We develop the CelloFuel Portable Biomass Refinery, for producing low-carbon bioethanol from sugarcane, sweet sorghum, sugar beet and softwood wood chips. Our goal is to make bioethanol at a lower cost than existing technologies while at the same time producing bioethanol with less carbon intensity.
The CelloFuel Portable Biomass Refinery has two parts, making ethanol-rich biomass using solid-state fermentation and extracting the ethanol using a patented biomass distillation column.
We reduce the capital expenses (CAPEX) of producing bioethanol by:
Our goal is a CAPEX of less than $0.50 per gallon/year for ethanol from sugarcane and sweet sorghum, which is less than that of a modern corn ethanol plant. Our goal is a CAPEX of less than $1 per gallon/year for ethanol from softwood wood chips, which is significantly less than that of lignocellulosic ethanol plants.
We reduce the operating expenses (OPEX) and carbon intensity of producing bioethanol by:
The CelloFuel modules produce hydrous ethanol at 80% to 95% Alcohol By Volume (ABV). This can be used to produce potable ethanol, fuel for motors and fuel for cooking. This hydrous ethanol can be transported to a central refinery for further production of transportation fuels or higher-value chemicals.
The CelloFuel Portable Biomass Refinery is made from multiple CelloFuel modules, each made of a vertical HDPE pipe. The pipes are loaded by rotating the pipe around its center of gravity on a trunnion.
The top and bottom of the HDPE pipe are joined with steel plates coated with fusion bonded epoxy, or alternatively type 444 stainless steel. The top cap circulates water for a distillation dephlegmator. The top cap can be lifted off the HDPE pipe for biomass loading and unloading. An induction heater, steam heater or hot oil heater is used to apply heat to the bottom cap. HDPE, fusion bonded epoxy and type 444 stainless steel are all resistant to corrosion by oxalic acid.
Multiple HDPE pipes are mounted in rows so that they can be loaded and unloaded efficiently. The loading time is 5 to 30 minutes, depending on whether the biomass is being size-reduced while loading. The unloading time is 5 minutes and the processing time is 3 to 4 days, so the time spent loading and unloading is a small fraction of the total time.
When performing dilute oxalic acid hydrolysis with 0.110 M oxalic acid the pH is 1.2. A leak of this oxalic acid solution can easily be neutralized with a dilute solution of calcium hydroxide and the resulting calcium oxalate is biodegradable. Calcium hydroxide is also very safe to handle.
Burning biomass that has been infused with oxalic acid and calcium hydroxide is environmentally friendly, since this only releases CO2 and water vapor to the atmosphere.
The top cap can be brought to the ground by rotating the pipe on the trunnion. The various connections to the HDPE pipe are easily accessible.
A CelloFuel module is a single vertical HDPE pipe rotated about the center of gravity with a trunnion. Scaling up to larger scales involves simply replicating the HDPE pipes and in arrays.
We are doing lab-scale tests of dilute oxalic acid hydrolysis with this test apparatus:
A scale model of the CelloFuel module is being built, and is scalable to 1 m in diameter and 6 m high. It has a volume of 1/2 m3, where the full-size CelloFuel module is 5 m3.
This is for testing rotation, biomass loading (tilted at 45 degrees), unloading (tilted at 135 degrees), and mixing with yeast and other reagents such as oxalic acid (turning upside down and back). We've tested with 1800 W of heat using double reflective insulation and found that this is very efficient and cost-effective.
There are two families of CelloFuel patents that have been granted in the US and around the world, including the EU, Canada, Russia, China, Mexico and Brazil. We are now licensing these technologies and providing engineering consulting for profitable implementation of these technologies.