Source: DUKE UNIVERSITY submitted to NRP
ULTRA-HIGH THROUGHPUT ANIMAL WASTE TREATMENT USING SUPERCRITICAL WATER PROCESSING
Sponsoring Institution
National Institute of Food and Agriculture
Project Status
COMPLETE
Funding Source
Reporting Frequency
Annual
Accession No.
1007224
Grant No.
2015-67030-24120
Cumulative Award Amt.
$100,000.00
Proposal No.
2015-02371
Multistate No.
(N/A)
Project Start Date
Sep 1, 2015
Project End Date
Aug 31, 2017
Grant Year
2015
Program Code
[A1801]- Exploratory: Exploratory Research
Recipient Organization
DUKE UNIVERSITY
BOX 90340 PHYTOTRON BUILDING
DURHAM,NC 27708
Performing Department
Civil Engineering
Non Technical Summary
A promising technology that could transform waste management at CAFOs is supercritical water processing, using either oxidation (SCWO), or gasification (SCWG). At supercritical conditions, all contaminants are converted to harmless end-products in seconds and all pathogens, endocrine disrupting chemicals, antibiotics, etc. are destroyed.The vision of this project is that SCWO/G could completely treat animal wastes in one single and very compact unit, converting the waste to harmless end-products, allowing resources (water, P, possibly N) recovery, generating carbon offsets and possibly renewable energy while reducing environmental impacts and improving socioeconomic surroundings.Thus the overall objective of the proposed exploratory research is to determine the technical and economic feasibility of treating selected animal wastes using SCWO/G. Specific tasks to reach this goal are:1. To conduct factorial SCWO/G experiments to show proof of concept and determine at scale, the applicability of supercritical water processing for both swine and chicken manure.2. To develop a techno-economic model that will guide the development of the technology and optimize environmental and economic benefits.
Animal Health Component
30%
Research Effort Categories
Basic
30%
Applied
30%
Developmental
40%
Classification

Knowledge Area (KA)Subject of Investigation (SOI)Field of Science (FOS)Percent
40353702020100%
Goals / Objectives
The overall objective of the proposed exploratory research is to determine the technical and economic feasibility of treating selected animal wastes using supercritical water processing, either by oxidation (SCWO) or by gasification (SCWG). Specific tasks to reach this goal are:1. To conduct factorial SCWO/G experiments to show proof of concept and determine at scale, the applicability of supercritical water processing for both swine and chicken manure.2. To develop a techno-economic model that will guide the development of the technology and optimize environmental and economic benefits.The vision of this proposed exploratory research is that SCWO/G could completely treat animal wastes in one single processing unit, converting the waste to harmless end-products, allowing resources (water, P, possibly N) recovery, generating carbon offsets and renewable energy while reducing environmental impacts and improving socioeconomic surroundings.Factorial SCWO and SCWG Experiments with Swine and Chicken ManureExperiments will be conducted at Duke with our pilot-scale prototype SCWO system. The rationale for using a pilot rather than a lab system is that proper assessment of the technology needs to include scale-specific issues such as energy losses and energy recovery, feedstock pre-processing and high-pressure feeding, corrosion and salt deposition, as well as operation and maintenance issues specific to scale operation.Factorial experiments will be used to quantify the reaction rates as a function of process conditions (feed nature and composition, reaction temperature and pressure, presence or excess oxidant and more), determine the composition of end-products (fate of organics, N, P, K, produced gases), and analyze key process parameters (corrosion of the reactor, precipitation of mineral salts). Advanced statistical methods will be used to extract trends since effects are not necessarily singular, linear or even monotonous, but clearly have a major impact on the process efficiency and economics. For example, excess air (as the oxidant) accelerates the reaction rate, impacts the fate of N, corrosion and energy balances.Throughout the project, data analysis and information generation will aim at the development of knowledge that is generically useful for the evaluation of SCWO/G systems, rather than information that is specific to our prototype. This will be attained by correlating results using dimensionless analysis, and the development of a conceptual model of the SCWO/G process based on fundamental principles using the COMSOL multiphysics package so that the results can be generically used outside the specific prototype. Overall, these results will delineate the process conditions for which SCWO and SCWG are feasible.Techno-Economic EvaluationThe objective of this task will be to develop a techno-economic model that incorporate the knowledge developed in the previous task, our extensive expertise in designing small SCWO and SCWG units, and life cycle assessment to guide the development of the technology while optimizing the environmental and economic benefits.The proposed approach will follow that of a streamlined life cycle assessment (LCA) combined with fundamental modeling (as developed above) with the objective to conduct multi-objective optimization. Examples of such approach have been reported in other fields. In short, the approach calls for defining and calculating all life cycle inventories as a function of the process technical and economic modeling. Therefore, life cycle impact assessment (LCIA) results are calculated as a function of process design and operation. A multi-objective optimization is then conducted which enables to understand the benefits and tradeoffs of specific design and/or operating condition choices.The techno-economic evaluation will rely heavily on results of the experimental campaigns. In addition to chemical kinetics and energy balances, we will consider O&M needs as identified and projected from the operation of the prototype. These will be assessed in context to adequately integrate SCWO/G with animal production systems. Currently, O&M needs of SCWO/G systems is unknown.
Project Methods
Typical experiments will proceed as follows. Swine and chicken manure will be procured and characterized for CHON content, chemical oxygen demand (COD), total organic content (TOC), moisture/solids and volatile solids contents (TS and VSS), calorific value. Swine waste will be from the Loyd Ray Farms facility while, chicken manure will be procured from a local egg laying farm. High solids content waste will be preferred. We will also reach out to Mike Williams, Director of the Animal and Poultry Waste Management Center at NCSU to consider the latest and emerging waste collection methods and incorporate these feedstocks into our protocols. Typically, 100-500 L manure will be needed per experiment. The prototype SCWO/G system will be started as is usual using water and a dilute (1-3% vol.) solution of isopropanol (IPA) in water. IPA serves as starter fuel in order to reach the required temperatures. IPA is convenient as it has a high calorific value and a low ignition temperature. When supercritical conditions will be reached, the feed will be switched to the manure slurry. Treatment will be continued until all conditions are steady, which is anticipated to be about 0.5 to 2 hours, depending on the conditions (thermal equilibrium is longest to reach). Experiments will not limited to steady-state as many useful information can be derived from transitions between steady-state, in particular when data are analyzed with advanced conceptual models. During the entire experiment, the PLC will serve as datalogger for all process parameters, while operators will take grab samples (gases and liquid) for off-line analysis. Post-experiment data analysis will include closure of all mass and energy balances, with specific focus on carbon, nitrogen, phosphorous, and oxygen. The fate of nitrogen will be specifically examined as it is highly relevant in this context and is expected to depend on the conditions, in particular the oxidant excess. For supercritical gasification and below oxygen stoichiometric amount, nitrogen should leave the system as dissolved ammonium, while in oxidation mode, one expects harmless nitrogen gas. Phosphorous is expected in the solids (as phosphates). Another focus will be on energy balances and full analysis of heat transfer and heat recovery. The energy efficiency of the system and means to capture and produce energy are key scale-parameters that will inform the techno-economic analysis. Selected liquid samples will be analyzed for metals (in particular chromium, iron and nickel, but a full suite analysis is easily obtained with our ICP-MS) as indication of corrosion and to ensure the produced water is safe for recycle, e.g., for animal consumption. A few samples will be analyzed for biological contamination (coliforms, indicator virus, helminthes eggs) although none is expected to survive at the treatment conditions. Similarly, selected samples will be analyzed for residual antibiotics and trace contaminants (none is expected to remain) using LC-MS.Experiments using SCWG mode will be fairly similar to those run in the oxidation mode with the important distinction that oxidation is exothermic and requires air, while gasification is endothermic, produces energy gas (primarily methane, or CO + H2 depending on the conditions) and is conducted in absence of air. Thus, for SCWG experimental campaigns, the prototype will be modified to include a gas-powered furnace in which some of the energy gas produced will be burned to provide the necessary heat to reach supercritical conditions. The techno-economic analysis will follow that of a streamlined life cycle assessment (LCA) combined with fundamental modeling with the objective to conduct multi-objective optimization. Examples of such approach have been reported in other fields. In short, the approach calls for defining and calculating all life cycle inventories as a function of the process technical and economic modeling. Therefore, life cycle impact assessment (LCIA) results are calculated as a function of process design and operation. A multi-objective optimization is then conducted which enables to understand the benefits and tradeoffs of specific design and/or operating condition choices. Sampling and analysis of liquid samples (for NPK, N species and COD) will be in accordance with USDA and Standard Methods, and using Hach kits. Liquid samples will also be analyzed for total organic and inorganic carbon (TOC/TIC), and metals (using ICP-MS). Gas composition will be determined by gas chromatography for CH4, H2, and CO and non-dispersive infrared (NDIR) for CO2. Gas/vapor flow rate are determined using various on-line mass flow meters, and analog flowmeters. Process conditions (temperatures, pressures, power consumption, etc.) are all monitored using specific sensors connected to the programmable logic controller (PLC). All analytical procedures are subjected to standard QA/QC procedures already in place in Deshusses' lab. QA/QC include routine calibrations and comparison of all on-line sensors with off-line measurements, multiple replicates and advanced statistical data analysis.The results will provide a very extensive body of data on the processing of swine and chicken manure using supercritical water oxidation and gasification. The originality and uniqueness of these results is that they will be generated with an industrial-scale prototype thus providing scale-relevant information such as realistic energy balances, energy recovery, and materials processing data. These results will also support the development of a detailed understanding of supercritical water oxidation/gasification of animal wastes which is currently lacking. The new knowledge will be generically useful for the evaluation of the proposed waste to energy systems (rather than be prototype specific), thereby increasing the impact of the proposed research.The techno-economic model will enable to incorporate various dimensions and multi-objective optimization (economic, environmental, and social) to maximize the benefits and impact on animal production systems. In particular, deliverables will include the sensitivity to CAFO type and size, and clearly and quantitatively distinguish the benefits of SCWO and SCWG and their design and operating parameters. Outputs such as environmental footprint, generation of renewable energy credits (RECs) and carbon offsets, land use for waste treatment will all be included. The evaluation framework will enable to guide future research and technology development, as well as minimizing the risk of project progression.

Progress 09/01/15 to 08/31/17

Outputs
Target Audience:The target audiences are those involved closely or remotely with CAFOs. These include, but are not limited to farmers, aggregators, meat producers, national and state animal associations (pork, poultry, cattle, etc.), regulators, policy makers, local communities, municipalities where CAFOs operate, technology providers, and consultants. Because this project was exploratory research, the above mentioned audience was not reached, but recommendations made include informing the target audiences about the outcome of this study. Changes/Problems: Nothing Reported What opportunities for training and professional development has the project provided? Nothing Reported How have the results been disseminated to communities of interest? Nothing Reported What do you plan to do during the next reporting period to accomplish the goals? Nothing Reported

Impacts
What was accomplished under these goals? SUMMARY OF THE RESULTS Because of space limitations, the report is succinct. A more extensive report can be obtained from Dr. Deshusses (marc.deshusses@duke.edu). 1.1 SCWO and SCWG Comparison Comparison of supercritical water oxidation (SCWO) and gasification (SCWG) was conducted and concluded that SCWO was a superior technology to SCWG for animal waste treatment at CAFOs. SCWO provides cleaner effluent that does not require further treatment. The energy balances are more favorable for SCWO, and SCWO systems can be more compact than gasification ones (because of the shorter reaction time), thereby reducing CAPEX. 1.2 SCWO Treatment Performance A technical scale SCWO prototype designed by Dr. Deshusses and his team was used for the experiments reported in here. The system is housed in a standard 20 feet shipping container and can treat about 1 m3 of slurry per day. Typical animal wastes were found to be suitable for SCWO treatment, however many issues were experienced during high pressure pumping of manure. These were in part due to the small scale of our pilot, and also due to large particles, hair or feathers in the manure that was attempted to be treated. After these were resolved, treatment studies demonstrated that slurries could be very effectively treated (Table 1). Table 1. Typical steady-state performance of our SCWO treatment for animal waste. Here treatment of dog feces (10% dry solids content) augmented with 4% isopropanol (IPA) is reported. IPA was added to increase the calorific value of the slurry treated because we could not pump greater solids content (see text above). COD influent 192,000 mg/L Effluent 65-280 mg/L Removal >99.85% Total N influent 4,700 mg-N/L Effluent 220-420 mg-N/L Removal >91.1% Total P influent 14,500 mg-P/L Effluent 13.4-63.9 mg-P/L Removal >99.6% Examination of Table 1 reveals very high treatment levels across the board. Nitrogen in the manure left the system as harmless nitrogen gas while the phosphorous was precipitated as inert minerals and was easily recovered. Given increasing concerns about the release in the environment of trace contaminants such as antibiotics, pharmaceuticals, etc. spiking of three trace contaminants was conducted. These were acetaminophen (Tylenol), ibuprofen (Advil) and Triclosan (a common antimicrobial agent, e.g. in soap and hand sanitizers). Treatment performance shown in Table 2 indicates that these compounds were very well removed as all effluent concentrations were below our detection limit. Table 2. Treatment of trace contaminants spiked in fecal slurry in our SCWO prototype. Acetaminophen influent 10 mg/L Effluent <1 µg/L Removal >99.99% Ibuprofen influent 10 mg/L Effluent <1 µg/L Removal >99.99% Triclosan influent 100 µg/L Effluent <0.1 µg/L Removal >99.9% There were no odor emissions, and SOx, NOx and ammonia in the exhaust gas were always below our detection limit of 3, 10, and 3 ppmv, respectively. Because of the high temperature of the process, all pathogens were completely destroyed. This include all bacteria, virus, protozoa, prions. The complete elimination of antibiotic resistant bacteria is a clear asset of the SCWO technology. 1.3 Techno-economic evaluation A techno-economic study was conducted for two selected treatment capacities: 2000 head of swine and 10,000 head of swine (feeder to finish). Extrapolation to other animal CAFOs can be done using the specific manure production of various animals. Table 3. Techno-economic summary of SCWO treatment systems for CAFOs. Values are reported for small systems (2000 head of swine of 660 kg dry/day) /// large systems (10,000 head of swine or 3.3 tons dry/day) System footprint (ft2) 320 /// 960 CAPEX ($) $1.0M /// $2.5M OPEX1 ($/mo) $5.6k /// $8.1k Energy2 (kWh/d) +240 /// -300 Clean water generation (ga/d) 8,700 /// 49,000 1Not including CAPEX depreciation. 2The "+" indicates energy consumption, while the "-" indicates net surplus electricity produced. Highlights of Table 3 include the very small footprint of the systems. This will free up land for either more animal barns or planting cash crops. CAPEX values are high compared to lagoons, but SCWO provides complete treatment with many associated advantages. OPEX require further validation. The results suggest that building a single system to handle the waste of multiple farms should be investigated. Comparison with selected swine waste treatment technologies is shown in Table 4. SCWO treatment would be very competitive with an annual cost of $166/1000 lbs. steady state live weight (SSLW). This estimate takes into account revenues of $77/1000 Lbs SSLW/year, some of which are highly volatile. For instance, swine RECs in North Carolina could sell for as much as $100/REC, although even without revenues, SCWO treatment is competitive. Table 4 Comparison of selected swine waste management systems with SCWO treatment. Lagoon and sprayfield: Traditional practice. Simple process. Odorous, releases greenhouse gases and NH3, large footprint, requires land for spraying, breeds flies, possibly antibiotic resistant bacteria. Subject to changing regulations. 87 $/1000 Lbs SSLW/year. Composting ("SuperSoils"): Aerobic process primarily for dry matter (e.g. dewatered manure). Relatively simple process, makes low value product, releases odors and NH3, requires dewatering of the manure (and liquid waste management) and often addition of high C waste for co-composting. 83 $/1000 Lbs SSLW/year (for the dewatered fraction only). Anaerobic digestion + post-treatment (Loyd Ray Farms & AgriClean): Slow biological process for partial conversion of organics to biogas. Moderately complex, recovers some energy in the form of biogas, does not provide N or P management or pathogen control, usually requires post treatment (aerobic or land application). 210 - 221 $/1000 Lbs SSLW/year. SCWO (this study): High-tech engineered system for complete treatment. No odor or greenhouse gas emissions, complete elimination of all pathogens, small footprint, produces renewable energy. 166 $/1000 Lbs SSLW/year (See note #2) 1Costs for Loy Ray Farms are from Adair et al. (2016) Trans. ASABE 59: 1009-1018. All other costs are from NCSU 2006. Dev. of environm. superior technologies: Phase 3 report. https://projects.ncsu.edu/cals/waste_mgt/smithfield_projects/phase3report06/pdfs/report%20summary.pdf. 2Without any revenue, cost is $243/1000 lbs. SSLW/year. 2 RECOMMENDATIONS This project demonstrated the feasibility of using supercritical water oxidation (SCWO) for the complete treatment of organics, nutrients, trace contaminants and pathogens in manure. A techno-economic evaluation revealed that the cost would be very competitive. The environmental benefits of SCWO, reduction in land requirement and secondary benefits (e.g., possible animal health) will make SCWO treatment even more attractive. Recommendations include: Further examination of the applicability of SCWO at CAFOs is recommended, in particular through a feasibility study at a CAFO with a sufficiently large SCWO unit to enable identification of CAFO specific issues. A detailed study of the specific regulations and market place and generation of renewable energy credits (RECs) and carbon offsets is recommended. This location-specific information will enable to identify states where SCWO can generate income and possibly make manure treatment a cash positive operation. Further study and quantification of the secondary benefits (odor, environmental emissions, costs, animal and worker's health) of SCWO treatment at CAFOs is recommended. Finally, informing the target audiences about the outcome of this study is recommended. These include but are not limited to farmers, aggregators, meat producers, national and state animal (pork, poultry, cattle, etc.) associations, regulators, policy makers, local communities, municipalities where CAFOs operate, technology providers, and consultants.

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