Prompt template
Run these steps in order.
01
Act as a venture capital consultant and pitch architect. Develop a 12–15-slide pitch deck for LoopGen’s advanced carbon-to-value project in the Pilbara, Western Australia. 02
Build a Total System Efficiency narrative around the Advanced Loop model and its stated net energy efficiency of 78–82%. Clearly distinguish projections and claims from independently verified facts. 03
Prepare slides covering: 04
1. Vision & Title Slide: Present LoopGen’s name and a compelling hook about capturing carbon and advancing the circular economy in the Pilbara. 05
2. The Problem: Address industrial hard-to-abate emissions, rising carbon taxes, fossil diesel price volatility, demand for local green ammonia for explosives (ANFO), and the cost and intermittency challenges of first-generation green hydrogen projects. 06
3. The Solution: Introduce LoopGen 3.0 as a multi-product biorefinery featuring 1 Mtpa of calcium-looping carbon capture, 1.9 GW of electrolysis, and production of e-Diesel, SAF, and mxANFO. 07
4. Unfair Advantage: Explain process integration and oxygen valorisation, including the proposed use of electrolysis oxygen to power 300 MWe Allam-Fetvedt sCO₂ turbines. Present the stated 35% (875 MW) renewable energy CAPEX reduction, clarifying its basis. Explain recovery of Fischer–Tropsch and Haber–Bosch process heat into molten-salt storage, with a stated 8% reduction in site electricity use. 08
5. Market Opportunity: Highlight Pilbara mining demand for explosives and heavy-haul diesel. Explain how solar and wind resources and existing LNG infrastructure could reduce new-build costs, supporting claims with evidence where available. 09
6. Technology Stack: Discuss Fischer–Tropsch (TRL 9), Haber–Bosch (TRL 9), and calcium looping (TRL 6–7), and explain the benefits and integration risks. Include FT CANS™ technology and its stated 3× productivity and 50% CAPEX reduction in e-fuel synthesis. 10
7. Business Model & Revenue Streams: Define primary products (diesel, SAF, and mxANFO) and secondary revenue sources (ACCUs, CO₂ offtake agreements, and grid-stabilising excess power). Present the stated annual EBITDA target of A$885 million and seven-year base-case payback, identifying the assumptions behind these projections. 11
8. Strategic Operational Reductions: Explain how chemical-looping combustion (CLC) is intended to reduce calciner natural gas use by 70%, and how SE-SMR-CL integration is intended to downsize electrolysis infrastructure by 10%. 12
9. Project Timeline & Milestones: Detail the phases: pilot integration of SOEC, FT, and molten salt; FEED and long-term bankable offtake agreements; and full-scale deployment targeting the 2035 market. 13
10. Financial Performance Highlights: Present net CAPEX of US$3.629 billion, NPV of US$2.8 billion at a 10% discount rate, and IRR of 24.7%. Explain how these stated figures compare with the Gen 1.0 baseline and disclose key assumptions. 14
11. The Ask & Use of Funds: Specify funding needs for detailed Front-End Engineering Design (FEED) and de-risking integrated advanced power cycles, alongside strategic partnerships for Pilbara-based offtake. 15
Review all slide content and suggest improvements to enhance clarity, impact, and coherence. Identify missing investor essentials, such as team, competition, risks, and a clear closing, and recommend how to fit them within the 12–15-slide deck.