BioForce 9000
This fully-automated system performs complete transesterification fully converting all mono, di, and tri-glycerides contained in feedstock (such as animal fats and vegetable oils) into methyl esters (biodiesel). The efficiencies of our system reduce energy costs and improve yield resulting in incremental income of up to $0.10 for each gallon of biodiesel produced compared with industry-standard technology. Which translates into approx. $1mil savings for 10MGY plant annually, note the ROI could potentially be double the first year of operation. The Reactor Skid System is about the size of a subcompact car and is offered in 4 models ranging from 10 gallons per minute (GPM) to 100GPM however it can be scaled to virtually any size. The Bioforce 9000 can be used to retrofit less efficient reactor technology. It can also be incorporated into new or expanding biodiesel production facilities.
Ø Costs substantially less than competing technologies. The industry standard capital investment to build a biodiesel production facility is about $1 for each gallon of annual production capacity. Our system costs 25% less on average, than conventional technologies. Industrywide our application can potentially save $100’s of millions per year.
Ø Our systems demonstrate that biodiesel production can generate an attractive profit. We estimate that our BioForce 9000 Biodiesel Production System can reduce industry standard variable operating expenses by as much as $0.10 for each gallon of biodiesel produced. This can potentially amount to as much as $1mil in annual savings for a 10MGY production facility. Reduced energy consumption and multiple feedstock use contribute to our Bioforce 9000 System being able to produce ASTM (American Society for Testing and Materials) -grade biodiesel at reduced costs.
With the BioForce 9000 System: CTI offers new generation equipment for producing biodiesel which utilize Flow-Through Nano-Cavitation technology.
BioForce 9000 -Biodiesel is methyl (ethyl) ester, derived from vegetable oils in process of esterification: methanol (ethanol) is added to vegetable oil and processed together with acidic catalyst in NANO reactor.
Continuous biodiesel production
Any vegetable oils feedstock up to 4.5 % F.F.A.
Tallow and WVO up to 3.5% F.F.A.
While processing vegetable oils under 4.5% percent F.F.A. with necessary components in our reactor the molecules of fatty acids are broken apart with microexplosions. The velocity and quality of going of the esterification reaction also increase significally. Thus not only quality and quantity of pure biodiesel output but also its production rate
* ISO 9001:2000 & AS/EN 9100B Certified 
All of our skid systems equipped with GE-Fanuc VersaMax PLC & QuickPanel Touchscreen monitor.
Capability to run continues or batch, automated or manual modes. Timer settings available for batch run. Flexible recipe designed to store preset chemical formulas and technical parameters of the system designed for variety of feedstock. Precise dosing assures quality and provides savings in chemical use. Multiple reports capability will help you to stay on top of your production and chemical usage.
Video
Biodiesel samples from different oils and fats
Biodiesel Skid System
Automated and PLC Controlled
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ISO Testing Facility - NANO Reactors Skid Systems in works 
COMMERCIAL NANO BIODIESEL REACTORS SKID 24 GPM IN WORKS
Continuous-Flow BioForce 9000 Skids are scalable to virtually any size.
Our most popular capacities are:
10GPM, 24GPM, 30GPM and 40GPM
Start up costs are lower than those of any system available on the market, because our systems are real turnkey solution. 
Biodiesel- BioForce9000.
Our unique patent pending flow-through NANO cavitation technology (NCT) which reduces costs and time of biodiesel production process by 7-10 times.
Due to innovative and proprietary technology CTI's applications have very competitive prices with unbeatable competitive advantages.
Contact us for Details
The different ways in which cavitation can be used beneficially in the biodiesel processing applications are;
(a) Reaction time reduction (instant).
(b) Increase in the reaction yield.
(c) Use of less forcing conditions (temperature and pressure) compared to the conventional routes.
(d) Reduction in the induction period of the desired reaction.
(e) Possible switching of the reaction pathways resulting in increased selectivity.
(f) Increasing the effectiveness of the catalyst used in the reaction.
(g) Initiation of the chemical reaction due to generation of highly reactive free radicals
Each skid consist of the following:
Partial List
Skid (1)
Oil Pump (1)
Methanol dosage Pump (1)
Methoxide dosage Pump (1)
NANO reactor(s) with HP pumps (1-2)
Mixing chamber (1)
Gauges (flow, pressure, censors)
Electric panel with invertors (1)
GE-Fanuc VersaMax PLC & QuickPanel Touchscreen (1)
Oil filter (1)
316 Stainless steel piping
FLOW-THROUGH MULTI STAGE NANO-CAVITATOR REACTOR
NO MOVING PARTS
