX線回
折、平均粒径測定を行った。
A precipitate was obtained in the same manner as in Comparative Example 1 except for this. The yield was calculated in the same manner as in Example 1, and the precipitate was subjected to X-ray diffraction and average particle size measurement.

【0070】実施例4 反応母液に添加する沃化カリウムの量を500gとした
以外は実施例1と同様にして沈殿物を得た。実施例1と
同様に収率を計算し、沈殿物のX線回折、平均粒径測定
を行った。
Example 4 A precipitate was obtained in the same manner as in Example 1 except that the amount of potassium iodide added to the reaction mother liquor was changed to 500 g. The yield was calculated in the same manner as in Example 1, and the precipitate was subjected to X-ray diffraction and average particle size measurement.

【0071】実施例5 反応母液に沃化カリウムを添加しない以外は実施例1と
同様にして沈殿物を得た。実施例1と同様に収率を計算
し、沈殿物のX線回折、平均粒径測定を行った。
Example 5 A precipitate was obtained in the same manner as in Example 1 except that potassium iodide was not added to the reaction mother liquor. The yield was calculated in the same manner as in Example 1, and the precipitate was subjected to X-ray diffraction and average particle size measurement.

【0072】実施例6 弗化アンモニウムを添加した後、反応容器内の圧力を7
4,480Paとし、ポンプを用いて反応容器壁面に反
応液を散布し、液膜を形成させつつ溶媒を除去した。こ
の操作を7分間行った。濃縮前後の反応液の質量比は
0.93であった。
Example 6 After adding ammonium fluoride, the pressure in the reaction vessel was increased to 7
The reaction liquid was sprayed on the wall surface of the reaction vessel using a pump at 4,480 Pa, and the solvent was removed while forming a liquid film. This operation was performed for 7 minutes. The mass ratio of the reaction solution before and after concentration was 0.93.

【0073】これ以外は実施例1と同様の操作を行い、
沈殿物を得た。実施例1と同様に収率を計算し、沈殿物
のX線回折、平均粒径測定を行った。
Otherwise, the same operation as in the first embodiment is performed.
A precipitate was obtained. The yield was calculated in the same manner as in Example 1, and the precipitate was subjected to X-ray diffraction and average particle size measurement.

【0074】これらの結果を表1に纏めて示す。The results are summarized in Table 1.

【0075】X線回折の結果から、2θ=29.4°の
ピークを副生成物であるBaF2と同定した。
From the results of X-ray diffraction, a peak at 2θ = 29.4 ° was identified as BaF 2 as a by- product.

【0076】[0076]

【表1】 [Table 1]

【0077】表1から明らかなように、反応液から溶媒
を除去することにより、粒子の肥大化を防ぎつつ高収率
で、ユーロピウム付活弗化沃化バリウム輝尽性蛍光体前
駆体を得ることができる。粒子の肥大化を防ぐ効果はカ
リウムイオンの存在により顕著である。
As is clear from Table 1, by removing the solvent from the reaction solution, a europium-activated barium fluoroiodide stimulable phosphor precursor is obtained in high yield while preventing the particles from becoming large. be able to. The effect of preventing particle enlargement is remarkable due to the presence of potassium ions.

【0078】実施例7 反応母液に沃化セシウムを添加し、反応母液に添加する
弗化アンモニウム水溶液の量を700mlとし、21,
280Paの減圧で30分溶媒を除去した以外は実施例
2と同様にして沈殿物を得た。尚、溶媒の除去前後の反
応液の質量比は0.90であった。実施例1と同様に収
率を計算し、沈殿物のX線回折、平均粒径測定を行っ
た。
Example 7 Cesium iodide was added to a reaction mother liquor, and the amount of aqueous ammonium fluoride solution added to the reaction mother liquor was adjusted to 700 ml.
A precipitate was obtained in the same manner as in Example 2, except that the solvent was removed under a reduced pressure of 280 Pa for 30 minutes. The mass ratio of the reaction solution before and after the removal of the solvent was 0.90. The yield was calculated in the same manner as in Example 1, and the precipitate was subjected to X-ray diffraction and average particle size measurement.

【0079】実施例8 反応母液に沃化セシウムを添加し、反応母液に添加する
弗化アンモニウム水溶液の量を800mlとし、21,
280Paの減圧で35分溶媒を除去した以外は実施例
2と同様にして沈殿物を得た。尚、溶媒の除去前後の反
応液の質量比は0.88であった。実施例1と同様に収
率を計算し、沈殿物のX線回折、平均粒径測定を行っ
た。
Example 8 Cesium iodide was added to the reaction mother liquor, and the amount of the aqueous ammonium fluoride solution added to the reaction mother liquor was adjusted to 800 ml.
A precipitate was obtained in the same manner as in Example 2, except that the solvent was removed at a reduced pressure of 280 Pa for 35 minutes. The mass ratio of the reaction solution before and after the removal of the solvent was 0.88. The yield was calculated in the same manner as in Example 1, and the precipitate was subjected to X-ray diffraction and average particle size measurement.

【0080】比較例4 反応母液に沃化セシウムを添加し、反応母液の濃度を4
mol/Lから3.2mol/Lに変え、添加する弗化
アンモニウム溶液の量を480mlに変えた以外は実施
例2と同様にして沈殿物を得た。尚、溶媒の除去前後の
質量比は0.98であった。実施例1と同様に収率を計
算し、沈殿物のX線回折、平均粒径測定を行った。
Comparative Example 4 Cesium iodide was added to a reaction mother liquor, and the concentration of the reaction mother liquor was adjusted to 4
A precipitate was obtained in the same manner as in Example 2, except that the mol / L was changed to 3.2 mol / L, and the amount of the ammonium fluoride solution to be added was changed to 480 ml. The mass ratio before and after the removal of the solvent was 0.98. The yield was calculated in the same manner as in Example 1, and the precipitate was subjected to X-ray diffraction and average particle size measurement.

【0081】比較例5 反応母液の濃度を4mol/Lから3.2mol/Lに
変え、添加する弗化アンモニウム溶液の量を200ml
に変えた以外は比較例1と同様にして沈殿物を得た。実
施例1と同様に収率を計算し、沈殿物のX線回折、平均
粒径測定を行った。
Comparative Example 5 The concentration of the reaction mother liquor was changed from 4 mol / L to 3.2 mol / L, and the amount of the ammonium fluoride solution to be added was 200 ml.
A precipitate was obtained in the same manner as in Comparative Example 1 except that the precipitate was changed. The yield was calculated in the same manner as in Example 1, and the precipitate was subjected to X-ray diffraction and average particle size measurement.

【0082】実施例7〜8、比較例4,5の結果を表2
に纏めて示す。
Table 2 shows the results of Examples 7 and 8 and Comparative Examples 4 and 5.
It is summarized and shown.

【0083】[0083]

【表2】 [Table 2]

【0084】表2から明らかなように、本発明の製造方
法によれば、微細な輝尽性蛍光体前駆体を高収率で得る
ことが可能である。
As is clear from Table 2, according to the production method of the present invention, a fine stimulable phosphor precursor can be obtained in high yield.

【0085】(輝尽性蛍光体の製造)上記実施例1〜8
及び比較例1及び3〜5について、保温燒結により粒子
形状の変化、粒子間融着による粒子サイズ分布の変化を
防止するために、アルミナの超微粒子粉体を1質量%添
加し、ミキサーで充分撹拌して、結晶表面にアルミナの
超微粒子粉体を均一に付着させた。これを10Lの炉芯
容積を有するバッチ式ロータリーキルンの石英製炉芯管
に充填し、窒素/水素/酸素(93/5/2容量%)の
混合ガスを10L/minの流量で20分間流通させて
雰囲気を置換した。十分に炉芯内雰囲気を置換した後、
上記混合ガスの流量を2L/minに減じ、2rpmの
速度で炉心管を回転させながら10℃/minの昇温速
度で830℃まで加熱した。試料温度が830℃に到達
した後、試料温度を830℃に保ちながら窒素/水素
(93/5容量%)の混合ガスを10L/minの流量
で20分間流通させ、雰囲気を置換した。その後、窒素
/水素(93/5容量%)の混合ガスの流量を2L/m
inに減じ、90分間保持した。窒素/水素(93/5
容量%)の混合ガスの流量を2L/minに保持したま
ま、10℃/minの降温速度で25℃まで冷却した
後、雰囲気を大気に戻し、生成した酸素導入ユーロピウ
ム付活弗化沃化バリウム蛍光体を取り出した。
(Production of Stimulable Phosphor) Examples 1 to 8
For Comparative Examples 1 and 3 to 5, 1% by mass of ultrafine alumina powder was added in order to prevent a change in particle shape due to heat sintering and a change in particle size distribution due to fusion between particles, and a mixer was sufficient. By stirring, ultrafine alumina powder was uniformly attached to the crystal surface. This was filled into a quartz core tube of a batch type rotary kiln having a core volume of 10 L, and a mixed gas of nitrogen / hydrogen / oxygen (93/5/2% by volume) was passed at a flow rate of 10 L / min for 20 minutes. The atmosphere was replaced. After sufficiently replacing the atmosphere inside the furnace core,
The flow rate of the mixed gas was reduced to 2 L / min, and the reactor was heated to 830 ° C. at a rate of 10 ° C./min while rotating the furnace tube at a speed of 2 rpm. After the sample temperature reached 830 ° C., a nitrogen / hydrogen (93/5% by volume) mixed gas was passed at a flow rate of 10 L / min for 20 minutes while maintaining the sample temperature at 830 ° C. to replace the atmosphere. Thereafter, the flow rate of the mixed gas of nitrogen / hydrogen (93/5% by volume) was increased to 2 L / m.
in and held for 90 minutes. Nitrogen / hydrogen (93/5
(Volume%), the mixture was cooled to 25 ° C. at a rate of 10 ° C./min while maintaining the flow rate of the mixed gas at 2 L / min, the atmosphere was returned to the atmosphere, and the resulting oxygen-introduced europium-activated barium fluoroiodide The phosphor was taken out.

【0086】次に放射線画像変換パネルの製造例を示
す。
Next, an example of manufacturing a radiation image conversion panel will be described.

【0087】蛍光体層形成材料として、上記で得たユー
ロピウム付活弗化沃化バリウム蛍光体427g、ポリウ
レタン樹脂(住友バイエルウレタン社製:デスモラック
4125)15.8g、ビスフェノールA型エポキシ樹
脂2.0gをメチルエチルケトン、トルエン(1:1)
混合溶媒に添加し、プロペラミキサーによって分散し、
粘度25〜30PSの塗布液を調製した。この塗布液
を、ドクターブレードを用いて下塗付きポリエチレンテ
レフタレート(PET)フィルム上に塗布した後、10
0℃で15分間乾燥させて、蛍光体層を形成した。
As the phosphor layer forming material, 427 g of the europium-activated barium fluoroiodide phosphor obtained above, 15.8 g of polyurethane resin (Desmolac 4125, manufactured by Sumitomo Bayer Urethane Co., Ltd.), and bisphenol A type epoxy resin 0 g of methyl ethyl ketone, toluene (1: 1)
Add to the mixed solvent, disperse by propeller mixer,
A coating solution having a viscosity of 25 to 30 PS was prepared. After applying this coating solution on a polyethylene terephthalate (PET) film with an undercoat using a doctor blade,
After drying at 0 ° C. for 15 minutes, a phosphor layer was formed.

【0088】次に、保護膜形成材料として、弗素系樹脂
(フルオロオレフィン−ビニルエーテル共重合体,旭硝
子社製:ルミフロンLF100)70g、架橋剤(イソ
シアナート,住友バイエルウレタン社製:デスモジュー
ルZ4370)25g、ビスフェノールA型エポキシ樹
脂5g、及びシリコーン樹脂微粉末(信越化学工業社
製:KMP−590,粒子径1〜2μm)10gをトル
エン、i−プロピルアルコール(1:1)混合溶媒に添
加し、塗布液を作った。
Next, as a protective film forming material, 70 g of a fluorine-based resin (fluoroolefin-vinyl ether copolymer, Lumiflon LF100 manufactured by Asahi Glass Co., Ltd.) and 25 g of a cross-linking agent (isocyanate, Desmodur Z4370 manufactured by Sumitomo Bayer Urethane Co., Ltd.) , Bisphenol A type epoxy resin, 5 g, and silicone resin fine powder (KMP-590, manufactured by Shin-Etsu Chemical Co., Ltd .: KMP-590, particle size: 1-2 μm) are added to a mixed solvent of toluene and i-propyl alcohol (1: 1) and coated. I made a liquid.

【0089】この塗布液を、上記のように予め形成して
おいた蛍光体層上にドクターブレードを用いて塗布し、
次に120℃で30分間熱処理して熱硬化させると共に
乾燥し、厚さ10μmの保護膜を設けた。このようにし
て、輝尽性蛍光体層を有する放射線画像変換パネルを得
た。
This coating solution is applied onto the phosphor layer formed in advance as described above using a doctor blade.
Next, it was heat-treated at 120 ° C. for 30 minutes, thermally cured, and dried to provide a protective film having a thickness of 10 μm. Thus, a radiation image conversion panel having a stimulable phosphor layer was obtained.

【0090】(放射線画像変換パネルの評価)各放射線
画像変換パネルについて、以下の評価を行った。
(Evaluation of Radiation Image Conversion Panel) Each radiation image conversion panel was evaluated as follows.

【0091】《感度》放射線画像変換パネルに管電圧8
0kVpのX線を照射した後、パネルをHe−Neレー
ザー光(633nm)で操作して励起し、蛍光体層から
放射される輝尽発光を受光器(分光感度S−5の光電子
像倍管)で受光して強度を測定した。表3において、感
度は相対値で示される。
<< Sensitivity >> A tube voltage of 8 is applied to the radiation image conversion panel.
After irradiating with 0 kVp X-rays, the panel is excited by operating with a He-Ne laser beam (633 nm), and the photostimulable emission emitted from the phosphor layer is received by a photodetector (photoelectron image tube having a spectral sensitivity of S-5). ) And the intensity was measured. In Table 3, the sensitivity is shown as a relative value.

【0092】《鮮鋭度》放射線画像変換パネルに、鉛製
のMTFチャートを通して管電圧80kVpのX線を照
射した後、パネルをHe−Neレーザー光で操作して励
起し、蛍光体層から放射される輝尽発光を感度測定と同
じ受光器で受光して電気信号に変換し、これをアナログ
/デジタル変換して磁気テープに記録し、磁気テープを
コンピューターで分析して、磁気テープに記録されてい
るX線画像の変調伝達関数(MTF)を調べた。表3に
は、空間周波数2サイクル/mmにおけるMTF値
(%)が示される。
<Sharpness> After irradiating the radiation image conversion panel with X-rays having a tube voltage of 80 kVp through a lead MTF chart, the panel is operated with a He-Ne laser beam to be excited and emitted from the phosphor layer. The stimulated emission is received by the same light receiver as in the sensitivity measurement, converted into an electrical signal, converted from analog to digital, recorded on a magnetic tape, analyzed by a computer, and recorded on a magnetic tape. The modulation transfer function (MTF) of the existing X-ray image was examined. Table 3 shows the MTF value (%) at a spatial frequency of 2 cycles / mm.

【0093】《粒状性》放射線画像変換パネルに管電圧
80kVpのX線を照射した後、パネルをHe−Neレ
ーザー光で操作して励起し、蛍光体層から放射される輝
尽発光を上記と同じ受光器で受光して電気信号に変換
し、これをフィルムスキャナーによって通常の写真フィ
ルムに記録し、得られた画像の粒状性を目視で3段階評
価した。
<< Granularity >> After irradiating the radiation image conversion panel with X-rays at a tube voltage of 80 kVp, the panel is operated by He-Ne laser light to be excited, and the stimulated emission emitted from the phosphor layer is as described above. The light was received by the same light receiver and converted into an electric signal, which was recorded on an ordinary photographic film by a film scanner, and the granularity of the obtained image was visually evaluated in three steps.

【0094】尚、表3において、粒状性は増感紙(コニ
カ社製:SRO−250)とX線写真フィルム(コニカ
社製:SR−G)を使用した、従来、実用のX線写真撮
影によって得た画像の粒状性と比較して示した。
In Table 3, the graininess was determined by conventional X-ray photography using an intensifying screen (Konica: SRO-250) and an X-ray film (Konica: SR-G). The results are shown in comparison with the graininess of the image obtained.

【0095】○印は、前記の増感紙とフィルムを使用し
たX線写真撮影によって得た画像と同等の粒状性を意味
し、◎印は、それよりも良好な粒状性を意味する。又、
△印はX線写真撮影によって得た画像よりもやや荒い粒
状性を意味し、×印は、それよりも著しく荒い粒状性を
意味する。
The symbol ○ means graininess equivalent to that of an image obtained by X-ray photography using the intensifying screen and the film, and the symbol ◎ means better graininess. or,
The symbol “Δ” means graininess slightly coarser than the image obtained by radiography, and the symbol “×” means graininess significantly coarser than that.

【0096】各放射線画像変換パネルの評価結果を併せ
て表3に示す。
Table 3 also shows the evaluation results of each radiation image conversion panel.

【0097】[0097]

【表3】 [Table 3]

【0098】本発明に係る放射線画像変換パネルは、感
度、鮮鋭度、粒状性の何れにおいも優れている。
The radiation image conversion panel according to the present invention is excellent in sensitivity, sharpness, and granularity.

【0099】[0099]

【発明の効果】本発明によれば、輝度、鮮鋭性、粒状性
に優れた放射線画像変換パネルに必要な希土類付活アル
カリ土類金属弗化沃化物系輝尽性蛍光体を、高い生産性
で得ることができる。
According to the present invention, a rare earth activated alkaline earth metal fluoroiodide stimulable phosphor required for a radiation image conversion panel having excellent brightness, sharpness and granularity can be produced with high productivity. Can be obtained at

───────────────────────────────────────────────────── フロントページの続き (72)発明者 土屋 香苗 東京都日野市さくら町1番地 コニカ株式 会社内 Fターム(参考) 2G083 AA03 BB01 DD02 EE02 EE03 4H001 CA04 CA08 CF01 XA04 XA09 XA12 XA20 XA35 XA38 XA53 XA56 YA03 YA11 YA19 YA37 YA55 YA58 YA59 YA60 YA62 YA63 YA64 YA65 YA66 YA67 YA68 YA69 YA70  ────────────────────────────────────────────────── ─── Continued on the front page (72) Inventor Kanae Tsuchiya 1 Sakuracho, Hino-shi, Tokyo Konica Corporation F-term (reference) 2G083 AA03 BB01 DD02 EE02 EE03 4H001 CA04 CA08 CF01 XA04 XA09 XA12 XA20 XA35 XA38 XA53 XA56 YA03 YA11 YA19 YA37 YA55 YA58 YA59 YA60 YA62 YA63 YA64 YA65 YA66 YA67 YA68 YA69 YA70

Claims (9)

【特許請求の範囲】[Claims] 【請求項1】下記一般式(I)で示される酸素導入希土
類付活アルカリ土類金属弗化ハロゲン化物系輝尽性蛍光
体の液相での製造方法において、反応母液中のバリウム
濃度が3.3mol/L以上の溶液から溶媒を除去する
ことにより輝尽性蛍光体前駆体を得ることを特徴とす
る、希土類付活アルカリ土類金属弗化ハロゲン化物系輝
尽性蛍光体の製造方法。 一般式(I) Ba(1-x)2(x)FBr(y)(1-y):aM1,bLn,c
O 〔式中、M1はLi,Na,K,Rb及びCsから
選ばれる少なくとも1種のアルカリ金属、M2はBe,
Mg,Sr及びCaから選ばれる少なくとも1種のアル
カリ土類金属、LnはCe,Pr,Sm,Eu,Gd,
Tb,Tm,Dy,Ho,Nd,Er及びYbから選ば
れる少なくとも1種の希土類元素を表し、x,y,a,
b及びcは、それぞれ0≦x≦0.3,0≦y≦0.
3,0≦a≦0.05,0<b≦0.2,0≦c≦0.
1である。〕
1. A method for producing an oxygen-introduced rare earth-activated alkaline earth metal fluorohalide-based stimulable phosphor represented by the following general formula (I) in a liquid phase, wherein a barium concentration in a reaction mother liquor is 3: A method for producing a rare earth-activated alkaline earth metal fluorohalide-based stimulable phosphor, comprising obtaining a stimulable phosphor precursor by removing a solvent from a solution having a concentration of 3 mol / L or more. General formula (I) Ba (1-x ) M 2 (x) FBr (y) I (1-y): aM 1, bLn, c
O wherein M 1 is at least one alkali metal selected from Li, Na, K, Rb and Cs; M 2 is Be,
At least one alkaline earth metal selected from Mg, Sr and Ca; Ln is Ce, Pr, Sm, Eu, Gd,
Represents at least one rare earth element selected from Tb, Tm, Dy, Ho, Nd, Er and Yb, and represents x, y, a,
b and c are respectively 0 ≦ x ≦ 0.3, 0 ≦ y ≦ 0.
3, 0 ≦ a ≦ 0.05, 0 <b ≦ 0.2, 0 ≦ c ≦ 0.
It is one. ]
【請求項2】反応液の質量が(溶媒除去後/溶媒除去
前)≦0.97であることを特徴とする請求項1記載の
希土類付活アルカリ土類金属弗化ハロゲン化物系輝尽性
蛍光体の製造方法。
2. The rare earth-activated alkaline earth metal fluoride halide photostimulability according to claim 1, wherein the mass of the reaction solution is (after solvent removal / before solvent removal) ≦ 0.97. A method for producing a phosphor.
【請求項3】 反応溶媒を除去するため反応液を加熱
し、かつ他の溶媒を除去する手段を併用することを特徴
とする請求項1又は2記載の希土類付活アルカリ土類金
属弗化ハロゲン化物系輝尽性蛍光体の製造方法。
3. A rare earth activated alkaline earth metal halogen fluoride according to claim 1, wherein the reaction solution is heated to remove the reaction solvent, and a means for removing another solvent is used in combination. Method for producing a stimulable phosphor.
【請求項4】反応溶媒を除去するために反応容器内を減
圧に保つ過程を経ることを特徴とする請求項1、2又は
3記載の希土類付活アルカリ土類金属弗化ハロゲン化物
系輝尽性蛍光体の製造方法。
4. A rare earth-activated alkaline earth metal fluorinated halide stimulant according to claim 1, 2 or 3, wherein a step of keeping the inside of the reaction vessel under reduced pressure is performed to remove the reaction solvent. Method for producing luminescent phosphor.
【請求項5】溶媒を除去する方法が、乾燥気体を通気さ
せる方法であることを特徴とする請求項1、2又は3記
載の希土類付活アルカリ土類金属弗化ハロゲン化物系輝
尽性蛍光体の製造方法。
5. A rare earth-activated alkaline earth metal fluorohalide-based stimulable fluorescent light according to claim 1, wherein the method of removing the solvent is a method of passing dry gas. How to make the body.
【請求項6】溶媒除去の作業中、溶液が濡れ壁を形成す
ることを特徴とする請求項1、2又は3記載の希土類付
活アルカリ土類金属弗化ハロゲン化物系輝尽性蛍光体の
製造方法。
6. The rare earth-activated alkaline earth metal fluorohalide-based stimulable phosphor according to claim 1, wherein the solution forms a wetting wall during the operation of removing the solvent. Production method.
【請求項7】反応母液に予めアルカリ金属のハロゲン塩
が添加されていることを特徴とする請求項1〜6のいず
れか1項記載の希土類付活アルカリ土類金属弗化ハロゲ
ン化物系輝尽性蛍光体の製造方法。
7. The rare earth-activated alkaline earth metal fluoride halide stimulant according to claim 1, wherein an alkali metal halide is previously added to the reaction mother liquor. Method for producing luminescent phosphor.
【請求項8】請求項1〜7のいずれか1項に記載の製造
方法によって得られた希土類付活アルカリ土類金属弗化
ハロゲン化物系輝尽性蛍光体。
8. A rare earth-activated alkaline earth metal fluorohalide-based stimulable phosphor obtained by the production method according to claim 1.
【請求項9】請求項8に記載の希土類付活アルカリ土類
金属弗化ハロゲン化物系輝尽性蛍光体を含む蛍光体層を
有することを特徴とする放射線画像変換パネル。
9. A radiation image conversion panel comprising a phosphor layer containing the rare earth activated alkaline earth metal fluorohalide-based stimulable phosphor according to claim 8.
JP2001115073A 2000-05-16 2001-04-13 Method for producing rare earth activated alkaline earth metal fluoride halide photostimulable phosphor Expired - Fee Related JP4165029B2 (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006083329A (en) * 2004-09-17 2006-03-30 Konica Minolta Medical & Graphic Inc Photostimulable phosphor composed of rare earth-doped alkaline earth metal fluoride halide and radiological image conversion panel produced by using the same
WO2006054532A1 (en) * 2004-11-22 2006-05-26 Konica Minolta Medical & Graphic, Inc. Process for producing rare earth activated alkaline earth metal fluorohalide photostimulable phosphor
WO2006095613A1 (en) * 2005-03-09 2006-09-14 Konica Minolta Medical & Graphic, Inc. Rare earth activated alkaline earth metal fluorohalide photostimulable phosphor and radiation image conversion panel using the same

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006083329A (en) * 2004-09-17 2006-03-30 Konica Minolta Medical & Graphic Inc Photostimulable phosphor composed of rare earth-doped alkaline earth metal fluoride halide and radiological image conversion panel produced by using the same
WO2006054532A1 (en) * 2004-11-22 2006-05-26 Konica Minolta Medical & Graphic, Inc. Process for producing rare earth activated alkaline earth metal fluorohalide photostimulable phosphor
JPWO2006054532A1 (en) * 2004-11-22 2008-05-29 コニカミノルタエムジー株式会社 Method for producing rare earth activated alkaline earth metal fluoride halide stimulable phosphor
WO2006095613A1 (en) * 2005-03-09 2006-09-14 Konica Minolta Medical & Graphic, Inc. Rare earth activated alkaline earth metal fluorohalide photostimulable phosphor and radiation image conversion panel using the same
US7655926B2 (en) 2005-03-09 2010-02-02 Konica Minolta Medical & Graphic, Inc. Rare earth activated alkaline earth metal fluorohalide stimulable phosphor and radiation image conversion panel employing the same
JP4883005B2 (en) * 2005-03-09 2012-02-22 コニカミノルタエムジー株式会社 Rare earth activated alkaline earth metal fluorohalide stimulable phosphor and radiation image conversion panel using the same

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