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脱炭素ロードマップ:塗料・コーティング産業における優先順位付き緩和ヒエラルキー

Decarbonization Roadmap: Prioritized Mitigation Hierarchy in the Paint and Coating Industry (原題)

(著者不明)

Sustainability📚 査読済 / ジャーナル2026-09-09#Scope 3Origin: EU経営インパクト: 調達リスク対象セクター: chemicals
DOI: 10.3390/su18189266
原典: https://doi.org/10.3390/su18189266
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🤖 gxceed AI 要約

日本語

塗料・コーティング製造14拠点の実データと監査済みベースライン工場(年35,640トン)を用い、ライフサイクルGHG会計を実施。上流原材料調達(カテゴリ4)が全排出の89.48%を占めることを示した。MCDA(多基準意思決定分析)により、削減ポテンシャル・TRL・資本強度・回収期間を統合し、バイオ樹脂代替を最優先とする6段階の脱炭素ヒエラルキーを構築した。

English

Using operational data from 14 coating manufacturing sites and an audited baseline facility (35,640 t/yr), this study applies lifecycle GHG accounting, finding upstream raw materials (Category 4) dominate at 89.48% of the 192,834 tCO2e footprint. An MCDA framework integrating abatement potential, TRL, capital intensity, and payback yields a prioritized Six-Tier Decarbonization Hierarchy, with bio-based resin substitution as top priority.

Unofficial AI-generated summary based on the public title and abstract. Not an official translation.

📝 gxceed 編集解説 — Why this matters

日本のGX文脈において

CSRD・CSDDD・CBAM対応が日本企業のサプライチェーンにも波及する中、Scope3カテゴリ4の削減優先順位と投資判断フレームは、SSBJ開示や有報でのScope3記載を迫られる化学・素材メーカーにとって実務的示唆が大きい。

In the global GX context

Provides a replicable MCDA-based prioritization method for Scope 3 Category 4 abatement in chemicals, directly relevant to CSRD/CBAM compliance and transition planning under ISSB. Offers a sector-specific template for translating lifecycle accounting into capital allocation decisions.

👥 読者別の含意

🔬研究者:Scope3カテゴリ4優位性とMCDAによる脱炭素優先順位付けの実証事例として、化学産業の脱炭素研究に有用。

🏢実務担当者:バイオ樹脂代替やPPAなど、投資回収と削減量を踏まえた段階的削減策の優先順位決定に活用可能。

🏛政策担当者:CBAM・CSRD下でのScope3削減支援策や、化学産業向け技術中立な政策設計の参考になる。

📄 Abstract(原文)

Anthropogenic greenhouse gas (GHG) emissions from chemical manufacturing present substantial operational, compliance, and competitive challenges under international climate accords and emerging regulatory frameworks, including the European Union Corporate Sustainability Due Diligence Directive (CSDDD), the Corporate Sustainability Reporting Directive (CSRD), and the Carbon Border Adjustment Mechanism (CBAM). This study provides an empirically grounded, multi-site decarbonization framework combining longitudinal quarterly operational datasets collected from 14 industrial coating manufacturing facilities (2024–2025) with an audited baseline manufacturing facility producing 35,640 metric tonnes annually. Lifecycle GHG accounting reveals that upstream raw material procurement and synthesis (Category 4) dominate the value-chain carbon footprint, contributing 89.48% (172,557 tCO2e) of the total 192,834 tCO2e baseline organizational footprint. In contrast, direct stationary combustion (Category 1) and purchased electricity (Category 2 location-based) account for only 0.89% (1711 tCO2e) and 2.46% (4741 tCO2e), respectively. To resolve implementation trade-offs, a Multi-Criteria Decision Analysis (MCDA) framework integrates annual carbon abatement potential, Technology Readiness Level (TRL), capital intensity, and payback dynamics to establish a prioritized Six-Tier Decarbonization Hierarchy: Tier 1 (Priority 1)—upstream bio-based resin and binder substitution, delivering an estimated baseline reduction of 25,880–60,050 tCO2e/year (13.4–31.1% of baseline emissions); Tier 2 (Priority 2)—drop-in bio-based and circular solvent replacement, achieving 4820–9640 tCO2e/year (2.5–5.0% baseline reduction); Tier 3 (Priority 3)—thermal process electrification via high-temperature industrial heat pumps (COP 2.5–3.1), eliminating 1027–1369 tCO2e/year; Tier 4 (Priority 4)—contractual and on-site renewable electricity procurement via corporate Power Purchase Agreements (PPAs) and solar PV (4490–4741 tCO2e/year; 2.3–2.5% baseline reduction); Tier 5 (Priority 5)—systemic formulation transitions to waterborne, high-solids, and powder coating architectures (15,000–35,000 tCO2e/year); and Tier 6 (Priority 6)—stream-conditional Carbon Capture, Utilization, and Storage (CCUS), strictly restricted to concentrated combustion stacks (CO2 ≥ 8 vol%) and excluded from dilute post-thermal oxidizer off-gases (CO2 ≤ 1–4 vol%) where capture is economically unviable ($180–$260/tCO2e).

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