2007
DOI: 10.1016/j.surfcoat.2007.05.009
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Batch ALD: Characteristics, comparison with single wafer ALD, and examples

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Cited by 120 publications
(103 citation statements)
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“…17 However, they suffer from a limited thermal stability which can lead to a parasitic CVD component and might result into high impurity concentrations and poor film uniformity. 25 In addition, Kukli et al have demonstrated that the HfO 2 ALD process using TEMAH in combination with H 2 O as oxygen source leads to an increment in GPC from 0.9 Å /cycle at 250 C to 1.5 Å / cycle at 325 C, indicating the decomposition of the precursor at temperatures !300 C. 17 To overcome this, an ALD process using the cyclopentadienyl (Cp ¼ C 5 H 5 ) precursor type was investigated. A higher thermal stability was achieved and ALD saturation was realized at a relative high substrate temperature of 400 C. 22 However, a lower GPC of $0.5 Å /cycle was obtained when using Cp-precursors like (CpMe) 2 HfMe 2 and (CpMe) 2 Hf(OMe)Me as compared to the alkylamides ($0.9 Å /cycle).…”
Section: Introductionmentioning
confidence: 99%
“…17 However, they suffer from a limited thermal stability which can lead to a parasitic CVD component and might result into high impurity concentrations and poor film uniformity. 25 In addition, Kukli et al have demonstrated that the HfO 2 ALD process using TEMAH in combination with H 2 O as oxygen source leads to an increment in GPC from 0.9 Å /cycle at 250 C to 1.5 Å / cycle at 325 C, indicating the decomposition of the precursor at temperatures !300 C. 17 To overcome this, an ALD process using the cyclopentadienyl (Cp ¼ C 5 H 5 ) precursor type was investigated. A higher thermal stability was achieved and ALD saturation was realized at a relative high substrate temperature of 400 C. 22 However, a lower GPC of $0.5 Å /cycle was obtained when using Cp-precursors like (CpMe) 2 HfMe 2 and (CpMe) 2 Hf(OMe)Me as compared to the alkylamides ($0.9 Å /cycle).…”
Section: Introductionmentioning
confidence: 99%
“…Unfortunately, these prerequisites are considered to be the weak points of ALD. One way to increase the throughput of an ALD system is to do batch processing, 5 but this is not always compatible with the in-line processes often used in the before mentioned applications. A significant reduction of the cost of ownership of ALD processes and equipment must be realized to make ALD economically viable for these new applications.…”
Section: Introductionmentioning
confidence: 99%
“…ALD film properties, surface reaction conditions, and pore geometries for the four studies to which our modeling results are compared. Values in parentheses () are estimated from known quantities; for example the pressure and exposure times corresponding to the Gordon et al study were computed to match the known exposure of 9000 L (Langmuir); likewise, the pore dimensions were fitted to the known AR ¼ 43. study film Gordon [2] HfO 2 Granneman [1] HfO 2 Rubloff [19] HfO 2 George [20] …”
Section: Comparison To Previous Knudsen Transport Resultsmentioning
confidence: 99%
“…The importance of ALD time-scale analysis from an industrial perspective is presented in Granneman et al [1] where several configurations of single-wafer reactors and multi-wafer batch reactor systems are analyzed. In the cited study, the authors break down the time-scale analysis to ALD precursor chemisorption on flat substrates and within high-aspect-ratio cylindrical pores; these processes are then combined with overall precursor material balances corresponding to the macroscopic-scale transport through each reactor system.…”
Section: Previous Workmentioning
confidence: 99%