Spreadsheet: 2428094c-651a-4e2a-8a37-93092e98b117
Sheet: Application Data Table

Application Data Key Performance Parameters Table |  |  | PROPRIETARY/BUSINESS SENSITIVE
Project Title:
TECHNICAL DATA INPUTS
Section | Key Performance Parameter | Demonstrated [NAME])* | Targeted Value(s) |  | Basis/Justification** | Notes / Directions / Examples
 |  |  | Period of Performance 1 | Period of Performance 2
Product (s) and By-Products | List all products (biofuels and biofuel intermediates) and by-products serving as revenue. |  |  |  |  | Please list here.  Example Products: biofuel intermediate,                                                                Example By-Products: high-value oil or meal, etc.
Envisioned Commercial Plant | Commercial Plant Design Capacity (gal biofuel intermediate/day)
 | Commercial Plant Pond/PBR Acreage (acres)
Feedstock | Algal Cultivar  (Genus/species defined) |  |  |  |  | It is understood that the lipid, carbohydrate, and protein content numbers are dependent on a particular growth condition.  It is assumed that the numbers reported will be representative of the systems described in the narrative.
Algae Cultivation | Time from innoculation to harvest (days) |  |  |  |  | Please note if these values are different based on seasonal variations.  If so, please include a range and note appropriately.
 | Net N demand (mg/g algae)
 | Net P demand (mg/g algae)
 | Make-up N, after [NAME] (mg/g algae) |  |  |  |  | This assumes nutrients are being recycled back into the cultivation system.  If nutrients are not recycled mark as NA.
 | Make-up P, after [NAME] (mg/g algae)
 | Media Cost ($/gal biofuel intermediate)
 | CO2 Source
 | CO2 Purity (wt%)
 | CO2 Usage (g/g algae)
 | CO2 Cost ($[NAME])
 | Algal Pond/PBR Productivity (g algae biomass/m2/day)
 | Algae Lipid Content (g/g algae biomass)
 | Water Source (s)
 | Make-up Water (gal/gal biofuel intermediate)
 | Cultivation Mixing Energy (kWhr/gal biofuel intermediate)
Algae Cultivation for Mixotrophic Process (if applicable) | Feed sugar stream type
 | Feed sugar stream rate (kg/gal biofuel intermediate)
 | Feed sugar stream organic/sugar concentration (wt%)
 | Feed sugar stream cost ($/kg) |  |  |  |  | as purchased
 | Make-up Nutrients (kg/gal biofuel intermediate)
 | Nutrient Cost ($/kg)
 | Make-up Water (gal/gal biofuel intermediate)
 | Make-up algae culture (kg/gal biofuel intermediate) |  |  |  |  | if relevant
 | Algae culture cost ($/kg)
 | Fermentation Time (hrs)
 | Algal Oil Lipid Content (wt%)
Harvesting, Dewatering, and Concentration (as applicable) | Algae Concentration at Harvest Step(g/L) |  |  |  |  | It is assumed that 3 steps are needed to harvest microalgae suspended in culture - harvest, dewatering, concentration.  Note and provide appropriate alternative information if proposed system differs from the baseline assumed in the FOA.
 | Algae Concentration to De-watering Step (g/L)
 | Algae Concentration to Concentrating Step (g/L)
 | Algae Concentration to Algal Biomass Processing (g/L) |  |  |  |  | It is assumed that there is a defined % solids of whole algae biomass necessary to size downstream preprocessing equipment (extraction, fractionation, thermal processing, etc.).  Note and provide appropriate alternative information if the proposed system differs from the baseline assumed in the FOA
 | Harvest Step Inlet Flow Rate (gpm)
 | De-watering Step Inlet Flow Rate (gpm)
 | Concentrating Step Inlet Flow Rate (gpm)
 | Algae Steam Flow Rate to Algal Biomass Processing (gpm)
 | Harvest and De-watering Efficiency (%) |  |  |  |  | g algae recovered/g algae fed
 | Water Recovery in Harvest and De-watering (%)
Algal Biomass Processing (as applicable) | Homogenization Type (if applicable) |  |  |  |  | It is assumed that the result of harvest operations are a wet slurry of whole algae biomass.  It is recognized that many operations are possible at this process point.  Please note and provide appropriate altenative information if the proposed system differs from the baseline assumed in the FOA.
 | Homogenization Power (kwhr/gal biofuel intermediate)
 | Extraction Solvent Type and Purity (if applicable)
 | Fraction of Solvent Recovered (%)
 | Lipid Recovery in Algal Biomass Processing (wt%)
 | Make-up Solvent (gal/gal biofuel intermediate)
 | Total Algal Biomass Processing Power Req's (kWhr/gal biofuel interm.)
 | Total Algal Biomass Processing Heat Req's (MMBTU/gal biofuel interm.)
 | Biofuel Intermediate Flow Rate (gpm)
 | Algal Biomass Processing Efficiency (g biofuel int/g algae fed)
 | Water Recovery in Algal Biomass Processing (%)
Biofuel Intermediate Characteristics | Moisture Content (wt%)
 | Metals Content (wt%)
 | Total N Content (wt%)
 | Total P Content (wt%)
 | Free Fatty Acid Content (wt%)
 | [NAME] (wt%)
* 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.