Source: LUNA INNOVATIONS INCORPORATED submitted to
ON DEMAND NITRATE PRODUCTION FOR FERTILIZERS
Sponsoring Institution
National Institute of Food and Agriculture
Project Status
COMPLETE
Funding Source
Reporting Frequency
Annual
Accession No.
1020485
Grant No.
2019-33610-30187
Cumulative Award Amt.
$625,000.00
Proposal No.
2019-02269
Multistate No.
(N/A)
Project Start Date
Sep 1, 2019
Project End Date
May 31, 2023
Grant Year
2019
Program Code
[8.13]- Plant Production and Protection-Engineering
Project Director
Merrill, M.
Recipient Organization
LUNA INNOVATIONS INCORPORATED
1 RIVERSIDE CIR STE 400
ROANOKE,VA 24016
Performing Department
(N/A)
Non Technical Summary
Luna is developing the LuNOX process to produce nitrates for use in nitrogenous fertilizers with less cost and lower energy requirements. Nitric acid (HNO3), which is the protonated nitrate ion, is primarily used by the fertilizer industry to make granular ammonium nitrate or urea ammonium nitrate (UAN) solutions. The conventional industrial approach first produces ammonia (NH3) from nitrogen (N2) using natural gas (CH4) resources through the Haber process. Ammonia is then burned using oxygen (O2) from air to produce nitric acid through the Ostwald process. These two processes are so energy intensive that worldwide ammonia and nitric acid production by the Haber and Ostwald processes, respectively, consumes 1 - 2 % of global energy generation and produces about 3 % of global anthropogenic CO2 emissions. The direct oxidation of nitrogen to nitric acid using air and steam (H2O), however, could use as little as a tenth of the energy compared to the Haber-Ostwald processes. Luna is therefore developing a dual phase catalytic membrane reactor to directly oxidize nitrogen to nitric acid through the LuNOX process. The separation of gaseous reactants and products with the LuNOX membrane is the key to thermodynamically achieving nitric acid production. The dramatic potential reductions in energy requirements by the LuNOX process are expected to enable significant decreases in nitrate production costs.The expected outcome of the multi-phase SBIR program is a new technology that significantly lowers both the production and transportation costs of nitrogenous fertilizers to farmers. Transportation typically represents 10 - 30 % of nitrogenous fertilizer costs, depending on distance from production facilities or ammonia pipeline terminals. The LuNOX process can significantly lower transportation costs by enabling the transition from nitric acid production from ammonia production facilities to production at ammonia pipeline terminals. The use of more local energy resources to produce nitric acid would support more effective integration of intermittent renewable energy (wind, solar) resources with fossil fuel power plants. Ideally, the steam and heat of heat recovery steam generators (HRSG) and boilers of fossil flue power plants would power the LuNOX process on demand while intermittent renewable energy resources supply electricity to the grid. Altogether, the LuNOX process is expected to enhance agricultural profitability by lowering energy costs by 70 - 90 %, feedstock/fertilizer transportation costs by 30 - 50 %, and the overall costs of producing corn and soy crops by 1 - 2 %.The overall goals of the proposed Phase II program are to scale up the membrane reactor technology into a representative prototype module and demonstrate the potential for commercial nitric acid production. The technical effort is designed to show that the membranes can practically function as intended by refining the membrane material compositions for improved performance and stability, advancing the membrane manufacturing and testing capabilities to scale up the LuNOX process by a factor of >100×, and evaluating the scaled up process performance in relevant operational conditions. This technical effort prepares the LuNOX process for techno-economic evaluation to quantitatively estimate the profitability of Luna's proposed nitric acid production process. A favorable techno-economic analysis generated by a reputable engineering firm, such as Trimeric Corporation (a Phase II partner), is critical for establishing potential customer and end-user confidence for new industrial processes. The successful Phase II demonstrations of technical and economic feasibilities will be used to secure Phase III partnerships and investments.
Animal Health Component
40%
Research Effort Categories
Basic
20%
Applied
40%
Developmental
40%
Classification

Knowledge Area (KA)Subject of Investigation (SOI)Field of Science (FOS)Percent
51152102000100%
Knowledge Area
511 - New and Improved Non-Food Products and Processes;

Subject Of Investigation
5210 - Fertilizers;

Field Of Science
2000 - Chemistry;
Goals / Objectives
The proposed research will improve plant production by significantly decreasing the energy and infrastructure cost of producing nitrates for fertilizer. Only about half of the world's population presently benefits from industrially produced nitrogenous fertilizers. Nitrates for fertilizer are conventionally produced by first reducing nitrogen gas, N2, to ammonia through the Haber process and then oxidizing ammonia (NH3) to nitric acid (HNO3) through the Ostwald process. In practice, the efficiency losses of the combined Haber and Ostwald processes waste over 1,000 kJ/mol HNO3. Worldwide nitrate production by the Haber and Ostwald processes consumes 1 - 2 % of global energy generation and produces about 3 % of the world's anthropogenic carbon dioxide CO2 emissions. In contrast, directly oxidizing N2 to nitrates is a small change in energy and an efficiency of only 40 % would waste less than 100 kJ/mol HNO3. Luna is proposing the LuNOX process for direct N2 oxidation that could use 10 times less energy than the conventional processes by avoiding the ammonia intermediate state. In the LuNOX process, a catalytic membrane reactor converts compressed air and steam to concentrated nitric acid using energy generated from renewable or fossil fuel sources. Lower infrastructure costs are also expected primarily because the LuNOX process uses lower temperatures and/or pressures than the Haber and Ostwald processes. Producing nitrates with less energy and fewer infrastructure requirements will lower the overall fertilizer costs, improve crop production and profitability, and increase access to industrial fertilizers to an even greater percentage of the world's population.The Functional Goals of the overall program are:Functional Goal 1: Decrease the amount of energy required to fix N2 as nitrates. In contrast to the Haber and Ostwald processes, the LuNOX process can potentially use as little as one-tenth the energy in scalable, distributed systems. This increased energy efficiency can be achieved by directly oxidizing N2 to nitrate in comparatively mild operational conditions.Functional Goal 2: Eliminate the dependence of N2 fixation on natural gas or other fossil fuels. The LuNOX process is designed to consume compressed air and steam. Unlike the conventional processes, this means the LuNOX process can be powered on demand by renewable energy sources, such as wind and solar.Functional Goal 3: Enable local fertilizer production on demand with minimal infrastructure. Using a single process (LuNOX) that uses relatively mild temperatures and pressures instead of the conventionally combined, intensive processes (Haber and Ostwald) will decrease infrastructure costs. The production of nitrogenous fertilizer with local energy resources will also minimize international and interstate import requirements and decreases transportation costs.The overall Phase I program technical objective is to demonstrate the direct oxidation of N2 to nitric acid with a catalytic dual phase membrane.The specific Phase I technical objectives are:Technical Objective 1: Develop the manufacturing capabilities to assemble and scale up multi-membrane modules to a surface area about 100 times greater than the Phase I test samples.Technical Objective 2: Demonstrate stable, functional operation in relevant conditions to define and validate parametric performance values.Technical Objective 3: Perform a detailed techno-economic analysis to quantitatively estimate the economic potential of the LuNOX process based upon input costs, output values, efficiency (e.g. 75 kJ/mol HNO3), operational and equipment costs, and other factors.Technical Objective 4: Detail the technical and commercial plans for advancing to the pilot scale of 1,000 - 100,000 tons of nitric acid per year using an integrated network of modules.
Project Methods
The Project methods are broken down by task:Task 1: Define System Requirements and SpecificationsLuna will define the detailed requirements and specifications for the LuNOX catalytic membrane reactor components, assembly, operation, and performance. The team of chemists, engineers, and Environmental Safety & Hazards personnel will review the synthesis reactor setup during design, assembly, and operational phases to ensure safety, control, and performance. Personnel will be trained for operating the reactor in accordance with a detailed Standard Operating Procedure. A kick-off meeting will be held with the National Program Leader to coordinate with and fulfill the goals of the National Institute of Food and Agriculture.Task 2: Develop Materials and Manufacturing ProcessesThe molten electrolyte phase formulation will be refined for improved performance and stability. The Phase I program focused on using the lowest melting point (eutectic) electrolyte mixtures to validate the key components and ensure that the electrolyte melting temperature was not limiting the lowest range of operational temperatures. The Phase II program will advance the electrolyte formulation by systematically varying molar ratios to improve permeability and stability. After reformulating the electrolyte, the catalyst composition will be further explored. Similar to the Phase I program, these electrolytes and catalysts will be assessed using the existing test platform with initial activity screening in the Parr vessel prior to temperature dependence and stability evaluation (e.g. 100 hours) in the 8 cm long tube samples. Select samples may undergo postmortem analysis with scanning electron microscopy (SEM) and energy dispersive X-ray spectroscopy (EDX) to assess the potential or absence of morphological or compositional changes, respectively.The ceramic phase material composition will be down selected between zirconia and alumina before scaling up to full length tubes manufactured by CoorsTek Ceramics. While zirconia has a greater strength, alumina is less expensive and has more commercially available options, including asymmetric design features that can confine the molten electrolyte to a thinner layer for faster performance. The most important factor, however, is long term stability and compatibility with the molten electrolyte and process chemistry. Samples of each material will be infilled with molten electrolyte, be exposed to conditions relevant to operation for 100 hours, have the molten electrolyte leached back out, and then be evaluated for strength loss with compression testing. After the chemical/mechanical stability testing, Luna will downselect the ceramic material and purchase 60 cm long tubes from CoorsTek to construct the membrane modules. Luna will advance and scale up the membrane manufacturing process.Task 3: Construct LuNOX Reactor Test Platform & ModulesLuna will construct a new platform that is capable of testing scaled up membrane modules. The Phase I test platform will continue to be used for Task 2 molten electrolyte development and single 8 cm tube testing. The Phase I test platform can only scale up to modules composed of seven 8 cm long tubes (70 cm2 total membrane area) because the tube furnace only has a narrow (15 cm), short (20 cm) heating zone and because of volumetric limitations in the gas preheating and back pressure regulation capabilities. This LuNOX membrane USDA SBIR Phase II program will build upon the module flange, interconnect, temperature monitoring with thermocouples, and assembly capabilities. The key module developments proposed in this USDA SBIR Phase II are focused on increasing the number and length of tubes to 19 and 60 cm, respectively, to a total surface area of 1,200 cm2.Task 4: Evaluate Performance and Operating ParametersThe refined electrolyte and catalyst formulation developed in Task 2 will undergo a performance evaluation as a function of operational temperature, gas pressure, and gas flow rate parameters. The performance as a function of relevant membrane operation conditions will be more extensively prescreened and characterized with the 8 cm sample tubes before transitioning to the modules. In addition to membrane performance, the temperature, pressure, and gas flow rates can affect other key balance of plant considerations, such as overall energy efficiency, equipment & infrastructure costs, nitric acid production rates and concentration, etc. This mapping out of performance as a function of operational conditions will therefore be critical for developing the techno-economic analysis in Task 5 as well as planning the Phase III prototype skid reactor.Task 5: Perform a Detailed Techno-Economic AnalysisTrimeric will perform the techno-economic evaluation of the LuNOX process at an American Association of Cost Engineers (AACE) Level 4 for feasibility studies. A process design basis will document the process flow diagram with inputs, operating conditions, throughput, and salable product purity requirements and estimated market values. The LuNOX process design will detail energy and utility requirements, NOX emission control and potential nitric acid distillation capabilities, and major equipment operational parameters and costs. The techno-economic analysis will estimate capital and operating costs, energy performance of the technology, and the overall potential to generate revenue per unit of nitric acid produced. Trimeric and Luna will work together to identify and develop any technical variants or options that can reduce or avoid key cost drivers. The goal of this feedback loop between analysis and technical development is to enhance productivity and minimize risk of future technical or process redesigns.Task 6: Develop Commercialization Opportunities & Phase III PlansLuna will prepare the LuNOX process for successful commercialization in Phase III by establishing relationships with key partners, a roadmap for technical development to the pilot scale, and a strategy to secure additional funding. Since it is infeasible for Luna to independently develop a pilot scale reactor capable of producing nitric acid on the 1 - 10 ton per day scale, additional investment will be sought from potential sources such as industrial partners, venture capital investors, and the Department of Energy.Luna will continue developing relationships with strategic industrial partners, such as Koch Ag & Energy Solutions and ThyssenKrupp Industrial Solutions. Koch distributes over 13 million tons of fertilizer annually, produces ammonia and nitric acid, and operates many of the ammonia pipeline terminals. ThyssenKrupp builds nitric acid production facilities for end users, such as Koch. Luna may sell or license the LuNOX process to ThyssenKrupp, who would be Luna's direct customer. ThyssenKrupp would install the LuNOX process at facilities operated by Koch, who would be the end user. Both Koch and ThyssenKrupp will be key commercialization partners both as potential funders of Phase III programs as well as technical contributors to pilot scale demonstrations.The goal of the Phase III technical planning is to identify achievements and capabilities required to prepare a pilot scale LuNOX skid. Pilot scale skids are designed to achieve technological readiness level (TRL) 7 than can be prepared and initially tested at an engineering or R&D facility, transported to the test site (e.g. a Koch nitric acid production facility) on a 40 foot tractor trailer, and then demonstrated and evaluated for a period of several months or more. This Phase III skid reactor would have integrated capabilities, such as steam generation, air compression, emission regulation, and a target production rate of 20 - 100 kg of HNO3 per day.

Progress 09/01/19 to 10/20/22

Outputs
Target Audience:The development of the LuNOx membrane and process will connect three key target audiences: the gas processing industry, the fertilizer industry, and the renewable energy community. Together, these three audiences will benefit farmers with lower fertilizer costs and the public through lower energy usage and decreased greenhouse gas emissions. The LuNOx process is based on a dual phase membrane technology for gas separation and processing. The development of dual phase membranes for new processes as well as the commercialization of this new technology is relevant to both the membrane community as well as the gas processing industry. Leaders of the gas processing industry (Air Products, AirLiquide, Praxair, Linde) have been developing ceramic-based membranes for primarily for air separation applications. These corporations are potential customers for commercially transitioning the ceramic-based LuNOx membrane to industry for converting air and steam into nitric acid. Luna has also been developing dual phase membrane technology variants for air separation and carbon capture applications, is presently engaging Air Liquide on these efforts, and will expand technology development conversations and efforts to include the LuNOx technology. The end users are expected to be engineering firms that construct and operate nitric acid production facilities, such as ThyssenKrupp, Koch Industries, CF Industries, and Nutrien. These end-users are fertilizer manufacturer that processes feedstocks (nitrates, ammonia, urea, etc.) into a complete fertilizer product for local distribution and agricultural use. These fertilizer manufacturers will incorporate the nitrates produced by the LuNOx process into complete fertilizer products relevant to the local agricultural community. Luna has already established preliminary relationships with ThyssenKrupp and Koch Industries and will cycle back to these potential partners upon having demonstrated a functional membrane module and further developed the techno-economic analysis through Luna's Phase II subcontract with Trimeric. The production of nitrates is ideally powered by renewable energy resources. Key renewable energy resources, such as wind and solar, are intermittent. There is currently no cost-effective means of storing energy when renewable energy is capable of capturing energy in excess of the electricity grid demand. Instead of going unused or uncaptured, this energy can be applied to fertilizer production because fertilizer products represent stored energy and local fertilizer demand is predictable. The operators of the LuNOx process with work with the local energy community to capitalize on and more effectively use intermittent energy. Changes/Problems:Most areas of the project have significant levels of delay to leverage the greatest extent of synergistic activities available from the related dual phase membrane technology variants for carbon capture, air separation, and hydrochloric acid extraction. These DOE-funded technology variants have higher funding levels, more options for follow-on projects, and higher frequencies for funding opportunities. Luna Labs has therefore been applying a strategy that only uses this USDA Phase II projects funds to support LuNOX-specific efforts and leveraging DOE funds to advance cross-cutting efforts that benefit all of the membrane variants. Currently, the next set of experiments has been delayed while Luna Labs awaits delivery of bilayer/asymmetric membranes from Median and Process Technology, which are expected in the next two months. Luna Labs has requested a 12-month no cost extension. 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?When Media and Process Technology delivers asymmetric tubes (Task 2.3), Luna Labs will be able to accelerate its testing program (Task 4) and customize its electrolyte approach for the reduced separation layer thickness (Task 2.1). Because of ongoing synergistic membrane programs through the DOE, Luna Labs has advanced its test setups and membrane manufacturing techniques so that progress will resume quickly when Media and Process Technology resolves its delays.

Impacts
What was accomplished under these goals? Luna is developing the LuNOx process for producing nitric acid, which is a dual phase catalytic separation membrane technology. Nitric acid is a key component of nitrogenous fertilizers. By producing nitric acid directly from air and steam, the LuNOx technology will reduce the costs of producing nitric acid primarily by using almost a tenth of the energy as the conventional approach based on the Haber + Ostwald processes. The LuNOx technology will decrease the overall costs of nitrogenous fertilizer and is projected to increase the profitability of common crops by a few percent. The greater energy efficiency and better capabilities for integrating into the industrial nitrogenous fertilizer production and transportation infrastructure will also increase the profitability of the fertilizer industry. The greater energy efficiency and improved potential for integration with renewable energy resources will help reduce the greenhouse gas emissions of agricultural community. Technical Objective 1: Develop the manufacturing capabilities to assemble and scale up multi-membrane modules to a surface area about 100 times greater than the Phase I test samples. Luna revised the molten phase chemistry for improved performance at lower temperatures, transitioned to from a manganese to iron catalyst for additional performance improvement, and is now refining catalyst concentration before proceeding to map out operational conditions. These efforts included preparing molten phase specimens of the dual phase membranes, characterizing their melting temperatures and stability limits with differential scanning calorimetry, and measuring nitric acid production and rates under relevant conditions in real time with a collection of gas and condensed nitric acid sensors. Manganese, iron, cobalt, and copper catalysts were screened for this new nitrate-based molten phase. The catalyst composition was down selected to iron(III) nitrate both because it was the most active and because there was no evidence that it was precipitating from the molten nitrate liquid phase at the upper limit of relevant temperatures (300 °C). The iron catalyst concentration in the molten was refined to 3 mol% because higher concentrations (e.g. 10 mol%) has an adverse effects on melting temperatures and viscosity. Technology development has therefore progressed to Objective 2. Technical Objective 2: Demonstrate stable, functional operation in relevant conditions to define and validate parametric performance values. The LuNOx membranes have begun testing in relevant conditions in Luna's Scale 1 testing platform (see attached report for technical description). The dual phase membranes are prepared by infilling the molten nitrate phase into the nanoporous walls of a high strength zirconia ceramic tube. Capillary action retains the non-volatile molten phase in the pores with pressures of 5 - 30 atmospheres. The Scale 1 tube membranes specimens are about the size of a pen at roughly 8 cm long, 1 cm in diameter, and 1 mm wall thickness. The customization of the ceramic materials, the manufacturing processes, and test methods have been completed. The performance of the membranes has just begun characterization as a function of temperature (150 - 300 °C), air pressure (1 - 5 ATM), and steam flow rates (0.1 - 0.5 ml/min). The construction of the Sale 2 testing platform has been completed and the Scale 2 membrane module has been finalized and is now under construction. The membrane consists of multiple (6X) longer tubes (40 cm) for a 30X scale-up. The final membrane advancement to a reduced separation layer thickness has not yet been achieved due to significant delays from Luna Labs' ceramic materials supplier, Media and Process Technology. The delivery of the bilayer membrane will enable a ~25x increase in permeation by reduction of the separation layer. MPT has confirmed tubes will be delivered for testing in the coming months. Once this scale-up milestone is achieved, Luna Labs will efficiently proceed to complete testing, techno-economic analysis, and scale-up planning. Luna Labs has been granted a 12-mont NCE. Technical Objective 3: Perform a detailed techno-economic analysis to quantitatively estimate the economic potential of the LuNOx process based upon input costs, output values, efficiency (e.g. 75 kJ/mol HNO3), operational and equipment costs, and other factors. Significant techno-economic analysis efforts will begin once the target operational conditions have been determined based on the Technical Objective 2 performance evaluation results. Technical Objective 4: Detail the technical and commercial plans for advancing to the pilot scale of 1,000 - 100,000 tons of nitric acid per year using an integrated network of modules. Significant efforts of this objective will progress once the techno-economic analysis efforts have progressed and the performance and simulation of the Scale 2 module have been characterized.

Publications


    Progress 09/01/21 to 05/31/22

    Outputs
    Target Audience: Nothing Reported 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?When Media and Process Technology delivers asymmetric tubes (Task 2.3), Luna Labs will be able to accelerate its testing program (Task 4) and customize its electrolyte approach for the reduced separation layer thickness (Task 2.1). Because of ongoing synergistic membrane programs through the DOE, Luna Labs has advanced its test setups and membrane manufacturing techniques so that progress will resume quickly when Media and Process Technology resolves its delays (Table 2).

    Impacts
    What was accomplished under these goals? Task 1:The project team of personnel, test equipment, and R&D procedures were reviewed at the beginning of the Phase II project. The testing, manufacturing, and data processing procedures were revised during the process of training the new personnel. After 2 years of use after initial construction, the Scale 1 thermochemical membrane testing platform underwent its first maintenance and update cycle to incorporate higher performance valves, enable faster gas purge times, improve ease and automation of testing, and reassess safety and control features. While this USDA project to develop the LuNOX technology has significantly contributed to the construction and development of the Scale 1 testing platform, the majority of efforts has been supported by the Department of Energy (DOE) through Luna Labs' related dual phase membrane technologies for applications that include carbon capture (DE-SC0017124, DE-AR0001315 ), separation of oxygen from air (DE-SC0019629), and ammonia from hydrochloric acid (DE-SC0017142). The funding from the DOE has also been leveraged to develop the Scale 2 testing platform that will enable Objective 1's scale up to higher numbers of larger tubes. Because of the higher funding levels and opportunities for multiple (follow-on) Phase II projects, Luna Labs has focused on using DOE funding to support the common dual phase membrane efforts, such as test platform construction and maintenance, R&D procedures, ceramic material developments, and modeling tools. Luna Labs has shifted towards reserving the USDA SBIR funds to efforts that only specifically benefit the LuNOX technology. While this strategy has enhanced the efficiency of the USDA funds for developing the LuNOX technology, this prioritized use of DOE funds has reduced how fast the USDA funds have been applied to technology development. Luna Labs has reviewed the progress of this USDA Phase II at the contract midterm and has requested a no cost extension. Task 2:The transition from porous ceramic material components manufactured by CoorsTek Ceramics to Media and Process Technology (MPT) manufacturers has led to the production of more robust, higher quality ceramic membrane materials. Unfortunately, delays in tube delivery have impacted Luna Labs' testing schedule. Additionally, problems sourcing correctly sized particles has led to delays of the production of the bilayer membrane, which is a key outstanding scale-up step. The delays are presently resolved and MPT plans to deliver bilayer tubes in the coming quarter.? The final deliverable expected in the next quarter from MPT will be 40 asymmetric membranes with a slipcast nanoporous ~40 micron layer on a support tube with dense ceramic interconnects ready for testing. Task 3:Luna Labs has employed the time to finish designing and build a 30X scale-up test rig for multiple long (40 cm) tubes (Figure 2, bottom left). The first long tube membrane testing began at the end of 2021. The cause of the significant delay in delivering the first batch of longer tubes by M&PT was never clearly communicated. The membrane test fixture for multiple parallel long tubes has been completed. Task 4:Task 4 testing is currently being delayed due to a lack of testable membrane materials from Media & Process Technology. Luna Labs has begun a partnership with Saint Gobain, and they are working on demonstrating new material methods and shipping testable tubes to Luna Labs before September. The final electrolyte formulation needs to be tuned to the bilayer tube design, and testing will resume as soon as Luna Labs has bilayer tubes in-hand. Task 5:Trimeric will perform the techno-economic evaluation of the LuNOX process at an American Association of Cost Engineers (AACE) Level 4 for feasibility studies. A process design basis will document the process flow diagram with inputs, operating conditions, throughput, and salable product purity requirements and estimated market values. The LuNOX process design will detail energy and utility requirements, NOX emission control and potential nitric acid distillation capabilities, and major equipment operational parameters (compressor power requirements, heat exchanger duties, etc.). The techno-economic analysis will estimate capital and operating costs, energy performance of the technology, and the overall potential to generate revenue per unit of nitric acid produced. This analysis will include a representative process simulation with AspenTech or similar software, vender budgetary estimates, and data found in the literature. Trimeric will calculate economic metrics for the process and identify key aspects of the technology that have the greatest impact on cost and/or have the most technological risk in relation to successful technology scale-up. Trimeric will perform relevant sensitivity studies regarding the key parameters that are identified and provide input regarding technical challenges associated with process development and scale-up. Luna Labs will provide key LuNOX data such as performance as a function of operational conditions, as well as review and provide guidance on the development of the analysis. Trimeric and Luna Labs will work together to identify and develop any technical variants or options that can reduce or avoid these cost drivers. The goal of this feedback loop between analysis and technical development is to enhance productivity and minimize risk of future technical or process redesigns. Significant efforts on this Task will begin once Luna Labs has resolved the key ranges temperature and pressures that will be established upon completion of the Task 2 electrolyte and catalyst development efforts. Task 6:Luna Labs may sell or license the LuNOX process to ThyssenKrupp, who would be Luna Labs' direct customer. ThyssenKrupp would install the LuNOX process at facilities operated by Koch, who would be the end user. Both Koch and ThyssenKrupp will be key commercialization partners both as potential funders of Phase III programs as well as technical contributors to pilot scale demonstrations. During commercialization discussions in the Phase I program, Ken Wabel (Ken.Wabel@kochind.com), Director of Strategy & Business Development for Koch Ag & Energy Solutions, has suggested that one of their existing nitric acid production facilities would be a good scale-up test site due to the availability of steam and other supporting infrastructure. Also during commercialization discussions in the Phase I program, Jens Mathiak, Executive Vice President of ThyssenKrupp Industrial Solutions (Jens.Mathiak@thyssenkrupp.com), has indicated that ThyssenKrupp would be an engineering resource that could contribute to the construction of a pilot scale LuNOX skid system and provide baseline data for comparison against conventional, state-of-the-art nitric acid production technology. Pending successful development and demonstration, ThyssenKrupp would acquire the LuNOX technology for commercial manufacture and distribution to the leading domestic and international nitrogenous fertilizer producers. The initiation of productiveconversations with these potential industrial partners regarding large scale process technologies requires significant technical demonstration to establish confidence and credibility.

    Publications


      Progress 09/01/20 to 08/31/21

      Outputs
      Target Audience: Nothing Reported Changes/Problems:Luna Labs is requesting a 12-month no cost extension to allow for additional time to complete the membrane development and scale-up efforts. In the six months since the previous REEport Luna has completed construction of a scaled-up multi-tube test module which effectively increases the membrane surface area 30X. Luna Labs has also designed and begun construction of a scale III membrane module capable of processing gas one the tonnes/day scale. The key outstanding material development is the production of bilayer membranes to demonstrate constant permeance through reduction of the separation layer thickness. Luna Labs' ceramic material supplier, Media and Process Technology, is experiencing delays from its source materials suppliers and also in their own in-house development and testing program. When Media and Process Technology delivers asymmetric tubes (Task 2.3), Luna Labs will be able to accelerate its testing program (Task 4) and customize its electrolyte approach for the reduced separation layer thickness (Task 2.1). Because of ongoing synergistic membrane programs through the DOE, Luna Labs has advanced its test setups and membrane manufacturing techniques so that progress will resume quickly when Media and Process Technology resolves its delays. 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?When Media and Process Technology delivers asymmetric tubes (Task 2.3), Luna Labs will be able to accelerate its testing program (Task 4) and customize its electrolyte approach for the reduced separation layer thickness (Task 2.1). Because of ongoing synergistic membrane programs through the DOE, Luna Labs has advanced its test setups and membrane manufacturing techniques so that progress will resume quickly when Media and Process Technology resolves its delays. Scaled-up module demonstration is a program priority as overall system performance and the resulting techno-economic projections will drive interest in the technology. Luna Labs also has plans to investigate the economic potential of a NOx separation membrane due to interest from a potential commercialization partner.

      Impacts
      What was accomplished under these goals? Luna is developing the LuNOx process for producing nitric acid, which is a dual phase catalytic separation membrane technology. Nitric acid is a key component of nitrogenous fertilizers. By producing nitric acid directly from air and steam, the LuNOx technology will reduce the costs of producing nitric acid primarily by using almost a tenth of the energy as the conventional approach based on the Haber + Ostwald processes. The LuNOx technology will decrease the overall costs of nitrogenous fertilizer and is projected to increase the profitability of common crops by a few percent. The greater energy efficiency and better capabilities for integrating into the industrial nitrogenous fertilizer production and transportation infrastructure will also increase the profitability of the fertilizer industry. The greater energy efficiency and improves potential for integration with renewable energy resources will help reduce the greenhouse gas emissions of agricultural community.

      Publications


        Progress 09/01/19 to 08/31/20

        Outputs
        Target Audience:The development of the LuNOx membrane and process will connect three key target audiences: the gas processing industry, the fertilizer industry, and the renewable energy community. Together, these three audiences will benefit farmers with lower fertilizer costs and the public through lower energy usage and decreased greenhouse gas emissions. The LuNOx process is based on a dual phase membrane technology for gas separation and processing. The development of dual phase membranes for new processes as well as the commercialization of this new technology is relevant to both the membrane community as well as the gas processing industry. Leaders of the gas processing industry (Air Products, Air Liquide, Praxair, Linde) have been developing ceramic-based membranes for primarily for air separation applications. These corporations are potential customers for commercially transitioning the ceramic-based LuNOx membrane to industry for converting air and steam into nitric acid. Luna has also been developing dual phase membrane technology variants for air separation and carbon capture applications, is presently engaging Air Liquide on these efforts, and will expand technology development conversations and efforts to include the LuNOx technology. The end users are expected to be engineering firms that construct and operate nitric acid production facilities, such as ThyssenKrupp, Koch Industries, CF Industries, and Nutrien. These end-users are fertilizer manufacturer that processes feedstocks (nitrates, ammonia, urea, etc.) into a complete fertilizer product for local distribution and agricultural use. These fertilizer manufacturers will incorporate the nitrates produced by the LuNOx process into complete fertilizer products relevant to the local agricultural community. Luna has already established preliminary relationships with ThyssenKrupp and Koch Industries and will cycle back to these potential partners upon having demonstrated a functional membrane module and further developed the techno-economic analysis through Luna's Phase II subcontract with Trimeric. The production of nitrates is ideally powered by renewable energy resources. Key renewable energy resources, such as wind and solar, are intermittent. There is currently no cost-effective means of storing energy when renewable energy is cable of capturing energy in excess of the electricity grid demand. Instead of going unused or uncaptured, this energy can be applied to fertilizer production because fertilizer products represent stored energy and local fertilizer demand is predictable. The operators of the LuNOx process with work with the local energy community to capitalize on and more effectively use intermittent energy. Changes/Problems:A strategic benefit to the Phase II project has also led to a modest delay in the schedule. Luna is developing the LuNOX technology, which is a dual phase membrane technology to produce nitric acid. Nitric acid is a key component of nitrogenous fertilizers. Decreasing the costs and environmental impact of nitric acid production will benefit the agricultural community. This dual phase membrane technology also has the potential to significantly benefit other large scale gas separation and processing technologies, such as carbon capture from flue gases and the separation of oxygen from air, through decreased costs and improving the environmental impact of our domestic energy economy. The development of these other dual phase membrane technology variants with funding by the US Department of Energy has benefited the development of the LuNOX membrane for nitric acid production through synergistic effects between projects. These DOE-funded technology variants have higher funding levels, more options for follow-on projects, and higher frequencies for funding opportunities. Luna has therefore been applying a strategy that only uses this USDA Phase II projects funds to support LuNOx-specific efforts and leveraging DOE funds to advance cross-cutting efforts that benefit all of the membrane variants. To date, Luna has focused the USDA SBIR Phase II project to develop the LuNOX membranes has shifted towards focusing only on the efforts that only benefit the LuNOX technology. These efforts specifically include developing the molten phase chemistry and catalysts responsible for oxidizing air's nitrogen and synthesizing nitric acid. The electrolyte composition has been revised for operation at lower temperatures and other performance enhancement effects, the catalyst composition has been down-selected to iron, and the catalyst concentration is presently being refined. All other technology efforts that are synergistically cross-cutting amongst the other dual phase membranes, such as the development of ceramic materials, testing platforms and procedures, the scale up to larger modules, and process simulations, and approaches to integrating heat and steam have been developed with funds from the Department of energy. This strategy is substantially enhancing the effectiveness of how the USDA funding is being applied to specifically benefit the nitric acid production application and will enable a greater advancement of the LuNOX technology from the awarded USDA funds. For example, Luna has been able to achieve most of the same technical goals of the Phase II project by spending almost half of the USDA funds. This strategic use of DOE funding to support cross-cutting membrane advancements that also benefit and advance the LuNOx technology has, however, has also contributed to a moderate delay in the overall Phase II project. Luna will therefore prepare to request a no cost extension. 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?The next reporting period will characterize the LuNOx membrane's nitric acid production performance as a function of operational conditions, such as temperature and steam sweep rate. Some situations will achieve higher performance at the cost of more energy intensive conditions. Performance will be evaluated as a function of the rate and concentration of nitric acid production, how much energy is required to compress (and potentially preheat) the air, and the steam generation requirements. This parametric performance analysis will be shared with Trimeric Corporation for the subcontracted techno-economic analysis. The technology integration approach will be developed based on the performance and process requirements. Process flow diagrams and stream tables will be prepared to model and describe the process. These efforts will enable quantification of the key attributes, such as cost, energy efficiency, functionality, etc., required to substantiate customer interest, continue investment, and scale-up. The scale up to the membrane module will proceed during and support the techno-economic analysis. The results of the techno-economic analysis will prepare the LuNOx technology for substantive communications with potential customers, other target audiences, and the patent attorney. Luna will work with Nixon & Vanderhye, PC to prepare and file a patent application to protect the LuNOx technology. Luna will time further cultivate the interest and communications with potential customers and commercialization partners so that so that execution of nondisclosure agreements with these target audiences will coincide with the patent filing submission.

        Impacts
        What was accomplished under these goals? Luna is developing the LuNOx process for producing nitric acid, which is a dual phase catalytic separation membrane technology. Nitric acid is a key component of nitrogenous fertilizers. By producing nitric acid directly from air and steam, the LuNOx technology will reduce the costs of producing nitric acid primarily by using almost a tenth of the energy as the conventional approach based on the Haber + Ostwald processes. The LuNOx technology will decrease the overall costs of nitrogenous fertilizer and is projected to increase the profitability of common crops by a few percent. The greater energy efficiency and better capabilities for integrating into the industrial nitrogenous fertilizer production and transportation infrastructure will also increase the profitability of the fertilizer industry. The greater energy efficiency and improves potential for integration with renewable energy resources will help reduce the greenhouse gas emissions of agricultural community. Technical Objective 1: Develop the manufacturing capabilities to assemble and scale up multi-membrane modules to a surface area about 100 times greater than the Phase I test samples. Luna revised the molten phase chemistry for improved performance at lower temperatures, transitioned to from a manganese to iron catalyst for additional performance improvement, and is now refining catalyst concentration before proceeding to map out operational conditions. These efforts included preparing molten phase specimens of the dual phase membranes, characterizing their melting temperatures and stability limits with differential scanning calorimetry, and measuring nitric acid production and rates under relevant conditions in real time with a collection of gas and condensed nitric acid sensors. Manganese, iron, cobalt, and copper catalysts were screened for this new nitrate-based molten phase. The catalyst composition was down selected to iron(III) nitrate both because it was the most active and because there was no evidence that it was precipitating from the molten nitrate liquid phase at the upper limit of relevant temperatures (300 °C). The iron catalyst concentration in the molten was refined to 3 mol% because higher concentrations (e.g. 10 mol%) has an adverse effects on melting temperatures and viscosity. Technology development has therefore progressed to Objective 2. Technical Objective 2: Demonstrate stable, functional operation in relevant conditions to define and validate parametric performance values. The LuNOx membranes have begun testing in relevant conditions in Luna's Scale 1 testing platform (see attached report for technical description). The dual phase membranes are prepared by infilling the molten nitrate phase into the nanoporous walls of a high strength zirconia ceramic tube. Capillary action retains the non-volatile molten phase in the pores with pressures of 5 - 30 atmospheres. The Scale 1 tube membranes specimens are about the size of a pen at roughly 8 cm long, 1 cm in diameter, and 1 mm wall thickness. The customization of the ceramic materials, the manufacturing processes, and test methods have been completed. The performance of the membranes has just begun characterization as a function of temperature (150 - 300 °C), air pressure (1 - 5 ATM), and steam flow rates (0.1 - 0.5 ml/min). The construction of the Sale 2 testing platform has been completed and the Scale 2 membrane module has been finalized and is now under construction. The membrane consists of multiple (6X) longer tubes (40 cm) for a 30X scale-up. Technical Objective 3: Perform a detailed techno-economic analysis to quantitatively estimate the economic potential of the LuNOx process based upon input costs, output values, efficiency (e.g. 75 kJ/mol HNO3), operational and equipment costs, and other factors. Significant techno-economic analysis efforts will begin once the target operational conditions have been determined based on the Technical Objective 2 performance evaluation results. Technical Objective 4: Detail the technical and commercial plans for advancing to the pilot scale of 1,000 - 100,000 tons of nitric acid per year using an integrated network of modules. Significant efforts of this objective will progress once the techno-economic analysis efforts have progressed and the performance and simulation of the Scale 2 module have been characterized. The technical objective of this USDA Phase II project are proceeding rather effectively and efficiently. The main technical challenges of preparing and manufacturing the membrane materials, modules, testing platforms, test methods, modeling simulations, and plant integration approaches have primarily been hammered out through projects funded by the Department of Energy. This has enabled Luna to focus on only leveraging these USDA funds on LuNOx-specific efforts. This approach will enable Luna to exceed the technical milestones and development efforts proposed for the Phase II project, which will better position the technology for commercialization. This cost efficiency is apparent in the comparison of the project schedule against the funds spent: the project is only technically about 30% behind schedule even though the funding spend rate is closer to 60% behind schedule. Luna is planning on requesting a no cost extension to continue facilitating the advancement of the LuNOx technology.

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