TWI719269B - Deposition of metal films - Google Patents
Deposition of metal films Download PDFInfo
- Publication number
- TWI719269B TWI719269B TW106140671A TW106140671A TWI719269B TW I719269 B TWI719269 B TW I719269B TW 106140671 A TW106140671 A TW 106140671A TW 106140671 A TW106140671 A TW 106140671A TW I719269 B TWI719269 B TW I719269B
- Authority
- TW
- Taiwan
- Prior art keywords
- metal
- nitride
- silicon
- substrate
- oxide
- Prior art date
Links
- 229910052751 metal Inorganic materials 0.000 title claims description 56
- 239000002184 metal Substances 0.000 title claims description 52
- 230000008021 deposition Effects 0.000 title claims description 38
- 239000000758 substrate Substances 0.000 claims abstract description 107
- 239000010936 titanium Substances 0.000 claims abstract description 65
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 57
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 54
- 238000000034 method Methods 0.000 claims abstract description 44
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 32
- 238000000623 plasma-assisted chemical vapour deposition Methods 0.000 claims abstract description 29
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 27
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 25
- 239000010703 silicon Substances 0.000 claims abstract description 25
- 230000008569 process Effects 0.000 claims abstract description 18
- 238000000151 deposition Methods 0.000 claims description 44
- 229910052581 Si3N4 Inorganic materials 0.000 claims description 30
- HQVNEWCFYHHQES-UHFFFAOYSA-N silicon nitride Chemical compound N12[Si]34N5[Si]62N3[Si]51N64 HQVNEWCFYHHQES-UHFFFAOYSA-N 0.000 claims description 30
- 239000002243 precursor Substances 0.000 claims description 27
- 239000001257 hydrogen Substances 0.000 claims description 22
- 229910052739 hydrogen Inorganic materials 0.000 claims description 22
- 229910052814 silicon oxide Inorganic materials 0.000 claims description 21
- LIVNPJMFVYWSIS-UHFFFAOYSA-N silicon monoxide Chemical compound [Si-]#[O+] LIVNPJMFVYWSIS-UHFFFAOYSA-N 0.000 claims description 17
- 239000000463 material Substances 0.000 claims description 16
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 claims description 14
- 239000000956 alloy Substances 0.000 claims description 13
- 150000002431 hydrogen Chemical class 0.000 claims description 11
- 229910044991 metal oxide Inorganic materials 0.000 claims description 11
- 150000004706 metal oxides Chemical class 0.000 claims description 11
- 150000004767 nitrides Chemical class 0.000 claims description 11
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 10
- 239000012159 carrier gas Substances 0.000 claims description 10
- 229910052732 germanium Inorganic materials 0.000 claims description 10
- 229910000577 Silicon-germanium Inorganic materials 0.000 claims description 9
- 229910045601 alloy Inorganic materials 0.000 claims description 9
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 7
- 229910052799 carbon Inorganic materials 0.000 claims description 7
- 229910001507 metal halide Inorganic materials 0.000 claims description 7
- 150000005309 metal halides Chemical class 0.000 claims description 7
- -1 titanium halide Chemical class 0.000 claims description 7
- 229910052735 hafnium Inorganic materials 0.000 claims description 6
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims description 5
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims description 5
- 229910052785 arsenic Inorganic materials 0.000 claims description 5
- RQNWIZPPADIBDY-UHFFFAOYSA-N arsenic atom Chemical compound [As] RQNWIZPPADIBDY-UHFFFAOYSA-N 0.000 claims description 5
- 229910052796 boron Inorganic materials 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 5
- 229910001092 metal group alloy Inorganic materials 0.000 claims description 5
- 229910052698 phosphorus Inorganic materials 0.000 claims description 5
- 239000011574 phosphorus Substances 0.000 claims description 5
- VBJZVLUMGGDVMO-UHFFFAOYSA-N hafnium atom Chemical compound [Hf] VBJZVLUMGGDVMO-UHFFFAOYSA-N 0.000 claims description 4
- 229910052726 zirconium Inorganic materials 0.000 claims description 4
- PDPJQWYGJJBYLF-UHFFFAOYSA-J hafnium tetrachloride Chemical compound Cl[Hf](Cl)(Cl)Cl PDPJQWYGJJBYLF-UHFFFAOYSA-J 0.000 claims description 2
- DUNKXUFBGCUVQW-UHFFFAOYSA-J zirconium tetrachloride Chemical compound Cl[Zr](Cl)(Cl)Cl DUNKXUFBGCUVQW-UHFFFAOYSA-J 0.000 claims description 2
- VSZWPYCFIRKVQL-UHFFFAOYSA-N selanylidenegallium;selenium Chemical compound [Se].[Se]=[Ga].[Se]=[Ga] VSZWPYCFIRKVQL-UHFFFAOYSA-N 0.000 claims 2
- 235000012239 silicon dioxide Nutrition 0.000 abstract description 8
- 239000000377 silicon dioxide Substances 0.000 abstract description 8
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 18
- 229910004298 SiO 2 Inorganic materials 0.000 description 14
- 230000015572 biosynthetic process Effects 0.000 description 12
- 238000005530 etching Methods 0.000 description 10
- 239000007789 gas Substances 0.000 description 10
- 229910052786 argon Inorganic materials 0.000 description 9
- 238000005229 chemical vapour deposition Methods 0.000 description 7
- 230000003647 oxidation Effects 0.000 description 7
- 238000007254 oxidation reaction Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 238000000231 atomic layer deposition Methods 0.000 description 5
- 239000000203 mixture Substances 0.000 description 5
- 239000003638 chemical reducing agent Substances 0.000 description 4
- 229910052736 halogen Inorganic materials 0.000 description 4
- 150000002367 halogens Chemical class 0.000 description 4
- 239000011261 inert gas Substances 0.000 description 4
- 238000003672 processing method Methods 0.000 description 4
- 239000000376 reactant Substances 0.000 description 4
- 229910021332 silicide Inorganic materials 0.000 description 4
- 230000008859 change Effects 0.000 description 3
- 230000007423 decrease Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 229910001510 metal chloride Inorganic materials 0.000 description 3
- 238000010926 purge Methods 0.000 description 3
- 230000002829 reductive effect Effects 0.000 description 3
- FVBUAEGBCNSCDD-UHFFFAOYSA-N silicide(4-) Chemical compound [Si-4] FVBUAEGBCNSCDD-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 2
- NRTOMJZYCJJWKI-UHFFFAOYSA-N Titanium nitride Chemical compound [Ti]#N NRTOMJZYCJJWKI-UHFFFAOYSA-N 0.000 description 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 238000007872 degassing Methods 0.000 description 2
- 238000001312 dry etching Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 229910052731 fluorine Inorganic materials 0.000 description 2
- 239000011737 fluorine Substances 0.000 description 2
- 125000005843 halogen group Chemical group 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- 230000002045 lasting effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000005240 physical vapour deposition Methods 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000004151 rapid thermal annealing Methods 0.000 description 2
- 239000004065 semiconductor Substances 0.000 description 2
- 229910021341 titanium silicide Inorganic materials 0.000 description 2
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 description 2
- 229910052721 tungsten Inorganic materials 0.000 description 2
- 239000010937 tungsten Substances 0.000 description 2
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- JBRZTFJDHDCESZ-UHFFFAOYSA-N AsGa Chemical compound [As]#[Ga] JBRZTFJDHDCESZ-UHFFFAOYSA-N 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229910001218 Gallium arsenide Inorganic materials 0.000 description 1
- 238000003917 TEM image Methods 0.000 description 1
- 229910008484 TiSi Inorganic materials 0.000 description 1
- 229910008482 TiSiN Inorganic materials 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- WYEMLYFITZORAB-UHFFFAOYSA-N boscalid Chemical compound C1=CC(Cl)=CC=C1C1=CC=CC=C1NC(=O)C1=CC=CN=C1Cl WYEMLYFITZORAB-UHFFFAOYSA-N 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 125000001309 chloro group Chemical group Cl* 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000004020 conductor Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000112 cooling gas Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000005137 deposition process Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002019 doping agent Substances 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 125000001153 fluoro group Chemical group F* 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000033444 hydroxylation Effects 0.000 description 1
- 238000005805 hydroxylation reaction Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000012212 insulator Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- QRXWMOHMRWLFEY-UHFFFAOYSA-N isoniazide Chemical compound NNC(=O)C1=CC=NC=C1 QRXWMOHMRWLFEY-UHFFFAOYSA-N 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 238000005121 nitriding Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000000059 patterning Methods 0.000 description 1
- 238000009832 plasma treatment Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229910052594 sapphire Inorganic materials 0.000 description 1
- 239000010980 sapphire Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000003608 titanium Chemical class 0.000 description 1
Images
Landscapes
- Chemical Vapour Deposition (AREA)
Abstract
Description
本發明的具體例大體上關於在金屬性(metallic)表面之上沉積金屬膜的方法。更明確地,本發明的具體例係關於改善底部膜覆蓋的方法,並進一步在不同材料(諸如金屬氧化物、金屬氮化物、或金屬-氧化物-氮化物)的表面上方,選擇性沉積金屬膜於金屬性表面之上。The specific example of the present invention generally relates to a method of depositing a metal film on a metallic surface. More specifically, the specific example of the present invention relates to a method of improving bottom film coverage, and further, selectively depositing metal on the surface of different materials (such as metal oxide, metal nitride, or metal-oxide-nitride) The film is on the metallic surface.
藉由在基板表面之上產生複雜圖案化材料層的處理而能夠製造積體電路。在基板之上產生圖案化材料需要用於期望材料的沉積的受控方法。在相對於不同表面的一表面之上選擇性沉積膜是有利於圖案化及其他應用。The integrated circuit can be manufactured by the process of producing a complex patterned material layer on the surface of the substrate. The production of patterned material on the substrate requires a controlled method for the deposition of the desired material. The selective deposition of a film on a surface relative to a different surface is beneficial for patterning and other applications.
由於製造者努力地增加電路密度與品質,包括觸點、通孔、線路、及用於形成多級互連(例如使用鈷、鎢、或銅)的其他特徵的高深寬比孔隙在尺寸上持續縮小。鈦被廣為人知地採用做為矽化物材料。選擇性鈦沉積是持續發展的目標以改善Rc(接觸電阻)效能。As manufacturers strive to increase circuit density and quality, high-aspect-ratio voids including contacts, vias, lines, and other features used to form multi-level interconnections (for example, using cobalt, tungsten, or copper) continue in size Zoom out. Titanium is widely used as a silicide material. Selective titanium deposition is an ongoing goal to improve Rc (contact resistance) performance.
電漿增強化學氣相沉積(PECVD)以TiCl4 做為前驅物以形成鈦被廣泛地使用在半導體產業中,但習知的TiCl4 狀態,例如600°C–700°C顯示出不佳的高深寬比孔隙的底部覆蓋,其隨著尺寸減少。Plasma-enhanced chemical vapor deposition (PECVD) uses TiCl 4 as a precursor to form titanium and is widely used in the semiconductor industry, but the conventional TiCl 4 state, such as 600°C–700°C, shows poor performance The bottom of the high aspect ratio pores is covered, which decreases with the size.
有著持續需求於在期望位置中提供矽化物層,包括鈦膜的底部覆蓋與選擇性沉積。 There is a continuing need to provide silicide layers in desired locations, including bottom coverage and selective deposition of titanium films.
本發明的一或多個具體例係關於處理方法,包含在處理腔室內的電漿增強化學氣相沉積(PECVD)處理期間,相對於第二表面選擇性沉積金屬膜於基板的第一表面之上,第二表面與基板的第一表面是不同的材料。 One or more specific examples of the present invention are related to processing methods, including during plasma enhanced chemical vapor deposition (PECVD) processing in a processing chamber, selectively depositing a metal film on the first surface of the substrate with respect to the second surface. Above, the second surface and the first surface of the substrate are of different materials.
本發明的額外具體例係關於處理方法,包含在處理腔室內定位基板表面。此基板表面之上具有至少一特徵,此至少一特徵創造具有底部、頂部、與側壁的間隙,此底部包含金屬性元素或合金,金屬性元素或合金的任一者被可選地摻雜,而側壁包含金屬氧化物、金屬氮化物、或金屬-氧化物-氮化物,金屬氧化物、金屬氮化物、或金屬-氧化物-氮化物的每一者被可選地摻雜碳。在電漿增強化學氣相沉積(PECVD)處理期間,此基板表面暴露於金屬鹵化物前驅物氣體與含氫還原性共反應前驅物,於範圍為約300℃至小於500℃中的基板溫度及範圍為約1至小於約700毫瓦/cm2中的電漿功率,以相對於特徵的側壁在底部之上形成金屬膜。 An additional specific example of the present invention relates to a processing method, including positioning the surface of the substrate in the processing chamber. There is at least one feature on the surface of the substrate, and the at least one feature creates a gap with a bottom, a top, and a sidewall. The bottom includes a metallic element or alloy, and any one of the metallic element or alloy is optionally doped, Whereas the sidewalls include metal oxide, metal nitride, or metal-oxide-nitride, each of the metal oxide, metal nitride, or metal-oxide-nitride is optionally doped with carbon. During the plasma-enhanced chemical vapor deposition (PECVD) process, the surface of the substrate is exposed to the metal halide precursor gas and the hydrogen-containing reductive co-reacting precursor at a substrate temperature in the range of about 300°C to less than 500°C. sidewall range from about 1 to less than about 700 mW / cm 2 in plasma power, with respect to the characteristics of the metal film is formed over the bottom.
本發明的進一步具體例係關於處理方法,包含在處理腔室中定位具有第一表面與第二表面的基板,此第一表面為:金屬性矽(Si)、金屬性鍺(Ge)、或SiGe合金,金屬性矽(Si)、金屬性鍺(Ge)、或SiGe合金的每一者被可選地摻雜磷(P)、砷(As)、及/或硼(B),而此第二表 面為金屬氧化物、金屬氮化物、或金屬-氧化物-氮化物,金屬氧化物、金屬氮化物、或金屬-氧化物-氮化物的每一者被可選地摻雜碳。金屬前驅物包含鈦鹵化物;鋯鹵化物,及/或鉿鹵化物;氫;及載體氣體流動進入此處理腔室。藉由在範圍為約1至小於約700毫瓦/cm2中的電漿功率與在範圍為約10kHz至約50MHz中的頻率的施加而賦能(energize)此金屬前驅物與氫。此賦能的金屬前驅物與氫被反應以至少約10:1的選擇性相對於第二表面在第一表面之上選擇性沉積金屬膜。 A further specific example of the present invention relates to a processing method, including positioning a substrate having a first surface and a second surface in a processing chamber, the first surface being: metallic silicon (Si), metallic germanium (Ge), or SiGe alloy, each of metallic silicon (Si), metallic germanium (Ge), or SiGe alloy is optionally doped with phosphorus (P), arsenic (As), and/or boron (B), and this The second surface is metal oxide, metal nitride, or metal-oxide-nitride, and each of the metal oxide, metal nitride, or metal-oxide-nitride is optionally doped with carbon. The metal precursors include titanium halides; zirconium halides, and/or hafnium halides; hydrogen; and carrier gas flows into the processing chamber. The metal precursor and hydrogen are energized by the application of plasma power in the range of about 1 to less than about 700 mW/cm 2 and the frequency in the range of about 10 kHz to about 50 MHz. The energized metal precursor and hydrogen are reacted to selectively deposit a metal film on the first surface with respect to the second surface with a selectivity of at least about 10:1.
本發明的具體例提供在含矽表面上沉積鈦膜的方法。Ti-矽化物用於做為在高深寬比孔隙中的矽化物形成層以用於接觸應用。當節點尺寸縮小至小於20 nm且採用金屬閘極時,基板處理溫度的熱預算下降(<500°C)。本發明有利地改善窄溝槽的Ti底部覆蓋及Si(主動接合面)與SiO2 (側壁與場區)之上的沉積選擇性,以減少在小於500°C沉積溫度的接觸電阻。以PECVD的Ti的底部覆蓋改善及Si與SiO2 之間的選擇性沉積容許用於後金屬填充處理的更寬廣空間及改善的裝置效能。A specific example of the present invention provides a method of depositing a titanium film on a silicon-containing surface. Ti-silicide is used as a silicide forming layer in high aspect ratio pores for contact applications. When the node size is reduced to less than 20 nm and metal gates are used, the thermal budget of the substrate processing temperature is reduced (<500°C). The present invention advantageously improves the Ti bottom coverage of the narrow trench and the deposition selectivity on Si (active bonding surface) and SiO 2 (sidewall and field region) to reduce the contact resistance at a deposition temperature less than 500°C. The improved bottom coverage of Ti by PECVD and the selective deposition between Si and SiO 2 allow a wider space for post-metal filling processing and improved device performance.
在本說明書與隨附申請專利範圍中使用時,用語「基板」及「晶圓」可互換地使用,兩者皆指稱一表面或一表面的一部分,在其上可進行處理。本領域的熟習技藝者也可理解到關於一基板也可僅指稱此基板的一部分,除非在上下文中清楚地指示並非如此。此外,關於在基板上沉積可意指原始(bare)的基板及具有一或多個膜或特徵沉積或形成在之上的基板兩者。When used in the scope of this specification and the accompanying patent application, the terms "substrate" and "wafer" are used interchangeably, and both refer to a surface or a part of a surface on which processing can be performed. Those skilled in the art can also understand that a substrate can also be referred to as a part of the substrate, unless the context clearly indicates otherwise. In addition, referring to deposition on a substrate can mean both a bare substrate and a substrate having one or more films or features deposited or formed thereon.
在此使用「基板」時,其指稱任何基板或形成在基板上的材料表面,在製造處理期間可在此基板或材料表面上實行膜處理。例如,其上可實行處理的基板表面包括材料,諸如矽、氧化矽、應變矽、絕緣體上矽(SOI)、碳摻雜氧化矽、氮化矽、摻雜矽、鍺、砷化鎵、玻璃、藍寶石、及任何其他材料,諸如金屬、金屬氮化物、金屬合金、及其他導電材料,取決於應用。基板包括(沒有限制於)半導體晶圓。基板可暴露於預處理製程以拋光、蝕刻、還原、氧化、羥基化(hydroxylate)、退火及/或烘烤基板表面。除了直接在基板本身的表面上的膜處理之外,在本發明中,揭示的任何膜處理步驟也可實行在如之後更詳細揭示的形成在基板上的下層之上,而用語「基板表面」意欲包括如上下文所指示的此下層。因此例如,在膜/層或部分的膜/層已經沉積在基板表面之上,此新近沉積的膜/層的暴露表面變成此基板表面。給定的基板表面所包含的事物將取決於將被沉積的膜種類,以及所使用的特定化學。在一或多個具體例中,第一基板表面將包含金屬,而第二基板表面將包含介電質,或反之亦然。在某些具體例中,基板表面可包含特定官能基(例如-OH、-NH,等等)。When "substrate" is used here, it refers to any substrate or the surface of a material formed on the substrate, and film processing can be performed on the surface of the substrate or material during the manufacturing process. For example, the substrate surface on which processing can be performed includes materials such as silicon, silicon oxide, strained silicon, silicon-on-insulator (SOI), carbon-doped silicon oxide, silicon nitride, doped silicon, germanium, gallium arsenide, glass , Sapphire, and any other materials such as metals, metal nitrides, metal alloys, and other conductive materials, depending on the application. The substrate includes (not limited to) a semiconductor wafer. The substrate may be exposed to a pretreatment process to polish, etch, reduce, oxidize, hydroxylate, anneal and/or bake the surface of the substrate. In addition to the film treatment directly on the surface of the substrate itself, in the present invention, any of the film treatment steps disclosed can also be performed on the lower layer formed on the substrate as disclosed in more detail later, and the term "substrate surface" It is intended to include this lower layer as the context dictates. So for example, where the film/layer or part of the film/layer has been deposited on the surface of the substrate, the exposed surface of this newly deposited film/layer becomes the surface of the substrate. What is contained on a given substrate surface will depend on the type of film to be deposited and the specific chemistry used. In one or more embodiments, the surface of the first substrate will include metal, and the surface of the second substrate will include dielectric, or vice versa. In some specific examples, the surface of the substrate may include specific functional groups (for example, -OH, -NH, etc.).
在本說明書與隨附申請專利範圍中使用時,用語「反應氣體」、「前驅物」、「反應物」、及類似物可互換地使用,以意指包括與基板表面反應的物種的氣體。When used in the scope of this specification and the accompanying patent application, the terms "reactive gas", "precursor", "reactant", and the like are used interchangeably to mean a gas that includes species that react with the surface of the substrate.
化學氣相沉積(CVD)處理,包括電漿增強化學氣相沉積(PECVD),是不同於原子層沉積(ALD)。ALD處理是自限(self-limiting)處理,其中使用二元(binary)(或更高級的)反應沉積單一材料層。此處理持續直到基板表面上的所有可用的活性部分已被反應。CVD處理不是自限處理,且膜可成長至任何預定厚度。PECVD仰賴於在電漿狀態中能量的使用以創造更多反應性自由基。 Chemical vapor deposition (CVD) processing, including plasma enhanced chemical vapor deposition (PECVD), is different from atomic layer deposition (ALD). The ALD process is a self-limiting process in which a binary (or higher) reaction is used to deposit a single material layer. This process continues until all available active parts on the surface of the substrate have been reacted. The CVD process is not a self-limiting process, and the film can be grown to any predetermined thickness. PECVD relies on the use of energy in the plasma state to create more reactive free radicals.
本發明的具體例提供處理方法以提供在期望位置中的鈦層,包括在高深寬比特徵中的鈦膜的改善的底部覆蓋與選擇性沉積。在本說明書與隨附申請專利範圍中使用時,用語「…的選擇性沉積」與「選擇性形成」在相對於另一表面的一表面之上的膜,及類似物,意味著第一量的膜沉積在第一表面之上而第二量的膜沉積在第二表面之上,其中第二量的膜小於第一量的膜或是不存在。在此使用的用語「相對於(over)」並不意味著在另一表面的頂部上的一表面的物理定向(physical orientation),而是相對於其他表面的一表面之化學反應的熱力學或動力學性質的關係。例如,相對於二氧化矽(SiO2)表面選擇性沉積鈦膜於矽(Si)表面之上意味著此鈦膜沉積在Si表面之上而較少的鈦膜沉積在SiO2表面之上;或在Si表面之上的此鈦膜的形成相對於在SiO2表面之上的鈦膜的形成是熱力學上或動力學上有利的。換言之,此膜可相對於第二表面選擇性沉積於第一表面之上意味著在第一表面之上的沉積相對於在第二表面之上的沉積是有利的。 Embodiments of the present invention provide processing methods to provide titanium layers in desired locations, including improved bottom coverage and selective deposition of titanium films in high aspect ratio features. When used in this specification and the scope of the appended application, the terms "selective deposition of" and "selectively formed" a film on a surface relative to another surface, and the like, mean the first amount The film of is deposited on the first surface and the second amount of film is deposited on the second surface, where the second amount of film is less than the first amount of film or is not present. The term "over" used here does not mean the physical orientation of a surface on top of another surface, but the thermodynamics or dynamics of a chemical reaction of a surface relative to the other surface The nature of the relationship. For example, the selective deposition of a titanium film on the silicon (Si) surface relative to the silicon dioxide (SiO 2 ) surface means that the titanium film is deposited on the Si surface and less titanium film is deposited on the SiO 2 surface; Or the formation of this titanium film on the Si surface is thermodynamically or kinetically advantageous relative to the formation of the titanium film on the SiO 2 surface. In other words, that this film can be selectively deposited on the first surface with respect to the second surface means that the deposition on the first surface is advantageous relative to the deposition on the second surface.
本發明的具體例關於使用PECVD相對於不同材料的表面優先地在金屬性表面之上沉積金屬膜的方法。圖1顯示根據本發明的一或多個具體例的處理100的處理流程圖。為了圖1,此金屬膜包含鈦,此金屬性表面
包含Si,而此不同材料包含SiOx或SiN。本發明關於金屬膜,可包含但不限於鈦、鋯、及/或鉿。這些金屬膜可被摻雜物可選地摻雜,此摻雜物包括但不限於磷(P)、砷(As)、及/或硼(B)。金屬性表面可包含但不限於Si、Ge、及/或SiGe。不同材料的表面可包含但不限於氧化矽(SiOx)、氮化矽(SiN)、矽氧化物-氮化物(SiON),前述物的每一者可選地摻雜碳。圖2是具有特徵的基板的部分剖面視圖而圖3是在特徵中選擇性沉積鈦膜的部分剖面視圖。參照圖1至3,包含具有底部表面212與側壁214、216的特徵210的基板200被提供用於處理於110處。在此具體例中,底部表面包含Si而側壁包含SiOx或SiN。在此使用時,用語「被提供」意指此基板被放置至一位置或環境中用於進一步處理。為了說明目的,某些圖式顯示具有單一特徵的基板;然後,本領域的熟習技藝者會理解到可以有多於一個特徵。特徵210的外形或輪廓可為任何合適外形或輪廓,包括但不限於(a)垂直側壁與底部表面、(b)錐形側壁、(c)過切(under-cutting)、(d)凹腔(reentrant)輪廓、(e)弓形、(f)微開溝(micro-trenching)、(g)彎曲底部表面、及(h)刻痕。在此使用時,用語「特徵」意指任何刻意的表面不規則。特徵的合適實例包括但不限於具有頂部、兩側壁與底部的溝槽及孔洞、具有頂部與兩側壁的尖峰。特徵可具有任何合適的深寬比(特徵的深度對於特徵的寬度的比率)。在某
些具體例中,此深寬比大於或等於約5:1、10:1、15:1、20:1、25:1、30:1、35:1或40:1。
The specific example of the present invention relates to a method of depositing a metal film on a metallic surface preferentially with respect to a surface of a different material using PECVD. Fig. 1 shows a process flow diagram of a
在120處,於第一腔室中,基板200被清洗以移除原生氧化物,留下乾淨基板表面。可藉由任何合適技術移除原生氧化物,包括但不限於習知為SiConiTM蝕刻的乾式蝕刻處理。SiConiTM蝕刻是遠端電漿輔助乾式蝕刻處理,涉及基板的同時暴露於H2、NF3及NH3電漿副產物。氫與氟物種的遠端電漿激發容許無電漿損害的基板處理。SiConiTM蝕刻主要地共形與選擇朝向氧化矽層,但不迅速地蝕刻矽,無論矽是否為非晶態、結晶態或多晶態。
At 120, in the first chamber, the
基板200具有(乾淨)基板表面220。至少一特徵210形成一開口在基板表面220中。特徵210從基板表面220延伸深度D至底部表面212,底部表面212包含矽(Si)。特徵210具有第一側壁214與第二側壁216,其界定特徵210的寬度W。側壁包含氧化矽(SiOx),例如二氧化矽(SiO2)或氮化矽(SiN)。藉由側壁與底部所形成的開放區域也被稱為間隙。
The
在圖1的130處,於第二腔室中,Si與SiOx/SiN表面暴露於使用鈦與還原劑前驅物及可選地載體氣體的PECVD沉積處理。在圖1的140處,相對於SiOx/SiN表面選擇性沉積鈦膜230於Si表面之上。在圖1的150處,有著可選的N2、H2、及/或NH3電漿處理或浸泡。在一具體例中,鈦膜230的形成包含在電漿產生的
狀況下將基板表面暴露於鈦前驅物及還原劑。關於氯化鈦與氫的使用,不被操作的任何特定理論所約束,料想氯化鈦與H+/H*物種反應以在基板上沉積鈦膜。鈦膜形成在特徵的Si及SiOx/SiN表面之上。未反應的氯化鈦被料想為蝕刻形成在SiOx/SiN表面之上的鈦膜,以選擇性沉積鈦膜於Si表面之上。以選擇性沉積中的蝕刻結果,鈦膜可相等地或不相等地形成在Si及SiOx/SiN表面之上。在某些具體例中,相較於SiOx/SiN表面,鈦膜有利地形成在Si表面之上,而蝕刻增加此選擇性。
At 130 of FIG. 1, in the second chamber, Si and SiO x / SiN surfaces exposed to PECVD deposition process using titanium precursors with a reducing agent and optionally a carrier gas. At 140 in FIG. 1, a
此沉積的選擇性為至少約1.3:1。此選擇性可在範圍為約1.3:1至少約100:1中。在某些具體例中,此選擇性大於或等於約1.5:1、2:1、5:1、8:1、10:1、15:1、20:1、25:1、50:1或更多。 The selectivity of this deposition is at least about 1.3:1. This selectivity can be in the range of about 1.3:1 at least about 100:1. In some specific cases, the selectivity is greater than or equal to about 1.5:1, 2:1, 5:1, 8:1, 10:1, 15:1, 20:1, 25:1, 50:1 or More.
根據一或多個具體例,金屬膜具有在底部金屬性/合金表面之上的範圍為約10Å至約100Å中的厚度及在側壁表面(金屬氧化物、金屬氮化物、金屬-氧化物、氮化物)之上的10Å至~0Å中的厚度。 According to one or more specific examples, the metal film has a thickness in the range of about 10Å to about 100Å above the bottom metallic/alloy surface and on the sidewall surface (metal oxide, metal nitride, metal-oxide, nitrogen The thickness of 10Å to ~0Å above the compound).
處理腔室可為適用於PECVD的任何腔室。流體前驅物被供應至處理腔室,流體前驅物之後在腔室的一區中被電漿功率激發。有著電氣耦接於處理腔室的電源供應器,電源供應器取決於處理可經設置以傳遞可調整數量的功率至腔室。 The processing chamber can be any chamber suitable for PECVD. The fluid precursor is supplied to the processing chamber, and the fluid precursor is then excited by the plasma power in a region of the chamber. There is a power supply electrically coupled to the processing chamber, and the power supply can be configured to deliver an adjustable amount of power to the chamber depending on the processing.
金屬前驅物可包含金屬鹵化物。鹵化物可為任何合適鹵素。金屬鹵化物可為不同鹵素的混合物或實質上 為相同的鹵素原子。在某些具體例中,金屬鹵化物實質上僅包含氯原子。在此使用時,「實質上僅」意指有著大於或等於約95原子百分比的所述鹵素物種。在某些具體例中,鹵素是氟、氯、溴或碘的一或多者。在某些具體例中,實質上沒有氟原子;意指在所有鹵素原子的原子基礎上有著小於約1%。 The metal precursor may include a metal halide. The halide can be any suitable halogen. The metal halide can be a mixture of different halogens or essentially Are the same halogen atoms. In some specific examples, the metal halide contains essentially only chlorine atoms. As used herein, "substantially only" means the halogen species having greater than or equal to about 95 atomic percent. In some embodiments, the halogen is one or more of fluorine, chlorine, bromine or iodine. In some specific examples, there are substantially no fluorine atoms; meaning that there are less than about 1% based on all halogen atoms.
在一或多個具體例中,金屬鹵化物是金屬氯化物。金屬氯化物可為鈦氧化態或實質上所有為相同的氧化態(即在原子基礎上>95%的相同的氧化態)的混合物。例如,氯化鈦TiClx可為鈦氧化態或實質上所有為相同的氧化態(即在原子基礎上>95%的相同的氧化態)的混合物。例如,氯化鈦可為TiCl3及TiCl4物種的混合物或其他物種。其他金屬氯化物包括氯化鋯與氯化鉿。 In one or more specific examples, the metal halide is a metal chloride. The metal chloride can be a titanium oxidation state or a mixture that is substantially all in the same oxidation state (ie, >95% of the same oxidation state on an atomic basis). For example, titanium chloride TiCl x may be a mixture of titanium oxidation state or substantially all of the same oxidation state (ie, >95% of the same oxidation state on an atomic basis). For example, titanium chloride may be a mixture of TiCl 3 and TiCl 4 species or other species. Other metal chlorides include zirconium chloride and hafnium chloride.
還原劑包含還原性共反應物,其可為含氫前驅物。含氫前驅物可包含選自H2、NH3、烴類、或類似物的至少一前驅物。在某些具體例中,第一前驅物包含氫(H2)且將第一前驅物賦能以產生H+及H*物種。在某些具體例中,氫離子與自由基形成為電漿的部分。 The reducing agent includes a reducing co-reactant, which may be a hydrogen-containing precursor. The hydrogen-containing precursor may include at least one precursor selected from H 2 , NH 3 , hydrocarbons, or the like. In some embodiments, the first precursor includes hydrogen (H 2 ) and the first precursor is energized to generate H + and H* species. In some specific examples, hydrogen ions and free radicals form part of the plasma.
沉積的金屬膜可包含金屬或主要由金屬構成,例如鈦、鋯、或鉿。在此使用時,用語「主要由…構成」意指此膜是大於或等於約95原子百分比的此特定組分。在某些具體例中,此金屬膜大於約96、97、98或99原子百分比的此特定組分。 The deposited metal film may contain metal or consist mainly of metal, such as titanium, zirconium, or hafnium. As used herein, the term "mainly composed of" means that the film is greater than or equal to about 95 atomic percent of the specific component. In some embodiments, the metal film is greater than about 96, 97, 98, or 99 atomic percent of the specific composition.
關於金屬膜的形成,金屬前驅物與還原劑可共伴流(co-flow)或交替地脈衝與可選的載體氣體一同進入PECVD處理腔室以形成直接電漿(direct plasma)。一範例載體氣體為Ar。基板可被加熱至範圍從約50℃至約500℃內的溫度,較佳地從約100℃至小於500℃、從約300℃至小於500℃、及又更佳地從約300℃至約440℃。 Regarding the formation of the metal film, the metal precursor and the reducing agent can be co-flowed or alternately pulsed together with an optional carrier gas into the PECVD processing chamber to form a direct plasma. An example carrier gas is Ar. The substrate can be heated to a temperature ranging from about 50°C to about 500°C, preferably from about 100°C to less than 500°C, from about 300°C to less than 500°C, and more preferably from about 300°C to about 500°C. 440°C.
電漿功率可在範圍為約1至小於約700毫瓦/cm2中,或約70至小於約350毫瓦/cm2,或甚至約90毫瓦/cm2及在前述範圍中的所有數值與子範圍。頻率可在範圍為約10kHz至約50MHz中,或350kHz至40MHz,或甚至約13.56MHz及在前述範圍中的所有數值與子範圍。工作週期可在範圍為1至90%中及前述範圍中的所有數值與子範圍。電漿功率可被脈衝化,提供功率於每約0.00001至約100秒持續約0.0000001至約90秒的期間及前述範圍中的所有數值與子範圍。 The plasma power can be in the range of about 1 to less than about 700 mW/cm 2 , or about 70 to less than about 350 mW/cm 2 , or even about 90 mW/cm 2 and all values in the foregoing range And sub-range. The frequency can be in the range of about 10 kHz to about 50 MHz, or 350 kHz to 40 MHz, or even about 13.56 MHz and all values and sub-ranges in the foregoing range. The duty cycle can be in the range of 1 to 90% and all values and sub-ranges in the aforementioned range. The plasma power can be pulsed, providing power for a period of about 0.0000001 to about 90 seconds every about 0.00001 to about 100 seconds and all values and sub-ranges in the foregoing range.
當使用例如氬的載體氣體時,流率可在範圍為3至400sccm中及前述範圍中的所有數值與子範圍。 When a carrier gas such as argon is used, the flow rate can be in the range of 3 to 400 sccm and all values and sub-ranges in the aforementioned range.
根據一或多個具體例,在形成金屬層之前及/或之後,此基板經受處理。例如,在一或多個具體例中,在圖1的160處,於金屬(例如鈦)層的可選地形成之後,氮化鈦沉積為阻障層。在破壞真空之後,於170處,實行可選的RTA(快速熱退火)以形成矽化鈦層。在破壞真空之後,於180處,特徵的剩餘部分的深度與寬度被鎢或鈷 所填充以形成互連。鈦及氮化鈦處理可在相同腔室中執行或在一或多個分開處理腔室中執行。或也可進行在沉積的Ti膜上的氮化,其藉由帶有施加RF電漿或浸泡的N2、H2、及/或NH3而處理。 According to one or more specific examples, the substrate is subjected to processing before and/or after forming the metal layer. For example, in one or more specific examples, at 160 in FIG. 1, after the optional formation of the metal (eg titanium) layer, titanium nitride is deposited as the barrier layer. After breaking the vacuum, at 170, an optional RTA (rapid thermal annealing) is performed to form a titanium silicide layer. After breaking the vacuum, at 180, the depth and width of the remaining part of the feature is filled with tungsten or cobalt to form an interconnection. Titanium and titanium nitride processing can be performed in the same chamber or in one or more separate processing chambers. Alternatively, nitridation on the deposited Ti film can be performed by treatment with N 2 , H 2 , and/or NH 3 with application of RF plasma or immersion.
在某些具體例中,基板從第一腔室移動至分開的下一個腔室用於進一步處理。基板可直接從第一腔室移動至分開的處理腔室,或基板可從第一腔室移動至一或多個移送腔室,然後移動至分開的處理腔室。因此,處理設備可包含以移送站連通的多個腔室。此種設備可被稱為「群集工具」或「群集系統」,及類似物。 In some embodiments, the substrate is moved from the first chamber to the next separate chamber for further processing. The substrate can be moved directly from the first chamber to a separate processing chamber, or the substrate can be moved from the first chamber to one or more transfer chambers and then to a separate processing chamber. Therefore, the processing equipment may include a plurality of chambers connected by a transfer station. Such equipment may be called "cluster tool" or "cluster system", and the like.
大體上,群集工具是包含多個腔室的模組系統,其執行各種功能,包括基板中心找尋及定位、除氣、退火、沉積及/或蝕刻。根據一或多個具體例,群集工具包括至少一第一腔室與一中央移送腔室。中央移送腔室可容納可在處理腔室與裝載閘腔室之間與之中運送基板的機器人。移送腔室通常維持在真空狀態且提供用於從一腔室運送基板至另一腔室及/或位在群集工具的前端處的裝載閘腔室的中間階段。本發明可採用的兩種廣為人知的群集工具是Centura®及Endura®,兩者可由加州聖克拉拉的應用材料公司獲得。然而,為了執行如本文所述的處理的特定步驟,可改變腔室的確切佈置與組合。可使用的其他處理腔室包括但不限於循環層沉積(cyclical layer deposition,CLD)、原子層沉積(ALD)、化學氣相沉積(CVD)、物理氣相沉積(PVD)、蝕刻、預清洗、 化學清洗、諸如RTP的熱處理、電漿氮化、除氣、定位、羥基化(hydroxylation)及其他基板處理。藉由在群集工具上的腔室中執行處理,在沉積後續膜之前,由於大氣雜質的基板表面汙染可被避免且沒有氧化現象。 In general, the cluster tool is a modular system containing multiple chambers, which performs various functions, including substrate center finding and positioning, degassing, annealing, deposition, and/or etching. According to one or more specific examples, the cluster tool includes at least a first chamber and a central transfer chamber. The central transfer chamber can accommodate a robot that can transport substrates between and in the processing chamber and the loading lock chamber. The transfer chamber is generally maintained in a vacuum state and provides an intermediate stage for transferring substrates from one chamber to another and/or a loading lock chamber at the front end of the cluster tool. Two well-known clustering tools that can be used in the present invention are Centura® and Endura®, both of which are available from Applied Materials of Santa Clara, California. However, in order to perform specific steps of the processing as described herein, the exact arrangement and combination of the chambers can be changed. Other processing chambers that can be used include, but are not limited to, cyclical layer deposition (CLD), atomic layer deposition (ALD), chemical vapor deposition (CVD), physical vapor deposition (PVD), etching, pre-cleaning, Chemical cleaning, heat treatment such as RTP, plasma nitriding, degassing, positioning, hydroxylation and other substrate processing. By performing the processing in the chamber on the cluster tool, the substrate surface contamination due to atmospheric impurities can be avoided without oxidation before the subsequent film is deposited.
根據一或多個具體例,此基板連續地處在真空或「裝載閘」狀態下,且當從一腔室移動至下一個腔室時,不暴露於周圍空氣。移送腔室因此處在真空下且被「泵回(pump down)」至真空壓力下。惰性氣體可存在於處理腔室或移送腔室中。在某些具體例中,惰性氣體用於做為淨化氣體以在基板的表面上形成層之後移除某些或所有的反應物。根據一或多個具體例,淨化氣體被注射在沉積腔室的出口處以避免反應物從沉積腔室移動至移送腔室及/或額外的處理腔室。因此,惰性氣體的流動在腔室的出口處形成簾幕。 According to one or more specific examples, the substrate is continuously in a vacuum or "load gate" state and is not exposed to ambient air when moving from one chamber to the next. The transfer chamber is therefore under vacuum and is "pumped down" to vacuum pressure. The inert gas may be present in the processing chamber or the transfer chamber. In some embodiments, the inert gas is used as a purge gas to remove some or all of the reactants after forming a layer on the surface of the substrate. According to one or more specific examples, the purge gas is injected at the outlet of the deposition chamber to prevent the reactants from moving from the deposition chamber to the transfer chamber and/or additional processing chambers. Therefore, the flow of inert gas forms a curtain at the outlet of the chamber.
在處理期間,基板可被加熱或冷卻。此加熱或冷卻可藉由任何合適方式完成,包括但不限於改變基板支撐件(例如基座)的溫度與流動加熱或冷卻的氣體至基板表面。在某些具體例中,基板支撐件包括加熱器/冷卻器,其可被控制以傳導地改變基板溫度。在一或多個具體例中,被應用的氣體(反應性氣體或惰性氣體)被加熱或冷卻以局部地改變基板溫度。在某些具體例中,加熱器/冷卻器定位在腔室內鄰近於基板表面以對流地改變基板溫度。 During processing, the substrate can be heated or cooled. This heating or cooling can be accomplished by any suitable means, including but not limited to changing the temperature of the substrate support (such as a susceptor) and flowing heating or cooling gas to the surface of the substrate. In some embodiments, the substrate support includes a heater/cooler, which can be controlled to conductively change the temperature of the substrate. In one or more specific examples, the applied gas (reactive gas or inert gas) is heated or cooled to locally change the substrate temperature. In some embodiments, the heater/cooler is positioned in the chamber adjacent to the surface of the substrate to convectively change the temperature of the substrate.
此基板在處理期間也可為固定的或旋轉的。旋轉的基板可被連續地旋轉或以分離步驟方式旋轉。例如, 基板可在整個處理過程中被旋轉,或基板可在暴露於不同的反應性氣體或淨化氣體之間被小量地旋轉。在處理期間旋轉基板(連續地或間隔地)可助於產生更均勻的沉積或蝕刻,藉由最小化例如在氣體流動幾何中的局部變化性的效應。 The substrate can also be fixed or rotating during processing. The rotating substrate can be rotated continuously or in a separate step manner. E.g, The substrate may be rotated throughout the process, or the substrate may be rotated in a small amount between exposure to different reactive gases or purge gases. Rotating the substrate (continuously or at intervals) during processing can help produce more uniform deposition or etching, by minimizing effects such as local variability in gas flow geometry.
實例1Example 1
對照組Control group
鈦膜形成在基板表面的特徵中,其中特徵的底部及特徵的側壁為二氧化矽(SiO2)。基板溫度為~440℃而壓力為5托。氯化鈦(TiCl4)、氫(H2)、及氬(Ar)被供應至PECVD腔室。在沉積持續~300秒之後,腔室被淨化且抽空。下方表1提供狀態及完成的鈦膜形成。 The titanium film is formed in the features on the surface of the substrate, where the bottom of the feature and the sidewalls of the feature are silicon dioxide (SiO 2 ). The substrate temperature is ~440°C and the pressure is 5 Torr. Titanium chloride (TiCl 4 ), hydrogen (H 2 ), and argon (Ar) are supplied to the PECVD chamber. After the deposition lasted ~300 seconds, the chamber was purged and evacuated. Table 1 below provides the status and completed titanium film formation.
實例2Example 2
功率及載體氣體流動的效果。鈦膜形成在基板表面的特徵中,其中特徵的底部及特徵的側壁是二氧化矽(SiO2)。基板溫度為~440℃而壓力為5托。氯化鈦(TiCl4)、氫(H2)、及氬(Ar)被供應至PECVD腔室。在沉積持續~600秒之後,腔室被淨化且抽空。下方表2提供狀態及完成的鈦膜形成。 The effect of power and carrier gas flow . The titanium film is formed in the features on the surface of the substrate, where the bottom of the feature and the sidewalls of the feature are silicon dioxide (SiO 2 ). The substrate temperature is ~440°C and the pressure is 5 Torr. Titanium chloride (TiCl 4 ), hydrogen (H 2 ), and argon (Ar) are supplied to the PECVD chamber. After the deposition lasted ~600 seconds, the chamber was purged and evacuated. Table 2 below provides the status and completed titanium film formation.
當比較2-A與1-A時,降低RF功率改善底部覆蓋與選擇性。較低RF功率促進降低Ti+以改善底部覆蓋並減少突出(overhang)與最小化H+/H*動能以減少 來自SiO2的氧還原。關於與2-A相比較的2-B,增加載體氣體流動造成100%底部覆蓋與可相較的選擇性。載體氣體中的增量增加TiCl4,其蝕刻在同時的沉積與蝕刻處理中SiO2之上未反應的Ti。 When comparing 2-A with 1-A, reducing the RF power improves bottom coverage and selectivity. Low RF power facilitate reducing Ti + to improve and reduce the bottom cover projection (overhang) and the minimum of H + / H * from the kinetic energy to reduce the oxygen reduction of SiO 2. Regarding 2-B compared to 2-A, increasing carrier gas flow results in 100% bottom coverage and comparable selectivity. The increase in the carrier gas increases TiCl 4 , which etches unreacted Ti on the SiO 2 in the simultaneous deposition and etching process.
圖4提供標準化鈦膜厚度相對於沉積時間(秒)的圖形,實例1-A(對照組)是圖形的虛線而實例2-B是圖形的實線。較高的載體氣體速率與較低的功率造成在Si之上相較於在SiO2之上較快的沉積,其可改善選擇性。 Figure 4 provides a graph of standardized titanium film thickness versus deposition time (seconds). Example 1-A (control) is the dotted line of the graph and Example 2-B is the solid line of the graph. Higher carrier gas rate and lower power resulting in faster compared to the above Si deposition on the SiO 2, which may improve the selectivity.
實例3Example 3
壓力的效果。鈦膜形成在基板表面的特徵中,其中特徵的底部是矽(Si)而特徵的側壁是二氧化矽(SiO2)。基板溫度為~440℃而壓力是變化的。氯化鈦(TiCl4)、氫(H2)、及氬(Ar)被供應至PECVD腔室。在沉積持續~300秒的3-A及持續~600秒的3-B與3-C之後,腔室被淨化且抽空。下方表3提供狀態及完成的鈦膜形成於SiN之上的區域處、與SiO2之上的側壁及在Si之上的底部處的矽化鈦的形成。 The effect of stress . The titanium film is formed in the features on the surface of the substrate, where the bottom of the feature is silicon (Si) and the sidewall of the feature is silicon dioxide (SiO 2 ). The substrate temperature is ~440°C and the pressure varies. Titanium chloride (TiCl 4 ), hydrogen (H 2 ), and argon (Ar) are supplied to the PECVD chamber. After deposition of 3-A lasting ~300 seconds and 3-B and 3-C lasting ~600 seconds, the chamber was purged and evacuated. Table 3 below provides complete status and a titanium film is formed over the region of SiN, is formed over the titanium silicide and the side wall at the bottom of SiO on Si.
較高的壓力降低Ti+及H+的動能。達成>200%的底部覆蓋及>10:1的選擇性。圖5至7分別顯示實例3-A至3-C的TiSix膜的形成之後的高深寬比結構的TEM影像。 Higher pressure reduces the kinetic energy of Ti + and H +. Achieve >200% bottom coverage and >10:1 selectivity. 5 to 7 respectively show the TEM images of the high aspect ratio structure after the formation of the TiSi x films of Examples 3-A to 3-C.
實例4Example 4
脈衝RF。鈦膜形成在基板表面的特徵中,其中特徵的底部是矽(Si)而特徵的側壁是二氧化矽(SiO2)。基板溫度為~440℃,在350kHz的RF功率是65W(90mW/cm2),載體流動速率是125sccm,而壓力是5托。氯化鈦(TiCl4)、氫(H2)、及氬(Ar)被供應至PECVD腔室。在沉積之後,腔室被淨化且抽空。下方表4提供狀態及完成的鈦膜形成。 Pulse RF . The titanium film is formed in the features on the surface of the substrate, where the bottom of the feature is silicon (Si) and the sidewall of the feature is silicon dioxide (SiO 2 ). The substrate temperature is ~440°C, the RF power at 350kHz is 65W (90mW/cm 2 ), the carrier flow rate is 125 sccm, and the pressure is 5 Torr. Titanium chloride (TiCl 4 ), hydrogen (H 2 ), and argon (Ar) are supplied to the PECVD chamber. After deposition, the chamber is cleaned and evacuated. Table 4 below provides the status and completed titanium film formation.
脈衝RF改善選擇性及底部覆蓋。 Pulsed RF improves selectivity and bottom coverage.
實例5Example 5
高RF頻率。鈦膜形成在基板表面的特徵中,其中特徵的底部是矽(Si)而特徵的側壁是二氧化矽(SiO2)。基板溫度為~440℃,載體流動速率是125sccm,而壓力是5托。氯化鈦(TiCl4)、氫(H2)、及氬(Ar)被供應至PECVD腔室。在沉積持續~600秒之後,腔室被淨化且抽空。下方表5提供狀態及完成的鈦膜形成,其中N/U代表非均勻性。 High RF frequency . The titanium film is formed in the features on the surface of the substrate, where the bottom of the feature is silicon (Si) and the sidewall of the feature is silicon dioxide (SiO 2 ). The substrate temperature is ~440°C, the carrier flow rate is 125 sccm, and the pressure is 5 Torr. Titanium chloride (TiCl 4 ), hydrogen (H 2 ), and argon (Ar) are supplied to the PECVD chamber. After the deposition lasted ~600 seconds, the chamber was purged and evacuated. Table 5 below provides the status and completed titanium film formation, where N/U represents non-uniformity.
13.56MHz改善帶有在Si之上的相似電阻率的選擇性。 13.56MHz improves selectivity with similar resistivity above Si.
實例6Example 6
工作週期的效果。鈦膜形成在基板表面的特徵中,其中特徵的底部是矽(Si)而特徵的側壁是氧化矽(SiOx)或氮化矽(SiN)。基板溫度為~450℃,在13.56MHz的RF功率是65W(90mW/cm2),壓力是5托。5sccm的氯化鈦(TiCl4)、6000sccm的氫(H2)、及18000sccm的氬(Ar)被供應至PECVD腔室。在沉積之後,腔室被淨化且抽空。下方表6提供狀態、在各種表面之上的鈦膜的完成厚度、及選擇性。 The effect of the work cycle . The titanium film is formed in the features on the surface of the substrate, where the bottom of the feature is silicon (Si) and the sidewall of the feature is silicon oxide (SiO x ) or silicon nitride (SiN). The substrate temperature is ~450°C, the RF power at 13.56MHz is 65W (90mW/cm 2 ), and the pressure is 5 Torr. 5 sccm of titanium chloride (TiCl 4 ), 6000 sccm of hydrogen (H 2 ), and 18,000 sccm of argon (Ar) are supplied to the PECVD chamber. After deposition, the chamber is cleaned and evacuated. Table 6 below provides the status, the finished thickness of the titanium film on the various surfaces, and the selectivity.
CVD SiN之上的選擇性從約3改善向上至具有低工作週期的約21:1。注意到沉積速率也降低。在SiOx之上的選擇性從約10改善向上至具有低工作週期的約19。 The selectivity over CVD SiN improves from about 3 up to about 21:1 with a low duty cycle. Note that the deposition rate also decreases. The selectivity over SiOx improved from about 10 up to about 19 with a low duty cycle.
實例7Example 7
在低工作週期的功率的效果。鈦膜形成在未圖案化的基板表面之上。基板溫度為~450℃,在13.56MHz的RF功率在10%工作週期是變化的,壓力是5托。5sccm的氯化鈦(TiCl4)、6000sccm的氫(H2)、及18000sccm的氬(Ar)被供應至PECVD腔室。在沉積之後,腔室被淨化且抽空。下方表7提供狀態、沉積時間、及完成的選擇性。 The effect of power on low duty cycles . The titanium film is formed on the surface of the unpatterned substrate. The substrate temperature is ~450°C, the RF power at 13.56MHz varies during a 10% duty cycle, and the pressure is 5 Torr. 5 sccm of titanium chloride (TiCl 4 ), 6000 sccm of hydrogen (H 2 ), and 18,000 sccm of argon (Ar) are supplied to the PECVD chamber. After deposition, the chamber is cleaned and evacuated. Table 7 below provides status, deposition time, and finish selectivity.
即使在低工作週期,較高功率增加在SiN基板之上的TiSiN形成。 Even at low duty cycles, higher power increases TiSiN formation on the SiN substrate.
實例8Example 8
脈衝頻率產生器及工作週期的效果。鈦膜形成在基板表面的特徵中,其中特徵的底部是矽(Si)而特徵的側壁是氧化矽(SiOx)或氮化矽(SiN)。RF功率是65W(92mW/cm2)。工作週期數反映出功率開啟多長的時間與功率關閉多長的時間。此脈衝以兩種不同頻率完成:10kHz與5kHz。基板溫度為~450℃,脈衝頻率與工作週期是變化的,壓力是5托。5sccm的氯化鈦(TiCl4)、6000sccm的氫(H2)、及18000sccm的氬(Ar)被供應至PECVD腔室。在沉積之後,腔室被淨化且抽空。下方表8提供狀態、在各種表面之上的鈦膜的完成厚度、及選擇性。 The effect of pulse frequency generator and duty cycle . The titanium film is formed in the features on the surface of the substrate, where the bottom of the feature is silicon (Si) and the sidewall of the feature is silicon oxide (SiO x ) or silicon nitride (SiN). The RF power is 65W (92mW/cm 2 ). The number of duty cycles reflects how long the power is on and how long the power is off. This pulse is done at two different frequencies: 10kHz and 5kHz. The substrate temperature is ~450°C, the pulse frequency and duty cycle are variable, and the pressure is 5 Torr. 5 sccm of titanium chloride (TiCl 4 ), 6000 sccm of hydrogen (H 2 ), and 18,000 sccm of argon (Ar) are supplied to the PECVD chamber. After deposition, the chamber is cleaned and evacuated. Table 8 below provides the status, the finished thickness of the titanium film on various surfaces, and the selectivity.
CVD SiN之上的選擇性從約2.3改善向上至具有低工作週期的約5.5:1。注意到沉積速率也降低。在SiOx之上的選擇性從約6改善向上至具有低工作週期的約11。 The selectivity over CVD SiN improves from about 2.3 up to about 5.5:1 with a low duty cycle. Note that the deposition rate also decreases. The selectivity over SiOx improved from about 6 up to about 11 with a low duty cycle.
儘管前述係關於本發明的具體例,在不悖離本發明的基本範疇下可構思本發明的其他及進一步的具體例,且本發明的範疇是由接下來的申請專利範圍所決定。 Although the foregoing is about specific examples of the present invention, other and further specific examples of the present invention can be conceived without departing from the basic scope of the present invention, and the scope of the present invention is determined by the scope of the following patent applications.
100:處理 100: processing
110、120、130、140、150、160、170、180:步驟 110, 120, 130, 140, 150, 160, 170, 180: steps
200:基板 200: substrate
210:特徵 210: Features
212:底部表面 212: bottom surface
214、216:側壁 214, 216: side wall
220:基板表面 220: substrate surface
230:鈦膜 230: titanium film
藉由參照具體例(某些具體例繪示在隨附圖式中),可獲得簡短總結於上的本發明的更明確的說明,以此方式可詳細理解本發明上述特徵。然而,將注意到隨附圖式僅繪示本發明的典型具體例,且因此不被認為限制本發明的範疇,由於本發明可容許其他相等有效的具體例。 By referring to specific examples (some specific examples are shown in the accompanying drawings), a clearer description of the present invention briefly summarized above can be obtained, and in this way, the above-mentioned features of the present invention can be understood in detail. However, it will be noted that the accompanying drawings only illustrate typical specific examples of the present invention, and therefore are not considered to limit the scope of the present invention, as the present invention may tolerate other equally effective specific examples.
圖1顯示根據本發明的一或多個具體例的處理的處理流程圖;圖2是具有特徵的基板的部分剖面視圖;圖3是在特徵中選擇性沉積的鈦膜的部分剖面視圖;圖4是標準化(normalized)的鈦膜厚度相對於沉積時間(秒)的圖形;以及圖5至7提供在鈦膜的形成之後的高深寬比結構的穿透式電子顯微鏡(TEM)影像。Figure 1 shows a processing flow chart of one or more specific examples of the present invention; Figure 2 is a partial cross-sectional view of a substrate with features; Figure 3 is a partial cross-sectional view of a titanium film selectively deposited in the features; 4 is a graph of normalized titanium film thickness versus deposition time (seconds); and FIGS. 5 to 7 provide transmission electron microscope (TEM) images of the high aspect ratio structure after the formation of the titanium film.
國內寄存資訊 (請依寄存機構、日期、號碼順序註記) 無Domestic hosting information (please note in the order of hosting organization, date, and number) None
國外寄存資訊 (請依寄存國家、機構、日期、號碼順序註記) 無Foreign hosting information (please note in the order of hosting country, institution, date, and number) None
210‧‧‧特徵 210‧‧‧Features
212‧‧‧底部表面 212‧‧‧Bottom surface
214、216‧‧‧側壁 214, 216‧‧‧ side wall
220‧‧‧基板表面 220‧‧‧Substrate surface
230‧‧‧鈦膜 230‧‧‧Titanium film
Claims (17)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201662426002P | 2016-11-23 | 2016-11-23 | |
| US62/426,002 | 2016-11-23 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| TW201825699A TW201825699A (en) | 2018-07-16 |
| TWI719269B true TWI719269B (en) | 2021-02-21 |
Family
ID=63640224
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| TW106140671A TWI719269B (en) | 2016-11-23 | 2017-11-23 | Deposition of metal films |
Country Status (1)
| Country | Link |
|---|---|
| TW (1) | TWI719269B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11430661B2 (en) | 2018-12-28 | 2022-08-30 | Applied Materials, Inc. | Methods and apparatus for enhancing selectivity of titanium and titanium silicides during chemical vapor deposition |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TW201619425A (en) * | 2014-11-07 | 2016-06-01 | 應用材料股份有限公司 | Method for thermally forming a selective cobalt layer |
-
2017
- 2017-11-23 TW TW106140671A patent/TWI719269B/en not_active IP Right Cessation
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TW201619425A (en) * | 2014-11-07 | 2016-06-01 | 應用材料股份有限公司 | Method for thermally forming a selective cobalt layer |
Also Published As
| Publication number | Publication date |
|---|---|
| TW201825699A (en) | 2018-07-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP7574360B2 (en) | Molybdenum Filling for 3D NAND and Other Applications | |
| TWI758398B (en) | Method of forming cobalt layer on substrate | |
| JP6502440B2 (en) | How to Enable Seamless Cobalt Gap Filling | |
| US10096514B2 (en) | Seamless trench fill using deposition/etch techniques | |
| TWI796388B (en) | Methods of reducing or eliminating defects in tungsten film | |
| US8586479B2 (en) | Methods for forming a contact metal layer in semiconductor devices | |
| US20180158686A1 (en) | Deposition Of Metal Films | |
| EP3539147A1 (en) | Methods for self-aligned patterning | |
| JP6946463B2 (en) | How to reduce wordline resistance | |
| JP7305622B2 (en) | Volume expansion of metal-containing films due to silicidation | |
| JP2023029868A (en) | Method of forming a tungsten pillar | |
| TWI719269B (en) | Deposition of metal films | |
| US20240332075A1 (en) | Gradient metal liner for interconnect structures | |
| US20240420996A1 (en) | Selective self-assembled monolayer (sam) removal | |
| US20230340661A1 (en) | Gapfill Process Using Pulsed High-Frequency Radio-Frequency (HFRF) Plasma | |
| JP2025011042A (en) | Gap-filling process using pulsed high frequency radio frequency (HFRF) plasma | |
| WO2025226900A1 (en) | Flux gradient molybdenum growth process | |
| TW202546259A (en) | Molybedenum fill |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MM4A | Annulment or lapse of patent due to non-payment of fees |