scholarly journals Scale-up of the production of highly reactive biogenic magnetite nanoparticles using Geobacter sulfurreducens

2015 ◽  
Vol 12 (107) ◽  
pp. 20150240 ◽  
Author(s):  
J. M. Byrne ◽  
H. Muhamadali ◽  
V. S. Coker ◽  
J. Cooper ◽  
J. R. Lloyd
Keyword(s):  
Magnetic Properties ◽  
Large Scale ◽  
Scale Up ◽  
Surface Reactivity ◽  
Geobacter Sulfurreducens ◽  
Scale Production ◽  
Buffer Solution ◽  
Pilot Plant Scale ◽  
Functional Biomaterials ◽  
Microbial Systems

Although there are numerous examples of large-scale commercial microbial synthesis routes for organic bioproducts, few studies have addressed the obvious potential for microbial systems to produce inorganic functional biomaterials at scale. Here we address this by focusing on the production of nanoscale biomagnetite particles by the Fe(III)-reducing bacterium Geobacter sulfurreducens , which was scaled up successfully from laboratory- to pilot plant-scale production, while maintaining the surface reactivity and magnetic properties which make this material well suited to commercial exploitation. At the largest scale tested, the bacterium was grown in a 50 l bioreactor, harvested and then inoculated into a buffer solution containing Fe(III)-oxyhydroxide and an electron donor and mediator, which promoted the formation of magnetite in under 24 h. This procedure was capable of producing up to 120 g of biomagnetite. The particle size distribution was maintained between 10 and 15 nm during scale-up of this second step from 10 ml to 10 l, with conserved magnetic properties and surface reactivity; the latter demonstrated by the reduction of Cr(VI). The process presented provides an environmentally benign route to magnetite production and serves as an alternative to harsher synthetic techniques, with the clear potential to be used to produce kilogram to tonne quantities.

scholarly journals PILOT PLANT SCALE-UP STUDIES FOR PARENTERAL - A REVIEW

2021 ◽  
Vol 12 (8) ◽  
pp. 58-63
Author(s):  
V. Manikandan
Keyword(s):  
Pilot Plant ◽  
Large Scale ◽  
Scale Up ◽  
Therapeutic Index ◽  
The Body ◽  
Plant Production ◽  
Scale Production ◽  
Large Scale Production ◽  
Production Techniques ◽  
Pilot Plant Scale

The dosage form of parenteral is sterile and gives a quick beginning of activity and gives an immediate action to accomplishing the medication impact inside the body. The route of parenteral administration is the most well-known and productive route for the conveyance of dynamic medication substances with poor bioavailability and medications with a tight therapeutic index. The principal objective of the technique was to endeavour to talk about the different procedures needed for the pilot plant production considers. The pilot plant is the term that is normally more modest than large-scale production plants yet it is the underlying scope of sizes. It is planned for learning, and making the definitions on a limited scale to accomplish the relationship with the enormous scope production, and they are normally more adaptable perhaps to the detriment of the economy. Most of the pilot plants are implicit in the maker's own research centres of the manufacturer utilizing stock lab hardware. These pilot plant studies are performed by using a technology transfer (TT) documentation report which is made by the research and development department for product development. Hence, this process would meet product quality, safety, and efficacy and further this production techniques will transfer to large-scale production for parenteral preparation.

Solid Lipid Nanoparticles: A Promising Drug Delivery Technology

2009 ◽  
Vol 2 (2) ◽  
pp. 509-516
Author(s):  
S. Pragati ◽  
S. Kuldeep ◽  
S. Ashok ◽  
M. Satheesh
Keyword(s):  
Drug Delivery ◽  
Solid Lipid Nanoparticles ◽  
Large Scale ◽  
Colloidal Particles ◽  
Scale Up ◽  
Lipid Nanoparticles ◽  
Scale Production ◽  
Research Activity ◽  
New Approach ◽  
Solid Lipid

One of the situations in the treatment of disease is the delivery of efficacious medication of appropriate concentration to the site of action in a controlled and continual manner. Nanoparticle represents an important particulate carrier system, developed accordingly. Nanoparticles are solid colloidal particles ranging in size from 1 to 1000 nm and composed of macromolecular material. Nanoparticles could be polymeric or lipidic (SLNs). Industry estimates suggest that approximately 40% of lipophilic drug candidates fail due to solubility and formulation stability issues, prompting significant research activity in advanced lipophile delivery technologies. Solid lipid nanoparticle technology represents a promising new approach to lipophile drug delivery. Solid lipid nanoparticles (SLNs) are important advancement in this area. The bioacceptable and biodegradable nature of SLNs makes them less toxic as compared to polymeric nanoparticles. Supplemented with small size which prolongs the circulation time in blood, feasible scale up for large scale production and absence of burst effect makes them interesting candidates for study. In this present review this new approach is discussed in terms of their preparation, advantages, characterization and special features.

Recombinant Protein Production in Microalgae: Emerging Trends

2020 ◽  
Vol 27 (2) ◽  
pp. 105-110 ◽  
Author(s):  
Niaz Ahmad ◽  
Muhammad Aamer Mehmood ◽  
Sana Malik
Keyword(s):  
Chloroplast Genome ◽  
Recombinant Proteins ◽  
Large Scale ◽  
Higher Plants ◽  
Scale Up ◽  
Chloroplast Transformation ◽  
Point Of View ◽  
Nuclear Transformation ◽  
Scale Production ◽  
Algal Chloroplast

: In recent years, microalgae have emerged as an alternative platform for large-scale production of recombinant proteins for different commercial applications. As a production platform, it has several advantages, including rapid growth, easily scale up and ability to grow with or without the external carbon source. Genetic transformation of several species has been established. Of these, Chlamydomonas reinhardtii has become significantly attractive for its potential to express foreign proteins inexpensively. All its three genomes – nuclear, mitochondrial and chloroplastic – have been sequenced. As a result, a wealth of information about its genetic machinery, protein expression mechanism (transcription, translation and post-translational modifications) is available. Over the years, various molecular tools have been developed for the manipulation of all these genomes. Various studies show that the transformation of the chloroplast genome has several advantages over nuclear transformation from the biopharming point of view. According to a recent survey, over 100 recombinant proteins have been expressed in algal chloroplasts. However, the expression levels achieved in the algal chloroplast genome are generally lower compared to the chloroplasts of higher plants. Work is therefore needed to make the algal chloroplast transformation commercially competitive. In this review, we discuss some examples from the algal research, which could play their role in making algal chloroplast commercially successful.

Characterization of Thin Film CdTe photovoltaic materials deposited by high plasma density magnetron sputtering

2011 ◽  
Vol 1323 ◽  
Author(s):  
A. Abbas ◽  
J.W. Bowers ◽  
B. Maniscalco ◽  
S. Moh ◽  
G.D West ◽  
...  
Keyword(s):  
Magnetron Sputtering ◽  
Plasma Density ◽  
Large Scale ◽  
Scale Up ◽  
High Plasma ◽  
Window Layer ◽  
Closed Field ◽  
Scale Production ◽  
Batch System ◽  
High Plasma Density

ABSTRACTA new magnetron sputtering strategy is introduced that utilizes high plasma density (~5mA.cm-2) to avoid or reduce high temperature processing. The technique uses magnetrons of opposing magnetic polarity to create a “closed field” in which the plasma density is enhanced without the need for high applied Voltages. A batch system has been used which employs a rotating vertical drum as the substrate carrier and a symmetrical array of linear magnetrons. The magnetrons are fitted with target materials for each of the thin films required in the photovoltaic (PV) stack including the CdTe absorber layer, CdS window layer, metal contact using the conventional superstrate configuration. The “closed field” sputtering technology allows scale up not only for larger batch system designs but it is also configurable for “in-line” or “roll to roll” formats for large scale production. The morphology of each of the layers is characterized using a variety of structural and optical techniques including Field Emission Gun SEM and X-ray diffraction (XRD).

Ultrasonic-Impregnation for Fiber-Reinforced Thermoplastic Prepreg Production

2017 ◽  
Vol 742 ◽  
pp. 17-24
Author(s):  
Steve Sockol ◽  
Christoph Doerffel ◽  
Juliane Mehnert ◽  
Gerd Zwinzscher ◽  
Steffen Rein ◽  
...  
Keyword(s):  
Large Scale ◽  
Matrix Material ◽  
Scale Up ◽  
Small Scale ◽  
Hydraulic Pressure ◽  
Scale Production ◽  
Fiber Reinforced ◽  
Technological Parameters ◽  
Ultrasonic Technology ◽  
High Processing

Fiber-reinforced thermoplastics have a high potential for big scale light weight process applications due to low processing times and recyclability. Further advantages are the low emissions during the manufacturing process and beneficial handling and storing properties of the semi finished materials. Thermoplastic composites are made of reinforcement fibers and a thermoplastic polymer matrix by applying two essential sub processes: (1) melting of the matrix-material and (2) impregnating the textile component with molten matrix-material. At present state of art both sub-processes are applied by using double-belt-presses, characterized by high processing temperatures and high processing forces. Therefore, a large amount of energy is needed to create the necessarily high compaction forces and temperatures with hydraulic cylinders and electric heating. Convection, infrared-radiation and the cooling (dynamic) of tempered machine parts leads to a significant dissipation of energy. Especially the process for generating the hydraulic pressure has a low level of efficiency. Therefore, in respect to economic and ecologic reasons, novel energy-efficient impregnation processes need to be investigated and developed. The represented novel impregnation process is based on ultrasonic technology. A stack of polymer film (outer layers) and a textile ply (inner layer) is formed and the energy is applied with an ultrasonic sonotrode. The efficient, fast and strongly concentrated energy application into the thermoplastic films allows the development of novel and highly flexible machine concepts. These can be used for development of small scale up to large scale production processes. The ultrasonic-technology allows a continuous impregnation of the textile component with molten matrix-material. A custom-designed prototype was developed. First material samples were produced and the technological parameters studied. A characterization of the experimental results, material samples, prototype machine and process is the focus of this paper.

scholarly journals Carbon Purchase Agreements, Dactories, and Supply-Chain Innovation: What Will It Take to Scale-Up Modular Direct Air Capture Technology to a Gigatonne Scale

2021 ◽  
Vol 3 ◽  
Author(s):  
David Izikowitz
Keyword(s):  
Carbon Dioxide ◽  
Supply Chain ◽  
Large Scale ◽  
Manufacturing Industry ◽  
Scale Up ◽  
Ambient Air ◽  
Scale Production ◽  
Solid Sorbent ◽  
Direct Air Capture ◽  
Air Capture

Natural and engineered carbon dioxide removal have become regular features of climate models which limit warming to 1.5°C or even 2°C above pre-industrial levels. This gives rise to an assumption that solutions, for example direct air capture (DAC)—involving the direct removal of carbon dioxide from ambient air—can be commercialised and deployed at the necessary speed and scale to have a material impact, in the order of gigatonnes, by mid-century. Modular, solid-sorbent DAC on a gigatonne scale will require the mass mobilisation of supply chains to manufacture millions of modular DAC units−20 million of the present state of the art 50 tonne/year modules to deliver 1 gigatonne per year, as well as the large-scale production of novel chemical sorbents. To achieve a climate relevant DAC industry will demand innovative procurement models, for example carbon purchase agreements (CPAs), and dedicated DAC manufacturing facilities or dactories. In addition, insight is offered through the work of DAC start-up Carbon Infinity into the industry supply-chain position, adopting lessons from computing, and energy technologies. In particular, we look at approaches to drive demand and scale-up DAC module production, and opportunities presented in the development of an integrated DAC manufacturing industry.

Towards the Large Scale Production of Fullerenes and Nanotubes by Solar Energy

2001 ◽  
Author(s):  
Tony Guillard ◽  
Gilles Flamant ◽  
Daniel Laplaze ◽  
Jean-François Robert ◽  
Bruno Rivoire ◽  
...  
Keyword(s):  
Production Rate ◽  
Large Scale ◽  
Scale Up ◽  
Product Yield ◽  
Transfer Model ◽  
Scale Production ◽  
Cooling Zone ◽  
Target Temperature ◽  
Reduced Pressure ◽  
Carbon Soot

Abstract Conventional methods for the synthesis of fullerenes and carbon nanotubes such as laser or electric arc ablation have failed when the process is scaled up. Our ultimate goal is to scale a solar process up from 2 to 500 kW; this paper shows that our method for achieving this scale up is valid because we were able to predict process performance variables at the 50 kW level from preliminary experimental results from 2 kW experiments. The key parameters that characterize this process are the carbon soot mass flow rate and the desired product yield. The carbon soot production rate is a function of the target temperature and this can be predicted in a straightforward way from a heat transfer model of the larger system. The yield is a more complicated function of specific reactor variables such as patterns of fluid flow, residence times at various temperatures and the reaction chemistry, but we have found that for fullerenes it depends primarily on the concentration of carbon vapor in the carrier gas, the target temperature and the temperature distribution in the cooling zone. Using these parameters, we scaled our process up to 50 kW and compared the predicted results to the measured performance. A graphite target 6 cm in diameter was vaporized in an argon atmosphere and a reduced pressure of 120–240 hPa with a solar flux density in the range 600–900 W/cm2. Vaporization rates of 20 g/h were measured with a fullerene production rate equal to or greater than 1 g/h, i.e. the expected results.

scholarly journals Heterotrophy as a tool to overcome the long and costly autotrophic scale-up process for large scale production of microalgae

2019 ◽  
Vol 9 (1) ◽  
Author(s):  
A. Barros ◽  
H. Pereira ◽  
J. Campos ◽  
A. Marques ◽  
J. Varela ◽  
...  
Keyword(s):  
Large Scale ◽  
Scale Up ◽  
Biomass Concentration ◽  
Growth Conditions ◽  
Pilot Scale ◽  
Industrial Scale ◽  
Scale Production ◽  
Two Stage ◽  
Chlorophyll Contents ◽  
Large Scale Production

Abstract Industrial scale-up of microalgal cultures is often a protracted step prone to culture collapse and the occurrence of unwanted contaminants. To solve this problem, a two-stage scale-up process was developed – heterotrophically Chlorella vulgaris cells grown in fermenters (1st stage) were used to directly inoculate an outdoor industrial autotrophic microalgal production unit (2nd stage). A preliminary pilot-scale trial revealed that C. vulgaris cells grown heterotrophically adapted readily to outdoor autotrophic growth conditions (1-m3 photobioreactors) without any measurable difference as compared to conventional autotrophic inocula. Biomass concentration of 174.5 g L−1, the highest value ever reported for this microalga, was achieved in a 5-L fermenter during scale-up using the heterotrophic route. Inocula grown in 0.2- and 5-m3 industrial fermenters with mean productivity of 27.54 ± 5.07 and 31.86 ± 2.87 g L−1 d−1, respectively, were later used to seed several outdoor 100-m3 tubular photobioreactors. Overall, all photobioreactor cultures seeded from the heterotrophic route reached standard protein and chlorophyll contents of 52.18 ± 1.30% of DW and 23.98 ± 1.57 mg g−1 DW, respectively. In addition to providing reproducible, high-quality inocula, this two-stage approach led to a 5-fold and 12-fold decrease in scale-up time and occupancy area used for industrial scale-up, respectively.

scholarly journals A Novel Approach Using Conventional Methodologies to Scale up BNC Production Using Komagataeibacter medellinensis and Rotten Banana Waste as Alternative

Processes ◽  
2020 ◽  
Vol 8 (11) ◽  
pp. 1469
Author(s):  
Carlos Molina-Ramírez ◽  
Juan Álvarez ◽  
Robin Zuluaga ◽  
Cristina Castro ◽  
Piedad Gañán
Keyword(s):  
Production Process ◽  
Large Scale ◽  
Culture Medium ◽  
Scale Up ◽  
Glucose Consumption ◽  
Human Consumption ◽  
Scale Production ◽  
Bacterial Nanocellulose ◽  
Large Scale Production ◽  
Glucose Diffusion

Currently, cellulose nanostructures are among the most promising structures, and extensive work in materials and biotechnology industries is aimed at identifying an efficient process of production. Even when production at the laboratory scale is successful, crucial aspects of increased commercial applications for cellulose nanostructures are linked to large-scale production. Large-scale production requires a balance between the cost of the culture medium and product value. Therefore, in this work, for the optimization and scaling up of bacterial nanocellulose, a culture medium consisting of rotten banana unsuitable for human consumption was used for the first time as an inexpensive feedstock. Initially, the bacterial nanocellulose (BNC) culture medium conditions were optimized, and it was established that a glucose concentration of 26.4 g/L and a V/A ratio of 2.2 cm were the optimal conditions for production reaching a BNC yield of 5 g/L, which was 42.4% higher than the best result initially obtained. Finally, the scale-up process was performed, implementing a regime analysis methodology by comparing the characteristic times of the critical mechanisms involved in BNC production, namely, microbial growth, glucose consumption, BNC production, and glucose diffusion into the BNC membrane, as the first approach for this type of BNC production process. The mechanism underlying the BNC production process is glucose diffusion into the BNC membrane (characteristic time, 675.47 h). Thus, the V/A ratio was selected as the scale-up criterion most suitable for producing BNC under static culture conditions, allowing the production of 16 g of BNC after 12 d of fermentation in a plastic bioreactor, which was 3378% higher than that produced in glass vessels. The results obtained in this study may initiate further improvements in BNC commercial production by exploiting different feedstocks.

Sign in / Sign up

Export Citation Format

Share Document