Science topic
Membranes - Science topic
Thin layers of tissue which cover parts of the body, separate adjacent cavities, or connect adjacent structures.
Questions related to Membranes
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.
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

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
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.
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?

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.
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.
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?
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.
PDVF membrane incorporated with CuO nanoparticles can be suitable for what degradation ?
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.
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).
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.
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
Who can advise how to carry out experiments on membrane adsorption of hollow fibers?to carry out experiments on membrane adsorption of hollow fibers?
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?

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
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?
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.


Is 1 Kilodaltons dialysis membrane is reusable for same sample? is tube or membrane is suitable for large quantity carbon dots filtration.\?
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.
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......
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.
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.
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
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,

what are the functions of F1 particles in mitochondria ?
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.
For example, in the process of electrodialysis.
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.
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?
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.
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.
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?
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.
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.
Sheath/skin layer could be in 10-100 nm range
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?
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.
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.
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.



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:
- Prepared single cell suspensions from fresh mouse spleens using a buffer containing 1x PBS, 2% FBS, EDTA, and antibiotics.
- 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.
- 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.
- Transferred the proteins to membranes and blocked the membranes with BSA at room temperature for one hour on a shaker.
- Washed the membranes three times with TBST containing 0.2% Tween-20.
- Incubated the membranes with primary antibodies overnight at 4℃ on a shaker.
- Washed the membranes three times with TBST containing 0.2% Tween-20.
- Incubated the membranes with secondary antibodies at room temperature on a shaker.
- Washed the membranes three times with TBST containing 0.2% Tween-20.
- After detecting phosphorylated proteins, stripped the membranes by adding deionized water and microwaving for four minutes.
- Blocked the membranes with BSA and incubated them with primary antibodies.

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.
What are the easiest ways to make polysulfone electrospun nanofibers hydrophilic to make TFCN membranes?
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?
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.
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.
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
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.
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.
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
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?
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.
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 !


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.
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?
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?
Are there any forms to display cholesterol in VMD for a pdb file within membrane?
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
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
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
MM/PBSA is done for protein in the membrane system. Can anyone please suggest something?
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!

I am a student, and my research about membranes, can I search for porosity membranes with SEM results or with others?
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?

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
What are the factors that affect membrane power generation?
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!
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,
