JP2013042094A - Wafer cleaning method - Google Patents
Wafer cleaning method Download PDFInfo
- Publication number
- JP2013042094A JP2013042094A JP2011179894A JP2011179894A JP2013042094A JP 2013042094 A JP2013042094 A JP 2013042094A JP 2011179894 A JP2011179894 A JP 2011179894A JP 2011179894 A JP2011179894 A JP 2011179894A JP 2013042094 A JP2013042094 A JP 2013042094A
- Authority
- JP
- Japan
- Prior art keywords
- filling
- wafer
- melt
- cleaning
- sublimation
- 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.)
- Withdrawn
Links
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- 238000000034 method Methods 0.000 title claims abstract description 94
- 238000011049 filling Methods 0.000 claims abstract description 163
- 239000000155 melt Substances 0.000 claims abstract description 95
- 239000007788 liquid Substances 0.000 claims abstract description 64
- 238000000859 sublimation Methods 0.000 claims abstract description 62
- 230000008022 sublimation Effects 0.000 claims abstract description 62
- 239000007787 solid Substances 0.000 claims abstract description 54
- 238000002844 melting Methods 0.000 claims abstract description 48
- 230000008018 melting Effects 0.000 claims abstract description 48
- 238000001816 cooling Methods 0.000 claims abstract description 33
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- 239000000463 material Substances 0.000 claims abstract description 16
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Landscapes
- Cleaning Or Drying Semiconductors (AREA)
Abstract
Description
本発明は、半導体デバイス製造などにおける基板(ウェハ)の洗浄技術に関する。 The present invention relates to a substrate (wafer) cleaning technique in manufacturing a semiconductor device or the like.
半導体チップの製造では、成膜、リソグラフィやエッチングなどを経てウェハ表面に微細な凹凸パターンが形成され、その後、ウェハ表面を清浄なものとするために、水(純水)や有機溶媒を用いて洗浄がなされる。素子は微細化される方向にあり、凹凸パターンの間隔は益々狭くなってきている。このため、水(純水)を用いて洗浄し、凹凸パターンの凹部に残留した水をウェハ表面から乾燥させて除去する際、凹部に残留した水と外部の空気との圧力差によって生じる毛細管現象により働く曲げの力により、凹凸パターンが倒れるという問題が生じやすくなってきている。この問題は、特に凹凸のパターン間隔がより狭くなった、例えばラインアンドスペース形状のパターンの場合、線幅(凹部の幅)が20nm台、10nm台世代の半導体チップにおいてより顕著になってきている。また、ウェハのパターン形状の多様化に伴って、凸部の中に脆弱な箇所を有するものもあり、当該箇所においても前記毛細管力が作用してパターン倒れが発生する問題が顕著になってきている。 In the manufacture of semiconductor chips, a fine uneven pattern is formed on the wafer surface through film formation, lithography, etching, etc., and then water (pure water) or an organic solvent is used to clean the wafer surface. Cleaning is done. The elements are in the direction of miniaturization, and the interval between the concave and convex patterns is becoming narrower. For this reason, when washing with water (pure water) and removing the water remaining in the concave portion of the concave / convex pattern by drying from the wafer surface, the capillary phenomenon caused by the pressure difference between the water remaining in the concave portion and the external air Due to the bending force acting on the surface, the problem that the concavo-convex pattern falls tends to occur. This problem has become more prominent in semiconductor chips having a line width (recess width) of 20 nm or 10 nm generation, particularly in the case of a pattern with a concave and convex pattern, for example, a line-and-space pattern. . Further, along with diversification of wafer pattern shapes, some convex portions have fragile locations, and the problem that pattern collapse occurs due to the capillary force acting also in those locations has become prominent. Yes.
特許文献1には、回路パターンを形成した基板表面を洗浄、リンス後、凹凸パターンの凹部に残留したリンス液を充填剤で置換し、該充填剤を固化し、固化後の充填剤を除去する、基板処理システムが開示されている。 In Patent Document 1, after cleaning and rinsing the substrate surface on which the circuit pattern is formed, the rinsing liquid remaining in the concave portions of the concavo-convex pattern is replaced with a filler, the filler is solidified, and the solidified filler is removed. A substrate processing system is disclosed.
特許文献2には、溶剤中に溶解させた昇華性材料を半導体装置の凹凸部や可動部に流し込み、その後、溶剤を蒸発させて昇華性材料を析出させ、固着を防止する技術が開示されている。この昇華性材料は、後に昇華させて取り除かれる。 Patent Document 2 discloses a technique for preventing sticking by pouring a sublimable material dissolved in a solvent into an uneven portion or a movable portion of a semiconductor device, and then evaporating the solvent to precipitate the sublimable material. Yes. This sublimable material is subsequently sublimed and removed.
特許文献3、4には、薄膜と基材との間の微小間隙の洗浄後に、洗浄溶液が乾燥する前に溶融状態の昇華性物質を微小間隙に付着させ、該昇華性物質を凝固させ、後に該昇華性物質を昇華させることにより、凹凸パターンの凹部に残留した洗浄液の乾燥時に前記微小間隙において薄膜と基板あるいは薄膜と薄膜とが洗浄液の表面張力により密着しないようにする方法等が開示されている。 In Patent Documents 3 and 4, after cleaning the micro gap between the thin film and the substrate, the sublimable substance in a molten state is attached to the micro gap before the cleaning solution is dried, and the sublimable substance is solidified. A method for preventing the thin film and the substrate or the thin film and the thin film from being in close contact with each other by the surface tension of the cleaning liquid in the minute gap when the cleaning liquid remaining in the concave portions of the uneven pattern is dried by sublimating the sublimable substance later is disclosed. ing.
また、超臨界二酸化炭素を用いる方法(特許文献5)や、凍結乾燥を用いる方法(特許文献6、7)なども開示されているが、いずれも特殊な装置や条件を必要とするものであり、操作が煩雑で結果的にコストが高くなってしまう問題がある。 Further, a method using supercritical carbon dioxide (Patent Document 5) and a method using freeze drying (Patent Documents 6 and 7) are also disclosed, but all of them require special equipment and conditions. There is a problem that the operation is complicated and the cost increases as a result.
パターン倒れは、ウェハの乾燥時に、パターンに毛細管力が作用することによって生じる。また、ウェハのパターン形状の多様化に伴って、凸部の中に脆弱な箇所を有するものもあり、当該箇所に前記毛細管力が作用してパターン倒れが発生する恐れがある。 Pattern collapse is caused by capillary force acting on the pattern when the wafer is dried. Further, along with the diversification of wafer pattern shapes, some of the convex portions have fragile locations, and the capillary force may act on the locations to cause pattern collapse.
このため、パターンの凹部に残留した液体を、乾燥により直接除去する代わりに、後工程で除去可能な固体で置き換え、該固体を除去することで、パターン倒れが解消すると期待できる。特許文献1には充填剤を回路パターンの間の凹部に充填し、パターンの倒壊を防止する技術が記載されているが、充填剤として開示されているポリマーやフォトレジストは、そのものが高価であることや、充填後に固化するには特別な条件下で反応させる必要があり、そのための装置や処理方法が煩雑となり、結果として高コストとなる問題がある。また、固化させた充填剤をプラズマ処理や現像処理により除去する方法においても、除去によりウェハ表面が損傷を受ける恐れがあることや、除去のための装置や処理方法が煩雑となり、結果として高コストとなる問題がある。 For this reason, instead of removing the liquid remaining in the concave portion of the pattern directly by drying, the liquid can be expected to be eliminated by replacing it with a solid that can be removed in a subsequent process and removing the solid. Patent Document 1 describes a technique for filling a recess between circuit patterns to prevent the pattern from collapsing. However, polymers and photoresists disclosed as a filler are themselves expensive. In order to solidify after filling, it is necessary to carry out the reaction under special conditions, and the apparatus and processing method therefor become complicated, resulting in a problem of high cost. Also, in the method of removing the solidified filler by plasma treatment or development treatment, there is a risk that the wafer surface may be damaged by the removal, and the removal apparatus and treatment method become complicated, resulting in high cost. There is a problem.
特許文献2〜4には昇華性材料を析出させる方法が記載されているが、開示されている構造物や微小間隙に、毛細管力が作用することによるパターン倒れを低減することについて想定されていないため、本目的に適用するためには改善の余地があった。 Patent Documents 2 to 4 describe a method for depositing a sublimable material, but it is not assumed to reduce pattern collapse due to the action of capillary force on the disclosed structures and minute gaps. Therefore, there was room for improvement in order to apply for this purpose.
本発明は、表面に凹凸パターンを有するウェハの該表面の洗浄において、前記凹凸パターンに働く毛細管力の影響を低減し、パターン倒れを低減する、ウェハの洗浄方法を提供することを課題とする。 It is an object of the present invention to provide a wafer cleaning method that reduces the influence of capillary force acting on the concavo-convex pattern and reduces pattern collapse in cleaning the surface of a wafer having a concavo-convex pattern on the surface.
本発明は、
表面に凹凸パターンを形成したウェハの該表面を洗浄液で洗浄する、洗浄工程、
洗浄工程後の前記ウェハの凹部に残留する洗浄液を、昇華性物質を含む充填用処理剤を加熱により融解した充填用融液で置換し、充填する、融液充填工程、
前記凹部に充填された前記融液を冷却することにより固体の昇華性物質を析出させる、冷却析出工程、
前記凹部に析出した固体の昇華性物質を昇華により除去する、昇華除去工程
を有するウェハの洗浄方法であって、前記充填用融液が、含有する昇華性物質の融点以上、融点+25℃以下の温度範囲内で充填用処理剤を融解させた融液であることを特徴とする、ウェハの洗浄方法である。
The present invention
A cleaning step of cleaning the surface of the wafer having a concavo-convex pattern on the surface with a cleaning liquid;
A melt filling process, in which the cleaning liquid remaining in the recesses of the wafer after the cleaning process is replaced with a filling melt obtained by melting a filling processing agent containing a sublimation substance by heating, and filling.
A cooling precipitation step of precipitating a solid sublimable material by cooling the melt filled in the recess,
A method for cleaning a wafer having a sublimation removal step, wherein a solid sublimable substance deposited in the recess is removed by sublimation, wherein the filling melt has a melting point of not less than the melting point of the sublimable substance contained and a melting point of + 25 ° C. or less. A wafer cleaning method characterized by being a melt obtained by melting a processing agent for filling within a temperature range.
前記充填用融液が、含有する昇華性物質の融点以上、融点+25℃以下の温度範囲内で充填用処理剤を融解させた融液であると、融液中での昇華性物質の蒸発に伴う気泡の発生が低減される。そのため、前記融液充填工程において、ウェハの凹部に前記融液を流入させる場合、前記凹部に気泡が発生し難くなり、その結果、毛細管力の作用を抑制しつつ充填することができる。融点未満の温度では前記昇華性物質が融解しないため、すなわち融液とならないため、前記洗浄液を置換することができない。融点+25℃を超える温度では、前記昇華性物質を含む融液となるものの、該昇華性物質の蒸発が早すぎるため、ウェハの凹部に残留する洗浄液を該融液で置換できたとしても、融液から昇華性物質が蒸発することにより前記凹部を充分に充填することができない。また、融液内で気泡の発生が多くなることから、凹部においても気泡が発生し易くなり、該気泡により凹部に毛細管力が作用してしまうため、パターンの倒壊に繋がる。前記融液が、含有する昇華性物質の融点以上、融点+15℃以下の温度範囲内で充填用処理剤を融解させた融液であると、冷却析出工程時に融液の温度をより早く冷却できるため、冷却析出工程時に昇華性物質が蒸発し減少する量を低減でき、その結果、ウェハ全面の凹部をより充填しやすいため、さらに好ましい。 When the filling melt is a melt obtained by melting the filling treatment agent within a temperature range of not less than the melting point of the sublimable substance contained and not less than the melting point + 25 ° C., the sublimable substance can be evaporated in the melt. The accompanying bubble generation is reduced. Therefore, in the melt filling step, when the melt is caused to flow into the recess of the wafer, bubbles are hardly generated in the recess, and as a result, the filling can be performed while suppressing the action of the capillary force. Since the sublimable substance does not melt at a temperature lower than the melting point, that is, does not become a melt, the cleaning liquid cannot be replaced. A temperature exceeding the melting point + 25 ° C. results in a melt containing the sublimable substance, but the sublimable substance evaporates too quickly, so even if the cleaning liquid remaining in the recesses of the wafer can be replaced with the melt, When the sublimable substance evaporates from the liquid, the concave portion cannot be sufficiently filled. In addition, since more bubbles are generated in the melt, bubbles are likely to be generated in the recesses, and capillary forces act on the recesses due to the bubbles, leading to collapse of the pattern. When the melt is a melt obtained by melting the filling treatment agent within the temperature range of the melting point of the sublimable substance to be contained and the melting point + 15 ° C. or less, the temperature of the melt can be cooled more quickly during the cooling precipitation process. Therefore, the amount of evaporation and reduction of the sublimable substance during the cooling precipitation process can be reduced, and as a result, the recesses on the entire surface of the wafer can be more easily filled.
また、前記充填用処理剤は、昇華性物質を60質量%以上、有機溶媒を40質量%以下含有するものであってもよい。昇華性物質が60質量%未満で有機溶媒が40質量%超の場合、冷却析出工程で析出する固体がポーラスとなったり析出する固体が少なくなったりし易く、ウェハの凹部を昇華性物質で充分に充填し難い恐れがあることや、含有する有機溶媒によってウェハの凹部に毛細管力が作用してしまう恐れがあることから、好ましくない。ウェハの凹部を昇華性物質で充分に充填する観点や、含有する有機溶媒によりウェハの凹部に作用する恐れがある毛細管力を低減する観点から、前記充填用処理剤は、昇華性物質を95質量%以上、有機溶媒を5質量%以下含有するものであることがより好ましい。 The filling treatment agent may contain 60% by mass or more of a sublimable substance and 40% by mass or less of an organic solvent. When the sublimable substance is less than 60% by mass and the organic solvent is more than 40% by mass, the solid deposited in the cooling deposition process becomes porous or the deposited solid tends to decrease, and the sublimated substance is sufficient for the recess of the wafer. It is not preferable because it may be difficult to fill the wafer, and a capillary force may act on the concave portion of the wafer by the organic solvent contained. From the viewpoint of sufficiently filling the concave portion of the wafer with the sublimable substance and reducing the capillary force that may act on the concave portion of the wafer by the organic solvent contained, the filling treatment agent contains 95 mass of the sublimable substance. More preferably, the organic solvent is contained in an amount of 5% by mass or less.
また、ウェハの凹部を昇華性物質で充分に充填する観点や、ウェハの凹部に毛細管力を作用させない観点から、前記充填用処理剤は昇華性物質からなるものであってもよい。 In addition, the filling treatment agent may be made of a sublimable substance from the viewpoint of sufficiently filling the concave portion of the wafer with the sublimable substance and preventing the capillary force from acting on the concave portion of the wafer.
また、前記有機溶媒が、充填用融液の温度よりも沸点が高い有機溶媒であることが好ましい。 The organic solvent is preferably an organic solvent having a boiling point higher than the temperature of the filling melt.
また、洗浄工程後の前記ウェハの凹部に残留する洗浄液が充填用融液の温度よりも沸点が高い有機溶媒であることが好ましい。 Moreover, it is preferable that the cleaning liquid remaining in the concave portion of the wafer after the cleaning process is an organic solvent having a boiling point higher than the temperature of the filling melt.
また、洗浄工程後の前記ウェハの凹部に残留する洗浄液が充填用融液に対して溶解性を有することが好ましい。 Moreover, it is preferable that the cleaning liquid remaining in the concave portion of the wafer after the cleaning process is soluble in the filling melt.
また、前記融液充填工程において、スピン方式によりウェハの凹凸パターンに充填用融液を供給することか、充填用融液槽内にウェハを浸漬することによって、凹部に残留する洗浄液を充填用融液で置換することが好ましい。 Further, in the melt filling step, the cleaning liquid remaining in the recesses is melted for filling by supplying the filling melt to the concave / convex pattern of the wafer by a spin method or immersing the wafer in the filling melt tank. Replacement with a liquid is preferred.
また、前記充填用処理剤中の液相での光散乱式液中粒子検出器によるパーティクル測定における0.5μmより大きい粒子の数は該処理剤を加熱により融解させて充填用融液とした際に該融液1mL当たり100個以下であることが好ましい。前記0.5μmより大きい粒子の数が該融液1mL当たり100個超であると、パーティクルによりパターンにダメージを誘発する恐れがありデバイスの歩留まり低下及び信頼性の低下を引き起こす恐れがある。なお、前記0.5μmより大きい粒子の数は該融液1mL当たり1個以上あってもよい。なお、融液中のパーティクルの数を直接測定することは困難なので、本発明における融液中のパーティクル測定は、例えば、予め前記融液1mLをイソプロピルアルコール等の有機溶媒に溶解し、該溶液に対して、レーザを光源とした光散乱式液中粒子測定方式における市販の測定装置を利用して測定するものであり、パーティクルの粒径とは、PSL(ポリスチレン製ラテックス)標準粒子基準の光散乱相当径を意味する。 In addition, the number of particles larger than 0.5 μm in the particle measurement by the light scattering type submerged particle detector in the liquid phase in the filling treatment agent is obtained when the treatment agent is melted by heating to obtain a filling melt. It is preferable that 100 or less per 1 mL of the melt. If the number of particles larger than 0.5 μm is more than 100 per mL of the melt, the particles may cause damage to the pattern, which may cause a decrease in device yield and reliability. The number of particles larger than 0.5 μm may be 1 or more per 1 mL of the melt. In addition, since it is difficult to directly measure the number of particles in the melt, the measurement of particles in the melt in the present invention is performed by, for example, dissolving 1 mL of the melt in an organic solvent such as isopropyl alcohol in advance. On the other hand, measurement is performed using a commercially available measuring device in a light scattering type liquid particle measurement method using a laser as a light source, and the particle size of particles is light scattering based on PSL (polystyrene latex) standard particles. Means equivalent diameter.
また、前記充填用処理剤中の、Na、Mg、K、Ca、Mn、Fe及びCuの各元素の金属不純物含有量は、該処理剤総量に対し各100質量ppb以下であることが好ましい。前記の各元素の金属不純物としては、金属微粒子、イオン、コロイド、錯体、酸化物や窒化物といった形で、溶解、未溶解に係らず処理剤中に存在するもの全てが対象となる。前記金属不純物含有量が、該処理剤総量に対し100質量ppb超であると、ウェハを用いたデバイスの接合リーク電流が増大する恐れがあり、デバイスの歩留まり低下及び信頼性の低下を引き起こす恐れがある。なお、前記金属不純物含有量は、該処理剤総量に対し各0.01質量ppb以上であってもよい。なお、充填用処理剤中の金属不純物含有量は、所定量の充填用処理剤から、揮発成分及び蒸発成分をすべて揮発及び蒸発させて、残った残渣をフッ硝酸に溶解させて、該溶液中の金属不純物含有量を、市販の誘導結合プラズマ質量分析装置を用いて測定し、そこから充填用処理剤中の金属不純物含有量を算出することで求めることができる。 Moreover, it is preferable that the metal impurity content of each element of Na, Mg, K, Ca, Mn, Fe, and Cu in the said processing agent for filling is 100 mass ppb or less with respect to this processing agent total amount. The metal impurities of each element described above are all in the form of metal fine particles, ions, colloids, complexes, oxides and nitrides, whether dissolved or undissolved, in the treatment agent. If the metal impurity content is more than 100 mass ppb with respect to the total amount of the processing agent, there is a possibility that the junction leakage current of the device using the wafer increases, which may cause a decrease in device yield and reliability. is there. In addition, 0.01 mass ppb or more of each may be sufficient as said metal impurity content with respect to this processing agent total amount. The content of metal impurities in the filling treatment agent is such that all volatile components and evaporation components are volatilized and evaporated from a predetermined amount of the filling treatment agent, and the remaining residue is dissolved in hydrofluoric acid. The metal impurity content of can be measured by using a commercially available inductively coupled plasma mass spectrometer and the metal impurity content in the filling treatment agent can be calculated therefrom.
特許文献1〜4では、ウェハの凹部に固体を固化するにあたって、または凹部に昇華性物質を析出するにあたって、パターンにダメージを誘発する恐れがあり、当該ウェハを用いたデバイスの歩留まり低下及び信頼性の低下を引き起こす原因となるパーティクルや、当該ウェハを用いたデバイスの接合リーク電流を増大させる恐れがある金属不純物の該凹部表面への混入を考慮されていないが、本発明では、前記処理剤中のパーティクルや金属不純物の含有量を上述した範囲内とすることで、それらに起因した不具合を改善することができる。 In Patent Documents 1 to 4, there is a risk of inducing damage to the pattern when solidifying a solid in a concave portion of a wafer or depositing a sublimable substance in the concave portion, and the yield and reliability of devices using the wafer are reduced. However, in the present invention, it is not considered to mix particles that cause a decrease in the surface of the concave portion or metal impurities that may increase the junction leakage current of the device using the wafer. By setting the content of the particles and metal impurities within the above-described range, it is possible to improve the problems caused by them.
また、前記充填用処理剤は、昇華性物質を昇華精製または蒸留精製したもの、昇華性物質と有機溶媒の混合物を昇華精製または蒸留精製したもの、及び、予め昇華精製または蒸留精製した昇華性物質と予め蒸留精製した有機溶媒とを混合したもの、からなる群から選ばれる少なくとも1つであると、前記処理剤中の液相での光散乱式液中粒子検出器によるパーティクル測定における0.5μmより大きい粒子の数を、該処理剤を加熱により融解させて充填用融液とした際に該融液1mL当たり100個以下に、前記処理剤中のNa、Mg、K、Ca、Mn、Fe及びCuの各元素の金属不純物含有量を、該処理剤総量に対し各100質量ppb以下にしやすいため好ましい。昇華精製とは、昇華性を有する物質の昇華及び堆積温度の差異を用いて精製する方法である。 In addition, the processing agent for filling includes a sublimation substance obtained by sublimation purification or distillation purification, a sublimation substance obtained by sublimation purification or distillation purification of a mixture of a sublimation substance and an organic solvent, and a sublimation substance obtained by sublimation purification or distillation purification in advance. And at least one selected from the group consisting of an organic solvent previously distilled and purified and 0.5 μm in particle measurement by a light scattering submerged particle detector in the liquid phase of the treatment agent When the treatment agent is melted by heating to obtain a filling melt, the number of larger particles is reduced to 100 or less per 1 ml of the melt, so that Na, Mg, K, Ca, Mn, Fe in the treatment agent are reduced. And it is preferable because the metal impurity content of each element of Cu and Cu is easily set to 100 mass ppb or less with respect to the total amount of the treatment agent. Sublimation purification is a method of purification using differences in sublimation and deposition temperatures of substances having sublimation properties.
また、前記昇華性物質は、ナフタレン、パラジクロロベンゼン、テトラクロロジフルオロエタン、樟脳、及びアルキルアミンの炭酸塩からなる群から選ばれる少なくとも1種の物質であることが好ましい。 The sublimable substance is preferably at least one substance selected from the group consisting of naphthalene, paradichlorobenzene, tetrachlorodifluoroethane, camphor, and alkylamine carbonate.
また、前記冷却析出工程において、融液を、大気圧下で放冷すること、加圧下で放冷すること、及び、前記ウェハにおいて凹凸パターンを形成していない部分に冷却剤を接触させること、からなる群から選ばれる少なくとも1つの方法により冷却することが好ましい。 Further, in the cooling precipitation step, the melt is allowed to cool under atmospheric pressure, allowed to cool under pressure, and a coolant is brought into contact with a portion where the uneven pattern is not formed on the wafer. It is preferable to cool by at least one method selected from the group consisting of:
なお、前記冷却析出工程において、凹部に固体の昇華性物質を析出させた際に、該凹部に固体の昇華性物質とともに有機溶媒が存在する場合は、該有機溶媒を蒸発させてから昇華除去工程を行うことが好ましい。凹部が固体の昇華性物質で充填されて保護されているので、前記有機溶媒が蒸発する際の毛細管力の影響が抑制されるためである。 In the cooling precipitation step, when a solid sublimable substance is deposited in the concave portion, if the organic solvent is present together with the solid sublimable substance in the concave portion, the organic solvent is evaporated and then the sublimation removing step. It is preferable to carry out. This is because the concave portion is filled and protected with a solid sublimable substance, so that the influence of capillary force when the organic solvent evaporates is suppressed.
また、前記昇華除去工程において、固体の昇華性物質を、大気圧下で室温〜昇華性物質の融点未満の温度で昇華させること、または、減圧下で室温〜昇華性物質の融点未満の温度で昇華させることが好ましい。 Further, in the sublimation removing step, the solid sublimable substance is sublimated at a temperature below room temperature to the melting point of the sublimable substance under atmospheric pressure, or at a temperature below the melting point of the sublimable substance under reduced pressure. Sublimation is preferred.
また、本発明は、上記のいずれかに記載のウェハの洗浄方法で用いる昇華性物質を含む充填用処理剤である。 Moreover, this invention is a processing agent for a filling containing the sublimable substance used with the cleaning method of the wafer in any one of said.
前記充填用処理剤は、昇華性物質を60質量%以上、有機溶媒を40質量%以下含有するものであってもよい。ウェハの凹部を昇華性物質で充分に充填する観点や、含有する有機溶媒によりウェハの凹部に作用する恐れがある毛細管力を低減する観点から、前記充填用処理剤は、昇華性物質を95質量%以上、有機溶媒を5質量%以下含有するものであることがより好ましい。また、ウェハの凹部を昇華性物質で充分に充填する観点や、ウェハの凹部に毛細管力を作用させない観点から、前記充填用処理剤は昇華性物質からなるものであってもよい。 The filling agent may contain 60% by mass or more of a sublimable substance and 40% by mass or less of an organic solvent. From the viewpoint of sufficiently filling the concave portion of the wafer with the sublimable substance and reducing the capillary force that may act on the concave portion of the wafer by the organic solvent contained, the filling treatment agent contains 95 mass of the sublimable substance. More preferably, the organic solvent is contained in an amount of 5% by mass or less. In addition, the filling treatment agent may be made of a sublimable substance from the viewpoint of sufficiently filling the concave portion of the wafer with the sublimable substance and preventing the capillary force from acting on the concave portion of the wafer.
また、前記充填用処理剤中の前記有機溶媒は、前記充填用融液の温度よりも沸点が高い有機溶媒であることが好ましい。 Moreover, it is preferable that the said organic solvent in the said processing agent for a filling is an organic solvent whose boiling point is higher than the temperature of the said melt for filling.
また、前記充填用処理剤中の、液相での光散乱式液中粒子検出器によるパーティクル測定における0.5μmより大きい粒子の数は該処理剤を加熱により融解させて充填用融液とした際に該融液1mL当たり100個以下であり、Na、Mg、K、Ca、Mn、Fe及びCuの各元素の金属不純物含有量は、該充填用処理剤総量に対し各100質量ppb以下であることが好ましい。 In addition, the number of particles larger than 0.5 μm in the particle measurement by the light scattering type submerged particle detector in the liquid phase in the filling treatment agent was melted by heating to obtain a filling melt. The amount of metal impurities of each element of Na, Mg, K, Ca, Mn, Fe and Cu is 100 mass ppb or less with respect to the total amount of the treating agent for filling. Preferably there is.
また、前記充填用処理剤は、昇華性物質を昇華精製または蒸留精製したもの、昇華性物質と有機溶媒の混合物を昇華精製または蒸留精製したもの、及び、予め昇華精製または蒸留精製した昇華性物質と予め蒸留精製した有機溶媒とを混合したもの、からなる群から選ばれる少なくとも1つであることが好ましい。 In addition, the processing agent for filling includes a sublimation substance obtained by sublimation purification or distillation purification, a sublimation substance obtained by sublimation purification or distillation purification of a mixture of a sublimation substance and an organic solvent, and a sublimation substance obtained by sublimation purification or distillation purification in advance. And at least one selected from the group consisting of a mixture of an organic solvent purified by distillation in advance.
また、前記昇華性物質は、ナフタレン、パラジクロロベンゼン、テトラクロロジフルオロエタン、樟脳、及びアルキルアミンの炭酸塩からなる群から選ばれる少なくとも1種の物質であることが好ましい。 The sublimable substance is preferably at least one substance selected from the group consisting of naphthalene, paradichlorobenzene, tetrachlorodifluoroethane, camphor, and alkylamine carbonate.
本発明のウェハの洗浄方法は、表面に凹凸パターンを有するウェハの凹部に残留する洗浄液を、昇華性物質を含む充填用処理剤を加熱により融解した充填用融液で置換し、充填した後、冷却により固体の昇華性物質を析出させ、固体の昇華性物質を昇華により除去する方法であり、特別な装置や特殊な条件を必要とすることなしに、凹部から洗浄液等の液体を乾燥除去する際に作用するような毛細管力の影響を抑制することができ、ひいては、パターン倒れを低減する効果を奏する。また、前記充填用融液が、含有する昇華性物質の融点以上、融点+25℃以下の温度範囲内で充填用処理剤を融解させた融液であることにより、融液中で気泡が発生し難くなり、その結果、毛細管力の作用を抑制しつつ充填することができる。 In the wafer cleaning method of the present invention, the cleaning liquid remaining in the concave portion of the wafer having a concavo-convex pattern on the surface is replaced with a filling melt obtained by melting a filling treatment agent containing a sublimation substance by heating, and after filling, This is a method in which a solid sublimable substance is precipitated by cooling and the solid sublimable substance is removed by sublimation, and the liquid such as the cleaning liquid is dried and removed from the recess without requiring special equipment or special conditions. It is possible to suppress the influence of the capillary force acting at the time, and as a result, there is an effect of reducing the pattern collapse. In addition, since the filling melt is a melt in which the filling treatment agent is melted within a temperature range of the melting point of the sublimable substance to be contained and the melting point + 25 ° C. or less, bubbles are generated in the melt. As a result, it can be filled while suppressing the action of capillary force.
以下、本発明について詳しく説明する。本発明の実施形態に係るウェハの好適な洗浄方法は、
表面に凹凸パターンを形成したウェハの該表面を洗浄液で洗浄する、洗浄工程、
洗浄工程後の前記ウェハの凹部に残留する洗浄液を、昇華性物質を含む充填用処理剤を加熱により融解した充填用融液で置換し、充填する、融液充填工程、
前記凹部に充填された前記融液を冷却することにより固体の昇華性物質を析出させる、冷却析出工程、
前記凹部に析出した固体の昇華性物質を昇華により除去する、昇華除去工程
を有する。
The present invention will be described in detail below. A preferred method for cleaning a wafer according to an embodiment of the present invention is as follows:
A cleaning step of cleaning the surface of the wafer having a concavo-convex pattern on the surface with a cleaning liquid;
A melt filling process, in which the cleaning liquid remaining in the recesses of the wafer after the cleaning process is replaced with a filling melt obtained by melting a filling processing agent containing a sublimation substance by heating, and filling.
A cooling precipitation step of precipitating a solid sublimable material by cooling the melt filled in the recess,
A sublimation removing step of removing the solid sublimable substance deposited in the concave portion by sublimation;
ウェハ表面に形成される凹凸パターンを、図1及び図2に模式的に示す。図1は、表面が凹凸パターン2を有する面とされたウェハ1を斜視したときの模式図を示し、図2は、図1中のa−a’断面の一部のパターンの凸部3と凹部4を示したものである。パターンの凹部の幅5は、図2に示すようにパターンの凸部3と凸部3の間隔で示され、「線幅」ともいう。凸部3のアスペクト比は、凸部3の高さ6を凸部の幅7で割ったもので表される。さらには、凹凸パターンの形状はDRAM等に使用されるシリンダータイプのものであってもよい。 The uneven pattern formed on the wafer surface is schematically shown in FIGS. FIG. 1 is a schematic view of a wafer 1 whose surface is a surface having a concavo-convex pattern 2, and FIG. 2 is a partial pattern of a convex portion 3 of a cross-section aa ′ in FIG. The recessed part 4 is shown. The width 5 of the concave portion of the pattern is indicated by the interval between the convex portion 3 and the convex portion 3 of the pattern as shown in FIG. 2, and is also referred to as “line width”. The aspect ratio of the convex portion 3 is expressed by dividing the height 6 of the convex portion 3 by the width 7 of the convex portion. Furthermore, the shape of the concavo-convex pattern may be a cylinder type used in a DRAM or the like.
本発明の洗浄方法のようなパターン倒れを考慮した洗浄方法がなされていない場合、洗浄工程でのパターン倒れは、凹部4の幅5が70nm以下、特には45nm以下、アスペクト比が4以上、特には6以上のときに生じやすくなる。また、上記の範囲から外れるものであっても、凸部の中に脆弱な箇所を有するようなパターン形状の場合、当該箇所に毛細管力が作用してパターン倒れが発生する恐れがある。 When the cleaning method considering the pattern collapse as in the cleaning method of the present invention is not performed, the pattern collapse in the cleaning process is such that the width 5 of the recess 4 is 70 nm or less, particularly 45 nm or less, and the aspect ratio is 4 or more. Tends to occur when the number is 6 or more. Moreover, even if the pattern is out of the above range, in the case of a pattern shape having a fragile portion in the convex portion, there is a possibility that the collapse of the pattern occurs due to the capillary force acting on the portion.
ウェハ表面に凹凸パターンを形成する方法の一例を以下に示す。まず、ウェハ表面にレジストを塗布したのち、レジストマスクを介してレジストに露光し、露光されたレジスト、または、露光されなかったレジストをエッチング除去することによって所望の凹凸パターンを有するレジストを作製する。また、レジストにパターンを有するモールドを押し当てることでも、凹凸パターンを有するレジストを得ることができる。次に、ウェハをエッチングする。このとき、レジストパターンの凹の部分が選択的にエッチングされる。最後に、レジストを剥離すると、表面に凹凸パターンを有するウェハが得られる。 An example of a method for forming an uneven pattern on the wafer surface is shown below. First, after applying a resist to the wafer surface, the resist is exposed through a resist mask, and the exposed resist or the resist that has not been exposed is removed by etching to produce a resist having a desired concavo-convex pattern. Moreover, the resist which has an uneven | corrugated pattern can be obtained also by pressing the mold which has a pattern to a resist. Next, the wafer is etched. At this time, the concave portion of the resist pattern is selectively etched. Finally, when the resist is removed, a wafer having a concavo-convex pattern on the surface is obtained.
本発明の洗浄方法で用いる凹凸パターンが形成されたウェハ、及び凹凸パターンの材質については特に問わず、ウェハとしては、シリコンウェハ、シリコンカーバイドウェハ、シリコン元素を含む複数の成分から構成されたウェハ、サファイアウェハ、各種化合物半導体ウェハ、プラスチックウェハなど各種のウェハを用いることができる。また、凹凸パターンの材質についても、酸化ケイ素、窒化ケイ素、多結晶シリコン、単結晶シリコンなどのシリコン系材料、窒化チタン、タングステン、ルテニウム、窒化タンタル、スズなどメタル系材料、及びそれぞれを組み合わせた材料を用いることができる。 Regardless of the material of the concavo-convex pattern used in the cleaning method of the present invention and the concavo-convex pattern, as a wafer, as the wafer, a silicon wafer, a silicon carbide wafer, a wafer composed of a plurality of components containing silicon element, Various wafers such as sapphire wafers, various compound semiconductor wafers, and plastic wafers can be used. In addition, as for the material of the concavo-convex pattern, silicon-based materials such as silicon oxide, silicon nitride, polycrystalline silicon, and single-crystal silicon, metal-based materials such as titanium nitride, tungsten, ruthenium, tantalum nitride, and tin, and combinations of these materials Can be used.
洗浄工程においてウェハの洗浄方式は特に限定されない。ウェハの洗浄方式としては、ウェハをほぼ水平に保持して回転させながら回転中心付近に洗浄液を供給してウェハを1枚ずつ洗浄するスピン洗浄に代表される枚葉方式や、洗浄槽内で複数枚のウェハを浸漬し洗浄するバッチ方式が挙げられる。なお、ウェハの凹凸パターン表面に洗浄液を供給するときの該洗浄液の形態としては、該凹凸パターン表面に保持された時に液体になるものであれば特に限定されず、たとえば、液体、蒸気などがある。 In the cleaning process, the wafer cleaning method is not particularly limited. As a wafer cleaning method, a wafer cleaning method represented by spin cleaning, in which a wafer is cleaned one by one by supplying a cleaning liquid near the rotation center while rotating the wafer while holding the wafer substantially horizontal, or a plurality of cleaning methods in a cleaning tank. One example is a batch system in which a single wafer is immersed and washed. The form of the cleaning liquid when supplying the cleaning liquid to the uneven pattern surface of the wafer is not particularly limited as long as it becomes liquid when held on the uneven pattern surface, and examples thereof include liquid and vapor. .
洗浄工程における洗浄液とは、水を主成分とする水系洗浄液又は水系洗浄液とは異なる洗浄液Aの少なくとも1つである。前記洗浄液Aとは、有機溶媒又は水系洗浄液と有機溶媒の混合物である。また、凹凸パターンを形成したウェハ表面を、水系洗浄液で洗浄した後に、水系洗浄液を洗浄液Aで置換してもよい。特に、後工程における充填用融液との置換性を考慮すると、有機溶媒からなる洗浄液Aを用いることが特に好ましい。 The cleaning liquid in the cleaning step is at least one of an aqueous cleaning liquid mainly containing water or a cleaning liquid A different from the aqueous cleaning liquid. The cleaning liquid A is an organic solvent or a mixture of an aqueous cleaning liquid and an organic solvent. In addition, the aqueous cleaning liquid may be replaced with the cleaning liquid A after the wafer surface on which the concavo-convex pattern is formed is cleaned with the aqueous cleaning liquid. In particular, it is particularly preferable to use the cleaning liquid A made of an organic solvent in consideration of the substitution with the filling melt in the subsequent step.
前記水系洗浄液の例としては、純水、又は水に有機溶媒、酸、アルカリ、界面活性剤、過酸化水素、オゾンのうち少なくとも1種が混合された水を主成分(例えば、水の含有率が50質量%以上)とする液体が挙げられる。 Examples of the water-based cleaning liquid include pure water or water in which at least one of organic solvents, acids, alkalis, surfactants, hydrogen peroxide, and ozone is mixed in water as a main component (for example, water content rate). Is 50% by mass or more).
前記洗浄液Aとして用いられることのある有機溶媒は特に限定されないが、炭化水素類、エステル類、エーテル類、ケトン類、含ハロゲン溶媒、スルホキシド系溶媒、アルコール類、多価アルコール類、多価アルコールの誘導体、含窒素化合物溶媒等が挙げられる。 The organic solvent that may be used as the cleaning liquid A is not particularly limited, but hydrocarbons, esters, ethers, ketones, halogen-containing solvents, sulfoxide solvents, alcohols, polyhydric alcohols, polyhydric alcohols. Examples thereof include derivatives and nitrogen-containing compound solvents.
前記炭化水素類の例としては、トルエン、ベンゼン、キシレン、ヘキサン、ヘプタン、オクタンなどがあり、前記エステル類の例としては、酢酸エチル、酢酸プロピル、酢酸ブチル、アセト酢酸エチルなどがあり、前記エーテル類の例としては、ジエチルエーテル、ジプロピルエーテル、ジブチルエーテル、テトラヒドロフラン、ジオキサンなどがあり、前記ケトン類の例としては、アセトン、アセチルアセトン、メチルエチルケトン、メチルプロピルケトン、メチルブチルケトン、シクロヘキサノン、イソホロンなどがあり、前記含ハロゲン溶媒の例としては、パーフルオロオクタン、パーフルオロノナン、パーフルオロシクロペンタン、パーフルオロシクロヘキサン、ヘキサフルオロベンゼンなどのパーフルオロカーボン、1,1,1,3,3−ペンタフルオロブタン、オクタフルオロシクロペンタン、2,3−ジハイドロデカフルオロペンタン、ゼオローラH(日本ゼオン製)などのハイドロフルオロカーボン、メチルパーフルオロイソブチルエーテル、メチルパーフルオロブチルエーテル、エチルパーフルオロブチルエーテル、エチルパーフルオロイソブチルエーテル、アサヒクリンAE−3000(旭硝子製)、Novec HFE−7100、Novec HFE−7200、Novec7300、Novec7600(いずれも3M製)などのハイドロフルオロエーテル、テトラクロロメタンなどのクロロカーボン、クロロホルムなどのハイドロクロロカーボン、ジクロロジフルオロメタンなどのクロロフルオロカーボン、1,1−ジクロロ−2,2,3,3,3−ペンタフルオロプロパン、1,3−ジクロロ−1,1,2,2,3−ペンタフルオロプロパン、1−クロロ−3,3,3−トリフルオロプロペン、1,2−ジクロロ−3,3,3−トリフルオロプロペンなどのハイドロクロロフルオロカーボン、パーフルオロエーテル、パーフルオロポリエーテルなどがあり、前記スルホキシド系溶媒の例としては、ジメチルスルホキシドなどがあり、アルコール類の例としては、メタノール、エタノール、プロパノール、ブタノールなどがあり、多価アルコール類の例としては、エチレングリコール、1,3−プロパンジオールなどがあり、前記多価アルコールの誘導体の例としては、ジ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、エチレングリコールモノブチルエーテル、プロピレングリコールモノメチルエーテル、プロピレングリコールモノエチルエーテル、ジエチレングリコールモノエチルエーテルアセテート、エチレングリコールモノメチルエーテルアセテート、エチレングリコールモノブチルエーテルアセテート、プロピレングリコールモノメチルエーテルアセテート(PGMEA)、プロピレングリコールモノエチルエーテルアセテート、ジエチレングリコールジメチルエーテル、ジエチレングリコールエチルメチルエーテル、ジエチレングリコールジエチルエーテル、ジエチレングリコールジアセテート、トリエチレングリコールジメチルエーテル、エチレングリコールジアセテート、エチレングリコールジエチルエーテル、エチレングリコールジメチルエーテルなどがあり、含窒素化合物溶媒の例としては、ホルムアミド、N,N−ジメチルホルムアミド、N,N−ジメチルアセトアミド、N−メチル−2−ピロリドン、ジエチルアミン、トリエチルアミン、ピリジンなどがある。 Examples of the hydrocarbons include toluene, benzene, xylene, hexane, heptane, and octane. Examples of the esters include ethyl acetate, propyl acetate, butyl acetate, and ethyl acetoacetate, and the ether. Examples of such classes include diethyl ether, dipropyl ether, dibutyl ether, tetrahydrofuran, dioxane and the like, and examples of the ketones include acetone, acetylacetone, methyl ethyl ketone, methyl propyl ketone, methyl butyl ketone, cyclohexanone, isophorone, and the like. Examples of the halogen-containing solvent include perfluorocarbons such as perfluorooctane, perfluorononane, perfluorocyclopentane, perfluorocyclohexane, hexafluorobenzene, 1,1,1, , 3-pentafluorobutane, octafluorocyclopentane, 2,3-dihydrodecafluoropentane, hydrofluorocarbons such as Zeolora H (manufactured by Nippon Zeon), methyl perfluoroisobutyl ether, methyl perfluorobutyl ether, ethyl perfluorobutyl ether, Hydrofluoroethers such as ethyl perfluoroisobutyl ether, Asahiklin AE-3000 (manufactured by Asahi Glass), Novec HFE-7100, Novec HFE-7200, Novec 7300, and Novec 7600 (all from 3M), chlorocarbons such as tetrachloromethane, chloroform Hydrochlorocarbons such as chlorofluorocarbons such as dichlorodifluoromethane, 1,1-dichloro-2,2,3,3,3-pe Tafluoropropane, 1,3-dichloro-1,1,2,2,3-pentafluoropropane, 1-chloro-3,3,3-trifluoropropene, 1,2-dichloro-3,3,3- There are hydrochlorofluorocarbons such as trifluoropropene, perfluoroethers, perfluoropolyethers, etc. Examples of the sulfoxide solvents include dimethyl sulfoxide, and examples of alcohols include methanol, ethanol, propanol, butanol. Examples of polyhydric alcohols include ethylene glycol and 1,3-propanediol, and examples of the polyhydric alcohol derivatives include diethylene glycol monoethyl ether, ethylene glycol monomethyl ether, ethylene glycol mono Butyl A Propylene glycol monomethyl ether, propylene glycol monoethyl ether, diethylene glycol monoethyl ether acetate, ethylene glycol monomethyl ether acetate, ethylene glycol monobutyl ether acetate, propylene glycol monomethyl ether acetate (PGMEA), propylene glycol monoethyl ether acetate, diethylene glycol dimethyl ether, Diethylene glycol ethyl methyl ether, diethylene glycol diethyl ether, diethylene glycol diacetate, triethylene glycol dimethyl ether, ethylene glycol diacetate, ethylene glycol diethyl ether, ethylene glycol dimethyl ether, etc., nitrogen-containing compound solvents Examples of are formamide, N, N-dimethylformamide, N, N-dimethylacetamide, N-methyl-2-pyrrolidone, diethylamine, triethylamine, pyridine and the like.
上記の有機溶媒からなる洗浄液Aの中でも、本発明の融液充填工程における充填用融液の温度よりも沸点が高い有機溶媒であると、充填用融液との置換時に該有機溶媒の沸騰に由来する気泡が発生し難くなり、その結果、該気泡による毛細管力の作用を抑制しやすいため、特に好ましい。ただし、前記有機溶媒の沸点が特に高いものは粘度が高い傾向があり、その結果、充填用融液との置換がし難くなる傾向があるため、前記有機溶媒の沸点の上限は250℃が特に好ましい。また、後工程で用いる充填用融液に対して溶解性を有するものであると、凹部に残留した洗浄液Aが該凹部に流入してきた充填用融液と相分離することなく、該融液中に溶解し取り込まれることでより効率的に置換を行うことができるため好ましい。なお、充填用融液に対して溶解性を有するとは、融液充填工程における融液の温度において、該融液に対して洗浄液Aが任意の濃度で相分離することなく溶け合うことを意味する。上記の好適な有機溶媒は、用いる昇華性物質によって異なるが、例えば、昇華性物質としてナフタレンを用いた場合、該有機溶媒といては、シクロヘキサノン、ジ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、エチレングリコールモノブチルエーテル、プロピレングリコールモノメチルエーテル、プロピレングリコールモノエチルエーテル、ジエチレングリコールモノエチルエーテルアセテート、エチレングリコールモノメチルエーテルアセテート、エチレングリコールモノブチルエーテルアセテート、プロピレングリコールモノメチルエーテルアセテート(PGMEA)、プロピレングリコールモノエチルエーテルアセテート、ジエチレングリコールジメチルエーテル、ジエチレングリコールエチルメチルエーテル、ジエチレングリコールジエチルエーテル、ジエチレングリコールジアセテート、トリエチレングリコールジメチルエーテル、エチレングリコールジアセテート、エチレングリコールジエチルエーテル、エチレングリコールジメチルエーテル等が挙げられる。 Among the cleaning liquid A composed of the above organic solvent, if the organic solvent has a boiling point higher than the temperature of the filling melt in the melt filling step of the present invention, the organic solvent will boil at the time of replacement with the filling melt. Since the bubble which originates becomes difficult to generate | occur | produce and it becomes easy to suppress the effect | action of capillary force by this bubble as a result, it is especially preferable. However, those having a particularly high boiling point of the organic solvent tend to have a high viscosity, and as a result, the replacement with the filling melt tends to be difficult. Therefore, the upper limit of the boiling point of the organic solvent is particularly 250 ° C. preferable. In addition, if it has solubility in the filling melt used in the subsequent step, the cleaning liquid A remaining in the recesses does not phase separate from the filling melt that has flowed into the recesses. It is preferable because it can be more efficiently substituted by being dissolved in and incorporated into the solution. In addition, having solubility in the filling melt means that the cleaning liquid A is melted in the melt at any concentration without phase separation at the melt temperature in the melt filling step. . The preferred organic solvent varies depending on the sublimation substance used. For example, when naphthalene is used as the sublimation substance, the organic solvent includes cyclohexanone, diethylene glycol monoethyl ether, ethylene glycol monomethyl ether, ethylene glycol monoester. Butyl ether, propylene glycol monomethyl ether, propylene glycol monoethyl ether, diethylene glycol monoethyl ether acetate, ethylene glycol monomethyl ether acetate, ethylene glycol monobutyl ether acetate, propylene glycol monomethyl ether acetate (PGMEA), propylene glycol monoethyl ether acetate, diethylene glycol dimethyl ether, Diethylene glycol ethyl ester Ether, diethylene glycol diethyl ether, diethylene glycol diacetate, triethylene glycol dimethyl ether, ethylene glycol diacetate, ethylene glycol diethyl ether, ethylene glycol dimethyl ether.
融液充填工程においては、前記ウェハの凹部に残留する洗浄液を、昇華性物質を含む充填用処理剤を加熱により融解した充填用融液で置換し、充填する。融液充填工程においてウェハ表面に充填用融液を供給する方式は特に限定されない。充填用融液の供給方式としては、ウェハをほぼ水平に保持して回転させながら回転中心付近に充填用融液を供給してウェハの凹凸パターンを1枚ずつ置換・充填処理するスピン方式に代表される枚葉方式や、充填用融液槽内に複数枚のウェハを浸漬しウェハの凹凸パターンを置換・充填処理するバッチ方式が挙げられる。図3に、充填用融液8で凹凸パターンの凹部4が充填された様子を示す。 In the melt filling step, the cleaning liquid remaining in the concave portion of the wafer is replaced with a filling melt obtained by melting a filling processing agent containing a sublimable substance by heating. The method for supplying the filling melt to the wafer surface in the melt filling step is not particularly limited. Typical filling melt supply method is a spin method in which the filling melt is supplied near the center of rotation while holding and rotating the wafer almost horizontally to replace and fill the wafer uneven pattern one by one. And a batch system in which a plurality of wafers are immersed in a filling melt tank to replace and fill the concavo-convex pattern of the wafers. FIG. 3 shows a state in which the concave / convex pattern 4 is filled with the filling melt 8.
充填用処理剤に含まれる昇華性物質は、昇華性を持つものであれば種類については特に問われず、常圧で加熱した場合に固体から液体を経ずに気体となる昇華点をもつ物質、および常圧で加熱した場合に固体から液体を経て気体となる物質で、融点をもち、融点未満で緩やかに昇華する物質の両方を指している。しかし、本発明の充填用融液を用いる洗浄方法では、充填用融液の作製を考慮すると、固体から液体を経て気体となる物質で、融点をもち、融点未満で緩やかに昇華する物質を用いることがより好ましい。これらの特性を持つ昇華性物質としてナフタレン、パラジクロロベンゼン、テトラクロロジフルオロエタン、樟脳、及びアルキルアミンの炭酸塩などが挙げられる。昇華性物質は、それぞれの材料の融点以上で加熱することで融解した充填用融液とすることができる。昇華性物質が常圧で融点を持たず、加熱すると昇華する場合、加圧することで融液とすることが可能である。 The sublimation substance contained in the processing agent for filling is not particularly limited as long as it has sublimability, and a substance having a sublimation point that becomes a gas from a solid to a liquid when heated at normal pressure, In addition, it refers to both a substance that becomes a gas from a solid through a liquid when heated at normal pressure, has a melting point, and gradually sublimates below the melting point. However, in the cleaning method using the filling melt of the present invention, considering the preparation of the filling melt, a substance that becomes a gas from a solid through a liquid, has a melting point, and uses a substance that gradually sublimates below the melting point. It is more preferable. Examples of sublimable substances having these properties include naphthalene, paradichlorobenzene, tetrachlorodifluoroethane, camphor, and alkylamine carbonates. The sublimable substance can be used as a filling melt melted by heating at a temperature equal to or higher than the melting point of each material. When a sublimable substance does not have a melting point at normal pressure and sublimates when heated, it can be melted by pressurization.
また、充填用融液は、含有する昇華性物質の融点以上、融点+25℃以下の温度範囲内で充填用処理剤を融解させた融液である。昇華性物質の融点未満の温度では、融液、すなわち液体とすることが難しい。一方、(融点+25℃)を超える温度では、昇華性物質の蒸発により、融液内で気泡の発生が多くなる。凹部において気泡が発生すると、該凹部に毛細管力が働くため、パターンの倒壊に繋がる。さらには、(融点+25℃)を超える温度では、昇華性物質の蒸発が早すぎるため、後工程の冷却工程において、ウェハ表面の融液を冷却する間も、融液からの昇華性物質の蒸発が継続し易く、その結果、析出した固体状の昇華性物質で充填できないウェハ表面が発生する。 The filling melt is a melt obtained by melting the filling treatment agent in a temperature range of the melting point of the sublimable substance to be contained and the melting point + 25 ° C. or less. At a temperature below the melting point of the sublimable substance, it is difficult to form a melt, that is, a liquid. On the other hand, at a temperature exceeding (melting point + 25 ° C.), the generation of bubbles in the melt increases due to evaporation of the sublimable substance. When bubbles are generated in the recess, a capillary force acts on the recess, leading to a collapse of the pattern. Furthermore, at temperatures exceeding (melting point + 25 ° C.), the sublimable substance evaporates too early, so that the sublimable substance evaporates from the melt while the wafer surface melt is cooled in the subsequent cooling step. As a result, a wafer surface that cannot be filled with the deposited solid sublimable substance is generated.
前記充填用処理剤は、融液にした際のレベリング性を向上する目的で有機溶媒を含んでいても良い。ただし、有機溶媒量が多すぎると、冷却析出工程において昇華性物質が析出する際に、蒸発する有機溶媒の毛細管力でパターンの倒壊が発生しやすいため好ましくない。また、有機溶媒の含有量が多いほど冷却析出工程で析出する固体がポーラスとなったり析出する固体が少なくなったりし易いため、本発明の目的であるパターンの倒れ防止効果が低くなる恐れがある。これらを考慮すると、有機溶媒量は少ないことが好ましく、充填用処理剤に含まれる昇華性物質量は60質量%以上が好ましく、さらに好ましくは95質量%以上である。 The filling treatment agent may contain an organic solvent for the purpose of improving the leveling property when it is made into a melt. However, when the amount of the organic solvent is too large, it is not preferable because the pattern collapse is likely to occur due to the capillary force of the organic solvent that evaporates when the sublimable substance is deposited in the cooling deposition step. In addition, the higher the content of the organic solvent, the more likely the solid deposited in the cooling deposition step becomes porous or the less deposited solid, so that the effect of preventing pattern collapse that is the object of the present invention may be reduced. . Considering these, the amount of the organic solvent is preferably small, and the amount of the sublimable substance contained in the filling treatment agent is preferably 60% by mass or more, and more preferably 95% by mass or more.
また、前記有機溶媒の種類は特に限定されないが、炭化水素類、エステル類、エーテル類、ケトン類、含ハロゲン溶媒、スルホキシド系溶媒、アルコール類、多価アルコール類、多価アルコールの誘導体、含窒素化合物溶媒等が挙げられる。 The type of the organic solvent is not particularly limited, but hydrocarbons, esters, ethers, ketones, halogen-containing solvents, sulfoxide solvents, alcohols, polyhydric alcohols, polyhydric alcohol derivatives, nitrogen-containing compounds A compound solvent etc. are mentioned.
前記炭化水素類の例としては、トルエン、ベンゼン、キシレン、ヘキサン、ヘプタン、オクタンなどがあり、前記エステル類の例としては、酢酸エチル、酢酸プロピル、酢酸ブチル、アセト酢酸エチルなどがあり、前記エーテル類の例としては、ジエチルエーテル、ジプロピルエーテル、ジブチルエーテル、テトラヒドロフラン、ジオキサンなどがあり、前記ケトン類の例としては、アセトン、アセチルアセトン、メチルエチルケトン、メチルプロピルケトン、メチルブチルケトン、シクロヘキサノン、イソホロンなどがあり、前記含ハロゲン溶媒の例としては、パーフルオロオクタン、パーフルオロノナン、パーフルオロシクロペンタン、パーフルオロシクロヘキサン、ヘキサフルオロベンゼンなどのパーフルオロカーボン、1,1,1,3,3−ペンタフルオロブタン、オクタフルオロシクロペンタン、2,3−ジハイドロデカフルオロペンタン、ゼオローラH(日本ゼオン製)などのハイドロフルオロカーボン、メチルパーフルオロイソブチルエーテル、メチルパーフルオロブチルエーテル、エチルパーフルオロブチルエーテル、エチルパーフルオロイソブチルエーテル、アサヒクリンAE−3000(旭硝子製)、Novec HFE−7100、Novec HFE−7200、Novec7300、Novec7600(いずれも3M製)などのハイドロフルオロエーテル、テトラクロロメタンなどのクロロカーボン、クロロホルムなどのハイドロクロロカーボン、ジクロロジフルオロメタンなどのクロロフルオロカーボン、1,1−ジクロロ−2,2,3,3,3−ペンタフルオロプロパン、1,3−ジクロロ−1,1,2,2,3−ペンタフルオロプロパン、1−クロロ−3,3,3−トリフルオロプロペン、1,2−ジクロロ−3,3,3−トリフルオロプロペンなどのハイドロクロロフルオロカーボン、パーフルオロエーテル、パーフルオロポリエーテルなどがあり、前記スルホキシド系溶媒の例としては、ジメチルスルホキシドなどがあり、アルコール類の例としては、メタノール、エタノール、プロパノール、ブタノールなどがあり、多価アルコール類の例としては、エチレングリコール、1,3−プロパンジオールなどがあり、前記多価アルコールの誘導体の例としては、ジ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、エチレングリコールモノブチルエーテル、プロピレングリコールモノメチルエーテル、プロピレングリコールモノエチルエーテル、ジエチレングリコールモノエチルエーテルアセテート、エチレングリコールモノメチルエーテルアセテート、エチレングリコールモノブチルエーテルアセテート、プロピレングリコールモノメチルエーテルアセテート、プロピレングリコールモノエチルエーテルアセテート、ジエチレングリコールジメチルエーテル、ジエチレングリコールエチルメチルエーテル、ジエチレングリコールジエチルエーテル、ジエチレングリコールジアセテート、トリエチレングリコールジメチルエーテル、エチレングリコールジアセテート、エチレングリコールジエチルエーテル、エチレングリコールジメチルエーテルなどがあり、含窒素化合物溶媒の例としては、ホルムアミド、N,N−ジメチルホルムアミド、N,N−ジメチルアセトアミド、N−メチル−2−ピロリドン、ジエチルアミン、トリエチルアミン、ピリジンなどがある。 Examples of the hydrocarbons include toluene, benzene, xylene, hexane, heptane, and octane. Examples of the esters include ethyl acetate, propyl acetate, butyl acetate, and ethyl acetoacetate, and the ether. Examples of such classes include diethyl ether, dipropyl ether, dibutyl ether, tetrahydrofuran, dioxane and the like, and examples of the ketones include acetone, acetylacetone, methyl ethyl ketone, methyl propyl ketone, methyl butyl ketone, cyclohexanone, isophorone, and the like. Examples of the halogen-containing solvent include perfluorocarbons such as perfluorooctane, perfluorononane, perfluorocyclopentane, perfluorocyclohexane, hexafluorobenzene, 1,1,1, , 3-pentafluorobutane, octafluorocyclopentane, 2,3-dihydrodecafluoropentane, hydrofluorocarbons such as Zeolora H (manufactured by Nippon Zeon), methyl perfluoroisobutyl ether, methyl perfluorobutyl ether, ethyl perfluorobutyl ether, Hydrofluoroethers such as ethyl perfluoroisobutyl ether, Asahiklin AE-3000 (manufactured by Asahi Glass), Novec HFE-7100, Novec HFE-7200, Novec 7300, and Novec 7600 (all from 3M), chlorocarbons such as tetrachloromethane, chloroform Hydrochlorocarbons such as chlorofluorocarbons such as dichlorodifluoromethane, 1,1-dichloro-2,2,3,3,3-pe Tafluoropropane, 1,3-dichloro-1,1,2,2,3-pentafluoropropane, 1-chloro-3,3,3-trifluoropropene, 1,2-dichloro-3,3,3- There are hydrochlorofluorocarbons such as trifluoropropene, perfluoroethers, perfluoropolyethers, etc. Examples of the sulfoxide solvents include dimethyl sulfoxide, and examples of alcohols include methanol, ethanol, propanol, butanol. Examples of polyhydric alcohols include ethylene glycol and 1,3-propanediol, and examples of the polyhydric alcohol derivatives include diethylene glycol monoethyl ether, ethylene glycol monomethyl ether, ethylene glycol mono Butyl A , Propylene glycol monomethyl ether, propylene glycol monoethyl ether, diethylene glycol monoethyl ether acetate, ethylene glycol monomethyl ether acetate, ethylene glycol monobutyl ether acetate, propylene glycol monomethyl ether acetate, propylene glycol monoethyl ether acetate, diethylene glycol dimethyl ether, diethylene glycol ethyl methyl There are ether, diethylene glycol diethyl ether, diethylene glycol diacetate, triethylene glycol dimethyl ether, ethylene glycol diacetate, ethylene glycol diethyl ether, ethylene glycol dimethyl ether, etc. Examples include formamide, N, N-dimethylformamide, N, N-dimethylacetamide, N-methyl-2-pyrrolidone, diethylamine, triethylamine, and pyridine.
上記の有機溶媒の中でも、本発明の融液充填工程における充填用融液の温度よりも沸点が高い有機溶媒であると、洗浄液との置換時及び充填時に該有機溶媒の沸騰に由来する気泡が発生し難くなり、その結果、該気泡による毛細管力の作用を抑制しやすいため、特に好ましい。 Among the above organic solvents, when the boiling point is higher than the temperature of the filling melt in the melt filling step of the present invention, bubbles derived from boiling of the organic solvent at the time of replacement with the cleaning liquid and filling Since it becomes difficult to generate | occur | produce and it becomes easy to suppress the effect | action of the capillary force by this bubble as a result, it is especially preferable.
その後、冷却析出工程において、前記凹部に充填した前記融液を冷却することにより固体の昇華性物質を析出させ、凹部に固体を充填する。図4に、昇華性物質の固体9で凹部4が充填された様子を示す。この充填された固体9により、パターンの倒壊が抑えられる。この冷却は、大気圧下、あるいは加圧下で放冷してもよいし、または、前記ウェハにおいて凹凸パターンを形成していない部分に水等の冷却剤を接触させることにより冷却しても良い。 Thereafter, in the cooling precipitation step, the melt filled in the recesses is cooled to precipitate a solid sublimable substance, and the recesses are filled with the solid. FIG. 4 shows a state in which the concave portion 4 is filled with a solid 9 of a sublimable substance. The filled solid 9 suppresses pattern collapse. This cooling may be performed under atmospheric pressure or under pressure, or may be performed by bringing a coolant such as water into contact with a portion of the wafer where the uneven pattern is not formed.
最後に、昇華除去工程において、固体の昇華性物質を昇華により除去する。この場合の除去は、大気圧下で行っても良いし、減圧下で行っても良い。常圧で加熱した場合に固体から液体を経て気体となり、融点をもち、融点未満で緩やかに昇華する物質を昇華性物質として用いた場合、昇華性物質の融点以上の温度で加熱すると、大気圧下では昇華性物質が融解して液体となり、液体が揮発する際の毛細管力でパターンの倒壊が発生する恐れがある。そのため、この場合は、室温〜昇華性物質の融点未満の温度で時間を掛けて昇華させるか、又は減圧下で昇華させることが好ましい。減圧下では、大気圧下では加熱したときに融点を持つ物質でも、昇華する場合がある。 Finally, in the sublimation removal step, the solid sublimable substance is removed by sublimation. The removal in this case may be performed under atmospheric pressure or may be performed under reduced pressure. When a substance that has a melting point and gradually sublimates below the melting point is used as a sublimation substance when heated at normal pressure, it will become atmospheric pressure when heated at a temperature above the melting point of the sublimation substance. Below, the sublimable substance melts and becomes a liquid, and there is a possibility that the pattern collapses due to the capillary force when the liquid volatilizes. Therefore, in this case, it is preferable to sublime over time at a temperature from room temperature to a temperature lower than the melting point of the sublimable substance, or sublimation under reduced pressure. Under reduced pressure, a substance having a melting point when heated under atmospheric pressure may sublime.
本発明の洗浄方法は、凹凸パターンの倒壊を防止する他の既知の洗浄方法と組み合わせて、洗浄を行っても良い。特に、凹凸パターン表面に撥水性保護膜を形成する方法と組み合わせて本発明の洗浄方法を行うと、凹凸パターンの倒壊を防止する効果がより高くなるため好ましい。ウェハの凹凸パターン表面に撥水性保護膜を形成するための撥水性保護膜形成用薬液を保持することで、該凹凸パターン表面に撥水性保護膜を形成することができる。凹凸パターンの表面に撥水性の保護膜を形成した後、本発明の洗浄方法である洗浄工程を行っても良いし、洗浄工程を行った後、凹凸パターンの表面に撥水性の保護膜を形成し、その後融液充填工程に移っても良い。なお、本発明の昇華除去工程の後に、前記撥水性保護膜は、例えば、ウェハ表面を光照射すること、ウェハを加熱すること、ウェハをオゾン曝露すること、ウェハ表面にプラズマ照射すること、ウェハ表面にコロナ放電すること等の処理によって除去できる。 The cleaning method of the present invention may be cleaned in combination with other known cleaning methods that prevent collapse of the concavo-convex pattern. In particular, it is preferable to perform the cleaning method of the present invention in combination with a method of forming a water-repellent protective film on the surface of the concavo-convex pattern because the effect of preventing collapse of the concavo-convex pattern becomes higher. By holding a chemical solution for forming a water repellent protective film for forming a water repellent protective film on the uneven pattern surface of the wafer, the water repellent protective film can be formed on the uneven pattern surface. After forming a water-repellent protective film on the surface of the concavo-convex pattern, the cleaning process of the present invention may be performed, or after performing the cleaning process, a water-repellent protective film is formed on the surface of the concavo-convex pattern Then, it may be transferred to the melt filling step. In addition, after the sublimation removal process of the present invention, the water-repellent protective film is formed by, for example, irradiating the wafer surface with light, heating the wafer, exposing the wafer to ozone, irradiating the wafer surface with plasma, It can be removed by a treatment such as corona discharge on the surface.
前記撥水性保護膜形成用薬液としては、凹凸パターンの表面に撥水性の保護膜を形成することができるものであれば、該薬液に含まれる撥水性保護膜を形成する化合物(以下、「化合物A」とも記載する)の種類は特に限定されない。化合物Aの例としては、例えば凹凸パターン表面が、酸化ケイ素、窒化ケイ素、多結晶シリコン或いは単結晶シリコンといったシリコン系材料の場合、ヘキサメチルジシラザン(HMDS)、トリメチルシリルジエチルアミン(TMSDEA)、テトラメチルジシラザン、トリメチルシリルジメチルアミン、オクチルジメチルシリルジメチルアミン、トリメチルシリルイミダゾール、トリメチルクロロシラン、プロピルジメチルクロロシラン、オクチルジメチルクロロシラン、ジメチルジクロロシラン、メチルトリクロロシラン、トリメチルメトキシシラン、トリメチルエトキシシランなどのシランカップリング剤が挙げられる。また、凹凸パターン表面が前記のシリコン系材料以外の場合は、該材料の表面に結合または吸着し、凹凸パターン表面に撥水性を付与するような物質を化合物Aとして用いても良い。 As the water-repellent protective film-forming chemical, any compound that forms a water-repellent protective film contained in the chemical (hereinafter referred to as “compound”) can be used as long as it can form a water-repellent protective film on the surface of the uneven pattern. The type of A) is also not particularly limited. As an example of compound A, for example, when the uneven pattern surface is a silicon-based material such as silicon oxide, silicon nitride, polycrystalline silicon or single crystal silicon, hexamethyldisilazane (HMDS), trimethylsilyldiethylamine (TMSDEA), tetramethyldisilane Examples include silane coupling agents such as silazane, trimethylsilyldimethylamine, octyldimethylsilyldimethylamine, trimethylsilylimidazole, trimethylchlorosilane, propyldimethylchlorosilane, octyldimethylchlorosilane, dimethyldichlorosilane, methyltrichlorosilane, trimethylmethoxysilane, and trimethylethoxysilane. . Further, when the surface of the concave / convex pattern is other than the above-mentioned silicon-based material, a substance that binds or adsorbs to the surface of the material and imparts water repellency to the surface of the concave / convex pattern may be used as the compound A.
撥水性保護膜形成用薬液において希釈に用いられることのある溶媒としては、例えば、炭化水素類、エステル類、エーテル類、ケトン類、含ハロゲン溶媒、スルホキシド系溶媒、アルコール類、多価アルコールの誘導体、含窒素化合物溶媒などの有機溶媒が好適に使用される。この中でも、炭化水素類、エステル類、エーテル類、ケトン類、含ハロゲン溶媒、スルホキシド系溶媒、多価アルコールの誘導体のうちOH基を持たないものを用いると、前記凹凸パターン表面に保護膜を短時間に形成できるためより好ましい。 Examples of the solvent that may be used for dilution in the chemical solution for forming a water-repellent protective film include, for example, hydrocarbons, esters, ethers, ketones, halogen-containing solvents, sulfoxide solvents, alcohols, and polyhydric alcohol derivatives. An organic solvent such as a nitrogen-containing compound solvent is preferably used. Of these, hydrocarbons, esters, ethers, ketones, halogen-containing solvents, sulfoxide solvents, and polyhydric alcohol derivatives that do not have an OH group can be used to shorten the protective film on the surface of the concavo-convex pattern. It is more preferable because it can be formed in time.
[充填用融液、及び、融液充填工程において充填された融液の外観評価]
充填用融液の外観を目視観察し、該融液が完全に充填用処理剤を融解できているかどうか、気泡が発生していないかどうかを確認した。また、表面に凹凸パターンを有するウェハでは、融液充填工程における気泡や相分離といった不具合の有無が確認できないため、平滑なウェハ表面上で融液充填工程と同様の操作を行って、該平滑なウェハ表面上に融液が充填された状態で外観を観察し、前記不具合の有無を確認した。
[Appearance evaluation of melt for filling and melt filled in melt filling step]
The appearance of the filling melt was visually observed, and it was confirmed whether the melt was able to completely melt the filling treatment agent and whether bubbles were generated. In addition, in a wafer having a concavo-convex pattern on the surface, since there is no confirmation of defects such as bubbles or phase separation in the melt filling process, the same operation as in the melt filling process is performed on the smooth wafer surface. The appearance was observed in a state where the melt was filled on the wafer surface, and the presence or absence of the defects was confirmed.
[充填用処理剤中の0.5μmより大きい粒子の数の評価]
充填用処理剤中のパーティクルの数を直接測定することは困難なので、予め前記処理剤を加熱により融解させて充填用融液とし、該融液1mLをイソプロピルアルコールに溶解し、該溶液に対して、光散乱式液中粒子測定装置(リオン社製、KS−42AF型)を用いて0.5μmより大きい粒子の数を測定した。なお、前記イソプロピルアルコールは予め蒸留精製及び、フィルター精製を行ったものを使用した。
[Evaluation of the number of particles larger than 0.5 μm in the treating agent for filling]
Since it is difficult to directly measure the number of particles in the filling treatment agent, the treatment agent is previously melted by heating to obtain a filling melt, and 1 mL of the melt is dissolved in isopropyl alcohol. The number of particles larger than 0.5 μm was measured using a light scattering type in-liquid particle measuring device (manufactured by Rion, KS-42AF type). The isopropyl alcohol used was previously purified by distillation and filter purification.
[充填用処理剤中の金属不純物含有量の評価]
所定量の充填用処理剤から、揮発成分及び蒸発成分をすべて揮発及び蒸発させて、残った残渣をフッ硝酸に溶解させて、該溶液中の金属不純物含有量を、誘導結合プラズマ質量分析装置(横河アナリティカルシステムズ製、Agilent 7500cs型)を用いて測定し、そこから充填用処理剤中の金属不純物含有量を算出した。
[Evaluation of metal impurity content in processing agent for filling]
All the volatile components and evaporating components are volatilized and evaporated from a predetermined amount of the filling treatment agent, the remaining residue is dissolved in hydrofluoric acid, and the content of metal impurities in the solution is measured by an inductively coupled plasma mass spectrometer ( Yokogawa Analytical Systems, Inc., Agilent 7500cs type) was used, and the metal impurity content in the processing agent for filling was calculated therefrom.
[実施例1]
(I−1)充填用融液の準備
昇華性物質であるナフタレン(融点:80℃)を予め昇華精製したものを充填用処理剤とした。ビーカー中で前記充填用処理剤を85℃で融解して充填用融液槽を準備した。前記融液を目視観察したところ、発泡は見られず、均一な液体であった。なお、前記充填用処理剤中の、液相での光散乱式液中粒子検出器によるパーティクル測定における0.5μmより大きい粒子の数は、該処理剤を加熱により融解させて充填用融液とした際に該融液1mL当たり100個以下であった。また、前記処理剤中のNa、Mg、K、Ca、Mn、Fe及びCuの各元素の金属不純物含有量は、該処理剤総量に対しそれぞれ、100質量ppb以下であった。なお、本実施例以降の実施例、及び比較例においても、同様の精製を行い、0.5μmより大きい粒子の数が処理剤を加熱により融解させて充填用融液とした際に該融液1mL当たり100個以下であり、Na、Mg、K、Ca、Mn、Fe及びCuの各元素の金属不純物含有量が、該処理剤総量に対しそれぞれ100質量ppb以下であることを確認した。
[Example 1]
(I-1) Preparation of Filling Melt Naphthalene (melting point: 80 ° C.), which is a sublimation substance, was previously purified by sublimation and used as a filling treatment agent. The filling treatment agent was melted at 85 ° C. in a beaker to prepare a filling melt tank. When the melt was visually observed, no foam was observed and the melt was a uniform liquid. The number of particles larger than 0.5 μm in the particle measurement by the light scattering liquid particle detector in the liquid phase in the filling treatment agent is determined by melting the treatment agent by heating and filling the filling melt. The number was 100 or less per 1 mL of the melt. Moreover, the metal impurity content of each element of Na, Mg, K, Ca, Mn, Fe, and Cu in the treatment agent was 100 mass ppb or less with respect to the treatment agent total amount. In addition, also in the examples and comparative examples after this example, the same purification was performed, and when the number of particles larger than 0.5 μm was melted by heating the treatment agent, the melt was used as a filling melt. It was confirmed that the metal impurity content of each element of Na, Mg, K, Ca, Mn, Fe, and Cu was 100 mass ppb or less with respect to the total amount of the processing agent.
(I−2)洗浄工程
平滑な窒化チタン膜付きウェハ(表面に厚さ50nmの窒化チタン層を有するシリコンウェハ)を1質量%の過酸化水素水に室温で1分間浸漬し、次いで純水に1分間浸漬した後、イソプロピルアルコール(iPA)に室温で1分間浸漬し、次いで、沸点が146℃でナフタレンの融液に対して溶解性を有するプロピレングリコールモノメチルエーテルアセテート(PGMEA)に室温で1分間浸漬させた。
(I-2) Cleaning Step A wafer with a smooth titanium nitride film (a silicon wafer having a titanium nitride layer with a thickness of 50 nm on the surface) is immersed in 1% by mass of hydrogen peroxide at room temperature for 1 minute, and then purified water After soaking for 1 minute, soaked in isopropyl alcohol (iPA) at room temperature for 1 minute, and then in propylene glycol monomethyl ether acetate (PGMEA) having a boiling point of 146 ° C. and soluble in naphthalene melt for 1 minute at room temperature. Soaked.
(I−3)融液充填工程
(I−2)で準備した窒化チタン膜付きウェハを、PGMEA浸漬槽から充填用融液槽に移し、充填用融液に3分間浸漬させた。この際に窒化チタン膜付きウェハの表面には気泡はなく、相分離も見られなかったことから、融液充填工程において不具合が発生しないことを確認した。
(I-3) Melt filling step The wafer with the titanium nitride film prepared in (I-2) was transferred from the PGMEA immersion tank to the filling melt tank and immersed in the filling melt for 3 minutes. At this time, since there were no bubbles on the surface of the wafer with the titanium nitride film and no phase separation was observed, it was confirmed that no trouble occurred in the melt filling step.
(I−4)冷却析出工程
前記ウェハを充填用融液から引き上げて、室温で該ウェハを水平にして静置し放冷した。10分後、ウェハ表面の外観を観察したところ、目視観察でウェハ全面に均一に析出した固体状のナフタレンが付着していた。
(I-4) Cooling Precipitation Step The wafer was pulled up from the filling melt, and the wafer was left to stand at room temperature and allowed to cool. Ten minutes later, when the appearance of the wafer surface was observed, solid naphthalene deposited uniformly on the entire wafer surface was observed by visual observation.
(I−5)昇華除去工程
(I−4)で得られた固体状のナフタレンが付着したウェハを、真空オーブン中で1mmHgまで減圧したのち、80℃まで昇温したところ、ウェハ上の固体状のナフタレンはすべて昇華し、消失した。
(I-5) Sublimation removal step The wafer with the solid naphthalene obtained in (I-4) was reduced to 1 mmHg in a vacuum oven and then heated to 80 ° C. All of the naphthalene sublimated and disappeared.
[実施例2]
融液充填工程における融液の温度を90℃とした以外は、実施例1と同じ条件で実施した。充填用融液を目視観察したところ、発泡は見られず、均一な液体であった。実施例1と同様に、融液充填工程で窒化チタン膜付きウェハを充填用融液に浸漬した際に、該ウェハの表面には気泡はなく、相分離も見られなかったことから、融液充填工程において不具合が発生しないことを確認した。また、実施例1と同様に冷却析出工程を行ったところ、目視観察でウェハ全面に均一に析出した固体状のナフタレンが付着していた。また、実施例1と同様の昇華除去工程によってウェハ上の固体状のナフタレンがすべて昇華し、消失することを確認した。
[Example 2]
It implemented on the same conditions as Example 1 except the temperature of the melt in a melt filling process having been 90 degreeC. When the filling melt was visually observed, no foaming was observed and the liquid was uniform. As in Example 1, when the wafer with the titanium nitride film was immersed in the filling melt in the melt filling step, there were no bubbles on the surface of the wafer and no phase separation was observed. It was confirmed that no defects occurred in the filling process. Further, when the cooling precipitation process was performed in the same manner as in Example 1, solid naphthalene deposited uniformly on the entire wafer surface was observed by visual observation. Further, it was confirmed that all the solid naphthalene on the wafer was sublimated and disappeared by the same sublimation removing process as in Example 1.
[実施例3]
融液充填工程における融液の温度を100℃とした以外は、実施例1と同じ条件で実施した充填用融液を目視観察したところ、発泡は見られず、均一な液体であった。実施例1と同様に、融液充填工程で窒化チタン膜付きウェハを充填用融液に浸漬した際に、該ウェハの表面には気泡はなく、相分離も見られなかったことから、融液充填工程において不具合が発生しないことを確認した。また、実施例1と同様に冷却析出工程を行ったところ、目視観察でウェハ全面に析出した固体状のナフタレンが付着していたものの、一部に固体状のナフタレンの付着量が少なくまだらに見える部分があった。これは、融液の温度が高いことにより該融液の冷却に時間がかかった結果、冷却析出工程時に昇華性物質が蒸発し減少する量が多くなってしまったためと考えられる。また、実施例1と同様の昇華除去工程によってウェハ上の固体状のナフタレンがすべて昇華し、消失することを確認した。
[Example 3]
Except that the temperature of the melt in the melt filling step was set to 100 ° C., the filling melt carried out under the same conditions as in Example 1 was visually observed. As a result, foaming was not observed and the liquid was uniform. As in Example 1, when the wafer with the titanium nitride film was immersed in the filling melt in the melt filling step, there were no bubbles on the surface of the wafer and no phase separation was observed. It was confirmed that no defects occurred in the filling process. Further, when the cooling precipitation process was performed in the same manner as in Example 1, solid naphthalene deposited on the entire wafer surface was observed by visual observation, but the amount of solid naphthalene deposited was small and partially visible. There was a part. This is presumably because the temperature of the melt was high and it took a long time to cool the melt, and as a result, the amount of the sublimable substance evaporated and decreased during the cooling precipitation process increased. Further, it was confirmed that all the solid naphthalene on the wafer was sublimated and disappeared by the same sublimation removing process as in Example 1.
[実施例4]
予め昇華精製を行ったナフタレンと予め蒸留精製を行ったシクロヘキサノン(沸点は156℃)を、80:20(質量比)で混合したものを充填用処理剤とした。ビーカー中で前記充填用処理剤を85℃で融解した。この融液を目視観察したところ、発泡は見られず、均一な液体であった。前記融液を充填用融液とした以外は、実施例1と同じ条件で実施した。実施例1と同様に、融液充填工程で窒化チタン膜付きウェハを前記融液に浸漬した際に、該ウェハの表面には気泡はなく、相分離も見られなかったことから、融液充填工程において不具合が発生しないことを確認した。また、実施例1と同様に冷却析出工程を行ったところ、目視観察でウェハ全面に均一に析出した固体状のナフタレンが付着していた。また、実施例1と同様の昇華除去工程によってウェハ上の固体状のナフタレンがすべて昇華し、消失することを確認した。
[Example 4]
A mixture of naphthalene that had been purified by sublimation in advance and cyclohexanone that had been purified by distillation in advance (boiling point: 156 ° C.) at 80:20 (mass ratio) was used as a treating agent for filling. The filling agent was melted at 85 ° C. in a beaker. When this melt was visually observed, foaming was not seen and it was a uniform liquid. It implemented on the same conditions as Example 1 except having made the said melt into the melt for filling. As in Example 1, when a wafer with a titanium nitride film was immersed in the melt in the melt filling step, there were no bubbles on the surface of the wafer and no phase separation was observed. It was confirmed that no defects occurred in the process. Further, when the cooling precipitation process was performed in the same manner as in Example 1, solid naphthalene deposited uniformly on the entire wafer surface was observed by visual observation. Further, it was confirmed that all the solid naphthalene on the wafer was sublimated and disappeared by the same sublimation removing process as in Example 1.
[実施例5]
充填用処理剤の、ナフタレンとシクロヘキサノンの質量比を、55:45とした以外は、実施例4と同じ条件で実施した。充填用融液を目視観察したところ、発泡は見られず、均一な液体であった。実施例4と同様に、融液充填工程で窒化チタン膜付きウェハを前記融液に浸漬した際に、該ウェハの表面には気泡はなく、相分離も見られなかったことから、融液充填工程において不具合が発生しないことを確認した。また、実施例4と同様に冷却析出工程を行ったところ、目視観察でウェハ全面に析出した固体状のナフタレンが付着していたものの、一部に固体状のナフタレンの付着量が少なくまだらに見える部分があった。これは、充填用処理剤中の昇華性物質の含有量が少ないことにより、冷却析出工程時に融液から析出する昇華性物質が少なかったためと考えられる。また、実施例4と同様の昇華除去工程によってウェハ上の固体状のナフタレンがすべて昇華し、消失することを確認した。
[Example 5]
It implemented on the same conditions as Example 4 except the mass ratio of naphthalene and cyclohexanone of the processing agent for filling having been 55:45. When the filling melt was visually observed, no foaming was observed and the liquid was uniform. As in Example 4, when a wafer with a titanium nitride film was immersed in the melt in the melt filling step, there were no bubbles on the surface of the wafer and no phase separation was observed. It was confirmed that no defects occurred in the process. Further, when the cooling precipitation process was performed in the same manner as in Example 4, solid naphthalene deposited on the entire surface of the wafer was observed by visual observation, but the amount of solid naphthalene deposited was small and partially visible. There was a part. This is presumably because there was little sublimable substance precipitated from the melt during the cooling precipitation process due to the low content of the sublimable substance in the filling treatment agent. Further, it was confirmed that all the solid naphthalene on the wafer was sublimated and disappeared by the same sublimation removing process as in Example 4.
[実施例6]
洗浄工程として、平滑な窒化チタン膜付きウェハ(表面に厚さ50nmの窒化チタン層を有するシリコンウェハ)を1質量%の過酸化水素水に室温で1分間浸漬し、次いで純水に1分間浸漬した後、イソプロピルアルコール(iPA)に室温で1分間浸漬し、次いで、沸点が156℃でナフタレンの融液に対して溶解性を有するシクロヘキサノンに室温で1分間浸漬させた。それ以外は、実施例1と同じ条件で実施した。実施例1と同様に、融液充填工程で窒化チタン膜付きウェハを前記融液に浸漬した際に、該ウェハの表面には気泡はなく、相分離も見られなかったことから、融液充填工程において不具合が発生しないことを確認した。また、実施例1と同様に冷却析出工程を行ったところ、目視観察でウェハ全面に均一に析出した固体状のナフタレンが付着していた。また、実施例1と同様の昇華除去工程によってウェハ上の固体状のナフタレンがすべて昇華し、消失することを確認した。
[Example 6]
As a cleaning process, a wafer with a smooth titanium nitride film (a silicon wafer having a titanium nitride layer having a thickness of 50 nm on the surface) is immersed in 1% by mass of hydrogen peroxide at room temperature for 1 minute, and then immersed in pure water for 1 minute. After that, it was immersed in isopropyl alcohol (iPA) at room temperature for 1 minute, and then immersed in cyclohexanone having a boiling point of 156 ° C. and soluble in naphthalene melt for 1 minute at room temperature. The other conditions were the same as in Example 1. As in Example 1, when a wafer with a titanium nitride film was immersed in the melt in the melt filling step, there were no bubbles on the surface of the wafer and no phase separation was observed. It was confirmed that no defects occurred in the process. Further, when the cooling precipitation process was performed in the same manner as in Example 1, solid naphthalene deposited uniformly on the entire wafer surface was observed by visual observation. Further, it was confirmed that all the solid naphthalene on the wafer was sublimated and disappeared by the same sublimation removing process as in Example 1.
[実施例7]
洗浄工程として、平滑な窒化チタン膜付きウェハ(表面に厚さ50nmの窒化チタン層を有するシリコンウェハ)を1質量%の過酸化水素水に室温で1分間浸漬し、次いで純水に1分間浸漬した後、イソプロピルアルコール(iPA)に室温で1分間浸漬し、次いで、沸点が61℃でナフタレンの融液に対して溶解性を有する住友3M製Novec HFE−7100に室温で1分間浸漬させた。それ以外は、実施例1と同じ条件で実施した。実施例1と同様に、融液充填工程で窒化チタン膜付きウェハを前記融液に浸漬した際に、該ウェハの表面には相分離は見られなかったものの気泡が見られた。また、実施例1と同様に冷却析出工程を行ったところ、目視観察でウェハ全面に均一に析出した固体状のナフタレンが付着していた。また、実施例1と同様の昇華除去工程によってウェハ上の固体状のナフタレンがすべて昇華し、消失することを確認した。
[Example 7]
As a cleaning process, a wafer with a smooth titanium nitride film (a silicon wafer having a titanium nitride layer having a thickness of 50 nm on the surface) is immersed in 1% by mass of hydrogen peroxide at room temperature for 1 minute, and then immersed in pure water for 1 minute. After that, it was immersed in isopropyl alcohol (iPA) at room temperature for 1 minute, and then immersed in Novec HFE-7100 manufactured by Sumitomo 3M, which has a boiling point of 61 ° C. and soluble in naphthalene melt, at room temperature for 1 minute. The other conditions were the same as in Example 1. As in Example 1, when a wafer with a titanium nitride film was immersed in the melt in the melt filling step, bubbles were observed on the surface of the wafer although no phase separation was observed. Further, when the cooling precipitation process was performed in the same manner as in Example 1, solid naphthalene deposited uniformly on the entire wafer surface was observed by visual observation. Further, it was confirmed that all the solid naphthalene on the wafer was sublimated and disappeared by the same sublimation removing process as in Example 1.
[実施例8]
予め昇華精製を行ったナフタレンと予め蒸留精製を行った住友3M製Novec HFE−7100(沸点は61℃)を、80:20(質量比)で混合したものを充填用処理剤とした。ビーカー中で前記充填用処理剤を85℃で融解した。この融液を目視観察したところ、均一な液体であったものの、発泡が見られた。前記融液を充填用融液とした以外は、実施例1と同じ条件で実施した。実施例1と同様に、融液充填工程で窒化チタン膜付きウェハを前記融液に浸漬した際に、該ウェハの表面には相分離は見られなかったものの気泡が見られた。また、実施例1と同様に冷却析出工程を行ったところ、目視観察でウェハ全面に均一に析出した固体状のナフタレンが付着していた。また、実施例1と同様の昇華除去工程によってウェハ上の固体状のナフタレンがすべて昇華し、消失することを確認した。
[Example 8]
A filling treatment agent was prepared by mixing naphthalene which had been purified by sublimation in advance and Novec HFE-7100 (boiling point: 61 ° C.) manufactured by Sumitomo 3M, which had been previously purified by distillation, at 80:20 (mass ratio). The filling agent was melted at 85 ° C. in a beaker. When this melt was visually observed, although it was a uniform liquid, foaming was observed. It implemented on the same conditions as Example 1 except having made the said melt into the melt for filling. As in Example 1, when a wafer with a titanium nitride film was immersed in the melt in the melt filling step, bubbles were observed on the surface of the wafer although no phase separation was observed. Further, when the cooling precipitation process was performed in the same manner as in Example 1, solid naphthalene deposited uniformly on the entire wafer surface was observed by visual observation. Further, it was confirmed that all the solid naphthalene on the wafer was sublimated and disappeared by the same sublimation removing process as in Example 1.
[実施例9]
洗浄工程として、平滑な窒化チタン膜付きウェハ(表面に厚さ50nmの窒化チタン層を有するシリコンウェハ)を1質量%の過酸化水素水に室温で1分間浸漬し、次いで純水に1分間浸漬した後、イソプロピルアルコール(iPA)に室温で1分間浸漬し、次いで、沸点が100℃でナフタレンの融液に対して溶解性を有さない純水に室温で1分間浸漬させた。それ以外は、実施例1と同じ条件で実施した。実施例1と同様に、融液充填工程で窒化チタン膜付きウェハを前記融液に浸漬した際に、該ウェハの表面には気泡は見られなかったものの一部に相分離が見られた。また、実施例1と同様に冷却析出工程を行ったところ、目視観察でウェハ表面に不均一に析出した固体状のナフタレンが付着していた。また、実施例1と同様の昇華除去工程によってウェハ上の固体状のナフタレンがすべて昇華し、消失することを確認した。
[Example 9]
As a cleaning process, a wafer with a smooth titanium nitride film (a silicon wafer having a titanium nitride layer having a thickness of 50 nm on the surface) is immersed in 1% by mass of hydrogen peroxide at room temperature for 1 minute, and then immersed in pure water for 1 minute. Then, it was immersed in isopropyl alcohol (iPA) at room temperature for 1 minute, and then immersed in pure water having a boiling point of 100 ° C. and not soluble in naphthalene melt for 1 minute at room temperature. The other conditions were the same as in Example 1. As in Example 1, when a wafer with a titanium nitride film was immersed in the melt in the melt filling step, no phase bubbles were observed on the surface of the wafer, but phase separation was observed in part. Moreover, when the cooling precipitation process was performed like Example 1, the solid naphthalene which precipitated nonuniformly on the wafer surface by visual observation had adhered. Further, it was confirmed that all the solid naphthalene on the wafer was sublimated and disappeared by the same sublimation removing process as in Example 1.
[比較例1]
予め昇華精製を行ったナフタレンを充填用処理剤とし、該処理剤をナフタレンの融点未満の温度である75℃で加熱し充填用融液としようとしたが、処理剤が融解せず融液とならなかった。
[Comparative Example 1]
Naphthalene, which has been subjected to sublimation purification in advance, was used as a filling treatment agent, and the treatment agent was heated to 75 ° C., which is a temperature lower than the melting point of naphthalene, to obtain a filling melt. did not become.
[比較例2]
融液充填工程における融液の温度を110℃とした以外は、実施例1と同じ条件で実施した。充填用融液を目視観察したところ、均一な液体であったものの、発泡が見られた。実施例1と同様に、融液充填工程で窒化チタン膜付きウェハを充填用融液に浸漬した際に、該ウェハの表面には相分離が見られなかったものの、気泡が存在することを確認した。また、実施例1と同様に冷却析出工程を行ったところ、目視観察でウェハ表面積のうち、析出した固体状のナフタレンが付着していたのは50%程度であり、充分に充填できないことが確認された。これは、融液の温度が高すぎることにより該融液の冷却に時間がかかった結果、冷却析出工程時に昇華性物質が蒸発し減少する量が多くなってしまったためと考えられる。
[Comparative Example 2]
It implemented on the same conditions as Example 1 except the temperature of the melt in a melt filling process having been 110 degreeC. When the filling melt was visually observed, although it was a uniform liquid, foaming was observed. As in Example 1, when a wafer with a titanium nitride film was immersed in the melt for filling in the melt filling step, phase separation was not observed on the surface of the wafer, but it was confirmed that bubbles were present. did. Further, when the cooling precipitation process was performed in the same manner as in Example 1, it was confirmed by visual observation that about 50% of the wafer surface area had deposited solid naphthalene adhered, and it could not be filled sufficiently. It was done. This is presumably because the temperature of the melt was too high and it took a long time to cool the melt, and as a result, the amount of sublimable substances evaporated and reduced during the cooling precipitation process increased.
1 ウェハ
2 ウェハ表面の微細な凹凸パターン
3 パターンの凸部
4 パターンの凹部
5 凹部の幅
6 凸部の高さ
7 凸部の幅
8 充填用融液
9 析出した固体の昇華性物質
DESCRIPTION OF SYMBOLS 1 Wafer 2 Fine uneven | corrugated pattern 3 on the wafer surface 3 Pattern convex part 4 Pattern concave part 5 Concave width 6 Convex height 7 Convex width 8 Filling melt 9 Precipitated solid sublimation substance
Claims (17)
洗浄工程後の前記ウェハの凹部に残留する洗浄液を、昇華性物質を含む充填用処理剤を加熱により融解した充填用融液で置換し、充填する、融液充填工程、
前記凹部に充填された前記融液を冷却することにより固体の昇華性物質を析出させる、冷却析出工程、
前記凹部に析出した固体の昇華性物質を昇華により除去する、昇華除去工程
を有するウェハの洗浄方法であって、
前記充填用融液が、含有する昇華性物質の融点以上、融点+25℃以下の温度範囲内で充填用処理剤を融解させた融液であることを特徴とする、ウェハの洗浄方法。 A cleaning step of cleaning the surface of the wafer having a concavo-convex pattern on the surface with a cleaning liquid;
A melt filling process, in which the cleaning liquid remaining in the recesses of the wafer after the cleaning process is replaced with a filling melt obtained by melting a filling processing agent containing a sublimation substance by heating, and filling.
A cooling precipitation step of precipitating a solid sublimable material by cooling the melt filled in the recess,
A method for cleaning a wafer having a sublimation removal step of removing a solid sublimable substance deposited in the recess by sublimation,
The wafer cleaning method, wherein the filling melt is a melt obtained by melting the filling treatment agent in a temperature range of not less than the melting point of the sublimable substance contained and not more than the melting point + 25 ° C.
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