Spreadsheet: 466b2d9c-13d6-4530-b279-1054dfb1bb57
Sheet: 2.  KPPs for Pyrolysis

Table 2.  Key Performance Parameters for Proposed Commercial Facility: Thermochemical- Pyrolysis Production of Biofuels |  |  |  |  | PROPRIETARY/BUSINESS SENSITIVE
Project Title:
 |  |  |  |  | [Metrics projected to commercial scale, based on demonstrated data]
TECHNICAL DATA INPUTS
Section | Key Performance Parameter | Demonstrated Value(s)* | Target Value(s) (if different than demonstrated) | Basis/Justification** (consistent with Table 1) | Notes / Directions / Examples
Product (s) and By-Products | List all products (biofuels and biofuel intermediates) and by-products serving as revenue. |  |  |  | Please list here.  Example Products: butanol, lipids, renewable diesel, jet fuel                                                               Example By-Products: electricity
Feedstock (as delivered) | Feedstock Type(s) |  |  |  | Examples: corn stover, switchgrass, forest residues
 | Feedstock Cost ($/BDMT)
 | Feedstock Moisture (wt %)
 | C, H, N, O, S (wt %) (dry basis)
 | Ash content wt (%) (dry basis)
Pyrolysis | Gas Yield (kg/BDMT)
 | Char/Ash Yield (kg/BDMT)
 | Water-Phase Yield (kg/BDMT)
 | Bio-Oil Yield (kg/BDMT)
 | Bio-Oil Moisture Content (wt%)
 | Bio-Oil Oxygen Content (wt%)  (dry basis)
 | Energy Efficiency  across Pyrolysis (%)  (LHV)
Bio-Oil Stabilization | Catalyst(s) usage/replacement in stabilization ($/gal biofuel(s)) |  |  |  | if applicable
(if applicable) | H2 Consumption in Stabilization (kg/gal biofuel(s)) |  |  |  | if applicable
 | [NAME] Yield (kg/kg of Bio-oil feed)
 | [NAME] and Ash Reduction in Stabilization (wt%)
 | Metals Reduction in Stabilization (wt%)
 | [NAME] Moisture Content (wt%)
 | [NAME] (wt%) (dry basis)
Upgrading to Fuel(s)/ | Catalyst(s) usage/replacement in upgrading ($/gal biofuel(s)) |  |  |  | if applicable
[NAME]) (If applicable) | H2 Consumption in Upgrading (kg/gal biofuel(s)) |  |  |  | if applicable
 | Gas Yield in Upgrading (kg/gal biofuel(s) produced)
 | Liquid Fuel(s)/Product(s) Yield in Upgrading (kg/kg oil feed)
 | Liquid Fuel(s)/Product(s) Oxygen Content (wt%)  (dry basis) |  |  |  | list separately for each product stream
 | Liquid Fuel(s)/Product(s) Moisture Content (wt%) |  |  |  | list separately for each product stream
 | Refinery Insertion Point for Liquid Fuel(s) |  |  |  | if applicable, list separately for each product/steam
 | Liquid Fuel(s)/Product(s) Miscibility with Petroleum Steam(s) |  |  |  | list separately for each product stream
Overall Yields | Overall Glucan to Product Biofuel(s) Yield (%) |  |  |  | for biochemical processes only
 | Overall Xylan to Product Biofuel(s) Yield (%) |  |  |  | for biochemical processes only
 | Overall minor sugars to Product Biofuel(s) Yield (%) |  |  |  | for biochemical processes only
 | Overall Yield from Biomass (unit/BDMT)                                                                --Jet Fuel (gal/BDMT) [NAME] (gal/BDMT) --Naphtha/gasoline (gal/BDMT)                                                                           --Export Power (kWhr/BDMT)                                                               --Export Steam (MMBTU/BDMT) --Other products/byproducts (unit/BDMT) |  |  |  | Provide separately for each product and by-product (e.g. gal ethanol/BDMT), kW of excess electricity/BDMT)
 | Overall Gate-to-Gate Energy efficiency (%) (LHV) |  |  |  | ([NAME]) and by-products out)/(Biomass plus other input fuels in)
Overall Usage Rates (based on demonstrated data and projected to commercial scale) | Chemicals and Materials Costs ($/gal biofuel(s)) |  |  |  | Include enzymes, chemical, catalysts, import [NAME], other materials, solvents, etc
 | Utilities Imported to/Purchased for Process: --Electricity (kWhr/gal biofuel(s))                                                                   --Natural gas (MMBTU/gal biofuel(s))                                                                 --Steam (MMBTU/gal biofuel(s)) |  |  |  | Example: purchased electricity = 1.2kWh/BDMT
 | Purchased water (gal/gal biofuel(s)) |  |  |  | Include process water, cooling water, boiler feed water makeup, etc.
Wastes (based on demo'd data/projected to commercial) | Waste Water for Treatment (gal/gal biofuel(s)) |  |  |  | Include assumptions for water recycle/re-use
 | [NAME] (kg/gal biofuel(s))
Capital Costs***  (projected to | Commercial Plant Design Capacity (BDMT/day) |  |  |  | Design capacity for capital cost estimate
commercial scale) | Total Capital Investment ($)
 | [NAME] (if applicable) ($) --Pyrolysis Equipment Cost ($) --Bio-Oil Stabilization Equipment Cost (if applicable) ($) --Upgrading/Separations Equipment Cost (if applicable) ($) --ISBL Installation Cost ($) --Utilities/OSBL ($) --Buildings ($) --Land ($) --Indirect Costs ($) --Contigency ($) |  |  |  | ISBL - inside battery limits; OSBL - outside battery limits
Labor Costs (projected to commercial scale) | Expected Commercial Plant Staffing (FTE) |  |  |  | Provide an estimate of the number of people it will take to operate the full-scale commercial plant. Include process operators and immediate supervision. Express as the number of Full Time Equivalent people.
* Provide the best value achieved to date based on actual data, not design specs or plans
**Describe  the basis or justification for current best result and the scale at which it was achieved. Examples of basis include: number of hours at steady state (steady state typically defined as continuous operation of the integrated process for ≥3 residence times), or the results of a number of replicate short runs of the isolated process step, etc. Include how the measurement was made (e.g. analysis of the gasifier outlet stream using gas chromatography).  Reference information in Table 1 as necessary.
***For Capital estimates, please include the level of confidence in the data and provide ranges if applicable.