R&DD

Comparative Performance and Machine Learning-based Optimization of TSA Configurations for NH₃ Removal from NH₃ Cracking Gas

In the quest to reduce ammonia (NH₃) levels in H₂ fuel cell applications to below 0.1 ppm, we've pioneered novel three-bed temperature swing adsorption (TSA) configurations using zeolite 4A and harnessed machine learning (ML) for optimization. We evaluated various TSA setups, with the TSA-TGER configuration proving most efficient in techno-economic comparisons, using H₂ pressure swing adsorption tail gas for cooling and NH₃ TSA off-gas for heating. Sensitivity analyses and ML models facilitated precise predictions with a significant reduction in computational costs. This approach reduced NH₃ removal costs to just 0.98% of overall H₂ production costs, making it a promising solution for effective NH₃ removal in NH₃ cracking gases.

TSA configurations for NH₃ removal from NH₃ cracking gas, performance of ANN model and scatter profiles for optimization of the main operating variables

Dynamic-model-based Artificial Neural Network for H₂ Recovery and CO₂ Capture from Hydrogen Tail Gas

We've pioneered an integrated process for H₂ recovery and CO₂ capture from hydrogen plant tail gases. This process, consisting of front and rear sectors, has been validated and optimized using a dynamic model and an artificial neural network. The outcome showcases cost-effective H₂ recovery and efficient CO₂ capture, providing a bridge between energy research gaps and sustainability. The dynamic-model-based ANN precisely predicts system behavior at a low computational cost. Additionally, a differential evolution approach optimizes operational conditions. This methodology can be validated with reference data for a hybrid cryogenic-membrane process, ultimately determining cost and energy efficiency.

Configuration of the integrated process for H₂ recovery and CO₂ capture from the tail gas of a H₂ SMR plant, results of ANN and dynamic model

Deep reinforcement learning optimization framework for a power generation plant considering performance and environmental issues

Achieving a balance between power production and emission limits is a complex task in the electric power generation sector. A deep reinforcement learning optimization framework (DRLOF) was developed for a circulating fluidized bed (CFB) power plant. The DRLOF utilized plant data to create an environment and interacts with an advantage actor-critic (A2C) agent. The framework maximized power generation while adhering to capacity constraints and environmental emission standards, considering the cost of operations. The separate-A2CN architecture achieved an increase in electricity generation and emission reduction with lower computational cost. The DRLOF demonstrated flexibility, adaptability, and lower computational burden through different test scenarios. This approach has implications beyond the CFB power plant, extending to other chemical processes and industries. The model contributes to optimization challenges, customization needs, and cost reduction in online operations.

A2C architecture to maximize the power generation and reduce NOx in CFB power plant

CO₂ capture capability of 0.5 MW MEA demo plant using three different deep learning pipelines

Three deep learning pipelines (S-DLP, SBE-DLP, and L-DLP) were developed to predict the CO₂ capture potential of amine-based capture processes. Real operating data from a 0.5 MW MEA demo plant were utilized for data cleaning, feature selection, and deep neural network-based prediction. After eliminating outliers, the L-DLP was selected as the best pipeline, providing accurate predictions of CO₂ capture rate and concentration. Furthermore, the L-DLP was used to predict temperature variation in the absorber and stripper, crucial for energy saving. The developed pipeline demonstrated its potential for accurate and efficient prediction of CO₂ capture in chemical processes.

Configuration of CO₂ capture process and the performance comparison of each pipelines

Techno-economic analysis and optimization using DNN model for a CO₂ absorption process using an MDEA/PZ solvent with a solvent looping system for steam methane reforming

The DNN model was developed for a pre-combustion CO₂ absorption process utilizing a solvent looping system with a blended MDEA/PZ solvent. The novel solvent looping system operated by recycling a portion of the solvent from a flash drum, thereby reducing energy consumption and the size of the stripper. Deep neural network (DNN) models were utilized to accurately predict capital and operating costs. A multi-variable mutation approach using DNN models was employed to optimize the operating conditions and minimize the CO₂ capture cost.

Prediction accuracy and optimal operating conditions using ANN for CO₂ absorption process. 

Actor-critic reinforcement learning using the DNN model to determine the optimal operating conditions of the hydrocracking process

An actor-critic reinforcement learning (RL) optimization strategy using a deep neural network (DNN) surrogate model was developed for optimizing the operating conditions of hydrocracking units because traditional mathematical models for optimization are costly and may not be suitable for the quick response and customization needs of hydrocracking units. The DNN surrogate model, built from a validated mathematical model, provides accurate predictions with minimal computational resources. The proposed RL framework achieved an accuracy of 97.86% to 98.5% in determining optimal operating conditions, demonstrating consistency and an average efficiency of 98% in case studies. The approach offers advantages such as quick response time, low computational burden, and customizability, making it practical for online implementation. This strategy can be extended beyond hydrocracking to other chemical industries, presenting a novel and valuable optimization solution.

Hydrocracking process Reinforcement Learning Optimization

Integrating mathematical modelling and machine learning for steam methane reformer in the chemical industry

The steam methane reformer (SMR) plays a crucial role in hydrogen production using natural gas, making it attractive to the chemical industry. A combined approach using mathematical modeling and artificial neural networks (ANN) was developed to enhance SMR performance. A rigorous dynamic model for the SMR was developed and validated, demonstrating its reliability in predicting temperature, pressure, mole fraction, and heat flux. The model was then used to generate performance data by varying catalyst parameters and operating conditions. The dataset was analyzed using principle components, and an ANN was trained to accurately map the relationship between operating variables and predicted outputs. The ANN achieved high accuracy with significantly reduced computational time compared to dynamic simulations. This methodology enables online operation, optimization, and system design for hydrogen production at low computational cost, making it valuable to the industry.

Comparison of dynamic model and ANN model results for SMR Process

ANN-based optimization for low-carbon H₂ production via a sorption-enhanced steam methane reforming (SESMR) process integrated with separation process

The ANN model was developed for an SESMR process integrated with a separation process for low-carbon H₂ production. The development aims to simplify optimization and control, provide guidance for sorbent-catalyst development, and leverage the potential of artificial neural networks (ANN) for accurate prediction. The integrated process consists of cyclic fluidized bed (CFB), pressure swing adsorption (PSA), and other units. Sensitivity analysis and feature selection were performed to identify main objectives and variables. An ANN-based optimization approach was developed to formulate a SESMR-driven model, resulting in a 15% cost reduction for high purity H₂ production and CO₂ capture compared to the traditional steam methane reforming process. The findings contribute to the operation, optimization, and control of integrated SESMR processes and have implications for sorbent and catalyst development in complex processes.

ANN-based SESMR process optimization and its results

ML model of commercial scale SMB for multi-component n-paraffin separation

The ML model was developed for the analysis and improvement of simulated moving bed chromatography (SMB) for the separation of a multi-component mixture of C10-14 normal paraffins from kerosene. To address the complexities of feed composition and operational variables, a mathematical dynamic model was used alongside data-driven machine learning methods, which employed real industrial data, to evaluate SMB performance. Analysis using the developed dynamic model suggested that optimizing the countercurrent ratio in different zones could enhance recovery, and the importance of 'zone flush' was highlighted for effective impurity removal. The complementary use of mathematical and data-driven models was recommended due to the limitations of available experimental data. Furthermore, an exergy analysis was conducted to assess energy flow in the overall SMB process, providing suggestions for potential improvements. The results contribute to the development of design and operation guidelines for improving SMB performance in the separation of normal paraffins.

Configuration of n-paraffin SMB adsorption chambers and scatter plot of the predicted impurities

Design guideline for CO₂ to methanol conversion process supported by generic model of various bed reactors

A novel reactor design guideline for the CO₂ to methanol (CTM) conversion process was introduced by developing a generic model. The analysis encompassed commercially viable Bed Reactors (BRs), and the various optimal operating conditions were determined. Different BRs had different optimal conditions, and the overall CTM process demonstrated minimum cost at specific reactor pressure and temperature values. Developed guidelines offer practical applications for CTM process design, operation, and decision-making, and the BR models can contribute to other CO₂ utilization processes.

Proper reactor selection zone for CTM process design vs. CO₂ feed rate from the highest to lowest material costs.

A Novel Process for Wet CO₂ to Methanol using a Catalytic Fluidized Bed Reactor integrated with Separators

This ML model and optimizer were developed for an advanced process to convert wet CO₂ into methanol using a catalytic fluidized bed reactor integrated with separators. With the increasing demand for large-scale green processes to neutralize carbon emissions, this model offers an attractive solution. An artificial neural network (ANN) model could optimize the process, accurately predicting performance and significantly reducing computational costs.

Optimization of the operating conditions using ML for SMR process

Deep Neural Network-based Surrogate Model for Dynamic Behaviors and Performance of Solid Propellant Combustion

The development focuses on predicting the dynamic behavior and performance of solid propellant combustion using a mathematical model and a deep neural network (DNN) surrogate model. The rigorous mathematical model has limited practicality due to its computational complexity. The DNN surrogate model was developed to address this limitation, accurately and quickly predicting combustion dynamic behaviors. The surrogate model outperformed dynamic simulations in terms of computational speed, being hundreds of times faster.

Results of dynamic behavior of solid propellant combustion using surrogate model

Advanced cartridge design using CFD for a gas respiratory protection system

Gas masks play a vital role in safeguarding individuals from hazardous materials, necessitating the development of advanced cartridges for next-generation gas respirators. The CFD model was validated using a prototype cartridge, and the respiration resistance and breakthrough time were compared for the three designs. A virtual reality (VR) system was also employed to observe the cartridges' performance visually. The CFD model contributes to developing and optimizing gas respirator cartridges, enhancing wearability, protection, and overall design efficiency.

Shape and geometry of gas cartridges and gas flow observed in VR.

Advanced process integration and machine learning-based optimization to enhance techno-economic-environmental performance of CO₂ capture and conversion to methanol

An integrated CO2 capture and methanol conversion process (CCTM) enhanced by machine learning-based optimization achieves significant improvements in energy consumption, production cost, and CO2 reduction. Advanced design reuses waste heat, off-gas, and water, improving energy efficiency by 14.73-16.30%, reducing production costs by 0.81-1.28%, and increasing net CO2 reduction by 3.13-3.38%. A deep neural network model optimized the process, achieving a 92.53% CO2 capture rate and an 8.21 $/tMeOH reduction in production cost. This approach offers a viable, sustainable solution for carbon neutrality in methanol production.

Advanced process integration and machine learning-based optimization to enhance techno-economic-environmental performance of CO2 capture and conversion to methanol

Blended-amine CO₂ capture process without stripper for high-pressure syngas

The paper presents a novel CO2 capture process using a blended MDEA/PZ solvent without a traditional stripper for high-pressure syngas. The process replaces the stripper with a low-pressure flash column, allowing solvent regeneration at lower temperatures (<373.15 K) and reducing energy consumption. Optimization using deep learning and NSGA-II resulted in a heat duty of 1.881 GJ/ton CO2, significantly lower than conventional methods. Economic analysis showed that with waste heat recovery, the process costs $32.89/ton CO2, emphasizing its potential for cost-effective CO2 capture in hydrogen production.

Blended-amine CO2 capture process without stripper for high-pressure syngas

Pre-combustion CO₂ capture using amine-based absorption process for blue H₂ production from steam methane reformer

A novel pre-combustion CO2 capture process using MDEA/PZ solvent for blue H2 production from steam methane reformer (SMR) is developed. Sensitivity analysis and ANN-based optimization were performed, showing significant energy savings with reboiler duties of 1.318 and 1.364 GJ/tonCO2 for 90% and 95% CO2 removal efficiencies, respectively. ANN optimization further reduced equivalent work by 0.3%. The process demonstrates over 40% lower energy consumption than traditional post-combustion methods, making it highly competitive for industrial applications, particularly beneficial for H2 recovery without additional compression energy.

Amine-based absorption process for CO2 capture in SMR syngas & Profiles for optimization of operating parameters at 90%

Prediction of CO₂ solubility in multicomponent electrolyte solutions up to 709 bar: Analogical bridge between hydrophobic solvation and adsorption model

A novel model predicting CO2 solubility in multicomponent electrolyte solutions up to 709 bar was developed using an analogy between hydrophobic solvation and an ideal adsorption model. The model, which uses just four parameters, accurately predicts CO2 solubility in solutions with various ions (e.g., Na+, Ca2+, Mg2+, K+, SO4²−, Cl−) by correlating CO2 pressure, system temperature, and concentration of electrostricted water molecules. With 1384 experimental data points for validation, the model achieved a 95% prediction accuracy, offering significant utility for industrial CO2 applications.

Experimental data vs. model predictions of CO2 solubility