Science topic

Membranes - Science topic

Thin layers of tissue which cover parts of the body, separate adjacent cavities, or connect adjacent structures.
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I am developing a gas diffusion layer(ORR cathode)
One side of the diffusion layer is inert gas (containing trace oxygen), and the other side is (1M) KOH. I hoped that there will be high reactivity on the membrane (2O2+H2O+4E>4OH- Under fix DC voltage)
If i use carbon base to make diffusion layer,PT is the best catalyst specific to oxygon?Are there other catalyst options?
Thank you.
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I suggest reviewing the following paper:
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Hello fellow researchers,
I'm having a puzzling problem in my Western blot experiment, can somebody help me? I conducted an experiment using prefrontal cortex samples, following a WB protocol that has previously yielded successful results (We took quite some time to standardize each step). However, this time around, I'm facing a situation where I'm not able to detect any bands, despite thoroughly checking various aspects of my protocol.
Here are some key details:
- My samples were homogeneized in RIPA buffer + proteases inhibitors as usual, and are relatively fresh, I homogenezeid last month, and I am realizing western blot with those samples since that.
- I run my electrophoresis in BioRad system, at 150V, 400mA, 2h, room temperature (10% acrylamide gel)
- I transfered to nitrocelulose membranes in semy dry transfer 30V, 1h, 164mA, room temperature
- I performed a Ponceau staining and confirmed that the samples were transferred correctly to the membrane (image is attached)
- I used three different antibodies in those membranes in the first time (I cut the membranes in three different sizes), it didn't work and I thought that it could be a old antibody solution problem. So I stripped the membranes and I incubated with new antibodies solutions (I got three new and sealed antibodies, including the secondaries) and none of them resulted in detectable bands.
- I was very careful to see that I incubated the correct primary antibodies, with their respective secondary antibodies
- Blocking (BSA 5%) and washing steps (3x with TBS-T) have been successful in previous experiments with those antibodies of the same brand.
- The protein quantity in the samples appears adequate, as good bands were visible in the Ponceau staining.
- I'm using high-quality and well-maintained Super-ECL reagent.
I'm completely stumped by this situation, especially because even the internal control protein, beta-actin, is not being detected. If anyone has faced a similar issue or has suggestions on what else I can investigate, please share your insights. Any assistance or guidance would be greatly appreciated.
Thank you for your attention and help!
Nicolle Platt
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Maybe check the blocking buffer? always use fresh made one or frozen stocks. Or does the Super-ECL reagent is fresh made? Or check the expose machine, do you use the correct filter?
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Dear researchers,
I bought some membrane production materials like PVDF, DMF, DMAc, PEG200, PVP, SiO2, etc.
How can I prove that these materials are pure and not from industrial grades or counterfeit materials available in the market with reputable brands?
What tests can I take for each of them like FTIR, XRD, etc.
Regards
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you could also perform thermal analysis, like DSC and TGA to distinguish the grade and/or purity.
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Do we need any pretreatment of proton exchange membrane before using it. if yes then what is the procedure? and please give information about if the water pass through proton exchange membrane as when we are keeping the water level higher in one side of the membrane after some time the level in both side of the membrane becomes equal.
So my question or doubt is that if some product will be formed on either side, will it not allow to pass through it. and how is it able to exchange only proton ? although it is exchanging the water through it.
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but if water can pass through it then it is obvious that product formed can also pass through it if we are doing any redox reaction.
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In this article, they the used this equation CCe = (Fe*Pp*Np)+(Fe*PVp*nv)
to calculate the Elements capital cost in the pressure vessel for RO membrane.
(membrane + pressure vessels)
What is the corrective factor (Fe) in this equation?
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Anyone who is expert in Reverse Osmosis? I'm still looking for an answer.
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currently I am modeling the membrane reactor. hydrogen (reaction product) as a permeated substance. when modeling a packed bed reactor I use:
D=(U*Dp)/(11*(1+(19.4*((Dp/(d1*2))^2))))
D= diffusion coefficient
U=velocity
DP=catalyst diameter
d1=reactor diameter (to membrane line)
to calculate the effective radial diffusion coefficient in packed bed (m2/s) and the results are in accordance with experimental.
but when modeling the membrane packed bed reactor, the simulation experienced an error.
Are there any suggestions regarding the diffusion coefficient equation for permeated substances that is more suitable for me to use?
Your answer will be greatly appreciated.
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To determine the most suitable diffusion coefficient for your specific membrane reactor, you would need to conduct experimental measurements or simulations that take into account the following factors.
-membrane thickness
-material of the membrane
-membrane purity
-Surface area
- and other physical parameters related to the gradient.
I suggest you to first run the computational simulation.
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I need to build a low-cost airflow humidifier which would not have a direct contact between water and the air to be humidified (i.e. not a bubbler or sponge). The "state of the art" on this are hollow-fiber cartridges containing hundreds of nafion tubes, but these are too costly for my application. Since regenerated cellulose (RC) dialysis membranes are permeable to water molecules (I've concentrated proteins through them), I wonder if transport of water through a RC dialysis tube may be efficient enough. Dialysis bags and cartridges are widely available.
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Since regenerated cellulose (RC) dialysis membranes allow water molecules to travel through them, it seems possible to use them to transport water for humidification without having water come into direct contact with the air. Let's talk about one way to make a dialysis bag or cartridge airflow humidifier for cheap:
Air-Misting System Modeled on Dialysis Technology:
Use a dialysis bag or cartridge with a large surface area to enhance water transport. Always keep in mind that a more significant surface area means greater efficiency.
The dialysis bag or cartridge must be submerged in a water reservoir. Maintain a steady level of water in the pool. The water level should constantly be above the membrane's surface for optimal humidification.
To avoid condensation, humidified air should be circulated in the dialysis bag or cartridge. A simple fan or blower will do the trick here. For optimal exposure and humidification, the flow should cover as much of the dialysis membrane's surface area as feasible.
Keeping a gradient in the water pressure across the membrane is essential for efficient water transfer. Creating a driving force for water molecules to migrate from the reservoir, across the membrane, and into the dry air can be accomplished by circulating dry air (low humidity) around the dialysis bag.
The rate at which water moves can be significantly impacted by ambient temperature. If possible, humidity rates can be increased by gradually warming the water reservoir.
Make sure you clean and maintain it regularly. The membrane could become clogged, or the water quality could decline over time. Consistent operation can be done by changing the water and periodically cleaning the system.
A cheap humidity sensor can be integrated into the system for advanced monitoring. This allows the output air's humidity to be tracked so the system can be fine-tuned.
Difficulties and Factors:
Water transport efficiency using RC membranes may be lower than that of more advanced Nafion-based devices. If we want to know whether or not this system can handle our unique humidification demands, we'll need to run some pilot tests.
Longevity of the membrane: It is unknown how long RC membranes will last when used for constant humidification. The membrane's effectiveness or integrity could decline with time.
As water vapour flows across the membrane, contaminants in the reservoir may become concentrated. Because of this, the performance of the membrane may degrade or become fouled.
RC dialysis membranes can achieve Humidification without air-water contact, making them a promising low-cost alternative. However, it is essential to be aware of the membranes' limitations and to optimize the system accordingly. Its performance may fall short of more expensive systems, but if well-designed and maintained, it can still perform adequately for some relatively inexpensive uses.
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The CO2 desorption in MOFs is performed by heating or applying low pressure(vacuum). It is observed that by incorporating MOFs in polymeric membranes, the CO2 selectivity increases in general. My question is that how desorption of CO2 occurs in continues permeation process? each time when MOF-based membrane is used at displays higher CO2 selectivity. so, why the MOfs saturated with CO2 do not show reduced selectivity in MOF-based membranes in continues permeation process?
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There is a recent study that considered CO2 absorption into hybrid graphene oxide/MOFs, which might be useful for your perusal:
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Do you have any suggestion how to get rid these non specific bands?
These are my protocols:
1. Osteoblast cells were cultured in 100-mm cell culture dishes in serum-deprived α-MEM overnight.
2. TNF-α were then added to the dishes for specific periods (0, 6h, 12h, 18h, and 24 h) in serum-deprived α-MEM.
3. Then, washed twice with ice cold PBS and lysed using RIPA buffer (Millipore, Burlington) containing 1% protease and phosphatase inhibitor (Thermo Fisher Scientific, Rockford,).
4. Protein were treated with β-mercaptoethanol and laemmli sample buffer (Bio-Rad, CA) and denatured at 95 ◦C for 5 min as a preparation for SDS-PAGE.
5. 50 ug were loaded into gels 4–15% Mini-PROTEAN TGX Precast Gels (Bio-Rad, Hercules,) and transferred to a PVDF Trans-Blot Turbo Transfer System (Bio-Rad, Hercules).
6. The membranes were blocked in Block-Ace (DS Pharma Biomedical, Osaka, Japan) for 1 h at room temperature and were probed AGTR1 Rabbit polyclonal Ab, phospho-SAPK/JNK (Proteintech; 1:1000 dilution) overnight at 4◦C.
7. The membranes were washed in TBS-T and TBS, then incubated with anti-rabbit IgG HRP-linked Antibody (Cell Signaling Technology, MA, USA; 1:5000 dilution) for 1 h at room temperature.
8. The membranes were washed in TBS-T and TBS again, then incubated with SuperSignal West Femto Maximum Sensitivity Substrate (Thermo Fisher Scientific, Rockford, IL, USA).
Here I attach the figure. The protein that I want to get has MW of 41 kDA.
Thank you so much for your kind help.
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Hi Rizki!
I think your blot has improved significantly! I think I accidentally advised you to use PBS for this... please ignore that. Unfortunately, the problem with anti-phospho antibodies is that they are highly selective, and its a general trend so probing with it seems like a difficult task anyway. W.R.T. the difference in band intensities could be because of the way you treated your samples. While serine phosphorylation remains relatively stable post-heating, histidine phosphorylation if you're probing that, is really labile, and it is possible that you have this background solely because of low specific binding. I think going by the trend of your blots, reducing the concentration of your primary antibody further and increasing the incubation time might help you. as Esra Buber suggested, you may increase the concentration of BSA too for blocking.
One more weird thing that has worked for me while attempting to remove non-specific signals, is to wash the blot a couple more times after you're done with original washes, with TBS without tween. See if it works...
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PDVF membrane incorporated with CuO nanoparticles can be suitable for what degradation ?
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Thank you Paola Bernardo
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Currently, I looking for the information about the hot topic membrane modification by using graphene oxide. Because I believe that graphene oxide have a good properties and easy to modify in membrane.
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Graphene oxide is an excellent building block for many membrane applications, including air dehumidification, water desalination, organic solvent mixtures pervaporation, electrocatalytic membranes.
But, it should be kept in mind, that:
1. Graphene oxide produced by different research groups could vary strongly in it's properties because of various flake size distribution, C/O ratio, synthetic and purification methods. So, when compare the data published by different groups, be careful.
2. Graphene oxide could be prone to ageing. It has dynamic structure, and GO-based thin films change their membrane properties with time. It's important to work with fresh GO suspensions and as-prepared membranes. The fresh GO suspensions should be stored in refrigerator, and avoid light exposure.
3. Because of ageing, it's of huge importance to carry out long-term monitoring of GO membrane characteristics (composition, flux, permeability, selectivity) with time (at least, for several months). To prove the stability of the membrane for practical applications.
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In the membrane distillation process, a spacer/mesh is used to prevent the membrane from sticking to the surface of the module. On which side of the membrane should this spacer be placed? on the surface of the membrane (in contact with feed) or behind the membrane (in contact with distilled water).
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What type of membrane distillation do you want to do? I have been working on direct contact MD and I do not use a spacer/mesh. The DCMD module has a rubber gasket on each side and the membrane is set in place by that and never sticks to the surface of the module. If you want/need to use the spacer/mesh, I suggest doing short experiments without it, with it on the permeate side and finally with it on the retentate side. After, you can analyze the system performance and characterize the membrane, and with that reach a better conclusion on the best approach. If your membrane has some type of support (I use a PTFE membrane with a PE support), the support faces the permeate side of the module.
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I am currently engaged in modeling the desalination performance of Cellulose Acetate (CA)/Graphene Oxide (GO)/POSS Mixed Matrix Membranes (MMMs) for reverse osmosis (RO) applications. The primary objective of my research is to develop a comprehensive understanding of the transport phenomena and rejection mechanisms within the membrane, utilizing the Donnan-Steric Pore Model (DSPM). As part of this endeavor, I am seeking to determine the effective membrane thickness.
During the membrane preparation process, I have acquired information that the solutions of composite membranes were cast onto a non-woven Hollytex polyester substrate taped to a clean glass plate with 250 μm thicknesses using casting knife. However, I am curious if there exists any way to determine the effective thickness of the membrane without resorting to experimental methods.
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Welcome dear Reihaneh.
Why not!
You can send me the SEM image and I will tell you the thickness. Be careful that the SEM image has to have a scale bar.
Best wishes
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The membrane distillation modules I work with have large dimensions and large membranes must be made. But in some membranes, a few tiny holes are created in different parts of the membrane, possibly due to dust or any other unknown reason. Is there a method to block these two or three small holes and use the membrane? Otherwise, I have to throw away the perforated membranes and fabricate new membranes again.
Best regards
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Thank you so much for your response. I edited my question. My flat sheet membranes are fabricated from PVDF and are porous and hydrophobic.
These holes are only in some membranes even when no additives are used. However, I wanna use these membranes in the module and check their performance because a lot of materials are used to fabricate these long membrane sheets.
Probably I can use a special type of glue in a very small amount to cover these tiny holes. But what is that glue?
Or, probably, there are some other solutions.
What type of plasticizers I can use in hydrophobic PVDF membranes?
Best regards
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Who can advise how to carry out experiments on membrane adsorption of hollow fibers?to carry out experiments on membrane adsorption of hollow fibers?
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skim milkMuhammad Mansoor Shaikh Muhammad Ishaque 、您可以在普通实验室中使用哪些方法,如 BSA 或脱脂牛奶
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Why the surface of electrospun fiber membrane be easily peeled off like a spider web, and layered with the fiber membrane below ? The polymer is PAN, the solvent is DMF, with a concentration of 12% and a receiving distance of 12cm. Is it because of high humidity?
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increase the concentration up to 15%, thickness is also low(increase it) and after collecting dry in a vacuum oven
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I am researching in the direction of composite membranes for gas separation membranes, and one question I have is: when doing things like FT-IR, XPS, and TG, is it necessary to cast the membrane layer separately (without the support layer), and will this have an effect on it? I have done FT-IR tests, and some of the effects are not obvious, but when testing for TG, it's not clear to me whether I should remove the support layer or not. On some references I found that this issue is not written about
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It all depends on the technology that you have chosen with or without a support layer. With a support layer, the membrane will be stronger, but this layer can interfere with filtration and contaminate the resulting product, the filtrate. Membrane characterization is secondary.
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What’s the difference between an AEM (Anion-Exchange Membrane) and a PEM (Proton Exchange Membrane)
Is AEM exclusively used for water electrolysis?
Is there an additional coating layer on AEM’s?
Different chemistries used comparing PEM and AEM?
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Good afternoon Max,
According to my AI desktop, which isn't always as reliable as I'd like:
"The main difference between AEM (Anion-Exchange Membrane) and PEM (Proton Exchange Membrane) is the ion that they transport. PEMs transport protons, while AEMs transport anions.
The main technical difference between AEM and PEM electrolyzers lies in the type of membrane used and the resulting electrochemical reactions that occur."
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I did a western blot yesterday, and I loaded two groups of the same samples in one gel, only separating them when I was incubating the primary antibody. The results show that my GAPDH is clean in low background, but my target gene is not clean in high background. Although they are from the same membrane and I treat them in the exact same condition.
Does anyone possibly know the reason?
Thank you!
Below are my target protein(smad2) and my GAPDH.
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All I can think of is that your primary antibody against SMAD2 is not specific enough? (i.e. it is binding non-specifically to other proteins, given than you see signal all over your lanes). Are you able to try a different primary antibody against SMAD2? The best thing to do is to check the literature associated with the antibody you are buying; most of the time, companies will link you to different papers which have published data using that specific antibody.
Maybe another thing you could try before buying a different antibody is to dilute the SMAD2 antibody further? Sometimes if your antibody is too concentrated it can bind more non-specifically and lead to unexpected bands.
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Is 1 Kilodaltons dialysis membrane is reusable for same sample? is tube or membrane is suitable for large quantity carbon dots filtration.\?
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A dialysis membrane of 1 Kilodalton is not reusable for the same sample. Dialysis is typically a one-time use procedure to avoid contamination. The size of the carbon dots and the membrane's molecular weight cutoff determine whether a dialysis membrane is suitable for large quantity carbon dots filtration. Other filtration methods, such as ultrafiltration or tangential flow filtration, may be more efficient for large-scale purification.
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I am working with a protein located in the mitochondrial inner membrane, and I would like to know in which conditions should I perform the denaturation step... maybe the "standard" denaturation at 95ºC-100ºC for 5 minutes does not work for that kind of proteins.
Thank you very much.
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Avoid to heat that much, it may lead to aggregate formation. In general, incubation in Laemmli buffer (containg SDS of course) at 37°C for one hour or so must be enough to give correct results on migration and Western Blot.
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in a typical MFC H+ ions will form in anode chamber. it is supposed to go through the membrane to the cathode.
many of the research papers use CEM. how is it possible, since H+ and NH4+ are the cations, to be passed through PEM?
or
proton exchange membranes do transfer cations as well?
someone, please clarify this......
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In Microbial Fuel Cells (MFCs), both Proton Exchange Membranes (PEMs) and Cation Exchange Membranes (CEMs) can be used as ion-selective barriers to separate the anode and cathode compartments. The choice between PEM and CEM depends on the specific MFC design, operating conditions, and the desired performance.
  1. PEM (Proton Exchange Membrane): Advantages: High proton conductivity: PEMs have excellent proton transport properties, allowing efficient transfer of protons from the anode to the cathode. Low electronic conductivity: PEMs are designed to have low electronic conductivity, preventing direct electron transfer between the anode and cathode and maintaining an electrochemical gradient for microbial activities. Suitable for air-cathode MFCs: PEMs are commonly used in air-cathode MFCs, where oxygen reduction occurs at the cathode. Considerations: Susceptible to dehydration: PEMs require adequate hydration to maintain their proton conductivity, making it crucial to manage water transport and avoid drying out during MFC operation.
  2. CEM (Cation Exchange Membrane): Advantages: Ion selectivity: CEMs selectively allow cation transport, maintaining a charge balance between the anode and cathode compartments. Good durability: CEMs are often more durable than PEMs and can withstand higher temperatures and pH ranges. Suitable for specific MFC configurations: CEMs are commonly used in certain MFC designs, such as anaerobic MFCs with solid-state cathodes. Considerations: Lower proton conductivity: CEMs generally have lower proton conductivity than PEMs, which can affect the overall performance of the MFC. Risk of biofouling: CEMs are susceptible to biofouling and scaling due to the accumulation of cations on the membrane surface.
Performance Comparison: The choice between PEM and CEM depends on the specific application and design considerations of the MFC. In general, PEMs tend to offer better performance in terms of proton transport and electron selectivity, which can lead to higher power output in air-cathode MFCs. However, in certain configurations and operating conditions, CEMs may provide suitable performance while offering advantages such as improved durability and resistance to biofouling.
It's important to note that ongoing research and development in the field of MFCs may lead to advancements in membrane materials and design, providing even better performance and efficiency in the future. When selecting a membrane for an MFC, it's crucial to consider the specific requirements and goals of the MFC application and conduct appropriate testing and evaluation to determine the most suitable membrane type for optimal performance.
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I expressed a GFP protein with my protein in Agrobacteria, I guess this protein will localization in the outer membrane, but the results are very confusing, does any friend know where the GFP localization is? Many thanks.
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GFP is a naturally occurring fluorescent protein that can be genetically engineered into bacteria and other organisms to track and visualize protein localization or expression. In bacteria, GFP can be expressed as a fusion with other proteins of interest to study their subcellular localization.
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I have read that I can use RIPA buffer for EV membrane disruption. Does this have to be followed by ultra centrifugation? Does anyone have a protocol for this?
Thanks.
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Dear Dr. Maral Tabrizi
RIPA lysis buffer which contains a combination of both ionic and non-ionic detergents results in the highest number of identified peptides and proteins.
Yes, you may lyse EVs in an appropriate volume of RIPA lysis buffer. You may add protease and phosphatase inhibitors at the time of lysis.
You may use the following protocol.
You may use the following inhibitors in the RIPA lysis buffer at the time of lysis.
1 mM Sodium orthovanadate,
50mM NaF,
5 µg/ml Pepstatin,
5 µg/ml Aprotinin,
5 µg/ml Leupeptin.
Lysis may be performed on ice for 30min and placed in an ice-cold sonication bath for 30 s. This step may be followed by a gentle mix on ice for 15 min followed by centrifugation at 15000 g for 10min. Discard the pellet.
You may add 1 volume of 100% (w/v) TCA to 4 volumes of the sample, vortex and incubate for 5 min at 4°C. After centrifugation at 15000 g for 5min at 4 °C, the supernatant may be discarded, and the pellet may be washed with cold acetone. Centrifuge at 15000g for 2 mins at 4°C. Discard the supernatant. Repeat the washing step but this time using 80% cold acetone. Discard the supernatant. Air-dry the pellet (proteins) for 3 mins. You may dissolve the protein in the buffer of choice.
The protein content may be assessed using BCA assay.
If you wish to use the micro-BCA assay, you may add 5μL of sample to a 96-well microplate followed by 100μL of BCA reagent. Mix plate thoroughly on a plate shaker for 30 seconds. The plate may be incubated in the dark for 30min at 37 °C. The absorbance may be measured at 560nm, and protein concentration may be determined from a BSA standard curve.
Regards,
Malcolm Nobre
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Dear All,
I am wondering how the Transwell inserts can be recovered from fixing to be then embedded?
After fixing, I put each membrane on nitrocellulose membrane to avoid curling and then I leave them in an embedding cassette to be processed - automated protocol of our histology facility.
When embedding, I cut each membrane into half and put them upright. This process is very difficult because the Transwells start curling and they are very thin, so they don't settle very well. Also, when sectioning, Transwells would break because of their thickness.
Do you have any alternative on how to manage them before processing and then embed?
Thank you!
Aurora
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Transwell inserts are permeable support device meant for the study of cell-lines to study angiogenic inducing or inhibiting effect on the migratory response of epithelial cells. I would request you to go through the publication of Sip CG, et al. Lap Chip 2014; 14:302-314; where it had been described with method compatible with conventional cell culture.
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I filtered sodium dodecyl sulfate in buffer solutions through a PES membrane. After that, I took some SEM images of my sample to visualize organic particles fouling on membrane. Here is one of my SEM image. I'm not sure if that looks like organic fouling. need some help. Thanks,
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Dear Makayla,
I am not sure if you can quantify the amount of fouling based on FTIR alone. But let's discuss your issue a bit and hope I get your point. for any analytical analysis, we need a calibration standard. Let's assume you have a known feed solution concentration and you are using cross-flow flow filtration, after you stop the filtration, the concentration of your concentrate and permeate can be determined, so assuming the rest caused fouling. Remember that the volume of your initial feed, and permeate and concentrate are important to verify the mass balance. At this point, you can assume that the fouling occuoccurredcross-flowred evenly and calculate the amount of foulant per area of the membrane.
Another method is also, to cut 3 pieces (known area) of the fouled membrane, and then put that in 3 separate glass tubes (triplicate) and add a known amount of solvent that can dissolve your foulant. Afterwards, use an analytical instrument that can determine the concentration of your foulant which you can easily convert to gr based on the known added volume to the tube. Calculate the average and divide per area.
Last but not least, you can start with different known concentrations of sodium dodecyl sulfate in buffer solutions and do the same procedure that I explained and further also use FTIR and connect the concentration to the intensity or area under specific peaks if the peak is specific to your foulant and not the membrane. Now you can have a calibration curve that connects the ftir and concentration of foulant per area of the membrane. Just remember the time of filtration and pressure, temperature, flow velocity, (turbulent flow), pH and other important factors should be constant.
In the case of real-time monitoring of fouling using Raman spectroscopy, you can read the article of my colleague and maybe get some hints.
In one of my papers, I was also trying to identify the amount of vanillin adsorbed on the membrane surface after my experiment and I explained the methods there, which is similar to what I have learned from my colleague in the abovementioned article.
Hope my explanation is clear and I got your point correctly.
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what are the functions of F1 particles in mitochondria ?
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Yes
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Hello everyone,
Does anyone have suggestions on how to achieve complete or almost complete stripping for the western blot membrane? My protein of interest has a molecular weight of 110kda and my loading control appears around 120kda. We have never achieved complete stripping and end up getting two bands which sometimes become very problematic while quantifying. Since the two molecular weight is very close we don't cut the membrane. We also tried to get a different molecular size loading control since our primary antibody is in-house but that didn't work. Therefore I was wondering whether anyone has any suggestions regarding a good stripping buffer. Thank you.
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Evan Kerek and Saddah Ibrahim thank you for your answers
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For example, in the process of electrodialysis.
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This paper comes to mind (not electrodialysis, but electrolysis): https://pubs.rsc.org/en/content/articlehtml/2020/ee/d0ee02173c
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in the model I am simulating, the mixture of ethylene glycol and water is flowing in the hollow fiber membrane (a cylindrical hollow tube made up of porous media). during the flow, the water in the mixture of ethylene glycol+ water will selectively evaporate through the porous media due to the pressure difference inside the hollow fiber membrane and outside hollow fibre membrane. Please help me to solve this. Any software can be recommended.
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To simulate evaporation through porous media with the evaporation-condensation method in Ansys Fluent, follow these steps:
Set up your porous media: Define the porous zone in your domain where you want to simulate evaporation. Assign the appropriate porous media properties, such as permeability and porosity.
Enable the evaporation-condensation model: In Fluent, go to the "Models" panel and enable the "evaporation-condensation" model.
Define phase change settings: Set the appropriate parameters for the evaporation-condensation model, such as the evaporation rate, condensation rate, and heat transfer coefficients.
Specify the initial conditions: Define the initial temperature, pressure, and other relevant properties for the domain and porous media.
Set boundary conditions: Apply appropriate boundary conditions, such as inlet and outlet conditions for the fluid flow and evaporation.
Initialize and solve: Initialize the simulation and run it to solve the fluid flow, heat transfer, and evaporation-condensation phenomena.
Post-process results: Analyze and interpret the simulation results to understand the evaporation behavior within the porous media.
Remember to consult Ansys Fluent documentation or tutorials for more detailed information on specific settings and inputs relevant to your simulation
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Hello dear colleagues! I would greatly appreciate it if you could recommend a protocol for a release assay of silver nanoparticles from a hydrogel membrane. I would like to know what amount of silver nanoparticles is eluted at different time points. Is it possible to run this test with uv-vis?
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Yes, of cause you may try to run UV-vis and try to detect the SPR peak of AgNPs in the range of 400-450 nm
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I did the subcellular fractionation of transfected HEK-293T cells.
For western blot analysis for the purity of fractions, I used anti-B actin antibody, anti-fibrillarin G4 antibody and anti-calnexin antibody for cytoplasmic, nuclear and membrane fractions, respectively.
Anti-B actin gave expression both in cytoplasmic and nuclear fraction. Later, I realized that B actin is also present in the nucleus!
With Anti-Fibrillarin, expression was detected in nuclear fraction only.
However, with Anti-Calnexin antibody, expression was both in nuclear and membrane fraction, with higher amounts in the former.
I was wondering, if that could be possibly be due to the contamination of nuclear fraction with membrane fraction.
Could anyone suggest me more specific markers for identifying the three fractions?
Thanks in advance.
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1. Yes, you are right. B-actin is also present in the nucleus, as a component of chromatin remodeling complexes. You may use α-tubulin as a marker for the cytoplasmic fraction.
The soluble α/β-tubulin is considered to be a reservoir of subunits that are available for microtubule polymerization in the cytoplasm, but there are reports supporting the presence of tubulin in the nucleus of cultured animal cells. The reason for nuclear accumulation of tubulin, which does not occur under normal circumstances, is a process of pathophysiological significance and may represent a defense mechanism against stress or malignant transformation. This is the reason why nuclear tubulin may be detected only in cancer or in transformed cells.
2. Calnexin is highly abundant in ER as well as the outer nuclear membrane. It has also been found at ER-mitochondria contact sites. But the possibility of contamination of nuclear fraction with membrane fraction cannot be ruled out. Nevertheless, you may try caveolin-1 for the membrane fraction. Caveolin-1 is a plasma membrane protein that has a fundamental role in the formation of caveolae and acts as a connective protein that organizes the macromolecular complexes on the cell surface which participates in intracellular signaling.
3. In addition to fibrillarin, you could use histone (H3) for the nuclear fraction. H3, one of the core histones along with H2A, H2B and H4 is known to form nucleosomes with nuclear DNA. It plays a crucial role in activating the spindle assembly checkpoint in response to a defect in mitosis.
You may try these markers.
Hope it helps!
Best.
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I am researching in the field of gas separation membranes because of subject matter funding. I have to use a micron wet film applicator for manual coating. I applied the membrane fluid on my support membrane, but the result was always unsatisfactory because the fluidity of the cast membrane fluid was very high, and the coated wet film was not homogeneous when observed by the naked eye. I would like to ask if there are any specific tips when applying the wet film. Also, I am fixing the support film on a flat glass plate by tape.
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Applying a uniform film manually using a wet film applicator can be challenging, especially with high-fluidity materials. Here are a few tips that could potentially help you improve your results:
  1. Viscosity Adjustment: If the fluidity of your membrane material is too high, it might be beneficial to adjust its viscosity. This could be done by allowing solvents to evaporate partially before application or by adding a viscosity-modifying agent if your formulation allows it. Remember, any modifications made should not affect the final membrane properties negatively.
  2. Application Speed: The speed at which you apply the film can greatly impact its uniformity. Try to maintain a steady, smooth, and moderate speed during application. Too fast can cause streaks and uneven distribution, while too slow might make the membrane too thin or cause it to dry before you're finished.
  3. Environment: Ensure that your working environment is free from dust and air drafts. Even a small particle can cause defects in the film, and drafts can cause the solvent to evaporate unevenly, leading to non-uniformity.
  4. Technique: Start applying from one edge of the support film and move steadily towards the other edge. This can help prevent the formation of air bubbles and ensure a more uniform distribution.
  5. Applicator Cleanliness: Ensure the applicator is clean before use. Any residue from previous use could affect the distribution of the material.
  6. Preparation of the Support Membrane: Ensure the support membrane is clean and free of dust or other particles before applying the film. Also, ensure it's securely and evenly attached to the flat glass plate. If the tape is causing unevenness, you might consider using a vacuum table to secure the membrane, if available.
  7. Multiple Coatings: Depending on the viscosity and the wet thickness required, you might consider multiple thin coatings instead of one thick one. This can often yield more uniform results, although you must allow each layer to dry sufficiently before applying the next.
Remember that practice is essential to develop a consistent technique, and even small adjustments can sometimes significantly impact the results. Don't be discouraged if you don't achieve perfect results right away; membrane preparation is an art as much as it is a science.
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I need to run western blot for total and phospho form of a protein. I am planning to transfer the proteins to the membrane, probe for the phospho form first, strip and re-probe for the total protein next. Is this method correct? Will there be some phospho antibody remaining in the membrane after stripping which will interfere with the binding of the total protein antibody later?
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Dear Dr. Denny Kollareth
The protocol that you have shared could have potential negative effects on data quality. The process of stripping and re-probing can take a considerable amount of time and reagents. Moreover, the membrane stripping procedure may remove sample proteins from the membrane. Therefore, quantification of phosphoproteins following membrane stripping would not be ideal.
I would suggest that the above drawbacks from the traditional chemiluminescent method of detection could be overcome by using fluorescent western blotting which will allow you to detect both versions of the protein (multiplexing) on the same membrane.
Multiplexing your western blot typically require antibodies against the total and phosphorylated protein raised in two different species. Fluorescent secondary antibodies bearing two different fluorophores (with non-overlapping spectra) can be used allowing for multiplexing which means both phosphorylated and non-phosphorylated species can be detected simultaneously.
Another important aspect is to select antibodies which are highly specific for the phosphorylated protein state only. If the antibody is not specific, this can result in simultaneous detection of total protein and confound the interpretation of your results.
Other factors that you should consider while detecting phosphoproteins are:
1. The phosphoprotein must be kept intact. For this reason, protease and phosphatase inhibitor cocktails must be added to cell lysis buffer prior to use. These will help prevent proteins from being degraded and dephosphorylated. Keep the lysate always on ice.
2. You should avoid using milk for blocking the membrane because milk contains casein, an abundant phosphoprotein that can cause high background. Use BSA instead.
3. You should avoid using phosphate-based buffers like PBS as it can interact with anti-phospho antibodies, affecting the binding of the antibody to the target protein. Use Tris-based buffers, for instance, Tris-buffered saline with Tween-20 (TBST) instead.
4. Use proper controls.
Regards,
Malcolm Nobre
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As far as I understand, a dispersion of particles is equivalent to a true solution in what respect to the osmotic phenomenon. This was demonstrated by Einstein. There appear to be several examples in the literature of such behavior using colloids. We are using egg membranes to carry on some simple, high-school grade, exploratory experiments on Osmosis. However, after spotting some inconsistencies on Internet regarding substances osmotically active and non active, I decided to test a suspension of 93-nm polystyrene particle. This particles are subject to Brownian motion. We did not observe any measurable osmotic effect after three weeks. This can possibly be related to the dilute concentration used. In contrast, a 10 to 20 mm change in the original height of the liquids in the containers was observed when using pure water and a saturated NaCl solution. Hence, despite the well known independence of Colligative properites on the structure of the molecules dissolved, I wonder, if in the case of suspensions there are other further requirements, or if there is new evidence regarding non polar molecules that I am not aware of.
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In relation to this topic, this paper nice paper really clarifies the situation:
Bayliss WM, The properties of colloidal systems. I. The osmotic pressure of congo-red and of some other dies. Proceedings of the Royal Society B 81, 269-286 (1909)
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I tried to record electrophysiological activities (eg: action potential) of neurons from cortical organoids at 100-day-olds using whole-cell patch clamp. I was able to get the giga seal easily. However, I cannot open the cell. Because the cells were quite small,attempted applying negative pressure to rupture the membrane would draw part of the cell into the pipette instead of rupturing it. So I tried to increase the resistance of the pipette from 6 MOhm (with positive pressure on) to ~8.5MOhm, and tried to rupture the membrane again. But still I cannot open the cell. I used potassium gluconate internal solution, and standard ACSF, recorded at 35 degree celsius, with flow rate ~2ml/min.
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Hi Mai,
If the cells are small, firstly I recommend that you use smaller tip electrodes ~10 megaOhms. Secondly, once you form giga-seal, instead of suction, apply incrementing voltage or current steps (0.5 ms long at 1Hz) till you break the membrane, as all membranes will eventually break under such electrical challange (ie., electroporation). For details of the method, please see my previous publication for details about membrane electroporation, without using a dye. Once you determined the membrane breakdown potential threshold then you can use the same amount of voltage or current to succesfully break down membrane in a more controlled manner. I have developed this method in retinal whole-mounts a while ago, but I have been regularly using it in brain slices, cultured cells and human IPSC derived or organoid cells. Once you get used to it success rate is over 90%, and it is relatively simple.
best wishes,
Refik
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Sheath/skin layer could be in 10-100 nm range
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Hello Mr. Alex. The most direct way to measure a skin layers (dense, non-porous portion) of a membrane is by direct observation with FESEM at high resolutions.
Alternatively, particularly for gas separation application, one can estimate the skin layer by backwards calculation from the equation to calculate gas permeance once the intrinsic permeability of the gas is determined from fully dense membrane. Example by Pesek and Koros (1994) [ ]
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I want to determine the colocalization of a transmembrane protein along with a membrane marker, could it be possible to obtain the result with fluorescence microscopy alone or it is must to have a confocal microscopy analysis?
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Dear Manisha,
In my opinion it is not a good idea to check xo-localization with a regular fluorescence microscope.
The staining of your proteins can come from two different focal planes, which means, proteins are not co-localized but look as if they were.
For membrane proteins it should be even more complicated , since you will have fluorescence from the membrane marker all over the cell.
Therefore, use a confocal microscope.
Good luck,
Sebastian
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I am currently engaged in the modeling of a membrane packed bed reactor, specifically in its initial stages where only a packed bed reactor is considered, and the model has not yet incorporated a membrane or its associated effects.
Regrettably, I have encountered a challenge during the modeling process.
In my current model, the desired total concentration is expected to remain constant, while the velocity should vary accordingly. However, I have observed the opposite effect, which is contrary to my expectations.
I kindly request your esteemed insights regarding the potential reasons behind this discrepancy. Despite thoroughly reviewing my methodology and variables, I have been unable to pinpoint the root cause. Any suggestions or recommendations you could offer to assist me in resolving this issue would be highly appreciated.
Thank you sincerely for your attention and expertise. I eagerly look forward to receiving your invaluable input.
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Jamoliddin Razzokov Ma'Mon Abu Hammad thank you for your responses, sir. I have taken note of the provided answer and will ensure its careful consideration. Thank you for your time and assistance.
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I am determining the in vitro release profile of citral from chitosan nanoparticles. I will be using the dialysis method using PBS at different ph as the release buffer. During the dialysis, once I put the dialysis membrane containing the sample and buffer into the release buffer in a beaker, do I leave it at room temperature until I take some buffer for analysis or I place it in a shaker and then once my time interval is up, I take the required volume of the release buffer for analysis?
Thank you.
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I would put the dialysis membrane in a beaker filled most of the way to the top with the buffer, add a magnetic stir bar, place the beaker on a magnetic stirrer, and set the stirring speed fairly high to make sure the contents of the bag are thoroughly mixed, but not so fast as to endanger a collision between the membrane and the stir bar. The volume of the beaker should be as small as feasible to contain the dialysis membrane while still allowing it to stir, thereby maximizing the concentration of citral in the buffer.
If this would not provide a sufficiently high concentration of citral because of the large volume of buffer, another idea would be to put the dialysis membrane in a sealed tube, such as a 50-ml conical tube with screw cap, filled with buffer and put it on a shaker platform, shaking at the fastest rate you consider to be safe for the dialysis membrane.
A possible problem with this experiment would be if the citral is not soluble in the dialysis buffer.
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Hello all,
I am used to using the TurboBlot for Western Blot and had no issues with exception of transferring high MW proteins. That's why I wanted to try the Wet transfer method. However, everytime I try it, the lower bands appear so badly on the membrane (the images are total protein blots). What could be the cause?
I am running the system (Biorad Criterion Blotter) with a constant voltage of 100V in a cold room (the problem is not overheating). The buffer I use is the recommended by Biorad (I do it myself). While I am running, I put an ice pack inside together with a magnetic stir. Could it be the magnetic stir motion causing this?
Thank you.
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Daniela Liebsch Thank you for your answer. Yes, the gel is totally fine. I always activate the gel for total protein and everything seems normal. I will try to troubleshoot by the possibilities you mentioned
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I am experiencing issues with the expression of phosphorylated proteins in my western blot experiments. Specifically, I observe strong phosphorylated protein expression but no expression of the corresponding total proteins in the same samples. For example, I detect phosphorylated STAT1 (pSTAT1) but not total STAT1 protein. Similar results were obtained for pSTAT3 and STAT3. I have thoroughly searched online but have been unable to find a possible explanation for this phenomenon.
I would greatly appreciate any advice or suggestions from anyone who has encountered a similar issue.
Here is my experimental protocol:
  1. Prepared single cell suspensions from fresh mouse spleens using a buffer containing 1x PBS, 2% FBS, EDTA, and antibiotics.
  2. Washed the cells once with ice-cold PBS and then lysed them using RIPA buffer (with proteinase and phosphatase inhibitors) by vortexing for 10 seconds every 5 minutes on ice, repeated 4 times.
  3. Quantified the protein concentration using the BCA assay and mixed 30 micrograms of protein with loading dye, boiling the mixture at 90℃ for 10 minutes.
  4. Transferred the proteins to membranes and blocked the membranes with BSA at room temperature for one hour on a shaker.
  5. Washed the membranes three times with TBST containing 0.2% Tween-20.
  6. Incubated the membranes with primary antibodies overnight at 4℃ on a shaker.
  7. Washed the membranes three times with TBST containing 0.2% Tween-20.
  8. Incubated the membranes with secondary antibodies at room temperature on a shaker.
  9. Washed the membranes three times with TBST containing 0.2% Tween-20.
  10. After detecting phosphorylated proteins, stripped the membranes by adding deionized water and microwaving for four minutes.
  11. Blocked the membranes with BSA and incubated them with primary antibodies.
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You might also try running separate, replicate gels, one for phospho- and one for total protein. Instead of stripping and reprobing.
Also, are you 100% confident in the specificity of the phospho antibodies? Is it possible the bands for pSTAT1 and/or pSTAT3 are really aomething else?
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Is it possible that a small protein goes through a nitrocellulose membrane? if the answer is yes, what´d it be the conditions that can be adjusted to prevent such passage.
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Yes, it does. There are several tips you can do:
1. As Mr. Manuele mentioned, check the pore size.
2. Air-dry the membrane after blotting.
3. Fix your membrane after blotting and before blocking (gonna add a reference).
4. Some labs use two membranes instead of one.
5. Adjust the time, current and voltage of blotting.
6. Make sure that you use 20% methanol in the blotting buffer (if you do not want to blot HMW proteins at the same time).
Pls refer to the following article for more information about fixation:
10.1016/0003-2697(89)90634-9
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What are the easiest ways to make polysulfone electrospun nanofibers hydrophilic to make TFCN membranes?
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@Foroogh Khodadadi
Thank you for your explanation
We know that PEG and PVP have different molecular masses. What molecule do you recommend to use for these substances?
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I have an idea to explain consciousness. About 8 years ago, Professor Donald Hoffman asked a very important question to help us understand consciousness. He asked, "How is it possible for calcium and potassium ions that enter and exit through neuronal membranes to give rise to our conscious experience of, for example, the color green, or a smell, or a sound?"
So, my idea that answers this question is that the color green, for example, has a specific frequency associated with it, and the same goes for the color red or any other stimuli around us. When these frequencies enter the brain, they can be considered as inputs.
The frequency of the color green, for example, has a specific code or pattern in the brain. This code represents the way that nerve cells communicate with each other through the exchange of calcium and potassium ions across neuronal membranes.
We can call this process that occurs in the brain "processing," and the brain, because it translates these frequencies, can be thought of as a compiler in a computer.
A compiler takes human-readable code and converts it into machine-readable code, known as machine language.
Then, somehow, our conscious experience of the color green emerges.
We can consider the formation of conscious experiences as outputs.
To me, this topic feels similar to programming. In programming, we have outputs, compilers, processing, and inputs. So, could it be possible that the brain is programmed to understand all these frequencies, decode their patterns, and create consciousness? I'm not saying that we are programmers, but rather, it's the brain itself.
What I'm trying to say is that everything in the universe has its own frequency and its own specific code. The brain decodes these codes through the electrical activity that occurs with the entry and exit of ions across neuronal membranes, and then consciousness is formed.
Is it possible that this could be true?
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Your idea presents an interesting perspective on explaining consciousness and its relationship to neural activity. It incorporates the concept of frequencies associated with sensory stimuli and suggests that the brain acts as a "compiler" to translate these frequencies into conscious experiences.
While your analogy to programming and the idea of the brain decoding specific codes is intriguing, it's important to note that the nature of consciousness is still a topic of active research and debate in the field of cognitive science. There is currently no widely accepted theory that fully explains how neural activity gives rise to subjective experiences.
The relationship between neural processes and conscious experiences is a complex and multifaceted phenomenon. It involves not only the transmission of signals across neuronal membranes but also the integration of information from various brain regions, the role of attention, memory, and the influence of cognitive and emotional factors.
While frequency processing and neural coding are areas of research interest, it is important to consider that consciousness likely involves more intricate mechanisms than a simple decoding of frequencies. It is likely to involve the dynamic interactions between neurons, the emergence of complex networks, and the integration of information at various levels of processing.
Overall, your idea provides a thought-provoking perspective, but it is essential to approach the study of consciousness with an open mind and consider multiple perspectives and theories. Ongoing scientific research continues to explore the nature of consciousness, and future discoveries may shed more light on this fascinating topic.
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I am fabricating TFC membranes using interfacial polymerization with TMC and piperazine as monomers. I have tried different dipping for both monomer solutions, dipping and annealing duration. I have also tried different ways for removing excess water from the surface after dipping the polysulfone as the lower layer, in piperazine solution, however, with none, the polyamide layer becomes continuous. It rather forms as discrete islands. I appreciate suggestions in this regard.
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Dear Zahra Khezri ,
Could you please add a photo of your synthesized membranes? Then, it would be easier to understand what is happening there.
Thank you so much
Best wishes
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I work with large proteins and try to transfer my western blot studies for his reason ı using 6% gel. In a semi-dry transfer system, my all proteins are transferred in 25V 1.5amper 9 minutes ı check my jel with commasie blue stain. Then bloking at 5% BSA TBST 1 hour at room temperature for 1 hour, wash three times, 1 hour at room temperature in 1:1000 primary antibody in 1% TBST BSA and wash three times, and finally, 1% TBST BSA 1 hour at room temperature 1:5000 secondary antibody. But the membrane seems very dark and dirty. After mild stripping of the membranes, I can only get imaging, but ı think that after mild stripping ı lost my protein because the bands seem very reduced.
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You can try with 40 - 60 minutes transfer adn blocking 2-3 hour
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right now I'm modeling a membrane pack bed reactor.
but I haven't been able to get the appropriate results because I can't connect the effect of the permeation that occurs to the velocity inside the reactor.
is there an equation I can use regarding this?
Thank You
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In a membrane-packed bed reactor, the presence of a membrane introduces permeation, which affects the fluid velocity distribution within the reactor. To model the effect of permeation on the velocity, you can consider the concept of mass conservation and use appropriate equations that account for both convective flow and permeation. One commonly used equation is the Continuity Equation. Here's how you can incorporate permeation effects into the velocity modeling:
  1. Continuity Equation: The Continuity Equation expresses the conservation of mass for an incompressible fluid flowing through a reactor:
∇ · (ρu) = 0
where:
  • ∇ is the gradient operator,
  • ρ is the fluid density, and
  • u is the velocity vector.
  1. Incorporating Permeation: To incorporate the effect of permeation, you need to consider the additional flow due to the permeating species across the membrane. This can be expressed as:
∇ · (ρu) + ∇ · (ρ_pu_p) = 0
where:
  • ρ_p is the density of the permeating species, and
  • u_p is the velocity vector of the permeating species.
This equation combines the convective flow (first term) and the permeation flow (second term).
  1. Relationship between Velocity and Permeation: The relationship between the velocity of the permeating species (u_p) and the velocity of the fluid (u) can be determined by considering the permeability and surface area of the membrane, as well as the concentration gradient across the membrane. This relationship is typically specific to the membrane material and the permeating species and may require experimental data or modeling approaches specific to the system you are working with.
It's important to note that the modeling of membrane-packed bed reactors involves additional considerations beyond just velocity, such as concentration profiles, reaction kinetics, and mass transfer limitations. Depending on the complexity of your system and the specific phenomena you want to capture, you may need to incorporate additional equations or models to accurately represent the reactor behavior.
Consider consulting literature related to membrane-packed bed reactors or reaching out to experts in the field for guidance on specific equations, correlations, or modeling approaches that would be most appropriate for your system.
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Human amniotic membrane (HAM) was immersed in diluted honey (0.02% & 0.3%) for 24 hours. After 24h, HAM (1cm2) was immersed and incubated in PBS (in 12 multi well plate). 1ml of PBS was collected at pre-determined time (1h, 3h, 12h, 24h & 72h) to observe the release of honey from HAM over time. 1ml of PBS was replenished at every sampling time.
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Asif Khan Thank you very much for the detailed explanation. Definitely helped me.
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I did Western Blot (WB) with Photo-cross linked protein. I had some unusual thing (maybe for me). When i added ECL substrate on membrane. The signals were getting weak with in just 1 mint and eventually completely dropped. What's the possible reason for this and how i can fix it.
Thank you so much for your valuable suggestions.
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Was it a strong signal? Remember, it's a reaction catalysed by the HRP you've stuck to your membrane, and if you've stuck a LOT of enzyme activity there, the reaction will proceed rapidly in that specific location.
For really intense signals its not uncommon to see "negative" blots, where the background levels of luminescence are visible on the film, while the actual signal is a blank void (having burned out all the ECL reagents before the film can even be applied).
You can fix this by...well, loading less on your gel.
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I am working with PEN membrane slides used in laser capture microdissection. When I try to cut the cells on the membrane, too many bubbles are seen. I made a tiny hole on the edge of the membrane and water came out. I did dehydratation steps after IHC and put the slides 60 C inside the hot plate to make them dry but I couldn't get rid of water without making a hole on the membrane. Do you have any idea what could be the reason of the water or any suggestions to make water-free slides? TIA
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My apologies, Burcu Yener Ilce . I focused on the problem and potential solution and didn't pay total attention to your explanation. To be clear, I the person I chatted with mentioned he air-dries the slides in the hood. I hope you find a solution soon. I should try it on Monday, but I am doing cryosectioning.
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I am working with chitosan membrane for food packaging and among all the papers i have read no one has mentioned this problem. how to over come this probem of folding membrane?
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Chitosan is mainly hydrophilic. If it shrinks, maybe your environment's relative humidity RH % is not too high, or the temperature is too high. I recommend looking for sorption isothermal graphs. Good luck.
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I am currently working on the synthesis of reverse osmosis membranes using a polysulfone support and a polyamide active layer. Upon testing membrane performance, I am getting very low salt rejection and high water permeability which is not consistent with literature.
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I agree with what the previous colleagues said. However, I think the crux of the matter is that your selection layer has some defects. Just like when the bathtub is filled with water, the water will all slip away from the downpipe. This question has run through the pre-experimental phase of every work I've done since I started doing membranes. Until one day, I suddenly wanted to understand this matter in a dream. Actually every material, every polyamide layer, is different, just like there are a thousand Shakespeares for a thousand people who read Hamlet.So, when you make each membrane, if it is what you said, I think you will get all kinds of strange and irregular results. In fact, for the synthesis process of each polyamide layer, I think that not only following the literature, but finding a method similar to interfacial polymerization, I think that the polyamide layer can be synthesized with peace of mind. As several colleagues said before, if it were me, I would have a high probability of not succeeding if I followed them strictly. Therefore, I think the most important thing for synthesizing a defect-free selection layer is to understand the properties of each component, pay attention to the details that are not mentioned in the literature, and boldly repeat the experiment. Just like some selective layers are not highly cross-linked, if you blow it with nitrogen with too much pressure during the drying process, it is bound to have defects. Therefore, dear colleague, I suggest that you use the slowest speed in history when you make a membrane next time. After each step is completed, think carefully about what contribution this step has made to the synthesis of the selective layer. What are the results. In this way, step by step, even if you are not successful, you will make new discoveries, and then you will be closer and closer to success. Some people attribute this process to "manipulation", but I am more inclined to sum up the experience in a large number of experiments, just like the old saying "practice makes perfect(熟能生巧)".
Hope my seemingly lengthy conversation can solve your problem. In the meantime, any comments from colleagues are welcome. good luck!
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Hey
I work on my thesis, but i have some problem
I know the result is not good, but something is happen, i dont know where/what?
I work on HERC1 520KD, I prepare lysate then did CO-IP with HERC1
Western Blot 8% of Acrylamide Gel, and the transfer is 2.5 hours.
when i add Primary Ab >> anti rector- 192KD- > then Anti Rabbit >> i got the First Picture.
i strip the membrane with Beta-mercapto >> 30 mins at 50C.
to develop another Ab which is HSP 90 the result like this "image 2 " !
Please if you have any Advice, Thank you any way !
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Difficult to guess what's going wrong. Have you tried other stripping methods, like 10mM or 100mM NaOH for a few minutes? Beware, too concentrated NaOH is dissolving NZ membranes quickly.
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I am modifying the yeast expression vector pYES2 to express a plant transporter. The gene is cloned but I failed to insert an appropriate signal sequence. If the recombinant protein contains multiple transmembrane domains, I am led to believe that these will self assemble upon localization/translation in the ER-membrane. If this is correct, I should be able to use a secretion signal preceding my transporter gene.
There are not any commercial expression vectors which are designed for membrane proteins. I would expect that such a vector feature, the inclusion of a membrane signal sequence, would be available. However the secretion signal, alpha-mating factor sequence, is indeed quite popular for expression in yeast. Perhaps I am looking in the wrong direction for studies on membrane localization in yeast? I cannot find anything on inserting "membrane signal sequences", specifically for yeast.
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Thank you Dr. Liger and Dr. Stolz.
For anyone interested, I've found the site below to be helpful in visuallizing transmembrane domains.
I'm still in the troubleshooting phase of this issue. I can see there are multiple transmembrane domains in my protein, although I don't know if any of these can be considered a signal sequence or not. Never mind whether or not it is cleavable...
I figured expression in yeast would be appropriate as a previous study injected capped-RNA of the coding sequence into frog eggs and produced functional transporters. I just need to re-sequence my expression vector maybe..
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I am doing multiplex immunofluorescence assay on FFPE section. I used CD3 to identify T cells and observed that some of T cells stained with CD3 showed nuclear staining instead of membranous. I am not sure why the staining pattern is nuclear for CD3? is it possible to see nuclear staining with CD3?
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This depends on the type of cancer you are investigating and the tissue from which the FFPE sections are made. As mentioned, e.g. T-cell lymphomas show cytoplasmic CD3 staining.
Try to figure out in which tissue/cell type you see the cytoplasmic CD3 staining.
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I am preparing cell membranes for 35s GTP gamma assay, I have two samples of 1.66 mg/ml and 1.4mg/ml protein concentration , and both are 100 microliters volume, how can I dilute them to be kept in freezer?
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  1. Determine the current protein concentration of your crude membrane samples. Let's assume you have Sample A with a concentration of X mg/ml and Sample B with a concentration of Y mg/ml.
  2. Calculate the dilution factor needed to achieve a final concentration of 1 mg/ml for both samples. Divide the current concentration (X or Y) by 1 mg/ml to obtain the dilution factor. For example, if Sample A has a concentration of 1.66 mg/ml, the dilution factor is 1.66/1 = 1.66.
  3. Prepare a dilution buffer suitable for your assay. This buffer should maintain the stability and activity of your samples. Use a buffer that is commonly used for membrane protein assays or consult your assay protocol for specific recommendations.
  4. Calculate the volume of dilution buffer required to achieve a 1 mg/ml concentration for each sample. Divide the desired final volume (100 μl) by the dilution factor obtained in step 2. For example, if the dilution factor for Sample A is 1.66, the volume of dilution buffer needed is 100 μl/1.66 = 60.24 μl.
  5. Add the calculated volume of dilution buffer to each sample and mix gently to ensure proper dilution.
  6. Aliquot 100 μl of each diluted sample into separate tubes suitable for freezing.
  7. Label the tubes with sample identifiers and the concentration (1 mg/ml).
  8. Freeze the aliquots at the appropriate temperature (-20°C or -80°C) for storage.
By following these steps, you will have diluted your crude membrane samples to a concentration of 1 mg/ml and stored them as 100 μl aliquots for future use in the 35sGTP gamma assay.
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Are there any forms to display cholesterol in VMD for a pdb file within membrane?
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Found it. Here are the lines that can display the cholesterol on VMD. In the display box just put: "resname CHL1" then create a rep and type "lipid and not water" and change the color IDs to be able to distinguish them. To see the resname for Cholesterol, open your PDB file textfile and search for CHL in the residues (usually at the bottom). I have attached pictures:
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Hi everyone,
I am planning a series of Western Blot experiments where I will be probing for a range of targets in my samples. Whilst optimising, I have been cutting my membranes at the relevant molecular weights for each of my proteins to minimise amount of sample used.
However I know that some journals request images of the 'full' membrane in order to publish now and was wondering if an image of the membrane (cut into pieces) would be acceptable?
Has anyone had any recent experience with this/any advice to give?
If I can get away without running separate experiments for each protein, it would save me a lot of time (and money!).
Many thanks,
Rebecca
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Hi Rebecca,
It is depend on how you cut the membrane. General rule for the WB full blot is that it contain ladder on the side (so that the protein size can be verified), have the internal control (so that the protein expression can be relatively quantified), and the blot exposure is optimised (so that there is not over- or under exposure that hinder the unspecific bands). While you can have different crop in the manuscript, but often reviewer will need to to have the full blot in the supplementary section so that they can verify the protein data. In other word, you can have the cut as it feed your work, but you will need to assembly them into a full blot so that the reviewer can assess it.
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Hi everyone,
I am planning a series of Western Blot experiments where I will be probing for a range of targets in my samples. Whilst optimising, I have been cutting my membranes at the relevant molecular weights for each of my proteins to minimise amount of sample used.
However I know that some journals request images of the 'full' membrane in order to publish now and was wondering if an image of the membrane (cut into pieces) would be acceptable?
Has anyone had any recent experience with this/any advice to give?
If I can get away without running separate experiments for each protein, it would save me a lot of time (and money!).
Many thanks,
Rebecca
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Probe the whole membrane and use a "rainbow" western for several targets. Cutting the membrane does not save sample, as you need a certain amount in a band for detection. It also does not really save primary antibody, as that solution can be used many times (use 0.1% BSA in PBS as solvent with timerosal as preservative, develop blots at 4 degrees o/n). But you preserve the information about antibody specificity (that you get a single band).
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What exactly is the 'initial water flux' in membrane systems and how do adjust it if for e.g I want the initial water flux of FO and RO to be the same
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what if I dont want to apply tmp on the FO?
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MM/PBSA is done for protein in the membrane system. Can anyone please suggest something?
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Arunima Verma I have the same problem. Did you find how to solve it?
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I found a bag of old tubes in the lab that look like spin columns(?). There are no labels so I cannot identify them. I spun some water just to see whether they are porous as they seem to have membranes inside but no water was extracted in the Eppendorf tubes they were placed in during the centrifugation. Are you able to identify the tubes from the picture? (-:
Thanks!
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Yes!! Very nice tube.
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I am a student, and my research about membranes, can I search for porosity membranes with SEM results or with others?
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I can't answer your question because I study only advanced compound semiconductors with SEM.
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I have kidney and heart samples with the same concentration of protein, but when I run tubulin control, there are many differences between the samples. The membranes were stained with Coomassie blue, and no significant difference was observed between them. What could be wrong?
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Just because the total protein expression was similar between samples and heart vs kidney doesn't mean the expression of a particular protein will be stable. You always should validate whether your loading control / reference protein expression is stable across your experimental groups.
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I am learning NAMD for simulating membrane embedded proteins. While running simulation, can we use different versions of Charmm parameter files?
Also, an error stating "FATAL ERROR: DIDN'T FIND vdW PARAMETER FOR ATOM TYPE ON3", is coming, but there are no ON3 atoms in my structure. For running this simulation, I have used parameter files as mentioned below:
parameters par_all36_lipid.prm
parameters par_all36m_prot.prm
parameters toppar_water_ions.str
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Hi,
I am getting the same error "FATAL ERROR: DIDN'T FIND vdW PARAMETER FOR ATOM TYPE ON3." There is no ON3 atom in the pdb and psf files.
Any solution how to troubleshoot this?
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What are the factors that affect membrane power generation?
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  1. Increase the surface area of the membrane: A larger membrane surface area can lead to a larger electric potential and current output. This can be achieved by increasing the number of membranes or by using a larger membrane surface area.
  2. Optimize the membrane composition: The properties of the membrane, such as its selectivity and permeability, can significantly impact the performance of the membrane power generation. By optimizing the composition of the membrane, such as its thickness, pore size, and material properties, the efficiency of the power generation process can be improved.
  3. Improve the solution composition: The composition of the solutions on either side of the membrane can also affect the power generation performance. By optimizing the concentration and pH of the solutions, the electric potential and current output can be increased.
  4. Enhance the ion transport: The ion transport across the membrane is the fundamental mechanism for generating electric potential and current. Enhancing the ion transport through the membrane, for example, by applying an external electric field or modifying the membrane surface properties, can improve the power generation efficiency.
  5. Utilize multi-stage processes: By connecting multiple membrane power generation stages in series, the overall signal can be enhanced, leading to higher electric potential and current output.
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I'm using LUVs as membrane models to study drug-membrane interaction. My composition of liposome is POPC : CHOL. I was confused about the selection of a buffer system for my liposomes. So far, I have tried PB and HEPES buffer. I am not getting good results on the DSC thermogram. Are there any guidelines for choosing a buffer depending on different experiments? If there, what are the compatible buffers for DSC and NMR studies of liposomes?
Kindly Help me with this. Any literature which gives a detailed analysis of liposomes with respect to buffer works fine.
Thank you!
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In reply to your question:
"How to choose suitable buffer for liposome preperation?"
We can chose from a huge list of buffers of alternative hydration media based on the application we aim for.
From the Reference (listed below and attached):
" ....
Liposome hydration or suspension media can comprise any of the above-mentioned buffers or saline solution (0.9% w/v of NaCl in distilled water) or isotonic sucrose solution (9.25% w/v sucrose in distilled water).
...."
"... Alternative hydration mediums are saline or nonelectrolytes such as a sugar solution. For an in vivo preparation, physiological osmolality (290 mOsmol/kg) is recommended and can be achieved using 0.6% saline, 5% dextrose, or 10% sucrose solu- tion (24). The aqueous medium can contain salts, chelating agents, stabilizers, cryo-protectants (e.g. glycerol) and the drug to be entrapped. ...."
Mozafari, M. R. (2010). Nanoliposomes: preparation and analysis. Liposomes: Methods and Protocols, Volume 1: Pharmaceutical Nanocarriers, 29-50.
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I took SEM pictures of my clean 0.2um pore size PES membrane filter. The first picture is coated with 5nm gold, and the second is with 20 nm carbon. Both pictures are 2500X magnification, and the scale is 4um. I wonder why the two pictures look significantly different. The picture I coated with gold doesn't look like the pore size is 0.2um.
Thanks,
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A lot of different suggestions have been made. Perhaps the key message is to only ever change exactly ONE parameter when comparing images of different structures, as there are many (acc. voltage, current, dose, vacuum level, detector type, coating thickness, coating type...) that can influence what you see. Certainly 20nm of C coating can already start to cover many small details incl. holes that tend to be overgrown (you can buy holey C films of about 10nm thickness as TEM supports, which look a bit like the images here). Whether you use Au or C coating, my suggestion would be to coat with as low amounts as you can get away with to just avoid charging - I also assume the polymer itself will be beam sensitive so try low kV and smallest possible beam current, and then watch your specimen while scanning the beam - it may change while you watch!