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JP2005281734A - Raw material solution for metal organic chemical vapor deposition, method for purifying Pb (dpm) 2 complex, and method for forming dielectric thin film using the raw material solution - Google Patents

Raw material solution for metal organic chemical vapor deposition, method for purifying Pb (dpm) 2 complex, and method for forming dielectric thin film using the raw material solution Download PDF

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JP2005281734A
JP2005281734A JP2004094231A JP2004094231A JP2005281734A JP 2005281734 A JP2005281734 A JP 2005281734A JP 2004094231 A JP2004094231 A JP 2004094231A JP 2004094231 A JP2004094231 A JP 2004094231A JP 2005281734 A JP2005281734 A JP 2005281734A
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Shingo Okamura
信吾 岡村
Nobuyuki Soyama
信幸 曽山
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Mitsubishi Materials Corp
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Abstract

【課題】原料溶液を所定期間保存しても気化特性及び気化安定性に優れる有機金属化学気相成長法用原料溶液を提供する。原料溶液を所定期間保存しても経時的に懸濁させないPb(dpm)2錯体の精製方法を提供する。
【解決手段】本発明の有機金属化学気相成長法用原料溶液は、Pb(dpm)2錯体が有機溶媒に溶解されてなり、波長500〜600nmの範囲における可視光の透過率が95%以上であることを特徴とする。また、本発明のPb(dpm)2錯体の精製方法は、Pb(dpm)2錯体を水分含有量が50ppm以下の溶媒に溶解して溶解液を調製する工程と、溶解液に所定の割合で水分吸着剤を添加し、水分吸着剤により溶解液中に含まれる残留水分を除去する工程と、水分を除去した溶解液から溶媒を除去して水分含有量が200ppm以下のPb(dpm)2錯体を得る工程とを含む。
【選択図】なし
Provided is a raw material solution for metal organic chemical vapor deposition which has excellent vaporization characteristics and vaporization stability even when the raw material solution is stored for a predetermined period. Provided is a method for purifying a Pb (dpm) 2 complex that is not suspended over time even if the raw material solution is stored for a predetermined period.
The raw material solution for metal organic chemical vapor deposition of the present invention comprises a Pb (dpm) 2 complex dissolved in an organic solvent, and has a visible light transmittance of 95% or more in the wavelength range of 500 to 600 nm. It is characterized by being. The method for purifying the Pb (dpm) 2 complex of the present invention comprises a step of preparing a solution by dissolving the Pb (dpm) 2 complex in a solvent having a water content of 50 ppm or less, and a predetermined ratio to the solution. Adding a moisture adsorbent and removing the residual moisture contained in the solution by the moisture adsorbent; and removing the solvent from the solution from which the moisture has been removed to remove the solvent to a Pb (dpm) 2 complex having a moisture content of 200 ppm or less Obtaining the step.
[Selection figure] None

Description

本発明は、半導体の強誘電体メモリーデバイス等を作製するために必要とされる酸化鉛等の鉛系薄膜を有機金属化学気相成長法(Metal Organic Chemical Vapor Deposition、以下、MOCVD法という。)により形成するに際して、膜形成用の原料溶液として好適なPb(dpm)2錯体を含むMOCVD用原料溶液及び該原料溶液の原料として好適なPb(dpm)2錯体の精製方法並びに該原料溶液を用いた誘電体薄膜の成膜方法に関するものである。 In the present invention, a lead-based thin film such as lead oxide required for manufacturing a semiconductor ferroelectric memory device or the like is formed by metal organic chemical vapor deposition (hereinafter referred to as MOCVD method). In the case of forming by the above, a raw material solution for MOCVD containing a Pb (dpm) 2 complex suitable as a raw material solution for film formation, a method for purifying a Pb (dpm) 2 complex suitable as a raw material for the raw material solution, and the raw material solution The present invention relates to a method for forming a dielectric thin film.

従来、半導体装置の強誘電体メモリーデバイス作製のための酸化鉛薄膜をMOCVD法により形成するに際して用いられる蒸着原料としては、ビス(2,2,6,6-テトラメチル-3,5-ヘプタンジオナト)鉛(II)(以下、Pb(dpm)2という。)錯体が知られている。このPb(dpm)2錯体は、気化特性が悪く、気化時に残留物が発生する。また、このPb(dpm)2錯体をそのままMOCVD用原料として用いた場合、気化特性の経時劣化が大きいために、成膜の再現性が悪いという問題があった。 Conventionally, bis (2,2,6,6-tetramethyl-3,5-heptanedionato) is used as a deposition material for forming a lead oxide thin film for manufacturing a ferroelectric memory device of a semiconductor device by MOCVD. Lead (II) (hereinafter referred to as Pb (dpm) 2 ) complexes are known. This Pb (dpm) 2 complex has poor vaporization characteristics, and a residue is generated during vaporization. Further, when this Pb (dpm) 2 complex is used as a raw material for MOCVD as it is, there is a problem that the reproducibility of the film formation is poor because the vaporization characteristic is greatly deteriorated with time.

そこで本出願人は、Pb(dpm)2錯体を有機溶剤に溶解してなることを特徴とするMOCVD用原料溶液を提案した(例えば、特許文献1参照。)。特許文献1に示される有機溶剤としてはテトラヒドロフラン、ジメチルテトラヒドロフラン及びジメチルフランよりなる群より選ばれる1種又は2種以上が挙げられる。上記MOCVD用原料溶液によれば、MOCVD法により高い成膜速度にて安定かつ効率的に鉛系薄膜を成膜することができ、超伝導材料、強誘電体材料、半導体薄膜材料等として有用な鉛系薄膜の製造に有効に利用することができる。
また、本出願人は、1種又は2種以上の有機金属化合物原料を、環式もしくは非環式ジエーテル、アルキル置換環式モノエーテル、モノもしくはジ分岐アルキルモノエーテル、アルコキシアルコール、ジオール、並びにアセト酢酸エステルから選ばれた1種又は2種以上の溶媒に溶解させた溶液からなるMOCVD法による複合酸化物系誘電体薄膜形成用の溶液原料を提案した(例えば、特許文献2参照。)。上記特許文献2に示される溶液原料を使用して、MOCVD法により誘電体薄膜を形成すると、原料の各有機金属化合物が熱分解や不揮発性化を起こさずに安定して成膜室に供給されるため、基板温度が変化しても溶液原料中の金属の組成比に近い組成比を持つ複合酸化物型の誘電体薄膜を、段差があっても一様な厚みで確実に形成することができ、段差のあるFeRAMのキャパシタ用電極上に良好な誘電特性を持つ誘電体薄膜を安定して成膜することができる。
Therefore, the present applicant has proposed a raw material solution for MOCVD characterized by dissolving a Pb (dpm) 2 complex in an organic solvent (see, for example, Patent Document 1). Examples of the organic solvent disclosed in Patent Document 1 include one or more selected from the group consisting of tetrahydrofuran, dimethyltetrahydrofuran, and dimethylfuran. According to the MOCVD raw material solution, a lead-based thin film can be stably and efficiently formed at a high film formation rate by the MOCVD method, which is useful as a superconducting material, a ferroelectric material, a semiconductor thin film material, and the like. It can be effectively used for the production of lead-based thin films.
In addition, the present applicants can use one or more organometallic compound raw materials as a cyclic or acyclic diether, an alkyl-substituted cyclic monoether, a mono- or di-branched alkyl monoether, an alkoxy alcohol, a diol, and an acetoate. The solution raw material for complex oxide type dielectric thin film formation by the MOCVD method which consists of the solution dissolved in the 1 type (s) or 2 or more types of solvent chosen from acetate was proposed (for example, refer patent document 2). When the dielectric thin film is formed by the MOCVD method using the solution raw material shown in Patent Document 2, each organometallic compound of the raw material is stably supplied to the film forming chamber without causing thermal decomposition or non-volatility. Therefore, even if the substrate temperature changes, a complex oxide type dielectric thin film having a composition ratio close to the composition ratio of the metal in the solution raw material can be reliably formed with a uniform thickness even if there is a step. In addition, a dielectric thin film having good dielectric properties can be stably formed on the capacitor electrode of FeRAM having a step.

一方、金属化合物を次の式(1)に示すシクロヘキサン化合物に溶解させてなる金属化合物溶液が開示されている(例えば、特許文献3参照。)。   On the other hand, a metal compound solution obtained by dissolving a metal compound in a cyclohexane compound represented by the following formula (1) is disclosed (for example, see Patent Document 3).

Figure 2005281734
Figure 2005281734

式中、R5は水素原子又は炭素数1〜4のアルキル基を表し、pは1〜2の整数を表す。
上記特許文献3に示される金属化合物溶液によって、溶液CVD法に適する安定性と濃度を有する金属化合物溶液、該溶液からなるCVD用原料を提供することができる。
特開平10−195086号公報(請求項4及び請求項5、段落[0071]) 特開平11−323556号公報(請求項1、段落[0139]) 特開2001−234343号公報(請求項1、段落[0007])
In the formula, R 5 represents a hydrogen atom or an alkyl group having 1 to 4 carbon atoms, and p represents an integer of 1 to 2.
The metal compound solution disclosed in Patent Document 3 can provide a metal compound solution having stability and concentration suitable for the solution CVD method, and a CVD raw material comprising the solution.
JP-A-10-195086 (Claims 4 and 5, paragraph [0071]) JP 11-323556 A (Claim 1, paragraph [0139]) JP 2001-234343 A (Claim 1, paragraph [0007])

しかしながら、Pb(dpm)2錯体は他の有機鉛錯体と比べても特に水分に弱いため、水分の存在下では経時的に水酸化物を形成してしまう問題がある。そのため、Pb(dpm)2錯体を上記特許文献1〜3に示される有機溶媒に溶解させてMOCVD用原料溶液を調製した場合であっても、原料溶液を所定期間保存した際に原料溶液中でコロイド状の沈殿物を形成し、溶液が懸濁してしまう問題があった。この沈殿物は気化特性が悪く、気化器のノズル部を詰まらせてしまったり、気化時に残留物が発生するという問題があった。 However, since the Pb (dpm) 2 complex is particularly vulnerable to moisture compared to other organic lead complexes, there is a problem that a hydroxide is formed over time in the presence of moisture. Therefore, even when a raw material solution for MOCVD is prepared by dissolving the Pb (dpm) 2 complex in the organic solvent disclosed in Patent Documents 1 to 3, the raw material solution is stored in the raw material solution when stored for a predetermined period. There was a problem that a colloidal precipitate was formed and the solution was suspended. This precipitate has a problem that the vaporization characteristics are poor, and the nozzle portion of the vaporizer is clogged, and a residue is generated during vaporization.

本発明の目的は、原料溶液を所定期間保存しても溶液安定性、気化特性及び気化安定性に優れる有機金属化学気相成長法用原料溶液を提供することにある。
本発明の別の目的は、原料溶液を所定期間保存しても経時的に懸濁させないPb(dpm)2錯体の精製方法を提供することにある。
An object of the present invention is to provide a raw material solution for metal organic chemical vapor deposition which is excellent in solution stability, vaporization characteristics and vaporization stability even when the raw material solution is stored for a predetermined period.
Another object of the present invention is to provide a method for purifying a Pb (dpm) 2 complex that does not suspend the raw material solution over time even when stored for a predetermined period.

請求項1に係る発明は、Pb(dpm)2錯体が有機溶媒に溶解されてなり、波長500〜600nmの範囲における可視光の透過率が95%以上であることを特徴とする有機金属化学気相成長法用原料溶液である。
請求項1に係る発明では、波長500〜600nmの範囲における可視光の透過率を95%以上に規定することで、所定期間保存しても溶液安定性、気化特性及び気化安定性に優れた原料溶液を提供することができる。
The invention according to claim 1 is characterized in that the Pb (dpm) 2 complex is dissolved in an organic solvent, and the visible light transmittance in the wavelength range of 500 to 600 nm is 95% or more. This is a raw material solution for a phase growth method.
In the invention according to claim 1, by defining the transmittance of visible light in the wavelength range of 500 to 600 nm to 95% or more, a raw material excellent in solution stability, vaporization characteristics and vaporization stability even when stored for a predetermined period A solution can be provided.

請求項2に係る発明は、請求項1に係る発明であって、溶液中に含まれる水分含有量が200ppm以下である原料溶液である。
請求項2に係る発明では、溶液中に含まれる水分含有量が200ppm以下に規定することにより、原料溶液を所定期間保存したとしても原料溶液中に沈殿物を生じることがないため、溶液安定性、気化特性及び気化安定性に優れた原料溶液を提供することができる。
請求項3に係る発明は、請求項1に係る発明であって、Pb(dpm)2錯体が水分含有量50ppm以下の有機溶媒に溶解されてなる原料溶液である。
The invention according to claim 2 is the raw material solution according to claim 1, wherein the water content contained in the solution is 200 ppm or less.
In the invention according to claim 2, since the moisture content contained in the solution is regulated to 200 ppm or less, no precipitate is generated in the raw material solution even if the raw material solution is stored for a predetermined period. It is possible to provide a raw material solution having excellent vaporization characteristics and vaporization stability.
The invention according to claim 3 is the invention according to claim 1, which is a raw material solution in which a Pb (dpm) 2 complex is dissolved in an organic solvent having a water content of 50 ppm or less.

請求項4に係る発明は、Pb(dpm)2錯体を水分含有量が50ppm以下の溶媒に溶解して溶解液を調製する工程と、溶解液に所定の割合で水分吸着剤を添加し、水分吸着剤により溶解液中に含まれる残留水分を除去する工程と、水分を除去した溶解液から溶媒を除去して水分含有量が200ppm以下のPb(dpm)2錯体を得る工程とを含むPb(dpm)2錯体の精製方法である。
請求項4に係る発明では、上記工程を経ることにより精製されたPb(dpm)2錯体を有機溶媒に溶解して原料溶液を調製した場合、この原料溶液は所定期間保存しても経時的に懸濁することがない。
The invention according to claim 4 includes a step of preparing a solution by dissolving a Pb (dpm) 2 complex in a solvent having a water content of 50 ppm or less, adding a water adsorbent to the solution at a predetermined ratio, Pb including a step of removing residual water contained in the solution by the adsorbent and a step of removing the solvent from the solution from which water has been removed to obtain a Pb (dpm) 2 complex having a water content of 200 ppm or less. dpm) 2 is a purification method of the complex.
In the invention according to claim 4, when a raw material solution is prepared by dissolving the Pb (dpm) 2 complex purified through the above steps in an organic solvent, the raw material solution may be stored over time even if stored for a predetermined period. There is no suspension.

請求項5に係る発明は、請求項4記載の方法で精製されたPb(dpm)2錯体である。
請求項6に係る発明は、請求項4記載の方法で精製されたPb(dpm)2錯体が水分含有量50ppm以下の有機溶媒に溶解されてなる有機金属化学気相成長法用原料溶液である。
請求項7に係る発明は、請求項1、2、3又は6いずれか1項に記載の原料溶液に有機ジルコニウム錯体又は有機チタン錯体のいずれか一方又はその双方を更に含むことを特徴とする有機金属化学気相成長法用原料溶液である。
請求項8に係る発明は、請求項4記載の方法で精製されたPb(dpm)2錯体に、有機ジルコニウム錯体又は有機チタン錯体のいずれか一方又はその双方を所定の割合で混合して混合物を調製し、混合物が水分含有量50ppm以下の有機溶媒に溶解されてなることを特徴とする有機金属化学気相成長法用原料溶液である。
請求項9に係る発明は、請求項1、2、3、6、7又は8いずれか1項に記載の原料溶液を用いて有機金属化学気相成長法により成膜することを特徴とする誘電体薄膜の成膜方法である。
The invention according to claim 5 is a Pb (dpm) 2 complex purified by the method according to claim 4.
The invention according to claim 6 is a raw material solution for metal organic chemical vapor deposition method in which the Pb (dpm) 2 complex purified by the method according to claim 4 is dissolved in an organic solvent having a water content of 50 ppm or less. .
An invention according to a seventh aspect of the invention is characterized in that the raw material solution according to any one of the first, second, third, or sixth aspect further includes one or both of an organic zirconium complex and an organic titanium complex. This is a raw material solution for metal chemical vapor deposition.
In the invention according to claim 8, the Pb (dpm) 2 complex purified by the method according to claim 4 is mixed with either one or both of an organic zirconium complex and an organic titanium complex at a predetermined ratio. A raw material solution for metal organic chemical vapor deposition characterized by being prepared and dissolved in an organic solvent having a water content of 50 ppm or less.
The invention according to claim 9 is a dielectric characterized in that a film is formed by metal organic chemical vapor deposition using the raw material solution according to any one of claims 1, 2, 3, 6, 7, or 8. This is a method for forming a thin body film.

本発明の有機金属化学気相成長法用原料溶液は、Pb(dpm)2錯体が有機溶媒に溶解された原料溶液であり、波長500〜600nmの範囲における可視光の透過率を95%以上に規定することで、所定期間保存しても溶液安定性、気化特性及び気化安定性に優れた原料溶液とすることができる。本発明の原料溶液は、溶液中に含まれる水分含有量が200ppm以下であることが好ましい。溶液中に含まれる水分含有量を200ppm以下に規定することにより、原料溶液を所定期間保存したとしても原料溶液中に沈殿物を生じることがないため、従来用いられてきた原料溶液よりも溶液安定性に優れ、また気化残渣を抑えることができる。
これにより、例えばチタン酸ジルコン酸鉛(PZT)等の鉛系薄膜をMOCVD法で成膜する場合、原料溶液を安定に供給することができ、膜組成の制御性を向上することが期待できる。また、複数種類の有機金属錯体を含む原料溶液の場合には、膜組成の制御を原料溶液中に含まれる複数種類の有機金属錯体の濃度比により制御することができる。
The raw material solution for metal organic chemical vapor deposition of the present invention is a raw material solution in which a Pb (dpm) 2 complex is dissolved in an organic solvent, and the visible light transmittance in the wavelength range of 500 to 600 nm is 95% or more. By prescribing, a raw material solution having excellent solution stability, vaporization characteristics, and vaporization stability can be obtained even when stored for a predetermined period. The raw material solution of the present invention preferably has a water content contained in the solution of 200 ppm or less. By defining the water content contained in the solution to 200 ppm or less, even if the raw material solution is stored for a predetermined period, no precipitate is generated in the raw material solution. Excellent in properties and can suppress vaporization residue.
Thereby, for example, when a lead-based thin film such as lead zirconate titanate (PZT) is formed by the MOCVD method, the raw material solution can be stably supplied, and the controllability of the film composition can be expected to be improved. In the case of a raw material solution containing a plurality of types of organometallic complexes, the film composition can be controlled by the concentration ratio of the plurality of types of organometallic complexes contained in the source solution.

次に本発明を実施するための最良の形態を説明する。
本発明のMOCVD用原料溶液は、Pb(dpm)2錯体が有機溶媒に溶解されてなり、波長500〜600nmの範囲における可視光の透過率が95%以上であることを特徴とする。波長500〜600nmの範囲における可視光の透過率を95%以上に規定することで、所定期間保存しても溶液安定性、気化特性及び気化安定性に優れた原料溶液を提供することができる。
本発明のMOCVD用原料溶液におけるモル濃度は、0.01〜0.5mol/lの範囲内が好適である。0.1〜0.3mol/lの範囲内が特に好ましい。有機溶媒としては、テトラヒドロフラン、メチルテトラヒドロフラン、ジメチルテトラヒドロフラン、フラン、ジメチルフラン、ヘキサン、シクロヘキサン、メチルシクロヘキサン、エチルシクロヘキサン、ヘプタン、シクロヘプタン、n-オクタン、イソオクタン、シクロオクタン、ピリジン、ルチジン、酢酸ブチル、酢酸アミル、グライム、ジグライム、トリグライム、テトラグライム、ジエチレングリコールジエチルエーテル、ジエトキシエタン、エチレンジアミン、ジエチレントリアミン、トリエチレンテトラミン等が挙げられ、これら溶媒を単独で使用してもよいし、2種以上を混合して使用してもよい。
Next, the best mode for carrying out the present invention will be described.
The raw material solution for MOCVD of the present invention is characterized in that a Pb (dpm) 2 complex is dissolved in an organic solvent, and the visible light transmittance in the wavelength range of 500 to 600 nm is 95% or more. By defining the visible light transmittance in the wavelength range of 500 to 600 nm to 95% or more, a raw material solution having excellent solution stability, vaporization characteristics, and vaporization stability can be provided even when stored for a predetermined period.
The molar concentration in the raw material solution for MOCVD of the present invention is preferably in the range of 0.01 to 0.5 mol / l. A range of 0.1 to 0.3 mol / l is particularly preferable. Organic solvents include tetrahydrofuran, methyltetrahydrofuran, dimethyltetrahydrofuran, furan, dimethylfuran, hexane, cyclohexane, methylcyclohexane, ethylcyclohexane, heptane, cycloheptane, n-octane, isooctane, cyclooctane, pyridine, lutidine, butyl acetate, acetic acid Examples include amyl, glyme, diglyme, triglyme, tetraglyme, diethylene glycol diethyl ether, diethoxyethane, ethylenediamine, diethylenetriamine, triethylenetetramine, etc. These solvents may be used alone or in combination of two or more. May be used.

また、本発明のMOCVD用原料溶液は、溶液中に含まれる水分含有量が200ppm以下であることが好ましい。溶液中に含まれる水分含有量を200ppm以下に規定することにより、原料溶液を所定期間保存したとしても原料溶液中に沈殿物を生じることがないため、気化特性及び気化安定性に優れた原料溶液を提供することができる。また、本発明のMOCVD用原料溶液は、Pb(dpm)2錯体を水分含有量50ppm以下の有機溶媒に溶解して作製してもよい。水分含有量の少ない有機溶媒を用いることで、本発明のMOCVD用原料溶液の調製がし易くなる。 Moreover, it is preferable that the moisture content contained in the raw material solution for MOCVD of this invention is 200 ppm or less. By defining the water content contained in the solution to 200 ppm or less, even if the raw material solution is stored for a predetermined period, no precipitate is generated in the raw material solution, so that the raw material solution has excellent vaporization characteristics and vaporization stability. Can be provided. The raw material solution for MOCVD of the present invention may be prepared by dissolving a Pb (dpm) 2 complex in an organic solvent having a water content of 50 ppm or less. By using an organic solvent having a low water content, the MOCVD raw material solution of the present invention can be easily prepared.

次に、本発明のPb(dpm)2錯体の精製方法を説明する。
先ず、Pb(dpm)2錯体を水分含有量が50ppm以下の溶媒に溶解して溶解液を調製する。次いで、溶解液に所定の割合で水分吸着剤を添加し、水分吸着剤により溶解液中に含まれる残留水分を除去する。本発明の精製方法で使用される水分吸着剤としては、硫酸マグネシウム、硫酸カルシウム、硫酸ナトリウム、モレキュラーシーブ等が挙げられる。次に、水分を除去した溶解液から溶媒を除去して水分含有量が200ppm以下のPb(dpm)2錯体を得る。上記工程を経ることにより精製されたPb(dpm)2錯体は、この精製されたPb(dpm)2錯体を有機溶媒に溶解して原料溶液を調製した場合、調製した原料溶液は所定期間保存しても経時的に懸濁することがない。
Next, a method for purifying the Pb (dpm) 2 complex of the present invention will be described.
First, a Pb (dpm) 2 complex is dissolved in a solvent having a water content of 50 ppm or less to prepare a solution. Next, a moisture adsorbent is added to the solution at a predetermined ratio, and residual moisture contained in the solution is removed by the moisture adsorbent. Examples of the moisture adsorbent used in the purification method of the present invention include magnesium sulfate, calcium sulfate, sodium sulfate, and molecular sieve. Next, the solvent is removed from the solution from which moisture has been removed to obtain a Pb (dpm) 2 complex having a moisture content of 200 ppm or less. When the Pb (dpm) 2 complex purified through the above steps is prepared by dissolving the purified Pb (dpm) 2 complex in an organic solvent, the prepared raw material solution is stored for a predetermined period. However, it does not suspend over time.

また、本発明のMOCVD用原料溶液は、前述した原料溶液に有機ジルコニウム錯体又は有機チタン錯体のいずれか一方又はその双方を更に含んだ複数種類の有機金属錯体を含む原料溶液としてもよい。また、本発明のMOCVD用原料溶液は、上記方法により精製されたPb(dpm)2錯体に、有機ジルコニウム錯体又は有機チタン錯体のいずれか一方又はその双方を所定の割合で混合して混合物を調製し、この混合物を水分含有量50ppm以下の有機溶媒に溶解して複数種類の有機金属錯体を含む原料溶液を調製してもよい。Pb(dpm)2錯体と、有機ジルコニウム錯体又は有機チタン錯体のいずれか一方又その双方の混合割合は、この原料溶液を用いて作製することができる複合膜の組成比に応じて任意に調製することが可能である。
有機ジルコニウム錯体としては、Zr(dmhd)x(dpm)4-x(0≦x≦4)、Zr(O-iPr)y(dpm)4-y(0≦y≦4)、Zr(O-tBu)z(dpm)4-z(0≦z≦4)等が挙げられる。有機チタン錯体としては、Ti(O-iPr)2(dpm)2、Ti(O-tBu)2(dpm)2、Ti(O-iPr)2(dmhd)2、Ti(O-tBu)2(dmhd)2、[TiO(dpm)22等が挙げられる。ここでdmhdは2,6-ジメチル-3,5-ヘプタンジオン残基を、O-iPrはイソプロポキシドを、O-tBuはターシャリーブトキシドをそれぞれ示す。
Moreover, the raw material solution for MOCVD of the present invention may be a raw material solution containing a plurality of types of organometallic complexes in which one or both of an organic zirconium complex and an organic titanium complex are further included in the raw material solution described above. In addition, the MOCVD raw material solution of the present invention is prepared by mixing the Pb (dpm) 2 complex purified by the above method with either or both of an organic zirconium complex and an organic titanium complex at a predetermined ratio. Then, this mixture may be dissolved in an organic solvent having a water content of 50 ppm or less to prepare a raw material solution containing a plurality of types of organometallic complexes. The mixing ratio of one or both of the Pb (dpm) 2 complex and the organic zirconium complex or the organic titanium complex is arbitrarily prepared according to the composition ratio of the composite film that can be prepared using this raw material solution. It is possible.
Examples of the organic zirconium complex include Zr (dmhd) x (dpm) 4-x (0≤x≤4), Zr (O-iPr) y (dpm) 4-y (0≤y≤4), Zr (O- tBu) z (dpm) 4-z (0 ≦ z ≦ 4) and the like. Examples of the organic titanium complex include Ti (O—iPr) 2 (dpm) 2 , Ti (O—tBu) 2 (dpm) 2 , Ti (O—iPr) 2 (dmhd) 2 , Ti (O—tBu) 2 ( dmhd) 2 , [TiO (dpm) 2 ] 2 and the like. Here, dmhd represents a 2,6-dimethyl-3,5-heptanedione residue, O-iPr represents isopropoxide, and O-tBu represents tertiary butoxide.

次に本発明の実施例を比較例とともに詳しく説明する。
<実施例1>
先ず、金属鉛20.7gに無水トルエン200mlを添加して懸濁液を調製した。この懸濁液を激しく攪拌しながら脱水精製したジピバロイルメタンを金属鉛に対して2倍当量となる36.9gを加えた後、懸濁液を24時間加熱還流して反応させた。次いで、反応液を80℃、10Torr(約1.33kPa)にまで減圧濃縮することにより、Pb(dpm)2錯体を得た。次に、精製工程として、得られたPb(dpm)2錯体を水分含有量が50ppm以下のテトラヒドロフラン200mlに溶解して溶解液を調製した。この溶解液に水分吸着剤として硫酸マグネシウムを20g加えて、溶解液中に残留する水分を除去した。続いて水分を除去した溶解液をろ過して水分吸着剤を取り除いた後、得られたろ液を80℃、10Torr(約1.33kPa)の条件で減圧濃縮することによりテトラヒドロフランを除去してPb(dpm)2錯体の精製物を得た。
<比較例1>
精製工程を施さない以外は実施例1と同様にしてPb(dpm)2錯体を得た。
Next, examples of the present invention will be described in detail together with comparative examples.
<Example 1>
First, 200 ml of anhydrous toluene was added to 20.7 g of metallic lead to prepare a suspension. After adding 36.9 g of dipivaloylmethane, which was dehydrated and purified while vigorously stirring the suspension, to a 2-fold equivalent to metal lead, the suspension was heated to reflux for 24 hours to be reacted. Next, the reaction solution was concentrated under reduced pressure to 80 ° C. and 10 Torr (about 1.33 kPa) to obtain a Pb (dpm) 2 complex. Next, as a purification step, the obtained Pb (dpm) 2 complex was dissolved in 200 ml of tetrahydrofuran having a water content of 50 ppm or less to prepare a solution. 20 g of magnesium sulfate as a water adsorbent was added to the solution to remove water remaining in the solution. Subsequently, the solution from which moisture was removed was filtered to remove the moisture adsorbent, and then the obtained filtrate was concentrated under reduced pressure at 80 ° C. and 10 Torr (about 1.33 kPa) to remove tetrahydrofuran and remove Pb ( A purified product of dpm) 2 complex was obtained.
<Comparative Example 1>
A Pb (dpm) 2 complex was obtained in the same manner as in Example 1 except that the purification step was not performed.

<比較評価1>
実施例1及び比較例1でそれぞれ得られたPb(dpm)2錯体に含まれるPb、C及びHの重量比を元素分析により求めた。また、実施例1及び比較例1でそれぞれ得られたPb(dpm)2錯体中に含まれる水分含有量をカールフィッシャー水分計により測定した。得られた分析結果を表1にそれぞれ示す。なお、表1中にPb(dpm)2錯体に含まれるPb、C及びHの理論値も併せて示す。
<Comparison evaluation 1>
The weight ratio of Pb, C and H contained in the Pb (dpm) 2 complex obtained in Example 1 and Comparative Example 1 was determined by elemental analysis. Moreover, the water content contained in the Pb (dpm) 2 complex obtained in Example 1 and Comparative Example 1 was measured with a Karl Fischer moisture meter. The obtained analysis results are shown in Table 1, respectively. In Table 1, the theoretical values of Pb, C and H contained in the Pb (dpm) 2 complex are also shown.

Figure 2005281734
Figure 2005281734

表1より明らかなように、精製工程を施さない比較例1のPb(dpm)2錯体には、原料溶液とする前の段階であるにも係わらず、多量の水分が含有していた。一方、実施例1のPb(dpm)2錯体では、水分含有量が大幅に低減されている結果となった。 As is clear from Table 1, the Pb (dpm) 2 complex of Comparative Example 1 that was not subjected to the purification step contained a large amount of water, even though it was a stage before the raw material solution. On the other hand, in the Pb (dpm) 2 complex of Example 1, the water content was significantly reduced.

<実施例2>
先ず、実施例1で得られたPb(dpm)2錯体を濃度0.3mol/lの割合となるようにテトラヒドロフランに溶解して原料溶液を調製した。次いで、調製した原料溶液を7分割し、カールフィッシャー水分計で確認しながら原料溶液中の水分含有量がそれぞれ50ppm、100ppm、200ppm、250ppm、300ppm、400ppm及び500ppmとなるように水分含有量を調節した。次に、水分含有量を調節した原料溶液をアルゴン雰囲気下で約2週間保存した。保存後の各原料溶液について透過率測定、熱重量分析後における残渣測定及び気化実験後における残渣測定をそれぞれ行った。
(1)透過率測定
紫外可視光吸光スペクトル装置を用い、保存後の原料溶液を試料セル内に入れ、比較対照サンプルとなる対照セルには原料溶液を調製した直後の測定対象となる原料溶液と同一の水分含有量に調節した原料溶液を入れて可視光540nm付近の波長における透過率を測定した。
(2)熱重量分析後における残渣測定
先ず、各原料溶液を減圧下に維持して全ての溶媒を除去した。次いで、溶媒を除去して得られた固形物を熱重量分析装置の測定試料ホルダに封入し、装置内をアルゴン雰囲気下に維持し、室温から500℃にまで10℃/分の昇温速度で熱重量分析を行った。次に、熱重量分析終了後における試料ホルダ内の残渣重量を測定した。
(3)気化実験後における残渣測定
先ず、MOCVD装置の気化器として市販されている気化器を用い、次の表2に示す気化条件により気化実験を行った。
<Example 2>
First, the Pb (dpm) 2 complex obtained in Example 1 was dissolved in tetrahydrofuran so as to have a concentration of 0.3 mol / l to prepare a raw material solution. Next, divide the prepared raw material solution into 7 parts and adjust the water content so that the water content in the raw material solution is 50 ppm, 100 ppm, 200 ppm, 250 ppm, 300 ppm, 400 ppm and 500 ppm, respectively, while checking with a Karl Fischer moisture meter. did. Next, the raw material solution whose water content was adjusted was stored for about 2 weeks under an argon atmosphere. Each raw material solution after storage was subjected to transmittance measurement, residue measurement after thermogravimetric analysis, and residue measurement after vaporization experiment.
(1) Transmittance measurement Using an ultraviolet-visible light absorption spectrum apparatus, the raw material solution after storage is placed in a sample cell, and the control cell serving as a comparative control sample contains the raw material solution to be measured immediately after the raw material solution is prepared. The raw material solution adjusted to the same water content was added, and the transmittance at a wavelength near 540 nm was measured.
(2) Residue measurement after thermogravimetric analysis First, all the solvent was removed by maintaining each raw material solution under reduced pressure. Next, the solid obtained by removing the solvent is sealed in a measurement sample holder of a thermogravimetric analyzer, and the inside of the apparatus is maintained in an argon atmosphere, and the temperature is increased from room temperature to 500 ° C. at a rate of 10 ° C./min. Thermogravimetric analysis was performed. Next, the residue weight in the sample holder after completion of thermogravimetric analysis was measured.
(3) Residue measurement after vaporization experiment First, a vaporization experiment was performed under the vaporization conditions shown in Table 2 below using a commercially available vaporizer as the vaporizer of the MOCVD apparatus.

Figure 2005281734
Figure 2005281734

次に、気化実験を終えた後の気化器に残留する気化残渣を回収した後、この気化残渣の重量を測定し、次の式に基づいて気化実験後の残渣率を求めた。
気化後の残渣率(%)=(気化残渣重量/溶解前のPb(dpm)2錯体重量)×100
各測定結果を次の表3にそれぞれ示す。
Next, after collecting the vaporization residue remaining in the vaporizer after the vaporization experiment was completed, the weight of the vaporization residue was measured, and the residue rate after the vaporization experiment was obtained based on the following equation.
Residue rate after vaporization (%) = (weight of vaporized residue / weight of Pb (dpm) 2 complex before dissolution) × 100
Each measurement result is shown in Table 3 below.

Figure 2005281734
Figure 2005281734

表3より明らかなように、透過率測定では、水分含有量が250ppmまでは原料溶液調製直後の対照サンプルと比較しても透過率に変化がなく透明度を保っている結果となった。一方、水分含有量が300ppmの原料溶液では透過率が低下しており、原料溶液中に含まれる水分含有量の増加とともに透過率も低下する傾向がみられた。これは、水分含有量の多い原料溶液を一定期間保存すると、原料溶液中に含まれる水分によってPb(dpm)2錯体の一部が水酸化物を形成してコロイド状沈殿物が析出することにより溶液が懸濁化したものと考えられる。
熱重量分析後における残渣測定では、水分含有量が250ppm以下の原料溶液を用いた場合には残渣が生じていなかった。一方、水分含有量が300ppmの原料溶液では、熱重量分析後に残渣が生じており、原料溶液中に含まれる水分含有量が増加するほど熱重量分析後の残渣量も増加する傾向がみられた。これは、水分含有量の多い原料溶液を一定期間保存すると、原料溶液中に含まれる水分によってPb(dpm)2錯体の一部が水酸化物を形成してコロイド状沈殿物を生じ、この沈殿物が熱分解せずに残渣となったと考えられる。
気化実験後における残渣測定では、水分含有量が250ppm以下の原料溶液を用いた場合には残渣が生じていなかった。一方、水分含有量が300ppmの原料溶液では、気化実験後に残渣を生じており、原料溶液中に含まれる水分含有量が増加するほど気化実験後の残渣量も増加する傾向がみられた。このように、多くの気化残渣を生じてしまう原料溶液を使用し続けた場合、MOCVD装置内の配管等で閉塞してしまったり、気化速度等を制御することが難しく、得られる膜の品質を低下させる原因となる。また、水分含有量が500ppmの原料溶液では析出物が多く、気化ノズルが閉塞してしまう結果となってしまった。
As is clear from Table 3, the transmittance measurement showed that the transmittance was not changed even when compared with the control sample immediately after preparation of the raw material solution until the water content was 250 ppm, and the transparency was maintained. On the other hand, in the raw material solution having a water content of 300 ppm, the transmittance decreased, and the transmittance tended to decrease as the water content contained in the raw material solution increased. This is because when a raw material solution having a high water content is stored for a certain period of time, a part of the Pb (dpm) 2 complex forms a hydroxide due to the water contained in the raw material solution, and colloidal precipitates are deposited. It is thought that the solution was suspended.
In residue measurement after thermogravimetric analysis, no residue was produced when a raw material solution having a water content of 250 ppm or less was used. On the other hand, in the raw material solution with a water content of 300 ppm, a residue was generated after thermogravimetric analysis, and the amount of residue after thermogravimetric analysis tended to increase as the water content contained in the raw material solution increased. . This is because when a raw material solution with a high water content is stored for a certain period of time, a part of the Pb (dpm) 2 complex forms a hydroxide due to the water contained in the raw material solution, resulting in a colloidal precipitate. The product is considered to be a residue without thermal decomposition.
In residue measurement after the vaporization experiment, no residue was produced when a raw material solution having a water content of 250 ppm or less was used. On the other hand, in the raw material solution having a water content of 300 ppm, a residue was generated after the vaporization experiment, and the amount of the residue after the vaporization experiment tended to increase as the water content contained in the raw material solution increased. In this way, when a raw material solution that generates a lot of vaporization residue is used continuously, it is difficult to control the vaporization rate, etc., because it is clogged with piping in the MOCVD apparatus, etc. It causes a decrease. Moreover, in the raw material solution with a water content of 500 ppm, there were many precipitates, and the vaporization nozzle was blocked.

<実施例3>
先ず、実施例1で得られたPb(dpm)2錯体を、Zr(dmhd)4錯体及びTi(O-iPr)2(dpm)2錯体と、Pb(dpm)2錯体が0.30mol/l、Zr(dmhd)4錯体が0.15mol/l及びTi(O-iPr)2(dpm)2錯体が0.15mol/lとなるようにそれぞれ混合し、この混合物をオクタンに溶解して複数種類の有機金属錯体が溶解した原料溶液を調製した。次いで、調製した原料溶液を7分割し、カールフィッシャー水分計で確認しながら原料溶液中の水分含有量がそれぞれ50ppm、100ppm、200ppm、250ppm、300ppm、400ppm及び500ppmとなるように水分含有量を調節した。次に、水分含有量を調節した原料溶液をアルゴン雰囲気下で約2週間保存した。保存後の各原料溶液について実施例2と同様に透過率測定、熱重量分析後における残渣測定及び気化実験後における残渣測定をそれぞれ行った。なお、(3)気化実験後における残渣測定における気化条件は次の表4に示す条件とした。
<Example 3>
First, the Pb (dpm) 2 complex obtained in Example 1 was converted into a Zr (dmhd) 4 complex, a Ti (O-iPr) 2 (dpm) 2 complex, and a Pb (dpm) 2 complex at 0.30 mol / l. , Zr (dmhd) 4 complex is mixed at 0.15 mol / l and Ti (O—iPr) 2 (dpm) 2 complex is mixed at 0.15 mol / l. A raw material solution in which the organometallic complex was dissolved was prepared. Next, divide the prepared raw material solution into 7 parts and adjust the water content so that the water content in the raw material solution is 50 ppm, 100 ppm, 200 ppm, 250 ppm, 300 ppm, 400 ppm and 500 ppm, respectively, while checking with a Karl Fischer moisture meter. did. Next, the raw material solution whose water content was adjusted was stored for about 2 weeks under an argon atmosphere. Each raw material solution after storage was subjected to transmittance measurement, residue measurement after thermogravimetric analysis, and residue measurement after a vaporization experiment in the same manner as in Example 2. Note that (3) the vaporization conditions in the residue measurement after the vaporization experiment were the conditions shown in Table 4 below.

Figure 2005281734
Figure 2005281734

各測定結果を次の表5にそれぞれ示す。   Each measurement result is shown in Table 5 below.

Figure 2005281734
Figure 2005281734

表5より明らかなように、透過率測定では、水分含有量が250ppmまでは原料溶液調製直後の対照サンプルと比較しても透過率に変化がなく透明度を保っている結果となった。一方、水分含有量が300ppmの原料溶液では透過率が低下しており、原料溶液中に含まれる水分含有量の増加とともに透過率も低下する傾向がみられた。これは、水分含有量の多い原料溶液を一定期間保存すると、原料溶液中に含まれる水分によってPb(dpm)2錯体の一部が水酸化物を形成してコロイド状沈殿物が析出することにより溶液が懸濁化したものと考えられる。
熱重量分析後における残渣測定では、水分含有量が250ppm以下の原料溶液を用いた場合には残渣が生じていなかった。一方、水分含有量が250ppmを越える300ppm、400ppm及び500ppmの原料溶液では、熱重量分析後に残渣が生じており、原料溶液中に含まれる水分含有量が増加するほど熱重量分析後の残渣量も増加する傾向がみられた。これは、水分含有量の多い原料溶液を一定期間保存すると、原料溶液中に含まれる水分によってPb(dpm)2錯体の一部が水酸化物を形成してコロイド状沈殿物を生じ、この沈殿物が熱分解せずに残渣となったと考えられる。
気化実験後における残渣測定では、水分含有量が250ppm以下の原料溶液を用いた場合には残渣が生じていなかった。一方、水分含有量が250ppmを越える300ppm及び400ppmの原料溶液では、気化実験後に残渣を生じており、原料溶液中に含まれる水分含有量が増加するほど気化実験後の残渣量も増加する傾向がみられた。このように、多くの気化残渣を生じてしまう原料溶液を使用し続けた場合、MOCVD装置内の配管等で閉塞してしまったり、気化速度等を制御することが難しく、得られる膜の品質を低下させる原因となる。また、水分含有量が500ppmの原料溶液では析出物が多く、気化ノズルが閉塞してしまう結果となってしまった。
As apparent from Table 5, the transmittance measurement showed that the transmittance was not changed even when compared with the control sample immediately after preparation of the raw material solution until the water content was 250 ppm, and the transparency was maintained. On the other hand, in the raw material solution having a water content of 300 ppm, the transmittance decreased, and the transmittance tended to decrease as the water content contained in the raw material solution increased. This is because when a raw material solution having a high water content is stored for a certain period of time, a part of the Pb (dpm) 2 complex forms a hydroxide due to the water contained in the raw material solution and colloidal precipitates are deposited. It is thought that the solution was suspended.
In residue measurement after thermogravimetric analysis, no residue was produced when a raw material solution having a water content of 250 ppm or less was used. On the other hand, in the 300 ppm, 400 ppm and 500 ppm raw material solutions whose water content exceeds 250 ppm, residues are generated after thermogravimetric analysis, and the residual amount after thermogravimetric analysis increases as the water content contained in the raw material solution increases. There was a tendency to increase. This is because when a raw material solution with a high water content is stored for a certain period of time, a part of the Pb (dpm) 2 complex forms a hydroxide due to the water contained in the raw material solution, resulting in a colloidal precipitate. The product is considered to be a residue without thermal decomposition.
In residue measurement after the vaporization experiment, no residue was produced when a raw material solution having a water content of 250 ppm or less was used. On the other hand, in the 300 ppm and 400 ppm raw material solutions whose water content exceeds 250 ppm, residues are generated after the vaporization experiment, and the residual amount after the vaporization experiment tends to increase as the water content contained in the raw material solution increases. It was seen. As described above, when a raw material solution that generates a large amount of vaporization residue is used continuously, it is difficult to control the vaporization rate or the like because it is clogged with piping in the MOCVD apparatus or the like. It causes a decrease. Moreover, in the raw material solution with a water content of 500 ppm, there were many precipitates, and the vaporization nozzle was blocked.

<実施例4>
先ず、実施例1で得られたPb(dpm)2錯体を、Zr(dmhd)4錯体及びTi(O-iPr)2(dpm)2錯体と、Pb(dpm)2錯体が0.30mol/l、Zr(dmhd)4錯体が0.15mol/l及びTi(O-iPr)2(dpm)2錯体が0.15mol/lとなるようにそれぞれ混合し、この混合物をテトラヒドロフランに溶解して複数種類の有機金属錯体が溶解した原料溶液を調製した。次いで、調製した原料溶液を7分割し、カールフィッシャー水分計で確認しながら原料溶液中の水分含有量がそれぞれ50ppm、100ppm、200ppm、250ppm、300ppm、400ppm及び500ppmとなるように水分含有量を調節した。次に、水分含有量を調節した原料溶液をアルゴン雰囲気下で約2週間保存した。保存後の各原料溶液について、基板加熱式のMOCVD装置を用い、次の表6に示す成膜条件により電極としてPtが蒸着されたシリコン基板上にPZT誘電体薄膜を形成した。
<Example 4>
First, the Pb (dpm) 2 complex obtained in Example 1 was converted into a Zr (dmhd) 4 complex, a Ti (O-iPr) 2 (dpm) 2 complex, and a Pb (dpm) 2 complex at 0.30 mol / l. , Zr (dmhd) 4 complex is mixed at 0.15 mol / l and Ti (O—iPr) 2 (dpm) 2 complex is mixed at 0.15 mol / l. A raw material solution in which the organometallic complex was dissolved was prepared. Next, divide the prepared raw material solution into 7 parts and adjust the water content so that the water content in the raw material solution is 50 ppm, 100 ppm, 200 ppm, 250 ppm, 300 ppm, 400 ppm and 500 ppm, respectively, while checking with a Karl Fischer moisture meter. did. Next, the raw material solution whose water content was adjusted was stored for about 2 weeks under an argon atmosphere. For each raw material solution after storage, a PZT dielectric thin film was formed on a silicon substrate on which Pt was deposited as an electrode under the film forming conditions shown in Table 6 below using a substrate heating type MOCVD apparatus.

Figure 2005281734
Figure 2005281734

得られたPZT誘電体薄膜をICP分析して薄膜中に含まれるPb、Zr及びTiの元素比を求めた。各測定結果を次の表7に示す。   The obtained PZT dielectric thin film was subjected to ICP analysis to determine the element ratio of Pb, Zr and Ti contained in the thin film. The measurement results are shown in Table 7 below.

Figure 2005281734
Figure 2005281734

表7より明らかなように、水分含有量が250ppm以下の原料溶液は、2週間保存しても原料溶液中で沈殿物を生じないため、成膜した薄膜中のPb、Zr及びTiの割合を原料溶液中の濃度比で制御することが可能であり、組成制御性に優れた原料溶液であることが判る。これに対して原料溶液中の水分含有量が250ppmを越えている300ppm及び400ppmの原料溶液では、2週間保存したことにより原料溶液中に沈殿物が析出し、この沈殿物を気化することができなかったため、薄膜中の元素比を原料溶液中の濃度比で制御することができなくなってしまっていた。また水分含有量が500ppmの原料溶液は、成膜時において気化器のノズル部を閉塞させてしまったため、PZT誘電体薄膜を成膜できなかった。
As is clear from Table 7, since the raw material solution having a water content of 250 ppm or less does not produce precipitates in the raw material solution even after being stored for 2 weeks, the ratio of Pb, Zr and Ti in the formed thin film is It can be controlled by the concentration ratio in the raw material solution, and it can be seen that the raw material solution has excellent composition controllability. On the other hand, in the 300 ppm and 400 ppm raw material solutions in which the water content in the raw material solution exceeds 250 ppm, a precipitate is deposited in the raw material solution after being stored for 2 weeks, and this precipitate can be vaporized. As a result, the element ratio in the thin film could not be controlled by the concentration ratio in the raw material solution. Further, the raw material solution having a water content of 500 ppm could not form a PZT dielectric thin film because the nozzle part of the vaporizer was blocked during the film formation.

Claims (9)

Pb(dpm)2錯体が有機溶媒に溶解されてなり、
波長500〜600nmの範囲における可視光の透過率が95%以上であることを特徴とする有機金属化学気相成長法用原料溶液。
Pb (dpm) 2 complex is dissolved in an organic solvent,
A raw material solution for metal organic chemical vapor deposition characterized by having a visible light transmittance of 95% or more in a wavelength range of 500 to 600 nm.
溶液中に含まれる水分含有量が200ppm以下である請求項1記載の原料溶液。   The raw material solution according to claim 1, wherein a water content contained in the solution is 200 ppm or less. Pb(dpm)2錯体が水分含有量50ppm以下の有機溶媒に溶解されてなる請求項1記載の原料溶液。 The raw material solution according to claim 1, wherein the Pb (dpm) 2 complex is dissolved in an organic solvent having a water content of 50 ppm or less. Pb(dpm)2錯体を水分含有量が50ppm以下の溶媒に溶解して溶解液を調製する工程と、
前記溶解液に所定の割合で水分吸着剤を添加し、前記水分吸着剤により前記溶解液中に含まれる残留水分を除去する工程と、
前記水分を除去した溶解液から溶媒を除去して水分含有量が200ppm以下のPb(dpm)2錯体を得る工程と
を含むPb(dpm)2錯体の精製方法。
Dissolving a Pb (dpm) 2 complex in a solvent having a water content of 50 ppm or less to prepare a solution;
Adding a water adsorbent in a predetermined ratio to the solution, and removing residual water contained in the solution by the water adsorbent;
Pb (dpm) 2 purification process of the complex and a step of water content by removing the solvent from the solution obtained by removing the water to obtain the following Pb (dpm) 2 complex 200 ppm.
請求項4記載の方法で精製されたPb(dpm)2錯体。 A Pb (dpm) 2 complex purified by the method according to claim 4. 請求項4記載の方法で精製されたPb(dpm)2錯体が水分含有量50ppm以下の有機溶媒に溶解されてなる有機金属化学気相成長法用原料溶液。 A raw material solution for metal organic chemical vapor deposition, wherein the Pb (dpm) 2 complex purified by the method according to claim 4 is dissolved in an organic solvent having a water content of 50 ppm or less. 請求項1、2、3又は6いずれか1項に記載の原料溶液に有機ジルコニウム錯体又は有機チタン錯体のいずれか一方又はその双方を更に含むことを特徴とする有機金属化学気相成長法用原料溶液。   7. A raw material for metal organic chemical vapor deposition characterized by further comprising one or both of an organic zirconium complex and an organic titanium complex in the raw material solution according to claim 1, 2, 3 or 6. solution. 請求項4記載の方法で精製されたPb(dpm)2錯体に、有機ジルコニウム錯体又は有機チタン錯体のいずれか一方又はその双方を所定の割合で混合して混合物を調製し、前記混合物が水分含有量50ppm以下の有機溶媒に溶解されてなることを特徴とする有機金属化学気相成長法用原料溶液。 A Pb (dpm) 2 complex purified by the method according to claim 4 is mixed with one or both of an organic zirconium complex and an organic titanium complex at a predetermined ratio, and the mixture contains water. A raw material solution for metal organic chemical vapor deposition characterized by being dissolved in an organic solvent having an amount of 50 ppm or less. 請求項1、2、3、6、7又は8いずれか1項に記載の原料溶液を用いて有機金属化学気相成長法により成膜することを特徴とする誘電体薄膜の成膜方法。
A method for forming a dielectric thin film, comprising forming a film by a metal organic chemical vapor deposition method using the raw material solution according to any one of claims 1, 2, 3, 6, 7, or 8.
JP2004094231A 2004-03-29 2004-03-29 Raw material solution for metal organic chemical vapor deposition, method for purifying Pb (dpm) 2 complex, and method for forming dielectric thin film using the raw material solution Pending JP2005281734A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009129964A (en) * 2007-11-20 2009-06-11 Fujitsu Microelectronics Ltd ORGANIC METAL RAW MATERIAL, FILM-FORMING APPARATUS AND SEMICONDUCTOR DEVICE MANUFACTURING METHOD
JP2010219292A (en) * 2009-03-17 2010-09-30 Tokyo Electron Ltd Film forming method
JP2010258046A (en) * 2009-04-21 2010-11-11 Ulvac Japan Ltd Method for forming pzt thin film, and method for manufacturing semiconductor device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009129964A (en) * 2007-11-20 2009-06-11 Fujitsu Microelectronics Ltd ORGANIC METAL RAW MATERIAL, FILM-FORMING APPARATUS AND SEMICONDUCTOR DEVICE MANUFACTURING METHOD
JP2010219292A (en) * 2009-03-17 2010-09-30 Tokyo Electron Ltd Film forming method
JP2010258046A (en) * 2009-04-21 2010-11-11 Ulvac Japan Ltd Method for forming pzt thin film, and method for manufacturing semiconductor device

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