Wet chemistries often incorporate multidentate chelating agents that form stable complexes with metallic byproducts, thereby weakening the structural integrity of the post-etch crust, similar to mechanisms utilized in post-CMP defect removal .
Following the PMD 4 Oxide Etch, the Metal 1 trench is
physically defined, but the dielectric surface is heavily contaminated with residual photoresist, bottom anti-reflective coating (BARC), and crosslinked fluorocarbon (CFx) polymers generated during the RIE process . This Ashing & Strip/Clean step must completely remove these organic and organometallic residues to expose a pristine dielectric surface before the subsequent Ta-based liner deposition . If residues remain, they will severely degrade the adhesion of the Ta liner, inhibit proper Cu seed coverage, and ultimately lead to electromigration failures and high contact resistance in the interconnect . This specific step is distinct from other ash/clean steps in the flow because it occurs exactly at the transition into the copper damascene metallization (MET1), meaning the delicate PMD/low-k dielectric sidewalls are now fully exposed and highly susceptible to chemical and plasma-induced damage . The cleaning process fundamentally operates through a combination of structural modification and selective chemical dissolution . During the preceding oxide etch, fluorocarbon plasmas intentionally deposit highly crosslinked, C–F rich fluoropolymer networks on the trench sidewalls to maintain etching anisotropy . Traditional high-temperature O2 plasma ashing can cause the photoresist to undergo severe crosslinking and hardening, leaving carbon-rich polymeric residues that are extremely difficult to remove via conventional wet treatments . To break this resilient network without damaging the porous low-k dielectric, the process can utilize ultraviolet (UV) irradiation at nanoscale to induce photochemical chain scission of the C–C and C–F bonds within the polymer backbone, which reduces crosslink density and introduces polar groups to lower surface energy . Subsequently, a specialized wet processing solution containing water-soluble organic solvents and specifically engineered active components is introduced . This solution selectively dissolves the functional groups in the modified photoresist and chemically complexes the inorganic-organic composite crust, stripping it away through penetration and interfacial delamination . The selection of a carefully controlled wet clean, or a hybrid low-damage ash/wet clean sequence, is dictated by the extreme sensitivity of the nanoscale low-k dielectric layers . Because conventional oxygen or fluoro-oxygen plasmas strip out methyl groups and aggressively raise the dielectric constant (k-value) of porous low-k films, low-damage all-wet or modified-ash solutions are strictly required . Wet chemistries often incorporate multidentate chelating agents that form stable complexes with metallic byproducts, thereby weakening the structural integrity of the post-etch crust, similar to mechanisms utilized in post-CMP defect removal . The introduction of megasonic agitation enhances mass transport of the chemical liquid into the high-aspect-ratio nanoscale trenches via cavitation and microjets, significantly overcoming the physical transport limitations inherent to fine structures . Furthermore, wet processing solutions can be buffered with specific metal ions or mild alkaline components to regulate interfacial interactions, promoting the swelling of highly cross-linked etch residues while simultaneously suppressing chemical attack on the delicate low-k dielectric framework . At the 40nm node, the physical dimensions of the M1 trenches severely restrict the process window for residue removal (Engineering Practice). Due to capillary forces and micro-loading effects, liquid transport into and out of dense trenches is restricted, necessitating precise optimization of parameters such as temperature, megasonic power, and solvent composition . An overly aggressive clean will laterally etch the dielectric sidewalls, leading to trench widening, Ta-liner voiding, and unacceptable shifts in wire capacitance . Conversely, insufficient solvent penetration leaves polymer pinch-off residues near the trench bottom, directly causing metal opens during the subsequent copper fill .
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