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Dynamics of Capillary? Driven Flow in Paper? Based Microfluidic Devices, 2018 Advanced Coating Symposium

Dynamics of Capillary? Driven Flow in Paper? Based Microfluidic Devices, 2018 Advanced Coating Symposium

Online measurement of bulk, tensile, brightness, and ovendry content of bleached chemithermomechanical pulp using visible and near infrared spectroscopy, TAPPI JOURNAL April 2018

Online measurement of bulk, tensile, brightness, and ovendry content of bleached chemithermomechanical pulp using visible and near infrared spectroscopy, TAPPI JOURNAL April 2018

A targeted approach to produce energy-efficient packaging materials from high-yield pulp, TAPPI Journal August 2025

ABSTRACT: Unlike fossil-based plastics, wood-based packaging materials can be produced in an ecofriendly manner using wood chip residuals from sawmills and pulpwood. To produce high-yield pulp like chemithermomechanical pulps (CTMPs) for paperboard and liquid packaging, it is crucial to reduce the electric energy consumption during fiber separation. The ultimate objective is to revolutionize paperboard production by achieving a middle-layer CTMP process that consumes less than 200 kilowatt-hours per metric ton (kWh/t), significantly improving from the current 500•600 kWh/t energy demand. Optimizing the CTMP impregnation process of sodium sulfite (Na2SO3) in wood chips is crucial for achieving uniform softening, ideally at the fiber level. The properties of the fibers are significantly affected by the content of lignin sulfonates within the walls of the fiber and the middle lamellae. In this study, we employed in-house developed X-ray fluorescence (XRF) techniques, validated by beamline measurements, to map the distribution of sulfonated lignin within fibers. It also seemed possible to enhance the surface area of lignin-rich pulp fibers while losing minimal bulk by refining them with well-optimized low consistency (LC) refining. We aimed to achieve a highly efficient separation of coniferous wood fibers by co-optimizing the sulfonation and the temperature in the preheater and chip refiner. Additionally, we explored how lignin’s softening behavior and potential crosslinking influence subsequent unit operations, including pressing, peroxide bleaching, and drying, following the defibration process. In defibration during chip refining, the maximum softening of wood fibers is preferred to maximize fiber preservation and minimize energy consumption. However, optimizing the stiffness of finished pulp fibers is preferable to reduce bulk loss during paperboard production. It can strive to optimize processes to develop stronger, lighter, and more sustainable composite packaging materials. Reducing environmental impact and electric energy can help create a more sustainable future.

Conversion of paper-grade pulp from rice straw into dissolving pulp, TAPPI Journal June 2025

ABSTRACT: About 1,165 million metric tons of rice straw is generated every year worldwide, which can be a good source for the circular bioeconomy. In this research paper, the paper-grade pulp from rice straw was converted to dissolving-grade pulp by fractionation in a biorefinery initiative. Rice straw was cooked at an optimum condition of 8% potassium hydroxide (KOH) charge for 120 min at 150°C and produced a pulp yield of 47.2% with a kappa number of 18.5. Subsequently, D0(EP)D1 bleaching was carried out for the produced pulp, and the brightness of the pulp reached to 82.4%. From the black liquor, 16.5% of the lignin and 11.9% of the hemicellulose were isolated for producing biobased products and chemicals, and then the spent liquor was used for soil amendment. The bleached pulp was fractionated in a Bauer McNett fiber classifier. The pulp fibers retained on 16-, 30-, and 50-mesh screens were used as a longer fiber fraction pulp, and pulp fibers retained on 100- and 200-mesh screens were used as a shorter fiber pulp. The longer and shorter fiber fraction pulps were analyzed for cellulose, R10, pentosan, and viscosity. The long fiber fraction pulps were characterized by higher cellulose (88.2% vs. 83.1%) and lower pentosan (11.3% vs. 13.0%) content than the shorter fiber fraction pulps. The longer fiber fraction was further treated with cold KOH to remove residual hemicellulose. The KOH extraction reduced pentosan content in pulp to 6.3% and increased á-cellulose content to 91.3%. The short fiber fraction was converted to monomeric sugars using cellulase enzymes with varying reaction time, temperature, and consistency. The efficiency of cellulase activity was assessed through glucose yield and residual dry weight. A temperature of 45°C, 5.0 pH, 5% consistency, and 6 filter paper units/gram (FPU/g) o.d. pulp resulted in maximum sugar conversion of 85.7%.

Multilayer Barrier Paperboard Based on Nanocellulose and Biodegradable Thermoplastics, 2021 TAPPICon Live (21TAPL)

Characterization of Ink Adhesion Failure; Effect of Pre-dampening of Carbonate Containing Coatings , 2008 Advanced Coating Fundamentals Symposium

Characterization of Ink Adhesion Failure; Effect of Pre-dampening of Carbonate Containing Coatings , 2008 Advanced Coating Fundamentals Symposium

A theoretical approach to understanding microstructure-tensile modulus relations in paper coatings , 2008 Advanced Coating Fundamentals Symposium

A theoretical approach to understanding microstructure-tensile modulus relations in paper coatings , 2008 Advanced Coating Fundamentals Symposium

Effect of Particle Size Distribution and Packing Compression on Fluid Permeability: A Comparison of Experiments and Monte-Carlo/Lattice-Boltzmann Simulations, 2008 Advanced Coating Fundamentals Symposium

Effect of Particle Size Distribution and Packing Compression on Fluid Permeability: A Comparison of Experiments and Monte-Carlo/Lattice-Boltzmann Simulations, 2008 Advanced Coating Fundamentals Symposium

SHORT-TIME COATING DEWATERING: A NOVEL TEST METHOD AND MODEL, 2008 Advanced Coating Fundamentals Symposium

SHORT-TIME COATING DEWATERING: A NOVEL TEST METHOD AND MODEL, 2008 Advanced Coating Fundamentals Symposium

Latex Dispersions as Carriers for Glucose Oxidase Oxygen Scavenging Systems, 2008 Advanced Coating Fundamentals Symposium

Latex Dispersions as Carriers for Glucose Oxidase Oxygen Scavenging Systems, 2008 Advanced Coating Fundamentals Symposium