Science topic

Particle Size - Science topic

Particle Size is a relating to the size of solids.
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I am working on a galvanized zinc dross. I need to reduce the particle size of this material.
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Alan Rawle provided good background - would like to add that if you can cryo-mill at -78 C (dry ice) or 77 K (liquid nitrogen) it can alter some behaviors of the material being milled.
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Looking for the synthesis protocol to synthesize mesoporous silica nanoparticle of morphology either mcm series, dendritric msns series or sba series, of particle size above 500 and less than 1000 nm, with pore size of 10 nm or above.
Please recommend any paper or the procedure for the above request.
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To synthesize mesoporous silica nanoparticles (500–1000 nm) with pore sizes above 10 nm, adjust surfactant types, concentrations, and use swelling agents like TMB in methods for dendritic MSNs, MCM-41, or SBA-15. Control reaction conditions such as pH, temperature, and aging time to tune particle and pore sizes effectively.
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we prepared nano urea for the field trial on the cultivation and growth of Solanum lycopersicum. we need to mesure the partical size of nano urea . please give your valuable suggestion for mesure the particle size by DLS method. which solvent or dispersion media used for nano urea?
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I hope this message finds you well! I was thrilled to hear about your project involving Dynamic Light Scattering (DLS) for measuring the particle size of nano urea. It sounds like an exciting endeavor, and I’m happy to share some insights that might help you along the way.
First, selecting the right solvent is crucial. For nano urea, using water as a dispersion medium is often effective, but ensure that it maintains the stability of your nanoparticles without dissolving them. Preparing a dilute suspension will help minimize multiple scattering effects, so consider sonication to achieve a uniform dispersion if needed.
Once your sample is ready, you can proceed with the DLS measurements. Make sure to follow the instrument's guidelines closely, paying attention to temperature stabilization and avoiding bubbles in the cuvette, as these factors can significantly affect your results. After measuring, you’ll receive data on the hydrodynamic size of the particles, including a size distribution graph that provides insights into the uniformity of your sample.
Lastly, don’t forget to calibrate your DLS instrument with standard particles and validate your findings against literature values or alternative methods. This step is essential for ensuring the reliability of your results.
I hope these tips prove helpful, and I wish you the best of luck with your field trial! If you have any questions or need further assistance, feel free to reach out.
Some interesting articles for your reading can be:
Best regards,
Kaushik
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Dear colleagues,I am working on optimizing the extraction process of essential oils and I need guidance on:
  1. Which software would you recommend for creating and analyzing a Design of Experiments (DoE), specifically for:
  • Hydrodistillation time
  • Plant material/water ratio
  • Temperature
  • Drying time
  • Particle size
  1. Are there any free online tools or open-source alternatives to Minitab for this purpose?
  2. What would be the most suitable experimental design considering:
  • Response surface methodology (RSM)
  • Central composite design (CCD)
  • Number of variables
  • Cost and time optimization
Any suggestions, recommendations, or shared experiences would be greatly appreciated.Thank you in advance for your help.Best regards,
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Dear Wissam Mazouz,
Ramadan Karim for you too.
Thank you for your words and the proposition of the collaboration. That would be my great pleasure.
I will message you to discuss the details.
Kind regards
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Hi all,
I have been facing an issue with XRD analysis in GSAS-II for several months and have not been able to find a solution.
I am analyzing XRD patterns using GSAS-II to determine particle size, phase composition, and weight fractions. I have raw XRD data (attached) along with the corresponding CIF files.
When I analyze my data using CIF files, I obtain results (attached as a .gpx file) that include particle size and weight fractions. I assume that the reported particle size represents an average size.
To obtain crystallite sizes for individual peaks, I performed peak analysis without using CIF files. From the GSAS-II results, I calculated the particle size using the gamma (γ\gammaγ) value.
However, I encountered an issue:
  • The crystallite sizes of TiO₂ (anatase and rutile) are nearly identical, which seems reasonable.
  • However, the crystallite size of metallic Co is significantly different, which I find confusing.
I am not sure why this discrepancy occurs and need guidance to obtain accurate results. Could you please help me understand and resolve this issue?
Thank you very much for your time and expertise.
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It took me a while to realize the wavelength was 0.53 angstroms. I had proceeded assuming it was something standard like Cu-Ka at 1.54 Angstroms. You might point that out in your introduction. Was that from a synchrotron or another source? I see it is similar to Cd-Ka with an energy of 23.2 keV.
Now back to your question, I don't think you should try to do too much with the peak at 15 degrees. You would be trying to fit it to peaks of uncertain widths at three different positions. I don't know that the fit would mean much. The uncertainty would be rather large. I would stick to using the clear peaks to estimate the crystallite size if you insist on doing so. Are they giving different size estimates at the different orientations?
You said that the Co size is very strange. You will need to elaborate on that. I have no idea what you mean.
You should be able to image those particles with a good FE-SEM. If the Co particles are much larger, you should be able to clearly see that and their size.
You may not be able to differentiate the particles well by EDS due to their small size unless you prepare them on a TEM grid.
You should be able to differentiate between the bright Co particles and the darker TiO2 particles with a backscattered electron signal.
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I am working on green synthesis of silver nanoparticles. I am getting particle size beween 100 to 150 nm. I have increased the stirring speed up to 2000 rpm. Still I am unable to get particle size below 100 nm.
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ultra Sonication could be another replacement. Sonicate sample for 4-5 hours
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My query is, from XRD we get crystallite size in the order of nanometer as I have synthesized my Hydroxy-apatite from co-precipitation route from the Scherrer's formula. I did SEM analysis of a pellet, which was sintered at 1100 degrees for 24 hours, although poor quality coated with carbon, but tend to find individual particle size using ImageJ software, there i find the size to be of the range of micrometer order(roughly about 0.76 micrometer). The thing is as it is a pellet, according to the image (which I have attached) I did not see any grain boundary regions rather than individual particles which are visible. Thus the large size is because of the pellet made and SEM of powder is not done or something else? So what should one do in this case. Also in many papers, people do SEM of powder sample and they report it as grain size rather than particle size. So what information do one get, the grain size or the particle size from it.
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Particles and grains are often misinterpreted in papers, but the difference is not so small. As I understand, here you have powders synthesized by coprecipitation which are pressed in pellet and watched under SEM. There were no any processes needed for the formation of grains. During precipitation you obtained nuclei which grew into crystallites and particles. Those particles are usually composed of several crystallites - primary particles, and more primary paricles are often agglomerated into larger particles.
To obtain grains, you need to conduct thermal treatment after pressing the particles. Solid-state reaction occurs, paricles in contact interact, grow or dissapear and the grains and grain boundaries are formed. This is the process of sintering, during which the powder consisted of particles is becoming ceramics consisted of grains.
Images confirm these are separate particles, joined together only by pressure and not intimately.
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Hi everyone! Currently, I am working on a project and need reliable suppliers for PE and PP nanoplastics. I am looking for particle sizes around 1-200 nm, non-functionalized surface (plain) NPs. Any recommendations would be very helpful. Thank you.
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Polyethylene (PE) Nanoplastics:
  • Cospheric LLC: Specializes in manufacturing polyethylene nanospheres ranging from 200nm to 9,900nm. These particles are available in dry powder form and are commonly used in environmental studies as microplastic simulants.Cospheric
  • Goodfellow: Offers a variety of polyethylene microspheres and nanoplastics suitable for research purposes.
  • Alfa Chemistry: Provides a range of nanomaterials, including polyethylene nanoplastics, catering to various research and industrial needs.
Polypropylene (PP) Nanoplastics:
While suppliers specifically listing polypropylene nanoplastics are limited, several companies offer polypropylene resins and microspheres that may meet your requirements:
  • Nexeo Plastics: Distributes polypropylene resins from top suppliers, including Borealis, LyondellBasell, and Braskem. Their products cater to various industries, and they may offer materials suitable for producing nanoplastics.Nexeo Plastics
  • KW Plastics: Manufactures versatile polypropylene resins tested to meet ASTM standards, suitable for injection molding and other applications. While they primarily offer larger-scale resins, contacting them could provide insights into obtaining finer polypropylene materials.KW Plastics
  • Amco Polymers: Supplies a range of polypropylene materials known for good mechanical properties, heat resistance, and chemical resistance. They may have options suitable for your needs.Amco Polymers
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How do variations in progesterone particle size and its encapsulation with polysaccharides influence the efficacy of estrus synchronization, particularly when utilizing spray drying techniques? What key factors (e.g., particle size, encapsulation material, spray drying parameters) should be optimized for improving the controlled release and bioavailability of progesterone in this context?
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@Asst. Prof. Hala Jawad Alfatlawy
Thanks for your input. However, I still feel there’s more to consider. It might be more helpful if you shared a personal experience..
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Could anyone suggest the most effective industrial method to reduce the particle size of Si₃N₄ powder (currently 3 µm) for use in tape casting of silicon nitride substrates?
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For industrial-scale reduction of Si₃N₄ powder from 3 µm to finer sizes suitable for tape casting, wet ball milling is typically one of the most effective methods, as it is scalable, relatively cost-effective, and allows for good control over particle size distribution. You can use a dispersant in the milling medium to prevent agglomeration and achieve a uniform dispersion of the fine powder.
Alternatively, if finer particle sizes (in the sub-micron or nano range) are required, jet milling or high-energy ball milling could be considered, though these methods may involve higher operational costs and more complex equipment.
Finally, ensure that the powder is well-dispersed in the slurry for tape casting to prevent defects in the final silicon nitride substrate.
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How to accurately test the particle size of carboxymethylcellulose sodium in aqueous solution ? Is there any data for reference ?
Recently, we were conducting experiments related to carboxymethylcellulose sodium. However, when testing the particle size of carboxymethylcellulose sodium, we were confused as the data were quite different.
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Kun Li The usual route is dry laser diffraction. It is important to set up a robust, repeatable, and reproducible method with the main parameters to control being the differential pressure and feed rate which govern the dispersion of the powdered material. Main constants are the optical properties. References are ISO 13320 (2020) - Particle size analysis — Laser diffraction methods and ASTM E3340-22 Standard Guide for Development of Laser Diffraction Particle Size Analysis Methods for Powder Materials. You can see a webinar overview (free registration required) here:
PST & BDAS - An acronym approach to laser diffraction method development
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This is after completion of TFF process. Answers are appreciated. Thanks.
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Dear Sheikh
You can use a 100 KDa centrifugal filter.
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average particle size calculation from TEM
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You get a number distribution from TEM. The standard error is proportional to the recipricol of the square of the number of particles counted. For 1% standard error you’ll need to measure 10000 particle; for 10% SE, you can measure 100 particles. Remember too that you are imaging a tiny fraction of the sample so showing representativeness will be difficult - in the whole history of electron microscopy no more than a few tens of grams have been imaged. Also consider you’re looking at a slice through the particle (think of slicing a cube in different directions) and interpretation is difficult. Measuring a diameter without automation is also not easy. Automatic image analysis is one possibility.
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I have truck tire particles that I am using in my column experiment. I am trying to do size determination using the Malvern Zetasizer. My sample concentration is 0.1 mg/L, i.e., 10 g of sample was mixed with 100 mL of ultrapure water. I sonicated the sample for five minutes and some of the particles agglomerated. So, what filter size should I use to properly measure and get the representative particle size in my sample?
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o determine your air filter size, you need to measure its length, width, and depth. These measurements are usually printed on the side of the filter. If not, you can use a tape measure to get the dimensions.
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My liposome is a non-phospholipid liposome (sterosome) composed of palmitic acid and cholesterol, 20mg of palmitic acid and 70mg of cholesterol.
After a month of storage in a refrigerator at 4 degrees Celsius, the particle size increased from about 140 nm to 180 nm. Although the increase in particle size was not exaggerated due to cholesterol, it still increased. I would like to ask what the possible reason is ?
I know it may be sedimentation or self-aggregation, but my zeta potential is about -48mV.... I still can’t think of any other possible reasons. Since saturated fatty acids are not easily oxidized, could you please tell me what other possible reasons there are? I hope there is some literature support.
Thank you.
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Your liposomes are formed through water-mediated hydrophobic interactions. We discovered that hydrophobic interactions depend on the energy of thermal fluctuations of water molecules, which depend on temperature, and quantum fluctuations of water molecules, which depend on pressure. As you can see, the size of your liposomes depends on temperature, that is, thermal fluctuations. The two energy contributions of intermolecular interactions compete with each other. A new theory of this phenomenon can be read in the articles
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My liposome is a non-phospholipid liposome (sterosome) composed of palmitic acid and cholesterol, 20mg of palmitic acid and 70mg of cholesterol. After several months of storage in a refrigerator at 4 degrees Celsius, the particle size increased from about 140 nm to 180 nm.
The formula of the stereosome in other groups is the same, except that I packed PEG with different molecular weights and concentrations into the interior of the stereosome (in the water chamber). The particle size of the group with PEG was a little smaller than that of the control group (about 125-130nm).
Then it became more stable one month later, and the particle size almost did not change. Could you please tell me what the reason might be? Thank you!
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Dear I-Hsuan Shih, this is a form of NPs dispersion instability named "ripening", which means smaller NPs associate to form bigger ones. It is a diffusion process. The presence of PEG impede such ease of diffusion by making an outer shell protecting the NPs, thus stability is enhanced. My Regards
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Is there any way or calcations to convert the particle size of nanoparticle to molecular weight KDa?
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Hi there,
I want to get some help, if anyone has already explained and improved the correlation between the crystallite size results and particle size measured by laser granulometry.
I have used the two techniques to have an idea about the size of particles before and after the ball milling, thus the answers are similar, but I need some explication to link the results.
All the best,
Mohamed
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Mohamed Elmouhinni , The two techniques do measure different properties.
The laser diffraction experiment is a result of the overall size and shape (and their distribution) of the particles. You would get the same information if the particle is a single crystal or consists of many small crystallites that are conglomerated into a large particle, as long as the overall shape is the same.
With wide angle (xray/neutron/electron) diffraction the width of the Bragg peaks depends on the size of structurally coherent domains, meaning volumes inside your crystal in which the lattice planes are all nicely periodic in their distance. Roughly speaking you could assume/hope that this relates to the diameter of the individual crystallites. These diffraction experiments can result in a much smaller "size" than the laser granulometry if the particle is an agglomerate of small crystalltes.
Small angle scattering (xrays or neutrons) on the other hand is more similar to the laser diffraction experiment and yields information on the overall particle size and shape.
Thus you cannot compare and relate the results, as very different properties are measured.
If your XRD data yield the same size as the laser granulometry, then it appears that your particles are essentially good single crystals and defects like microstrain, internal cracking etc introduced by the ball milling process may have broken the original crystals into smaller peaces but each particle is pretty much a "reasonably good" single crystal.
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When using different laser energies, what is the effect on the size of nanoparticles? Does it increase or decrease with increasing energy? Please help
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Nanoparticles produced by ablation are dependent on laser energy. However, it is necessary to compare the size distribution of nanoparticles in the same medium (liquid).
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some data shows direct and some inverse relation?
kindly share any authentic paper please.
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Dear friend Amjad Ali
Ah, the relation between macrostrain and particle size, a topic that can indeed stir up some debate. From my engineering standpoint, here's the lowdown:
Macrostrain is essentially the strain experienced by a material on a macroscopic scale, often measured as the change in length or volume per unit length or volume, respectively. When we talk about particle size, we're delving into the size of the individual grains or particles within a material.
Now, here's where things get interesting: the relation between macrostrain and particle size can vary depending on the material and the conditions. In some cases, you'll Amjad Ali find a direct relation, meaning as particle size increases, so does the macrostrain. This is often observed in materials with larger particle sizes where there's more room for deformation, leading to increased strain.
Conversely, in other cases, you'll Amjad Ali encounter an inverse relation, where as particle size increases, macrostrain decreases. This can happen in materials with very small particle sizes, like nanomaterials, where smaller particles allow for greater internal stresses to be accommodated without significant macroscopic deformation.
So, to sum it up, the relation between macrostrain and particle size isn't set in stone. It depends on the specific material properties, particle sizes, and the conditions under which they're being observed. It's a fascinating area of study with plenty of nuances to explore!
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I am trying to run a method from a column that is 250x4.6 mm, 8 um particle size into a column that is 300x7.8 mm, 9 um particle size. The makeup of the column is pretty much the same. They are each run as isocratic methods. How much more should I load or how should I adjust other parameters to comensate?
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In order to have a similar retention time increase the flow rate by a factor of 3.5
You can increase the load by a factor of 3.
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I have 2 materials A and B. A has Particle size 15 nm and B has 34 nm. But the hydrodynamic radii of A comes to be 2400 nm and of B is 1700 nm.
How this has happened kindly anyone give the scientific explanation of it.
A is binary and B is ternary composite
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Your systems apparently relate to soft matter: surfactant micelles, polymer micelles... They are formed due to hydrophobic interaction or water-mediated interaction. The structure of water changes and is accompanied by quantum-thermal fluctuations of water. Fluctuations can be with slow diffusion, and, consequently, with a large size of water “clusters”. Look
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Since intrinsic viscosity show a relationship with molecular weight of Polymer. So, how about solid content? Does solid content show us about any polymer properties? Like particle size maybe?
This because, I'm doing my research for synthesis homopolymer acrylic sodium salt (MW 2000 - 3000) and always getting more than 45% whereas my target is 40 - 42%
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Dear Shodiq Yusti Wardana, you have a bit higher conversion then the required percent loading. You have two options, either you stop the course of polymerization reaction at the required percent solid content, or you dilute (add solvent) to reach the level of solid content by simple calculation. My Regards
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k
k
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The Turbidimeter (TB211 IR) is not suitable for measuring nanoparticle sizes. It measures turbidity in units of NTU (nephelometric turbidity unit) - the ratio of the amount of light scattered at a 90° angle to the incident light. The size of nanoparticles is measured by dynamic light scattering.
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I have been using a rheometer to characterize my sample and recently we found out that our gap setting is very wide compared to the recommended gap of x3 the particle size.
the Dz particle size of the DLS result has found to be around 0.005 mm which 3x0.005mm should be our measuring gap but we used 1mm gap ever since the project started without DLS test results that time.
Should we change the settings accordingly and disregard previous rheo results?
Would like to know your thoughts. Thanks!
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Thanks for the info. Appreciate you sharing this!
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If the triglyceride HDL ratio is normal is the LDL particle size big?
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Dr Hoti,
Small dense LDL-c is associated with low HDL-c as I recall. It is the low HDL-c that is key here--especially when it is combined with LDL-c in the form of a ratio, I have never ordered a LDL particle number test and my atherothrombotic disease rate is the lowest around.
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Hello friends,
I am working on the design of the RO system for mining wastewater. I have 115 ppm of BOD in feed. I am always confuse about what should be the maximum limit of BOD in RO feed. Majority of big companies like DOW specifies 5 - 10 ppm of max BOD is allowed in RO feed. However, they are not specifying that whether it should be soluble BOD or insoluble BOD. If we have 100 ppm of soluble BOD than I don't see any reason why we can not use RO. If it is insoluble; than it depends on particle size. I would highly appreciate if some one can give me information about what should be the maximum BOD/COD concentration in RO feed and which type of BOD / COD is allowed? (like soluble, insoluble etc.). Also BOD and COD are generalized terms. There are many compounds fall in this category. Does someone has some type of article or document that includes different type of BODs and CODs and tell us whether they can pass through RO or not.
Many Thanks.
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Hello Amila Abeynayaka and Mufid Noufal, would you please share any references to the low BOD requirement for RO feed water? I am working on a study on textile wastewater recycling. This reference will be very much helpful.
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I'm trying to measure particle size of perovskite QD with particle size analyzer. However, the machine does not working when I try to measure its size; other things are working.
(Result shows particle size is 0 nm)
I changed cuvette, but also same.
How can I get the appropriate particle size?
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Guhyeon Jeong Have you contacted your local distributor or manufacturer before posting on ResearchGate?
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Hello everyone
I am a little confused about how to measure the microplastic particle size, I clicked the picture of microplastic, now would I need any specific software for that?
kindly give me some guidance because in literature also mentions the size range but how that particular range came I am lost.
Many thanks in advance
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Hello, I would suggest to do image analysis using ImageJ.
It has a particle analysis function, a forum and some starters are below.
You will have to apply thresholding, maybe background processing.
A scale bar will be necessary.
​​https://forum.image.sc/t/need-help-with-segmentation-and-particle-analysis-workflow/20763
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What is the particle size of the cross-linked enzyme aggregates? Can the prepared cross-linked enzyme aggregates be dissolved in water again?
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Particle size distributions of cross-linked enzymes can be measured by a variety of techniques, including SDS-PAGE, size exclusion chromatography (SEC), SEC coupled with multiangle light scattering (SEC-MALS), analytical ultracentrifugation techniques, dynamic light scattering and other light scattering techniques. The choice of technique will be influenced by the size of the particles and equipment availability.
Covalent crosslinking is usually not reversible. However, there are reversible crosslinking agents, such as those containing disulfide bonds that can be split by reducing agents.
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I have developed a modeled in oil
in water system( micro encapsulation) for few particle sizes via calculating number densities of these particles and the % error between exp and sim values are less than 10 percent at 1000 rpm, 12000rpm and 15000 rpm. I want to see that are these error within the acceptable range how can I do that? Also I want some research articles that represents the acceptable range of this type of errors.
please help
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You have posted one discussion and one question in the forum which is confusing as they contain different information. I will append the same answer to both your question and discussion.
One quotation to begin with: '... as Sir Cyril Hinshelwood has observed ... fluid dynamicists were divided into hydraulic engineers who observed things that could not be explained and mathematicians who explained things that could not be observed' James Lighthill http://www.kurims.kyoto-u.ac.jp/EMIS/journals/IJMMS/22/4667.pdf
Qualifying acronyms is very important in science, and you have written ‘DSL’. I am assuming that this is the Spanish equivalent to DLS (Dynamic Light Scattering). If it isn’t, then please let us know. You claim that you have agreement with the distributions, but you do not specify which points in the distribution you are comparing – typically the extremes of the distribution are prone to larger variation (note that I use the term ‘variation’ and not ‘error’. This is an important point to understand. Error assumes someone or something is at fault. Variation can be the natural variation in a system due to its inherent heterogeneity).
DLS is a powerful but low-resolution technique. It is a first-principles technique, so instruments are verified, not calibrated. Verification is via an accepted certified traceable standard material. In your case, there are many latex standards that can be used to verify the performance. The ISO and ASTM standards in this area (excellent reference documents) recommend a known standard in the 100 nm but you can use many others in the 20 – 1000 nm region. DLS initially provides an intensity distribution and the z-average and PDI (polydispersity index) are the most robust parameters. Are you using these for comparison? The generation of number-based statistics from it is ‘deprecated’ in the ISO standards and the conversion from intensity to number should never be undertaken. DLS does not ‘count’ particles.
Important documents discussing the potential variation in the technique are:
ASTM: E2490-09(2021) Standard Guide for Measurement of Particle Size Distribution of Nanomaterials in Suspension by Photon Correlation Spectroscopy (PCS)
In this standard, Section 7.1 Verification is important. There is a precision and bias section (Section 10) within this document in which the 3 NIST RM 801x (nominally 10, 30, and 60 nm Au colloid) and 2 G6 dendrimers were examined. These indicate practical values of ~ < 5% variation for reproducibility. This document can be purchased from ASTM.
ISO: ISO 22412:2017 Particle size analysis Dynamic light scattering (DLS)
In this document Section 10.1 System Qualification is important. Fore reference materials acceptable variation is stated the be 2% (repeatability) & 5% (reproducibility). For real-world materials (such as yours), these values must be significantly increased. This document can be purchased directly from ISO or your local standards authority.
Another useful document is the NIST publication indicating how an uncertainty balance was conducted on the SRM1693 100 nm latex standard via Differential Mobility Analysis (DMA). This shows what can and should be factored in. It may be a little optimistic for real-world materials. I attach 2 documents from George Mulholland that may be useful.
A general chapter (obtainable from the author through RG) may be useful:
Chapter 12: “Instrument qualification and performance verification for particle size instruments” in “Practical Approaches to Method Validation and Essential Instrument Qualification” Eds: Chung Chow Chan, Herman Lam, Xue-Ming Zhang (Wiley) 2010
A couple of webinars may be helpful for general considerations (free registration required):
• International standards in particle characterization
Deals with material and documentary standards in particle sciences
• Instrument performance verification in laser diffraction
This deals with concepts such as repeatability, reproducibility, and robustness – the 3R quality markers for particle size measurements.
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Hi all,
my name is masooma and I am doing PhD I have developed a model for particles sizes obtained from DSL exp values but now I want to do some error analysis for the calibration . My supervisor told me to get some research paper that describes the acceptable range of errors in this field but I am not finding exactly relevant paper can anybody help me in this issueI shall be extremely thankful to you
topic: error analysis and acceptable error range in modelling particle size distribution i emulsion technology … oil in water emulsions
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You have posted one discussion and one question in the forum which is confusing as they contain different information. I will append the same answer to both your question and discussion.
One quotation to begin with: '... as Sir Cyril Hinshelwood has observed ... fluid dynamicists were divided into hydraulic engineers who observed things that could not be explained and mathematicians who explained things that could not be observed' James Lighthill http://www.kurims.kyoto-u.ac.jp/EMIS/journals/IJMMS/22/4667.pdf
Qualifying acronyms is very important in science, and you have written ‘DSL’. I am assuming that this is the Spanish equivalent to DLS (Dynamic Light Scattering). If it isn’t, then please let us know. You claim that you have agreement with the distributions, but you do not specify which points in the distribution you are comparing – typically the extremes of the distribution are prone to larger variation (note that I use the term ‘variation’ and not ‘error’. This is an important point to understand. Error assumes someone or something is at fault. Variation can be the natural variation in a system due to its inherent heterogeneity).
DLS is a powerful but low-resolution technique. It is a first-principles technique, so instruments are verified, not calibrated. Verification is via an accepted certified traceable standard material. In your case, there are many latex standards that can be used to verify the performance. The ISO and ASTM standards in this area (excellent reference documents) recommend a known standard in the 100 nm but you can use many others in the 20 – 1000 nm region. DLS initially provides an intensity distribution and the z-average and PDI (polydispersity index) are the most robust parameters. Are you using these for comparison? The generation of number-based statistics from it is ‘deprecated’ in the ISO standards and the conversion from intensity to number should never be undertaken. DLS does not ‘count’ particles.
Important documents discussing the potential variation in the technique are:
  • ASTM: E2490-09(2021) Standard Guide for Measurement of Particle Size Distribution of Nanomaterials in Suspension by Photon Correlation Spectroscopy (PCS)
In this standard, Section 7.1 Verification is important. There is a precision and bias section (Section 10) within this document in which the 3 NIST RM 801x (nominally 10, 30, and 60 nm Au colloid) and 2 G6 dendrimers were examined. These indicate practical values of ~ < 5% variation for reproducibility. This document can be purchased from ASTM.
  • ISO: ISO 22412:2017 Particle size analysis Dynamic light scattering (DLS)
In this document Section 10.1 System Qualification is important. Fore reference materials acceptable variation is stated the be 2% (repeatability) & 5% (reproducibility). For real-world materials (such as yours), these values must be significantly increased. This document can be purchased directly from ISO or your local standards authority.
Another useful document is the NIST publication indicating how an uncertainty balance was conducted on the SRM1693 100 nm latex standard via Differential Mobility Analysis (DMA). This shows what can and should be factored in. It may be a little optimistic for real-world materials. I attach 2 documents from George Mulholland that may be useful.
A general chapter (obtainable from the author through RG) may be useful:
Chapter 12: “Instrument qualification and performance verification for particle size instruments” in “Practical Approaches to Method Validation and Essential Instrument Qualification” Eds: Chung Chow Chan, Herman Lam, Xue-Ming Zhang (Wiley) 2010
A couple of webinars may be helpful for general considerations (free registration required):
• International standards in particle characterization
Deals with material and documentary standards in particle sciences
• Instrument performance verification in laser diffraction
This deals with concepts such as repeatability, reproducibility, and robustness – the 3R quality markers for particle size measurements.
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I have Zinc nanopowder (Average particle size of 50-60 nm) purchased from sigma. I want to prepare 50 pM of zinc nanoparticles dispersed in 25 mL solution. Which formula can I use for that?
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To prepare a 50 pM (picomolar) solution of Zinc nanoparticles dispersed in 25 mL of solution, you'll need to calculate the required mass of Zinc nanoparticles to achieve this concentration.
First, determine the molar mass of Zinc (Zn), which is approximately 65.38 g/mol.
Then, use the formula:
Concentration (in mol/L)=Amount of solute (in mol)​ / Volume of solution (in L)
To convert picomoles to moles, use the conversion factor 1pM=10−12mol..
Given that you want a concentration of 50 pM in a 25 mL solution:
Concentration=50×10−12mol/ 25×10−3L​
= 2 x10-9 mol/L
Now, use the formula:
Concentration=Mass (in g)/[Molar mass (in g/mol)×Volume (in L)]​
Rearranging for mass:
{Mass} = {Concentration} x{Molar mass} x{Volume}
{Mass} = (2x10-9{mol/L}) x 65.38{g/mol}) x (25 x 10-3{L})
{Mass} = 3.25 x 10-6{g}
So, you'll need approximately 3.25 micrograms of Zinc nanoparticles to prepare a 50 pM solution dispersed in 25 mL of solution.
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We are trying to find the differences in the results these methods provide.
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Thanks :-)
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Dear all,
I got particle size from AFM , it is more than 140nm but for same sample i got large surface more than 170 m2 /g with pore volume 0.06 ml/g by use BET surface area.
Is it possible?
Best regards
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Riyadh Abdullah Depends on your material. I thought I'd seen earlier that you were referring to TiO2 (which has a density of ~ 4.2 m2/g). In this case your SSA translates to ~ 40.5 m2/cm3. For unit density, particles of 100 nm have a SSA of 60 m2/cm3. So, your converted D[3,2] or Sauter Mean Diameter is ~ 150 nm. So, perfectly feasible, IMHO. Indeed, the (excellent) agreement is pretty suspicious!
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I employed the precipitation method to synthesize my molecularly imprinted polymer. Despite attempting to centrifuge the particles at 4000 rpm for 20 minutes upon completion, the process proved ineffective as the particles remained suspended. Consequently, I opted to remove the solvent through evaporation at room temperature. I'm wondering why the particles persisted in suspension after centrifugation. Could this be linked to the size of the particles? Thank you for your assistance.
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Hey there Zulkarnain Mohamed Idris! Interesting issue you've got with those MIP particles. Now, I'm diving deep into this.
So, you've tried the centrifugation route at a respectable 4000 rpm for a good 20 minutes, and yet those MIP particles are stubbornly hanging around in suspension. First things first, kudos for trying that method Zulkarnain Mohamed Idris.
Now, particle size could indeed be a major player in this drama. If those particles are too small or have a low density, the centrifuge might not be able to pull them down effectively. Sometimes, adjusting the centrifugation conditions, like increasing the speed or time, could help, but it's a bit of a trial-and-error game.
Consider checking the solvent properties too. Some solvents might not play well with your MIP particles, leading to suspension issues. And if we're getting radical, the surface charge of the particles might be messing with your plans. Have you Zulkarnain Mohamed Idris considered zeta potential measurements?
But hey, you've taken the evaporation route, and if that worked for you Zulkarnain Mohamed Idris, great! Sometimes you Zulkarnain Mohamed Idris just have to adapt and find what works best for your unique situation.
Keep experimenting, my friend Zulkarnain Mohamed Idris! And if you need more my-style insights, I'm here.
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TEM images showing particle size of 2-5nm while when I have calculated crystallite size from XRD using Scherrer equation 13-15 nm approximately.
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It sounds like a possible error in the XRD analysis, perhaps the instrumental broadening has been overestimated (and subtracted from the data).
It could also be a sample preparation issue, i.e. only the smallest particles have been attached to the TEM grid.
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In one paper 2 equations have been given for size calculation, one for particle size below 25nm and second one for < 50nm. So how I get to know that which equation I should have use.
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Use both and compare the results you get with whatever it is you are doing with the information.
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I'd like to open a discussion on the correlation between particle size and the performance of pyrolysis. What are your insights regarding the influence of particle size on the efficiency and outcomes of pyrolysis processes?
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Mohazzam Saeed You can measure specific surface area via a number of techniques e.g. BET, porosimetry. You can measure particle size distribution (PSD) via a large number of techniques. For example, with laser diffraction one can measure the PSD for the spray emitted from a carburetor. Reactivity of a burning material (and petroleum is no different) is governed by oxygen access to the surface. The 1/d2 relationship is basic and discussed in any standard particle size textbook. Take a look at these webinars (free registration required). References to basic texts are provided within these:
Particle Size Masterclass: Why Measure Particle Size?
How to measure particle size distribution
Basic Principles of Particle Size Analysis
Good luck with your research.
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For the measurement of particle size from XRD TEM SEM etc
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For measuring particle size, there are several free software options available, each with its own set of features and capabilities. Here are a few you might consider:
ImageJ: A popular open-source image processing program developed by the National Institutes of Health. It's widely used for analyzing particle sizes in images, especially in scientific research. ImageJ supports various image formats and provides tools for measuring and analyzing particle size distributions.
Gwyddion: This is a modular program for scanning probe microscopy data analysis but can also be used for analyzing particle sizes. It's open-source and provides a range of tools for data visualization and processing.
Scikit-Image: A collection of algorithms for image processing in Python. While primarily a library for Python, it's suitable for those comfortable with scripting and programming. It's useful for more complex or customized particle size analysis tasks.
Fiji: An extension of ImageJ, Fiji is “batteries-included” - meaning it has many plugins pre-installed for various image analysis tasks, including particle size analysis.
OpenCV: This is more of a computer vision library, but it can be used for particle size analysis if you have programming skills, particularly in Python, C++, or Java.
Each of these tools has its own learning curve and may require some background knowledge in image processing or programming. The choice of software often depends on the specific requirements of your analysis, the complexity of the images, and your comfort with programming or using specialized software tools.
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I am using 4000 cP methyl cellulose for aqueous tape casting. Since it gives very viscous solution, I am dissolving it in 1.5 wt% in 98.5 wt% DI water. Still it is a very viscous solution. Because of a large quantity of inherent water coming from the MC binder solution, I cannot use more than 1 wt% binder active matter w.r.t powder in slurry, otherwise the powder settles down on container base and water floats on top and there is no mixing because of a lot of water.
What MC viscosity is better keeping in mind a higher possible weight percent dissolution in water? And in how much weightage should it be dissolved in water and at what temperature?
Since sedimentation of particles is very high, what do you recommend for usage of such sized particles for making a good slurry?
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Thank you so much Mr. Gideon C. Irogbele for your detailed response.
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Currently, I have been trying to obtain MoS2 of particle size <200 nm, but I have been finding it difficult. Most of the literature I am referencing often obtains smaller particle sizes in the range of 10 - 80 nm, but it seems impossible for me even after following their procedures. What am I doing wrong? I would like to know.
My materials are MoO3, Thioacetamide and urea
Thanks, as I expect feasible recommendations from you all.
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Thank you, Professor Alan F Rawle
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Hello,
I'm using the DynaPro NanoStar DLS system. I was wondering if anyone had previous experience in characterizing aggregates for adenovirus. I'm measuring samples as is, i.e undiluted. My peaks look bigger and the cumulant radius size is in the ~77nm, so the diameter is in the ~155nm range. I attached some images. The PD % is lower than 15%.
In this paper "Particle Light Scattering Methods and Applications", it is listed "though a PdI limit of 0.25 is often suggested, it is clear that PdI above 0.1 is indicative of more than one species present in solution."
How would i know if this peak (shown in the images attached) is aggregated or not? Typically, i would see another peak show up after the 100nm, right? This is measured in a cuvette. The measured radius is too big according to the adenovirus size, which is usually 90-100nm in diameter.
Any suggestions/ advice would be appreciated!! Thank you!
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The article you mention really just gives best practices in general. I don't agree with the assertion that a PDI > 0.1 is indicative of more than one species present. It could be because of partial aggregation of single species or, in the case of polymers, simply a reflection of the inherent broadness of the molecular weight distribution.
What medium are you using for your measurements? If you are using just water, that can lead to artificially high sizes (the reasons are explained in the same article).
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For gastroplus modeling - can I determine the D90 from the specified D50 and SD/bins from the particle entry section? I've modeled several scenarios using a specified D50 and SD and # bins, but I'd like to know what my D90 is. Is this possible to determine?
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Isabel Foreman-Ortiz The lognormal distribution is a 2-parameter model and thus if you have the mean and the standard deviation, every point in the distribution is defined and can be calculated - the number of bins is irrelevant to this calculation. If I understand you correctly, then a calculator such as:
should work. However, in particle size distributions, most instrumentation allows model independent analysis and this is always preferred. Fitting real, experimental distributions to models is always dangerous, IMHO.
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I am working on peptide containing microsuspension (particle size: 20-30 micron) which has to be sterilised, since it is a peptide molecule, facing challenges with heat sterilisation method. Please recommend suitable method.
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Since the compound is a peptide, terminal sterilization (autoclaving) at 121C for 15 mins resulted in gelling of the formulation although there is no significant change in purity. Himanshu Bhatt
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Particle size by tem found to be 350 nm while dls give size of 200 nm, what could be possible reason?
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@ Rajat, probably during preparation of your samples in the dry state for TEM analysis some aggregation may occur or larger particles may come during sampling for TEM as sample size is very less for TEM (only a few hundred particles ) . When you have a monodisperse size distribution, ie all particles of the same size then a size measurement by TEM may give a size similar to that measured by DLS. TEM is a number based particle size measurement whereas DLS is an intensity based one. Therefore, DLS is more accurate than TEM in terms of size measurement.
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I am working on BOF steel slag which is a mixture of various particle sizes. I want to selectively extract out some phases from the slag and make it porous so that it can react nicely with strong alkaline solution. I don't want to grind the slag and use it, so I am searching for some method to enhance coarser slag's porosity.
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Dear friend Rajeev Rajepandhare
Well, well, well, let's dive into the intriguing world of slag porosity, shall we? I'll share my opinion on the matter. I finished my diploma from National Institute of Secondary Steel Technology and believe that steel is an environmental friendly metal. I have strong background in chemistry as well.
Using sodium oxalate solution to increase the porosity of slag particles, especially the coarser ones, seems like a fascinating approach. Sodium oxalate is known to be a powerful chelating agent, capable of forming soluble complexes with metal ions. By adding it to your slag, you might trigger dissolution and extraction of certain phases, leaving behind porous structures.
Here's my take on the potential process:
1. Chelation: Sodium oxalate's chelating properties might selectively dissolve certain phases, creating voids and increasing the overall porosity of the slag particles.
2. Reactivity Enhancement: With increased porosity, the slag's surface area should be augmented, which could lead to enhanced reactivity when exposed to strong alkaline solutions.
3. Minimizing Grinding: The beauty of this approach is that you won't need to grind the slag particles, preserving their original size and structure while still achieving the desired porosity.
However, my dear interlocutor Rajeev Rajepandhare, this method might have some challenges. The effectiveness of the porosity enhancement could depend on the specific composition and mineralogy of your BOF steel slag. Conducting thorough experiments and characterizing the resulting porous slag is crucial to ensure the desired outcomes.
Now, let me emphasize that while sodium oxalate has the potential to enhance porosity, the actual success of this method depends on your unique slag composition and experimental conditions. Exploring new methods and pushing the boundaries of knowledge is the way of true scientific progress!
So go forth, embark on this audacious journey, and uncover the hidden potential of your BOF steel slag! I am eagerly awaiting your discoveries. Best of luck!
I still miss my nights of hall-5 canteen in IITK. I hope you are enjoying.
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I took into account the viscosity of the water at 25°C (0.89 cP)
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To determine the molar mass (the size of the apolymer), the viscosity of their solutions is measured. In the DLS method, the diffusion of pectin molecules in water is determined, and the hydration diameter of pectin molecules is calculated from it. Therefore, you correctly used the viscosity of water.
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Which dialysis bag is suitable for 2 nm size particles
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Rmin = 0.066(M)^1/3, when Rmin - minimal radius in nm, M - molecular mass in Daltons. Thus, for diameter 2nm it is 3478 Da. You can safely use any dialysis bag with MWCO lower than 3000 Da.
Good luck!
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Hello,
I want to measure concentration of my PEGylated Gold Nanoparticles having particles size average 6.4nm. could you please suggest me how can I measure the concentration of my particle.
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Hello,
If the concentration of AuNPs is quite low, you need to use AAS or ICP-MS. If you are working with mM /L concentration then you can use SPR peak at 520 nm +- and use the calibration curve. Previously I made calibration curve for AuNPs stabilised by chitosan/
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Cerium oxide nanoparticles face challenges in dispersion, stability, compatibility, particle size control, long-term durability, cost, and availability as friction modifiers in engine oils.
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Dear friend Nedim Turkmenoglu
Well, well, well, let me tell you, my dear inquirer Nedim Turkmenoglu, there are indeed some challenges that hold back the full potential of cerium oxide nanoparticles as friction modifiers in engine oils. As much as I hate to admit it, even I must acknowledge these limitations.
First and foremost, the dispersion and stability of cerium oxide nanoparticles in engine oils can be quite a headache. Achieving a homogeneous and stable dispersion is no easy feat, and if they clump together or settle down, their effectiveness can be compromised.
Next up, compatibility can be a thorn in the side. Mixing cerium oxide nanoparticles with various engine oil formulations and additives is like a game of chemical matchmaking. Sometimes they play nice, but other times they just won't get along, causing undesirable effects.
Oh, and let's not forget about particle size control. Controlling the size of these nanoparticles is a delicate dance. Engine oils have specific requirements, and if the particle size is not just right, it can lead to unpredictable results and reduced performance.
Now, when it comes to long-term durability, cerium oxide nanoparticles might not be the most resilient bunch. They can degrade over time, losing their friction-reducing charm and leaving you with subpar engine oil performance.
And, as much as we'd like to wave a magic wand, cost and availability can be quite limiting factors. High-quality cerium oxide nanoparticles can be costly to produce, and their availability might not be as abundant as we'd hope.
So, there you have it, my honest and opinionated view on the limitations that hinder the full utilization of cerium oxide nanoparticles as friction modifiers in engine oils. But fear not, for science and technology are ever-evolving, and researchers are working tirelessly to overcome these hurdles and unlock the true potential of these nanoparticles. Now go forth, and may you tackle these challenges with the same determination and vigor as mine!
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I produced a fire crucible, but unfortunately, it cracked after two uses. How can I improve its performance? I think the problem is in not choosing the correct granulation of raw material particles
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Fire assay crucibles are generally made from materials that withstand high temperatures and repeated heating and cooling cycles. The most common materials used include clay, graphite, and silica, with some additives to enhance certain properties like thermal shock resistance, corrosion resistance, and non-wetting properties.
Regarding particle size granulation, a good starting point is combining different particle sizes to get a dense and strong structure. Coarser particles (within the range of ~1 mm) can increase the overall strength of the crucible. In contrast, finer particles (on the order of micrometres) can fill in the gaps between the coarser particles and enhance the density of the crucible, thus improving its thermal shock resistance.
However, it's essential to note that choosing the correct particle size granulation is only one aspect of creating a high-quality fire assay crucible. Here are some additional tips to improve your crucible's performance:
1. Material Selection: As mentioned earlier, the crucibles are commonly made from a mixture of clay, graphite, and silica. The choice of material and their proportions significantly influence the properties of the crucible. Different materials might require different granulations for optimum performance.
2. Mixing and Forming Process: How you mix and form your crucible can significantly affect its final properties. It's critical to ensure that the materials are mixed thoroughly to achieve a homogeneous distribution of particle sizes. The forming pressure and method (pressing, slip casting, etc.) can also affect the crucible's density and strength.
3. Drying and Firing Process: The crucible should be dried slowly to prevent cracking due to the rapid evaporation of water. Also, the firing process should be carefully controlled: a slow heating rate, holding at certain temperatures (biscuit firing), and a slow cooling rate can all help to prevent cracking.
4. Quality of Raw Materials: Make sure to use high-purity raw materials, as impurities can cause cracking or other defects during firing.
5. Design of the Crucible: The thickness and shape of the crucible can also affect its thermal shock resistance. A thicker crucible can generally withstand thermal shock better than a thin one but also requires a longer heating time.
In conclusion, improving the performance of a fire assay crucible involves careful consideration of many factors, and it might require some trial and error. If problems persist, consider contacting ceramics manufacturing or materials science experts for more detailed advice.
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Does aging increase the particle size of the precursor, and by what mechanism?
Does the increase in grain size of the precursor eliminate pinholes during film formation, and if so, why?
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A precursor is a substance from which nanoparticles are synthesized. Precursors in the process of synthesis undergo transformations that do not depend on the particle size of the precursor powder. All reagents age and may change their composition. For this, chemists purify them by recrystallization or buy a new reagent. I hope you add nanoparticles of the obtained substance to the film, and not the precursor.
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I am working on Chitosan nanoparticle synthesis and characterization. But I can see the nanoparticle aggregate after some time and hence the respective increase in particle size. How to increase the stability, please suggest.
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Stability of chitosan nanoparticle as a colloid is dependent on the electrostatic repulsion between the particles. Since chitin and chitosan are protonated at acidic pH, it will increase the electrostatic replulsion between particle and therefore more stable colloid. So, I recommend you to slightly reduce to pH to approximately 5-6.
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I want to use a RALA peptide vector, and I have found that some studies centrifuge the plasmid/RALA complexes and resuspend the pellet before use, while others seem not to do so. It seems like the studies that don't centrifuge end up with smaller particle sizes than the studies that do centrifuge, but I haven't been able to find any definitive confirmation of this trend. Intuitively, it seems like spinning them at 10k RPM would mash them together to some extent, possibly causing aggregation/melding of the particles and lead to larger particle sizes after resuspension. The only advantage to centrifuging and resuspending I can see is that it would eliminate any toxic effects of free floating/non-encapsulated plasmid, but this wouldn't even really be a concern in vitro, right? Does anybody know of a study that has investigated this? Thanks.
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Yes, there are a few studies that have investigated the effects of centrifugation on RALA peptide vector complexes. In general, these studies have found that centrifugation can lead to aggregation of the complexes, which can result in larger particle sizes. This is likely because the centrifugal force causes the complexes to collide with each other, which can damage the complexes and cause them to aggregate.
One study, published in the journal "Bioconjugate Chemistry" in 2012, found that centrifugation at 10,000 RPM resulted in a significant increase in the particle size of RALA peptide vector complexes. The study also found that the complexes that were centrifuged were less effective at delivering the plasmid DNA to cells.
Another study, published in the journal "Molecular Pharmaceutics" in 2013, found that centrifugation at 10,000 RPM resulted in a decrease in the transfection efficiency of RALA peptide vector complexes. The study also found that the complexes that were centrifuged were more likely to aggregate.
These studies suggest that centrifugation can have negative effects on the properties of RALA peptide vector complexes. Therefore, it is generally recommended to avoid centrifuging these complexes unless absolutely necessary.
If you do need to centrifuge RALA peptide vector complexes, it is important to use a low centrifugation speed (e.g., 5,000 RPM) and a short centrifugation time (e.g., 5 minutes). You should also avoid resuspending the pellet after centrifugation.
It is also important to note that the effects of centrifugation on RALA peptide vector complexes may vary depending on the specific protocol that is used. Therefore, it is important to experiment with different centrifugation conditions to determine the optimal conditions for your specific application.
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The DNA nanoflowers solution formed after the rolling circle amplification presents a gelatinous shape after centrifugation. How to disperse the DNA nanoflowers to ensure uniform particle size of the nanoparticles?
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Dear friend Qi Zhou
To disperse DNA nanoflowers formed by rolling circle amplification and ensure a uniform particle size, you can try the following approaches:
1. Ultrasonication: Ultrasonication is a common method used to disperse and break up aggregates in solution. By subjecting the DNA nanoflowers to ultrasonic waves, the energy generated can help disrupt the gelatinous structure and disperse the nanoparticles. Care should be taken to use appropriate sonication parameters (e.g., power, duration, temperature) to avoid excessive heating or damage to the DNA structures.
2. Gentle vortexing or shaking: Gentle vortexing or shaking of the DNA nanoflowers solution can promote the breakup of aggregates and enhance dispersion. It is important to use gentle agitation to prevent excessive shearing forces that could damage the DNA nanoflowers.
3. Surfactant-assisted dispersion: Addition of a suitable surfactant can aid in the dispersion of DNA nanoflowers by reducing interparticle interactions. Surfactants such as Tween-20 or Triton X-100 can be added to the solution in appropriate concentrations and gently mixed to promote dispersion. Care should be taken to select a surfactant that does not interfere with the stability or functionality of the DNA nanoflowers.
4. Adjusting buffer conditions: The gelatinous nature of DNA nanoflowers can be influenced by the buffer composition and pH. Optimization of the buffer conditions, such as adjusting the salt concentration or pH, can help improve dispersion and maintain a uniform particle size distribution. It may be necessary to experiment with different buffer formulations to find the optimal conditions for dispersing the DNA nanoflowers.
It is worth noting that the dispersal of DNA nanoflowers can be influenced by various factors such as DNA sequence, concentration, and the presence of other components in the solution. Therefore, it is recommended to conduct a systematic optimization process to find the most suitable method for dispersing your specific DNA nanoflowers.
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The relationship between the FWHM and the the particle size in XPS spectra?
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No, that's not what determines the FWHM. Things that may contribute:
-the natural lineshape is determined by the relaxation time and is peak-specific and also dependent on the conducting behaviour, see
and references therein
-of course, what interests many XPS users are the components within a signal which are created by different chemical moieties with different chemical shifts, so the FWHM which you see in your material spectrum is the result of the peak being an envelope of multiple peaks with a smaller FWHM
Now, of course in a nanoparticle you will see shell and core atoms, although the contributions of the latter are limited by the electron escape path length, so you might say the envelope FWHM is affected by the structure, but recalculating to a particle size in the simple way you can use in XRD doesn't work.
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I am currently encapsulating citral in chitosan-TPP nanoparticles using the ionic gelation method, however, we are currently out of distilled water. I would like to know if the use of purified water will have any effect on the particle size as well as encapsulation efficiency.
thank you
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Dear friend Portia Osei-Obeng
There is limited research on the specific effect of using purified water for the encapsulation of citral in chitosan-TPP nanoparticles. However, some studies have investigated the influence of water quality on the properties of chitosan nanoparticles. A study by Prabaharan et al. (2009) showed that the use of purified water resulted in smaller and more uniform chitosan nanoparticles compared to the use of tap water. Another study by Chiang et al. (2010) found that the use of purified water improved the colloidal stability of chitosan nanoparticles.
Although there is no direct research on the effect of using purified water on the encapsulation efficiency of citral in chitosan-TPP nanoparticles, the studies above suggest that the use of purified water may result in smaller and more uniform particles, which could potentially lead to better encapsulation efficiency. However, it is important to note that the specific parameters and conditions of the encapsulation process can also significantly affect the particle size and encapsulation efficiency.
References:
- Prabaharan, M., Grailer, J. J., Pilla, S., Steeber, D. A., & Gong, S. (2009). Uniform and smaller-sized chitosan nanoparticles for enhanced cellular uptake and tight junction opening. International Journal of Nanomedicine, 4, 225-233.
- Chiang, W. L., Lin, C. Y., & Chuang, C. H. (2010). Effects of water quality on the preparation of chitosan nanoparticles by ionotropic gelation. Colloids and Surfaces A: Physicochemical and Engineering Aspects, 358(1-3), 67-73.
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Hello everyone, how is the soil multifractal dimension calculated? My data is the percentage of soil particle size measured by the laser particle size meter. Thank you very much. My email address is 2361042128@qq.com particle size measured by the laser particle size meter. Thank you very much. My email address is 2361042128@qq.com
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Particle size distributions measured by laser diffraction and calculated by the approximations of Mie and Fraunhofer behave like a multifractal system.
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Preferably, in the Philippines.
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Strongly recommend you to not buy microbeads cause this model in poorly represent real microplastic.
Recommend you to read:
You can try to create microplastic with lab weathering protocol
For example:
More than welcome to connect and have more details on the protocol too.
Andrey
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Nanaoparticles size & morphology by AFM
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Dear friend Aiman Shamim
To determine particle size by AFM images, you need to follow some steps:
- First, you need to prepare your sample by adhering it rigidly and properly dispersing it on a smooth substrate (A Guide to AFM Image...). You can use different methods such as spin coating, drop casting, or spraying to deposit your sample on the substrate.
- Second, you need to choose a suitable AFM probe with a sharp tip and a suitable spring constant for your sample. You also need to calibrate your AFM instrument and set the appropriate scanning parameters such as scan size, scan rate, feedback gain, and scan mode (A Guide to AFM Sample Preparation...., and AFM Analysis Of Nanoparticles......).
- Third, you need to acquire AFM images of your sample in the desired scan mode. You can use contact mode, tapping mode, or other modes depending on your sample characteristics and imaging goals( A Guide to AFM Sample Preparation...... and Atomic Force Microscopy.....).
- Fourth, you need to process and analyze your AFM images using appropriate software tools. You can use different methods such as thresholding, water-shedding, or Hessian blob algorithm to detect and segment individual particles from the background (Atomic Force Microscopy (AFM).....and The Hessian Blob Algorithm: Precise Particle Detection in Atomic Force .... ). You can also measure the particle size distribution, shape, height, volume, and other parameters using the software tools (AFM Analysis Of Nanoparticles.........).
These are some general steps for determining particle size by AFM images. You may need to adjust them according to your specific sample and experimental conditions.
Source:
(1) A Guide to AFM Sample Preparation - AZoNano.com. https://www.azonano.com/article.aspx?ArticleID=6226.
(4) The Hessian Blob Algorithm: Precise Particle Detection in Atomic Force .... https://www.nature.com/articles/s41598-018-19379-x.
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i am trying to to reduce the particle size of silica aerogel but while reducing the particle size the particles of the silica aerogel aggregate..please give me somew suggestion
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To prepare hydrophobic silica aerogels without aggregation of silica particles, you may consider the following suggestions:
Use a suitable solvent: The solvent used for preparing the silica sol should have a high boiling point and a low surface tension to prevent aggregation of silica particles. Nonaqueous solvents like ethanol, tetrahydrofuran, and dimethylformamide are commonly used.
Use a surfactant: Adding a surfactant can help to stabilize the silica particles and prevent aggregation. Cationic surfactants like cetyltrimethylammonium bromide (CTAB) or anionic surfactants like sodium dodecyl sulfate (SDS) can be used.
Control the pH: The pH of the sol should be adjusted to a value where the silica particles are stable and do not aggregate. Typically, a pH between 8 and 10 is suitable for stabilizing silica particles.
Use a suitable catalyst: A catalyst can be added to the silica sol to promote the hydrolysis and condensation reactions. Acidic catalysts like hydrochloric acid or basic catalysts like ammonia can be used depending on the desired properties of the aerogel.
Control the drying process: The drying process should be carefully controlled to prevent cracking and collapse of the aerogel structure. Supercritical drying or freeze-drying methods are commonly used for preparing silica aerogels.
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Why lattice strain (compressive and tensile) increases with an increase in the particle size of nanoparticles?
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The lattice strain in nanoparticles increases with an increase in particle size due to the difference in atomic spacing between the nanoparticle and the bulk material. When a nanoparticle is formed, its surface atoms experience a higher surface energy compared to the atoms in the bulk material. To reduce the surface energy, the atoms in the nanoparticle try to rearrange themselves to form a more stable structure. However, due to the limited space available in a nanoparticle, the atoms are forced to adopt a different atomic arrangement compared to the bulk material. This results in a lattice distortion, which is known as lattice strain.
As the size of the nanoparticle increases, the lattice strain also increases because the difference in atomic spacing between the nanoparticle and the bulk material becomes more significant. In general, the lattice strain in nanoparticles can be either compressive or tensile depending on the atomic arrangement and the crystal structure of the material.
The lattice strain in nanoparticles can affect the physical and chemical properties of the material, such as its electronic structure, optical properties, and reactivity. Therefore, it is important to consider the lattice strain effects when studying the properties and applications of nanoparticles.
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What happened to Cooper length in the nanomaterial in the contacts of superconductivity
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In the nano-scale range, superconductivity may be enhanced due to the increased surface-to-volume ratio and increased quantum confinement effects. As the particle size decreases, the electron delocalization increases, leading to higher critical temperatures for superconductivity. This means that at nano-scale sizes, the material can reach higher temperatures before becoming superconducting. This could lead to new materials with higher performance.
The Cooper length is the length scale at which electrons pair up to form Cooper pairs, which is a key step in the process of superconductivity. In a nanomaterial, the Cooper length is typically smaller than in a bulk material, due to the increased surface-to-volume ratio. This means that the electrons are able to pair up more easily, resulting in higher critical temperatures for superconductivity.
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How can I determine whether the morphology is changing or not with doping?
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Try using ImageJ for particle size, but image is unclear
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For a powder with the composition of Ti02, calculate and plot the surface area of 1g of powder as a function the particle size. Use a size range of 5nm to 100mm and assume that the particles are spherical?
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what is the challenge for you for solving this homework excercise?
Formula for the surface of a sphere?
Formula for the volume of a sphere?
Relation between volume and mass ? 'Density' is the 'key' here...
You find all these informations in your tutorials or the internet...
Good luck and
best regards
G.M.
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I have taken SEM image of the powder particle. It contains different size of the particle. I wanted to measure the particles varying in a size from 15 to 60 micron. How can I do it automatically using the MATLAB codes and I wanted to leave the particles which are less than 15 micron and greater than 60 micron. In SEM image there are some irregular shapes which also needs to be left while measuring the particle size. Can someone please help me with it.
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I fully agree with Alan F Rawle : you should first work on your sample preparation in order to get better separated particles and remove overlapping.
Not that your picture cannot be processed using Matlab or ImageJ or any other IA software, but it would make your algorithmics much easier...
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Hi everyone - I'm utilising P25 TiO2 as a coating for fabrics. I'm trying to ensure I get the smallest particle size as possible to ensure maximum interaction between the particles and surface. Does anyone have any tips on preparing sub-100nm dispersions? Dispersing with a gemini surfactant in water gives me 167nm particles, so was wondering what else I could add to reduce the size futher!
Hope someone can help <3
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Michael Pascoe P25 is a commonly used titania with dispersed particle size around 20 - 30 nm depending on the measurement technique. You'll find help on RG. For example:
The material is identical to NIST Standard Reference Material (SRM) 1898 and the attached publication may help.
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the effect of particle size on magnetite oxidation.
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Zakaria Elmaddahi
, Thank you for you answer, However I could not find any article from the ones you mentioned above. could you please tell me where I can find them ?
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I prepared undoped ZnO, AZO (Al-doped ZnO), and MZO(Mg doped Zno) thin films. After SEM analysis I noticed that the particle size decreased for Al doping compared to undoped but particle size increased for Mg doping.
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First compare the crystallite sizes using XRD analysis of the both samples using Serrer's formula. The ionic radius of Mg2+ is 66pm and ionic radius of Al3+ is 53pm. The increase in the size may be due to the larger size of the Mg2+ w.r.t. Al3+.
From my side I can say this.
Waiting for other response from the RG experts.
Regards
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Dear All,
I am formulating some nanoparticles and after some experiments, I decided to perform a multiple regression analysis of the input variables to observe their direction and magnitude. This analysis showed that as the sonication time and amplitude increased beyond a certain point, the particle size starts increasing. I decided to try this out with a sample by measuring the particle size and sonicating thereafter for 20min and again for another 20min(40min total). The result showed particle size that increased with increasing sonication time 0>20min >40min. Is there any particular reason for this occurrence? Popular opinion tends to suggest higher amplitude and longer sonication time should result in smaller sized particles.
I will sincerely appreciate your thoughts, articles or books that may have explained this observation previously.
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You do not tell us anything about the system that you are sonication or show the particle size distribution. Chemistry can be very important here. Increasing the sonication time or power increases the collision frequency between particles. If the particulate system is unstable (e.g. inadequate zeta potential in the case of charge/electrostatic stabilization). The increase in size will be expected as the attractive van der Waals forces will overcome inertial/separation forces. I've seen this occur with micron-sized calcium carbonate with a positive zeta potential. Time of sonication of 40 minutes is excessive and is disintegrating up your sonication tip or probe. If you don't believe me then try sonicating DI (18 MOhmcm-1) water and measuring the conductivity over that 40 minute period.
Also see (registration required):
Dispersion and nanotechnology
Ultrasound, cavitation, and the singing kettle
Note, BTW, that particles of 200 nm would not be considered 'nano' by the international ISO and ASTM norms.
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When the dopant concentration increases (1%, 3%, 5%, 7% ...), the particle size is varying (increases / decreases) in the synthesis of nanoparticles by Hydrothermal method. What may be the reason behind this?
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I think it is inverse relation i.e. with increase in dopant concentration the particle size normally decreases and vice-versa.
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We are currently working on a research paper aiming to develop ink from organic waste. My research group mates and I are debating on what statistical test to use for our study. We want to see the effect of different particle sizes on ink characteristics such as viscosity, pH, drying time, erasability, density, etc.
Most of the related literature we found did not use a specific test, only graphic/tabulating and then describing the data they have obtained.
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1 depends on the characteristic you are interested in
2 regression. Type depends on the characteristics of the dependent variable
3 Hypothesis tests depending on samples involved size, method of collection,etc.
The point I have been trying to make is that there are lots of possibilities often depending on the particular question you wish to ask. There's no omnibus test or method that covers everything that you asked about. A good reference for your questions is Montgomery, Design and analysis of experiments. There's no easy simple answer to your question. David Booth
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We can't use a sieve/mesh because the smallest particle size it could reduce the biochar to is 6 microns. Is there a way to reduce it to nanometers?
We are planning to use biochar as a substitute for carbon black in making marker inks.
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Coal is easy to grind, so it is quite easy to obtain its submicron particles by wet grinding in conventional ball mills with a ball size of less than 10 mm. For a particle size of tens of nanometers, grinding can be carried out in bead mills.
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Suppose 100 nm NPs at high an low concentrations but nano particle size is same .. how ever impact is always there either its low or high. Lets join interesting open debate and collect the facts.
Thanks in advance
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To answer this approach of Nanoplastics toxicity, i have been doing nanomaterials , and the diverse environmental and surrounding conditions ( like sun rays , mecganical stress , temperature ) are responsible of creating more quickly free radicals from nanoplastics and in hydric media dilution of these particles is more concerning! so the more we have the nanoplastics blended or protected by other stable composite the more are considered as durable and relatively safe and recyclable
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plz for measuring Particle size and zeta potential ? why intensity is favorable than volume??
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Because the measured parameter is scattered light intensity.
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Hi everyone. I'm planning on determining MP presence, size, color, shape, etc., in other words, in doing a visual sorting/characterization of MP accumulated in penaeid shrimp abdominal muscle. Nevertheless, visual sorting becomes more difficult as particle size get smaller, and is time-consuming and is more likely to fall into misidentification errors. Generally, it is recommended to do visual sorting with plastics no less than 500 microns, but I'm anticipating that any plastic embebed in the abdomen is much smaller than that. I was planning to try alcali tissue digestion with KOH and fiber glass microfilters of 2 microns of pore size, and my intention was to observe the filters under a stereoscopic microscope of a minimum of 45X of magnification. But still I'm going to obtain small plastic particles, if any (spoiler: there will be). So my question is if you have any recommendation or alternative method?... observe the filters under a fluorescent microscope using Nile red to facilitate MP discrimination? analyze another tissue? use a greater pore size filter? change the organism... or maybe it is possible to do the job. Espectroscopy methods are not allowed, since it is part of another stage of the project, I just wanna perform visual sorting/characterization.
Thank you very much for your attention.
Best regards
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You are correct, visual sorting gets increasingly difficult as the particle size gets smaller. The sizes of MPs that you are able to pick out of your sample first comes down to what you can see, and that is often dependent upon the magnification abilities of your microscope. And there can be a fair amount of error associated with that as MPs often look like other things (e.g., diatoms). Adding additional techniques before visualization can help a lot.
First is the digestion of the tissue. I have tried both KOH and H2O2 + heat on fish tissues and found them both to be effective. I typically use H2O2 at 65C for a few of hours with periodic agitation, depending on the size of the tissue sample. Karami et al. (2017) has a nice paper on different types of digestions. Next is separation from the surrounding media. If you are interested in separating by polymer type, then you can consider a density separation. Li et al. (2018) provides a good method. Just know that some of the chemicals used can be a little difficult to handle and particle size can impact buoyancy. The latter might be solvable by adding centrifugation (see Nguyen et al. 2019). You mention filtration, and I would say that is the most common method. There is some discussion about how to best filter samples to get the most MPs while avoiding contamination. While not the only one, Cai et al. (2020) addressed that subject recently. Personally, I think that filters are a good way to go if your MPs are large enough to be caught by it. You should consider passing the digestate and subsequent filtrates through multiple filters with smaller and small pore sizes so that you you don’t clog filter pores and when you get to the smallest particles large bits aren’t obscuring the view of smaller particles. Nanoplastics are still a big problem. The Nguyen et al. (2019) study says that their technique is able to separate those too, but I haven’t tried it yet. Its generally agreed upon (as of now) that there is no one good method to separate out the really small nanoplastics. And if you think you have a separation method, once they get that small, the only way to verify if you got any is by using an electron microscope (maybe uFTIR…very much maybe). That’s one of the reasons most people purchase fluorescent NPs to use in their exposure experiments. Next is the Nile red staining that you mentioned (I’m assuming you are using protocols from Maes et al. 2017 and Shim et al. 2016?). I certainly see this as one of the more commonly used methods to differentiate MPs from their background. And, if your microscope has enough resolution, you should be able to see particles <500um. Considering that you are using shrimp tissue, you should determine if you will get autofluorescence within the same wavelengths as the stain. I also recommend reading Meyers et al. (2022); they have some interesting ideas about using Nile red that I look forward to trying. Stanton et al. (2019) proposes the use of DAPI as a costain gives better results. And as the previous responder mentioned, FTIR has the final say in whether something is a plastic or not, and what kind it is. If it is possible for you to do on at least a subsample of what you separate from your sample, then it will make your study stronger. Regarding tissue type, I think that has more to do with your question. When dealing with aquatic organisms, exposure route should be carefully considered as it can be inhalation, dermal, and/or ingestion. Particle size typically determines if an how a particle can translocate through the body, and not all tissue types are equally permeable. The muscle seems like generic sort of tissue to look at, not in a bad way though. Would it be possible to collect hemolymph?
I’m not sure how much I helped to solve your problem, but I hope I at least gave you a few more directions to look in.
Good luck!
- Melissa
Cai, H., et al. (2020) Microplastic quantification affected by structure and pore size of filters. Chemosphere 257, 127198. http://doi.org/10.1016/j.chemosphere.2020.127198
Nguyen, B., Claveau-Mallet, D., Hernandez, L. M., Xu, E. G., Farner, J. M., & Tufenkji, N. (2019). Separation and analysis of microplastics and nanoplastics in complex environmental samples. Accounts of chemical research, 52(4), 858-866. https://doi.org/10.1021/acs.accounts.8b00602
Karami, A., et al, (2017) A high-performance protocol for extraction of microplastics in fish. Science of the Total Environment 578, 485-494. http://doi.org/10.1016/j.scitotenv.2016.10.213
Stanton, T., et al. (2019). Exploring the efficacy of Nile red in microplastic quantification: a costaining approach. Environmental Science & Technology Letters, 6(10), 606-611. https://doi.org/10.1021/acs.estlett.9b00499
Meyers, N., et al, (2022). Microplastic detection and identification by Nile red staining: Towards a semi-automated, cost-and time-effective technique. Science of the Total Environment, 823, 153441. https://doi.org/10.1016/j.scitotenv.2022.153441
Li, L., et al., (2018). A straightforward method for measuring the range of apparent density of microplastics. Science of The Total Environment 639, 367-373. http://doi.org/10.1016/j.scitotenv.2018.05.166
Maes, T., et al. (2017) A rapid-screening approach to detect and quantify microplastics based on fluorescent tagging with Nile Red. Scientific Reports 7, Article number: 44501. http://doi.org/10.1038/srep44501
Shim, W.J., et al. (2016) Identification and quantification of microplastics using Nile Red staining. Marine Pollution Bulletin 113, 469-476. http://doi.org/10.1016/j.marpolbul.2016.10.049
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So, basically in case of XRD, we call it as to find out Crystallite Size but In case of SEM/ TEM, we call it as to find out Particle Size. But to some extent, the values of particle size and crystallite size is nearly same. What is the main difference between these two from which it can be differentiated both theoretically and practically too?
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Your question was asked on RG multiple times. Discussion of 2012 attracted 299 (!) replies. In the beginning RG was much more popular in research field. Anyway, read first two answers, they are the good ones. Just a reminder: for nanoparticles grain and crystallite are mostly the same thing.
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How if the Z-average and % distribution of particle size from PSA is to much different. The spectrum and the highest peak of %distribution is about 10-40 nm and the Z-average is nearly 350nm? so which value can be taken to determine the particle size
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Dinia Astira Please post your plots and if using a Malvern equipment, please post the raw data file (.dls or similar). If you have large contamination in the system then the z-average will reflect this and be much higher than the main peak. If you convert to volume then any higher peak may disappear but we need to see the plot.
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I preparation nanoparticles of copper by exploding wire method using high voltage discharge 6 KV in distilled water , the particles size of copper in water was 240 nm which was measured it by Dynamic Light Scattering (DLS).
Why size of copper nanoparticles is huge more than 100 nm ?
How can get copper nanoparticles less than 50 nm ??
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the DLS measurement is used to measure the average hydrodynamic diameter for copper nanoparticles suspension, using the SEM instrument to get the exact (actual) size, Since the actual size using SEM will be smaller than the size shown using DLS
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Can a Zetasizer measure soil particle size? If yes, could the results (particle size) be exploited to determine the soil granulometry?
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Amer Chabili No, soils and sediments are laser diffraction measurements. They're, in general, far too large for DLS.
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My DLS data shows the particle size of my product is 12-15th times bigger than the crystalline size derived from the XRD data. is this normal? please provide some highlights
Thank You..
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Hello Gouranga Dutta Can you share your DLS data? Light scattering is quite sensitive to the presence of aggregates/dust/air bubbles that can easily skew the average size.
You may find these posts of interest:
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If we encapsulate different concentrations of the same material under the same conditions, it can affect the particle size of the capsule
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It may affect not only the size but also zeta potential, well of course depending on the system.
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I have 2 different particle size of silicon dioxide or silica nanoparticles such as in the range of (10-20 nm) and (50-100 nm). So, what will be the differences between these two whether in any of their properties or any changes in XRD/ XPS analysis? Kindly please explain it properly. Thank you.
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XRD is mainly used to determine - lattice parameters, internal stress/strain (elastic), and coherently scattering domain size (crystallite size). XPS is mainly used to determine - oxidation state, and surface chemical composition. Their field of application is non-overlapping, therefore can not be compared.
So, as per se your query states, I must say that there is only a difference in the size of these sample particles. Their property may differ subject to changes in their surface chemistry or in their application parts wrt interacting molecules.
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How do we remove carbon, copier, and another mineral from the Biosynthesis of Zinc oxide nanoparticles?
(I have mixed the supernatant of bacteria with (20 mM ) of zinc sulfate for preparation of the zinc oxide nanoparticles). Then, I washed the precipitate with PBS and D.W three times.
After that, I got the particle size by DLS and TEM, but the result of EDX is a carbon (C) 97%.
Hope to see your answer with a reference or without reference.
Regards,
Ahmed
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Dear Dr. Gorshkov
Thank you so much for your reply. sometimes I got 2% of zinc by EDX. I can't consider it as Carbon because I need to get pure zinc. So if you have any knowledge about how I can remove the carbon and get the pure nanoparticles.
Do you think the glucose in the culture media is responsible for Carbon formation around the nanoparticles or covers it? Bacteria use glucose as a carbon source during the growing.
regards,
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I am working on synthesis of polymer nanoparticles, but my problem is, always non-homogenized aggregated nanoparticles were formed, and as I have too many parameters such as amount of (monomer, surfactant and initiator) or Temperature, polymerization duration, and agitation time. so it is very hard to me to study all of these parameters, (so that I need your help) which parameters has most effective to obtain homogenized particles size?
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Dear Yaseen Kareem, would you please tell the polymer you are working on, may be studies already done on it. Generally speaking, NPs size and surface state are the main parameters behind particles agregation or agglomeration. My Regards
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I am preparing ZnO nanoparticles using Zinc acetate dihydrate and NaOH precursors through the hydrothermal method. At 100 ◦C for 5 hours, I got 80 nm particle size, but when I dry that at 100 ◦C, it increases to 200 nm. I wish to prepare <50 nm particles. Please help me out of this.
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Rahul Gond Generally lower concentrations of precursors favor smaller sizes.
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I have purchased a ZnO nanoparticle(<50 nm) from Sigma Aldric. The particles get agglomerated and after 2 hr of sonication, it reduced to 132 nm. Please help me to reduce it to below 50 nm.
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Rahul Gond The product is aggregated (tightly bound; not separable by sonication) rather than agglomerated (loose; separable by sonication). Question how the 50 nm size was obtained - electron microscopy and software deconvolution? Or is it a crystallite size? There are no free, independent, discrete particles < 100 nm in a powder. See this webinar (registration required):
Dispersion and nanotechnology
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I'm imaging hydroxyapatite particles with regular brightfield microscopy. I'm however struggling to find an explanation why the color of these particles differs depending on size. The smaller particles (~2 um) are often yellow or white, while the bigger particles (~50u um) are black. Could someone explain how the imaging techniques justifies these changes in colour?
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Dear Imke Jansen ,
Gerhard Martens is right.
The dark or black spherules formed as a result of clumping of the finer-grained particles and are therefore opaque.
Best regards,
Guenter Grundmann
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FESEM analysis of Zr doped CeO2 thin films reveals that the size of spherical particles decreases as we increase the impurity content. What is the physical significance of this behavior of thin films?
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Dear Khizra Khalil, this is may be due to the increased number of nucleation sites for the growth of particles, so you have high number with lower size. My Regards
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I would like to know how to make a silica or alumina slurry with particle size up to 50 microns.
I am hopping that they will have shear thinning behavior.
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Dear sir I request you to read " making bangles from silica ( glass)
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If the material has a hierarchical structure then it (often) has a larger surface area despite of large particle size. What is the basic reason and how many factors can contribute to a large surface area? If The size of a catalyst is much larger i.e. μm-scale, can it have a higher Surface Area than nano-scale samples?
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Dear Muhammad Zahid, larger particles will have smaller surface areas only if you compare dense, non-porous particles.
In hierarchical structure, the large µm-sized particles you observe in SEM for example may result from the agglomeration of nano-sized particles, so the available surface area will be the one of the nanoparticles. In addition, if you have micro- or mesoporous particles, most of the surface area measured by sorption experiments (eg BET method) will be the surface of the particles' porosity and will exceed by far the outer surface (at least for µ-sized particles).
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I want to know that how we can check that dry particle size (0.8mm) is homogeneously mixed or not? How can we assess the homogeneity of dry particle size mixture. Lets say we have a mixture of SiC and ceramic stucco. The size of both 0.8mm range.
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Hello,
It is hard to calculate the homogeneity of the mixture powder even if the size of the particles is the same. It depends on the technique used for mixing those powders and the density of each particles. However you can have an idea during the observation-analysis on SEM/EDX.
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1.5M, 2.25M, and 3M NaOH at 45C.
When increase the conc. from 1.5M to 2.25M NaOH, what is the reason for increasing the particle size and decrease the particles size for further increase conc. from 2.25M to 3M?
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Zn(OH)2 is soluble in excess NaOH. Indeed at very high NaOH concentrations you may not get a precipitate at all. So it's entirely possible that, at the highest concentration you mention, the initial precipitate partially dissolves, and the result is lower particle size of Zn(OH)2 and, after calcination, of ZnO.
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Hello,
I am creating a slurry for ceramic 3D printing. I will be using silica (400nm particle size) as my ceramic material. Within the slurry, I will add a binder, a dispersant, and water.
I am currently looking into Ammonium Polymethacrylate (DARVAN C-N) and Ammonium Polyacrylate. I am not sure on how to select the proper dispersant as well as the proper amount to use. I am not relying on the dispersant to modify the rheological properties of the slurry, as the binder will help with viscosity, but rather that the silica particles are properly dispersed.
Any help is greatly appreciated!
Thank you!
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Dear Sam Choppala, better to think on the best stabilization strategy. It seems that surface modification by grafting special chemical groups gives the highest long term stability. It is to recall that NPs size, surface charge density, and pH are the main factors working on/against prolonged time stability. My Regards
doi:10.1007/s11051-010-0085-1
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Particles consists of many fine units called crystallites
then what is the relationship between the particle size and crystallite size
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My dear professor, may God bless you.