Longer, smoother runs ~ January, 2019
We opened 2019 with a run campaign of over 50 hours of continuous processing slurry. After investigating and mapping periodical pressure drops throughout the runs - our hard work paid off. We experimented with various capillaries sizes and operational configurations of the gas and liquid separators to enhance the effluent’s depressurization process. This enabled us to enjoy a very steady and stable reaction and perform smoother longer runs.
During our these runs, we experimented with new co-fuels - vegetable oil and spent motor oil which proved to be effective as IPA and diesel. This is great news since it shows the flexibility of the system to use different waste oils communities generate to co-treat fecal - a true Omni process!. Next on our list if food scraps – more updates coming soon!
PFOS/PFOA Treatment Results ~ December, 2018
During December, the hard work of improving our monitoring and control systems has paid off - where we experienced a smooth (even boring) run in which the SCWO team operated the system around the clock for two consecutive days. After further experimentation with treating PFOS/PFOA micro-pollutants with the SCWO system, we are glad to share the latest results in which we have reached the 99.1% elimination of PFOS and 99.9% of PFOA. Lastly, this month we launched our pilot program, in which we are inviting facilities to send us their most difficult-to-dewater and treat waste types from around the country, to perform pilot runs with the SCWO unit on Duke Campus – more updates coming soon!
Treating Primary Sludge ~ November, 2018
This month the SCWO team has traveled all the way to China, to participate in the much talked about Reinvent The Toilet Expo, organized by the Bill & Melinda Gates foundation. We had the chance to discuss our technology and progress to date with government officials and potential commercial partners. We have also successfully treated primary sludge for the first time, sent to us from Delphi - IN, where we reached a COD conversion of +99.1% and 234 mg/L of Ammonia. At the same time, we continued experimenting with treating PFOS and PFOA spiked feedstock and will share the latest updates as soon as we process the results. Having the new team members onboard, enabled us to further our data analysis efforts and look into improving the system’s operational costs by looking into improving our heat exchanger performance and reducing excess oxygen amount. Lastly, we were welcomed by the OWASA’s wastewater treatment plant team at Chapel Hill where we toured the facility and discussed possible future collaboration.
Treating Concentrated Slurries ~ October, 2018
October was all about treating higher percent solids slurries. The reason for pursuing this objective is twofold: firstly, in order for the system to reach the Foundation's requirement of 5 cents per person a day (CapEx + OpEx). we are focusing on reducing/eliminating the use of additional co-fuels to achieve autothermal reaction using only the energy embedded in the waste. This could be achieve at 12-16% solids. Secondly, in developed countries, current dewatering techniques focus on decreasing the volume of biosolids in order to decrease costs of transportation and tipping fees. This means that the biosolids coming off the belt-press or centrifuge in a wastewater treatment plant, would usually contain ~16-22% solids. The closer we get to this range, the less pre-treatment the feedstock would require when implementing the system in existing wastewater treatment plants.
Preparations for these runs included installing new transducers along the slurry line and mixing tee, so we can have clear indications of pressure buildups in critical areas, and to better our ability to mitigate these while the system is running. We ended up treating slurries of up to 13.9% solids - a point where we can eliminate the use of co-fuel and sustain a powerful reaction just by converting waste to energy. During our experiments, we started using Diesel as co-fuel (rather than IPA), which is a more common fuel source around the world with higher energy contents per volume. We were very pleased with its performance while using very small amounts (the more concentrated the slurry is, the less co-fuel required).
In addition we continued to experiment with PFAS spiked feedstocks where preliminary results show a conversion of 98.95 % (PFOS) and 99.98% (PFOA) - more data to come soon. Lastly, we continued upgrading the system by adding a cover to the hopper, updated the PLC with new transducers and furnace controls as well as calibrating the water pump.
System upgrades ~ September, 2018
September was an eventful month for the SCWO team - we welcomed two new team members joining us – Jon Ricker (environmental advocate and an Indy film director) and David Ballenghien (SCWO pioneer and Ex-Innoveox engineer). During this month we performed a lot of upgrade and maintenance work on our pilot plant. We started by replacing old furnace parts to improve its decreasing performance in previous runs. We inspected the heat exchangers and performed maintenance to the water and slurry pumps, as well as the air compressor. We then updated our PLC and HMI to reflect the new updates and algorithms that enable us to improve startup and shutdown time and better visualization of the system’s KPIs. The design for new high temperature gas/liquid separation vessels has been completed and the search for a fabricator in underway. In addition, we have set up a micron filter to filter the effluent and separate the clean water from the minerals to have a tighter control on our ash balance and further minerals properties’ investigation. This setup also enables us to test and integrate an on-site filtration solution, for water reuse. We are now ready for next month's increased percent solids testing – stay tuned!
Straight feed ~ August, 2018
Following the commissioning of the new pre-feed setup last month, we proceeded to testing straight feeding the system, in order to facilitate the unit’s operation. While on steady state, we started feeding the auger with biosolids and water (without premixing and diluting them in advance) where they were initially mixed into slurry. The slurry went through the grinder and pumped into the system through the lobe pump quickly and smoothly. This feeding process enabled us to test different slurry thickness levels, streamlining our processes as well as save valuable time on pre-run preparations.
As we prepare for treating higher percent solid slurries in the next quarter, we have designed and installed few new bypass and flush ports to facilitate clearing the different pipes during operation and maintenance.
We continued to treat WAS slurry this month and reached the following removal percantage: COD - 98.8%, Total Nitrogen - 90.3%, Phostphate - 96.7%.
New pre-feed pump set up installed and commissioned ~ July, 2018
This month we have enhanced our slurry preprocessing and feeding system in several ways to streamline our system’s ability to treat high percent solids and high viscosity slurry streams. The new pre-feed pump set up includes an auger, grinder and a lobe pump. The Auger fed lobe pump will allow us to pump slurry containing over 15% solids into the system, while the inline grinder reduces particle size in the slurry stream and facilitates its pre-processing. At the same time, we upgraded few of the system fittings (check valves with limiting clearances) that further reduce the potential for clogging. All these have enabled us to start treating WAS (Waste Activated Sludge) for the first time - as shown in the video (click the image above to play video). Additionally, we have updated our start up procedure to improve the overall reactor temperature stability during runs.
New lobe pump, grinder and auger delivered ~ June, 2018
Our new pre-feed pump integrated with an auger feed and inline grinder have been delivered. This equipment will streamline the pre-processing required for treating sludge, enable us to test higher solids percent sludge and create opportunities to diversify our feedstock with food waste, biomass and industrial waste which will ultimately reduce and eliminate our reliance on co-fuels.
Work is proceeding to get the new equipment set up and commissioned early next month. We have been improving our software algorithm and interlocks, that significantly reduce our overhead, startup and shutdown time. We have also made the effort to replace the air positioner while the new one has been installed and calibrated promptly.Lastly, we decided to measure the sound level around the SCWO unit during operation. The main attribute for the noise is the air compressor measuring 83 dB at the container wall (OSHA's limit without requiring hearing protection is an average of 85 dB over an 8 our shift). With future sound proofing on the compressor and during the time the compressor was off, the loudest sound measurement outside of the container was 75 dB. The background measurement with the system off was 70 dB.
Improving oxygen consumption ~ May, 2018
This month we preformed system upgrades in order to facilitate the reliability testing process and improve the performance of the SCWO prototype. We added a liquid and gas separator to the sample port to make taking samples easier. We updated the furnace control logic to reduce the magnitude of temperature swings during steady state. We noticed a remarkable improvement in the amount of excess oxygen the system was using the for the reaction while still maintaining over 99.6% conversion. At the same time, we continued testing the efficiency of the SCWO process and spiked the biosolids feedstock with high levels of Urea and learned that it gets broken down to Ammonia.
Shelly Eisen Livneh joins the SCWO team ~ April, 2018
Shelly joined the team as the Product Marketing Manager to facilitate the project management and help commercializing the SCWO technology. During thismonth we hosted Sun Kim and Erin McCusker from the Bill & Melinda Gates Foundation, shared our progress and presented our testing and technology risk reduction plans for the next two years. We also discussed paths to technology commercialization.
Began testing hazardous waste spiked feedstock ~ March, 2018
Polyfluorinated micro-pollutants are currently not being treated by traditional wastewater treatment plants and are persistent in the environment. We decided to rise to the challenge and spike the influent with PFOS and PFOA to test its conversion during the SCWO process. Analyses are pending.
System upgrades ~ February, 2018
Improved energy efficiency, depressurization capillaries and backpressure regulator for improved stability during operation. New CO, CO2, and O2 gas sensors were installed and integrated into the control system. We did not install SOx, NOx or NH3 sensors as grab sampling and analysis showed that the exhaust gas concentration of these gases was always below 3 ppm.
Exploring application in animal waste treatment and the effects of system capacity ~ January, 2018
Our team is using Aspen Plus to model and scale up the SCWO process for the treatment of animal waste (e.g., swine waste at confined feeding operations, or cafos) and has come up with capital and operating expenses estimates for systems of various sizes up to 30,000 people per day or farms with 10,000 hogs.
Image source: Wikimedia
Longer runs and more testing with pharmaceuticals spiked feedstock ~ November, 2017
November has been an eventful month for the SCWO team. We performed one of our longest runs during which the system was operational for 2 days straight. Additional insulation was added to the slurry lines in order to reduce heat losses. At the same time, we conducted more runs with sludge spiked with pharmaceuticals such as Ibuprofen, Acetaminophen and Triclosan and could not detect them in the effluent. This indicates that removal exceeded 99.99%.
Project review at the BMGF ~ October, 2017
This month we traveled to Seattle for the project’s TAG (technology advisory group) at the Bill & Melinda Gates Foundation. The team passed the go/no go decision and the project will continue to be funded; future focus will be on process optimization and pre-commercial activities. In addition, we successfully ran the unit with a new slurry heat exchanger.
Slurry Heat Exchanger Clog ~ September, 2017
In late August we experienced a clog in the slurry side of the slurry heat exchanger during steady state operation. Slurry ran through the outer annulus of this coil-in-coil heat exchanger. Attempts to clear the clog with acidic and caustic chemicals and flushing failed, and it was ultimately decommissioned and cut open. The clog appears to have been the result of small clearances in the outer annulus of the coil-in-coil design combined with the high viscosity of the feed stock.
New slurry pump on site ~ June, 2017
A new, custom dual piston slurry pump built by Terrasimco is being commissioned in the SCWO prototype after undergoing testing with solids slurries at high pressure at the manufacturer. The pump was designed to reliably pump high viscosity slurries at lower flow rates and with a larger maximum particle size than our previous slurry pump.
11 hour run with biosolids ~ May, 2017
On May 31, 2017, with the help of our two new operators, Luke Amrhein and Mahendra Joshi, we ran for 11 hours in steady state condition with a feedstock of 5% solids and 5% isopropyl alcohol (IPA)--the energy equivalent of 15% solids. Organic conversion was 99.9%, and the run rate represented the equivalent of 1,350 people/day.
Luke joined Duke in May from a local engineering lab, and Mahendra is a Duke MS student in Turbomachinery Aeromechanics working with us for the summer.
Energy recovery investigation ~ April, 2017
Over the past 10-12 months, the team has been evaluating the energy efficiency of the current prototype and investigating the energy efficiency and energy recovery potential for the next generation design. We've considered a range of energy recover technologies, system designs and scaling factors to maximize the energy balance of the second generation prototype. Preliminary designs are being modeled and refined with the help of a consultant, Dominion Engineering.
Sr. Process Engineer joins the team ~ February, 2017
Kobe Nagar joined the Duke SCWO team in February, 2017. He brings over 15 years of experience in the chemicals, power and defense industries. Kobe is taking the lead on energy recovery and the design of the next generation SCWO prototype.
Increasing our operational support ~ September, 2016
Walt Beckwith joined Duke in September, working part time and bringing a wealth of valuable hands-on experience with industrial equipment and processes. Walt contributes to the design, specification, commissioning, operation and maintenance of the SCWO prototype and its components.
Most successful solids run to date ~ June, 2016
On June 23 we ran the prototype for five hours in steady state on a feedstock slurry of 10% dog feces solids. This was both our longest run in steady state and the highest concentration of solids we've run. A co-fuel of 4% isopropyl alcohol was added to the feed slurry, but the solids quantity processed represented the waste of about 200 people. COD removal was very high, >99%. The system effluent was clear and free of odor. The ash particle size was small and settled out easily. The run was ended with a controlled shutdown when the feedstock was used up.
Feedstock pre-processing results ~ May, 2016
In preparation for upcoming solids testing, preprocessing methods to reduce the particle size of our feedstock below 200 micron have been investigated to accommodate the specifications of the double-hose diaphragm slurry pump. Multiple feedstocks were considered: chicken and cow manure, dog feces and biosolids from a local wastewater treatment plant. The dog feces and biosolids could be processed using a combination of a shearing mixer and colloid mill. Up to 99% of the biosolids and 90% of the dog feces slurry particles were reduced to less than 200 µm. The viscosity of the biosolids slurry was significantly higher than that of the dog poop due, perhaps, to polymers added to the biosolids during dewatered.
Two new SCWO specialists join the team ~ February, 2016
Florencia Yedro started at Duke January 18. She joins us from the University of Valladolid, Spain where she completed her PhD in the High Pressure Processing Group.
Sherif Elsayed started at Duke on February 15. He joins us from the Karlsruhe Institute of Technology where he worked on his PhD in Supercritical Water Gasification.
In an article titled “Separation of N2/CO2 Mixture Using A Continuous High-pressure Density-driven Separator”, Reza Espanani and colleagues from the Carbon Recycling Center at the University of Missouri demonstrate the possibility of capturing CO2 produced by supercritical water oxidation before it is released into the atmosphere.
Article Published in 'Chemosphere' ~ December, 2015
Andy Miller et al. article titled “Supercritical Oxidation of a Model Fecal Sludge Without the Use of a Co-fuel” describes the bench scale SCWO reactor used at the University of Missouri to inform the design of the prototype built at Duke. The effects of temperature, pressure, feed concentration and excess oxygen level on the conversion and heat transfer efficiency were evaluated using a factorial design.
Primary Investigator (PI) Marc Deshusses presented the project at the University of North Carolina's annual Water & Health conference October 28, 2015 in a session on wastewater treatment. Click on the image to the right to view his presentation.
CO-PI, Dr. William Jacoby presented the project in a talk titled “Continuous Treatment of Fecal Sludge in a Technical-scale Supercritical Water Oxidation System” at the 11th International Symposium on Supercritical Fluids” held October 11th-14th, 2015 in Seoul, South Korea.
Completed Liquids Testing ~ October, 2015
Liquids experimentation was completed in October. Detailed analysis of the results followed in November. The team began investigating and designing a fecal sludge pre-processing system which provides particle size reduction to support successful slurry pumping and subsequent solids testing. We are also considering alternate feedstocks for testing since the biosolids we have been using contain additives that facilitate agglomeration.
Liquids Testing ~ July, 2015
Since May, we have been running the prototype on isopropyl alcohol at various feedstock concentrations and flow rates to test the operating range of the system. We are analyzing COD (Chemical Oxygen Demand) removal and temperature profiles in the reactor and heat exchangers. We are also measuring O2, CO2 and CO in the vapor effluent to confirm that in steady state, the organic matter fed into the system is converted to CO2 and H2O. Running at supercritical conditions for over 130 hours has uncovered mechanical issues in the system which we’ve addressed along the way. We are currently testing lower feed concentrations at higher flow rates that reflect our original target operating specifications of ~1000kgwet/day flow rate with 10-20% solids.
Oxidized Fecal Sludge ~ May, 2015
On May 8, we successfully oxidized fecal sludge in the SCWO prototype for the first time. The bottle on the left contains a sample of the feedstock fed to the reactor; the bottle on the right shows the reactor effluent. For this initial test, we prepared a slurry with 3% solids fecal sludge and isopropyl alcohol mixed in as a co-fuel. We ran the system while continuously pumping this slurry for 3.5 hours. The solids at the bottom of the effluent vial are comprised of harmless salts that precipitate at supercritical conditions. This successful run marked the departure of veteran project engineer Doug Hendry and the arrival of our new engineer, Kura Duba.
Convening at Duke ~ March, 2015
In March, Program Officers Carl Hensman and Sun Kim from the Gates Foundation spent the day at Duke getting an update on our progress. They were able to see the reactor in operation and tour the container after cool-down. Bill Jacoby, our co-PI from the University of Missouri was here for his first visit, along with his doctoral student, Andy Miller. Duke's Jay Golden presented the economic model he has been developing with support of his graduate students. Kura Simon Duba who recently earned his PhD in supercritical fluids from the University of Trento was also able to join us. Kura will be starting full time on the project in the end of April.
Oxidizing IPA ~ February, 2015
In January, we began introducing dilute isopropyl alcohol (IPA) to the system and reached supercritical temperature and pressure. We have been running the prototype once or twice a week, fine tuning operation and the start-up procedure. In February we achieved steady state operation with full conversion of 6-8% IPA. Data collected during operation with IPA is enabling us to characterize and optimize heat transfer throughout the system and prepare for upcoming treatment of fecal sludge.
PLC and leak testing ~ December, 2014
In December, leak testing was successfully performed starting with low pressure air and working up to air and water at high pressure (3700 psi). The control system is operating reliably to date with ~75% of all control loops tested. Refinements in the system’s start-up procedure and equipment modifications have been made based on experience gained over numerous runs and varying conditions.
Piping complete ~ November, 2014
In November, the final connections were made to what is now a closed system. Leak testing and control system testing began. Insulation was partially installed to ensure proper piping and thermocouple alignment. The insulation will be completed before testing at high temperatures begins.
Pressure Vessel Code Inspection ~ October, 2014
In October, the NC Department of Labor reinspected our air tank and pressure relief valve configuration and confirmed it qualified for pressure vessel code certification. See the 'Photos and Videos' tab for photos of the capilary tubing that was installed as well as the control system interface. Fault code programming and data logging were completed, making the control system ready for testing.
Heat exchangers installed ~ September, 2014
In September, the last major component of the system, the custom designed heat exchangers were installed in container. The heat exchangers use a coil in coil design. As the process effluent flows through the inner pipe, it heats the water and air flowing through the upper outer coil and the slurry flowing through the lower outer coil.
Operation of Feluwa slurry pump ~ August, 2014
The Feluwa high-pressure slurry pump was run at our designed operating pressure, another successful step in the control system programming well underway.
Furnace, compressor and water pump tested ~ July, 2014
With power to the container, the bake-out procedure was performed on the Mellen furnace, the compressor and water pump were tested, and the control system software was employed to run the equipment for the first time. The control system logic underwent a detailed review.
480v power turned on ~ June, 2014
In June, our container’s electrical system passed inspection, and we were able to power up the unit for the first time. In addition to the main disconnect on the outside of the container, two power panels, a control panel, overhead lights and power outlets had been installed inside the container. This opened the door for component level testing of equipment.
Furnace mounted ~ April, 2014
Large components including the furnace and the high-pressure water pump were being mounted in the container. Electrical work to bring 480v electricity from a neighboring university building into the container was well underway. Procurement continued and entered its final stage.
Toilet Fair in Delhi, India ~ March, 2014
Six members of the SCWO project from Duke and the University of Missouri attended the Toilet Fair in Delhi co-hosted by the Government of India’s Biotechnology Department and the Bill & Melinda Gates Foundation. The fair provided a unique opportunity to talk to practitioners in the field, other research teams and entrepreneurs.
Milton Roy water pump in house ~ December, 2013
By the end of 2013, the prototype’s high pressure separation and depressurization system was designed, and the Feluwa high pressure slurry pump was ordered. ChemCAD temperature modeling of the prototype design was achieved with the help of Battelle. At the same time, the lab-scale SCWO unit at the University of Missouri was successfully oxidizing simulant using air as an oxidant.
Technical design review with Battelle Corporation ~ October, 2013
Duke entered into an agreement with Battelle in August, 2013 to provide technical consulting on the design of the supercritical water oxidation prototype. In October, the Duke team met with experts from Battelle in Richmond, Kentucky and toured the BGCAPP SCWO plant under construction there.
Shipping container delivered ~ September, 2013
The 20’ x 8’ x 8’ shipping container painted in Duke-blue was positioned behind Hudson Hall at the Pratt School of Engineering on Duke’s main campus. Meanwhile, prototype design was entering its final stage, and the procurement of parts was ramping up. Key components such as the air compressor and furnace were ordered.
Jose Abelleira joins the team ~ April, 2013
In August, 2013, Jose Abelleira came to Duke as a postdoctoral associate from the University of Cadiz in Spain, bringing with him experience in the design, construction, modeling and operation of SCWO systems.
The project begins ~ April, 2013
Duke University in collaboration with the University of Missouri was awarded $1.18 million from the Bill & Melinda Gates Foundation to design, build and test a prototype fecal sludge treatment system based on supercritical water oxidation technology. Marc Deshusses, Doug Hendry and Kathy Jooss represented the project team at a Gates Foundation grantee convening in Barcelona, Spain.