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

Table 2.  Key Performance Parameters for Proposed Commercial Facility: Biochemical 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 ($/BDMT)
 | Feedstock Moisture (wt %)
 | Range and average cellulose (glucan) content (wt %) (dry basis) |  |  |  | Example:  33-43%, 36.5%
 | Range and average hemicellulose (xylan) content (wt %) (dry basis)
 | Range and average lignin content (wt %) (dry basis)
 | Ash content wt (%) (dry basis)
Pretreatment | [NAME] in Pretreatment (%)
 | [NAME] to xylose Yield (%)
Hydrolysis/Sach. | [NAME] in Hydrolysis (%)
 | Hydrolysis Time (hrs)
 | Enzyme Loading (mg/g cell.)
 | Glucan to [NAME] (%)
Fermentation | [NAME] in Fermentation (%)
 | Fermentation time (days)
 | Sugars (and precursors for SSF) Conversion to Product Biofuel(s) (%)
 | Product Biofuel(s) Fermentation titer (g/L)
Overall Yields | Overall Glucan to Product Biofuel(s) Yield (%) |  |  |  | for biochemical processes only
 | Overall Xylan to Product Biofuel(s) Yield (%) |  |  |  | for biochemical processes only
 | Overall minor sugars to Product Biofuel(s) Yield (%) |  |  |  | for biochemical processes only
 | Overall Yield from Biomass (unit/BDMT)                                                                --Jet Fuel (gal/BDMT) [NAME] (gal/BDMT) --Naphtha/gasoline (gal/BDMT)                                                                           --Export Power (kWhr/BDMT)                                                               --Export Steam (MMBTU/BDMT) --Other products/byproducts (unit/BDMT) |  |  |  | Provide separately for each product and by-product (e.g. gal ethanol/BDMT), kW of excess electricity/BDMT)
 | Overall Gate-to-Gate Energy efficiency (%) (LHV) |  |  |  | ([NAME]) and by-products out)/(Biomass plus other input fuels in)
Overall Usage Rates (based on demonstrated data and projected to commercial scale) | Chemicals and Materials Costs ($/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 (TCI) ($)
 | [NAME] ($) --Hydrolysis/Sach. Equipment Cost ($) --Fermentation Equipment Cost ($) --Separations Equipment Cost ($) --ISBL Installation Cost ($) --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.